PART 2 ANNEXURE TO DRAFT ENVIRONMENTAL IMPACT … · Compliance Monitoring of Existing Plant A-287...
Transcript of PART 2 ANNEXURE TO DRAFT ENVIRONMENTAL IMPACT … · Compliance Monitoring of Existing Plant A-287...
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PART 2 ANNEXURE TO
DRAFT ENVIRONMENTAL IMPACT ASSESSMENT REPORT
PROPOSED EXPANSION PROJECT FOR MANUFACTURING OF SYNTHETIC ORGANIC CHEMICALS
(PHARMACEUTICAL BULK DRUGS & INTERMEDIATES) [CAPACITY: 287.77 TPM]
[SCHEDULE 5(f) - CATEGORY A]
SURVEY NO: 44/B, VILLAGE: NALDHARI SILUDI-VALIA ROAD, NEAR ANKLESHWAR,
TAL.: VALIA, DIST.: BHARUCH, STATE: GUJARAT
[TOR LETTER NO.: IA-J-11011/583/2017-IA-II(I) Dated 10/02/2018]
[STUDY PERIOD: MARCH 2017 – MAY 2017]
PREPARED BY:
(QCI-NABET ACCREDITED EIA CONSULTANT)
CERTIFICATE NO.: NABET/EIA/1619/SA 053 VALID UPTO 22/05/2019
3RD FLOOR, AKASHGANGA COMPLEX, B/S. SUVIDHA SHOPPING CENTRE, NR. PARIMAL UNDERPASS, PALDI, AHMEDABAD-380 007, GUJARAT
TELEFAX: (079) 2665 0878; E-MAIL: [email protected]
MAY, 2018
Doc. No.: EEC/A-188/16-17/EIA-21/Rev. 01
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ANNEXURES
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Intas Pharmaceuticals Ltd., Valia-Bharuch Environmental Impact Assessment Report Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
List of Annexure
LIST OF ANNEXURES
ANNEXURE NO. TITLE PAGE
NO.
1. Land Possession Documents A-1
2. Details of Manufacturing Process A-35
3. Details of Raw Materials Requirement A-167
4. Details of storage of Products & Raw Materials A-177
5. Layout Plan A-183
6. Acknowledgement of CGWA Application Slip A-184
7. Copy of Membership (NECL, BEIL) & LOI (RSPL) A-185
8. Details of fly ash generation A-188
9. Copies of Consent to Establish A-189
10. Copies of Consolidated Consent & Authorization (CC&A) A-207
11. Compliance of CC&A A-247
12. Annual Compliance (Form V) A-251
13. Third Party Monitoring Reports A-257
14. Compliance Monitoring of Existing Plant A-287
15. Notice and its compliance A-292
16. Inspection Reports from GPCB XGN A-312
17. PLI Policy A-342
18. License from PESO for storage of hazardous chemicals A-344
19. Compliance of CREP guidelines A-347
20. Photographs of baseline monitoring activities A-351
21. Methodology for Baseline Environmental Monitoring & Analysis A-352
22. Analysis report of Baseline Environmental Monitoring A-357
23. Details of Traffic Survey A-379
24. Basic amenities in the study area A-382
25. EHS Policy A-386
26. List of SOP’s for EHS A-388
27. Characteristic of Hazardous Chemicals A-390
28. Health Check up Form A-400
29. Analysis of Maximum Credible Accident Scenarios A-401
30. Checklist for Safety Compliance A-469
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Intas Pharmaceuticals Ltd., Valia-Bharuch Environmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
List of Annexure
ANNEXURE NO. TITLE PAGE
NO. 31. Proposed CSR Activities A-477
32. Do’s and Don’ts A-478
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ANNEXURE 1 LAND POSSESSION DOCUMENTS
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ANNEXURE 2 DETAILS OF MANUFACTURING
PROCESS
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Intas Pharmaceuticals Ltd., Valia-Bharuch Environmental Impact Assessment Report Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
MANUFACTURING PROCESS DETAILS
Product Code Name of Products PAGE
NO.
P1 Dabigatran Etexilate Mesylate A-35
P2 Lurasidone HCl A-43
P3 Lacosamide A-58
P4 Bendamustine HCl A-70
P5 Trazodone HCl A-81
P6 Gemcitabine HCl A-89
P7 Capecitabine A-98
P8 Erlotinib HCl A-104
P9 Imatinib Mesylate Alpha A-111
P10 Nilotinib A-116
P11 Dasatinib A-125
P12 Pazopanib HCl A-134
P13 Sorafenib A-143
P14 N-BZ-Bis-Lactam A-151
P15 N-BOC-Bis-Lactam A-154
P16 5-(4-(4-(5-Cyano-1H-indol-3-yl)-butyl)-piperazin-1-yl)
benzofuran-2-carboxamide
A-157
P17 2-acetamido-2-phenethylpropane-1,3-diyl-diacetate A-159
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
MANUFACTURING PROCESS DETAILS
P1. DABIGARTAN ETEXILATE MESYLATE
a) Manufacturing Process
Stage I (Intermediate)Amide formation of ethyl 3-(3-amino-4-(methylamino)-N-(pyridin-2-yl)
benzamido)propanoate with 2-((4-cyanophenyl) amino) acetic acid in presence of 1,1’-
Carbonyldiimidazole and N, N’-Dimethylformamide to give intermediate of Dabigatran
Amidine Intermediate Stage-I; which is further cyclized in presence of Acetic acid and
further react with maleic acid in presence of Ethyl acetate and Denature Ethanol to
give Dabigatran Amidine Intermediate Stage-I.
Stage II (Intermediate)Synthesis of Amidine of Dabigatran Amidine Intermediate Stage-I in presence of
Denature Ethanol and hydrochloric acid gas to form intermediate of Dabigatran Amidine
Intermediate; which is further reacting with ammonium carbonate in presence of
Denature Ethanol to give crude Dabigatran Amidine Intermediate and isolated in
Denature Ethanol and Isopropyl acetate to give pure Dabigatran Amidine Intermediate.
Stage I (Product)Dabigatran Amidine Intermediate react with n-Hexyl chloroformate in presence of
aqueous Potassium carbonate solution and Tetrahydrofuran. Separate the organic
layer followed by product extraction in tetrahydrofuran from aqueous layer. Combined
organic layer concentrate by solvent distillation. give charcoal treatment in Methylene
chloride. Give the water wash to organic layer. Remove the solvent by distillation. and
precipitate product in mixture of isopropyl alcohol and methyl isobutyl ketone. Isolate
solid by filtration. Purify the wet cake with mixture of isopropyl alcohol and methyl
isobutyl ketone. Isolate solid by filtration. Dry the wet material to get stage-I product.
Stage II (Product)Stage-I is dissolve in acetone and filter the reaction mass. Filtrate react with Methane
sulphonic acid and convert in to Dabigartan etexilate mesylate. Product precipitate by
cooling and isolate solid by filtration. Dry the wet material to get Dabigartan etexilate
mesylte.
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
b) Reaction Chemistry
Stage I (Intermediate)
Stage II (Intermediate)
Stage I
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Stage II
c) Process Flow Diagram
Input Qty., kg Output Qty., kg
2-((4-cyanophenyl)amino) Acetic Acid 76.60
N,N-Dimethyl Formamide 311.00
1,1’-Carbonyldiimidazole 78.20 Recovered Dimethyl Formamide 308.00
Ethyl 3-(3-amino-4-(methylamino)-N-(pyridin-2-
yl)benzamido) propanoate [DAP] 110.00 Recovery Loss 3.00
Acetic Acid (Glacial) 275.00
Recovered Acetic Acid 270.00 Recovery Loss 5.00
Ethyl Acetate 2,700.00 Sodium Carbonate 165.00
Sodium Chloride Solution 110.00 Aq. Effluent 5,892.90
Water 5,500.00
OLMaleic Acid 74.50
Ethanol 260.60
Ethyl Acetate 254.00 Org. Mother Liquor 3,280.00
Loss 9.00
Recovered Ethyl Acetate 7.00
Intermediate (Stage I) 140.00
Total 9,914.90 Total 9,914.90
Dabigatran Etexilate Mesylate (Stage-I)Process
Centrifugation
Reaction
Reaction
Distillation
Extraction & washing
Reaction
Drying
Dabigatran Amidine
Intermediate Stage-I
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Input Qty., kg Output Qty., kg
Intermediate (Stage I) 140.00 Ethanol 437.00 Recovered Ethanol 432.00
Hydrochloric Acid 9.30 Recovery Loss 5.00
Ethanol 1,100.00 Aluminium Carbonate 280.00
Ethanol 253.00 Solid Waste 280.00
Ethanol 530.00 Recovered Ethanol 1,868.00 Recovery Loss 15.00
Isopropyl Acetate 1,670.00
Isopropyl Acetate 157.00 Org Mother Liquor 1,862.30 Loss 13.00
Recovered Isopropyl Acetate 16.00
Intermediate (Stage II) 85.00
Total 4,576.30 Total 4,576.30
Dabigatran Etexilate Mesylate (Stage-II)Process
Dabigatran Amidine
Intermediate
Precipitation
Centrifugation
Drying
Reaction
Reaction
Filtration
Distillation
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Input Qty., kg Output Qty., kg
Dabigatran Amidine Intermediate 85.00
Water 255.00
Water 85.00 Aq. Effluent 325.00
wet cake
Tetrahydrofuran 1,513.00 Potassium Carbonate 65.75 n-Hexyl Chloroformate 31.32
Water 425.00
Tetrahydrofuran 227.00 Aq. Effluent 643.50
Methylene Chloride 226.00 Recovered Tetrahydrofuran 1,440.00 Recovery Loss 72.00 Recovered MDC+THF 215.00 Recovery Loss 9.00
Methylene Chloride 3,172.00 Aq. Effluent 860.00 Water 850.00 Spent Carbon 8.50
Activated Carbon 8.50 Loss 5.00
Rec MDC 2,980.00 Isopropyl Alcohol 134.00 Recovery Loss 150.00
Rec MDC+ IPA 150.00 Recovery Loss 3.00
Isopropyl Alcohol 1,128.00 Methyl Isobutyl Ketone 285.20
Isopropyl Alcohol 54.00 Methyl Isobutyl Ketone 14.00 Org Mother liquor 1,530.00
Loss 12.00
Toluene 148.00 Recovered Toluene 150.00 Recovery Loss 3.00
Toluene 370.00 Methyl Isobutyl Ketone 340.00
Toluene 74.00 Org. Mother Liquor 915.77 Methyl Isobutyl Ketone 68.00
Recovered Toluene + MIBK 34.00
Intermediate (Stage III) 53.00
Total 9,558.77 Total 9,558.77
Process
Intermediate (Stage III)
Centrifugation
Extraction
Distillation
Filtration
Distillation
Precipitation
Wet cake Purification
Precipitation
Centrifugation
Drying
Dabigatran Etexilate Mesylate (Stage-III)
Reaction
Centrifugation
Reaction
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
d) Summary of Mass Balance
Capacity of Finished Product, TPM : 0.8
Working Days Per Month : 26
Stage I (Intermediate)
S. No Input Kg/
Batch Remarks Output Kg/Batch Remarks
1
Ethyl 3-(3-amino-4-(methylamino)-N-(pyridin-2-yl)benzamido) propanoate [DAP]
110.00 Reactant Intermediate (Stage I) 140.00 Intermediate
(Stage I)
22-((4-cyanophenyl)amino) Acetic Acid
76.60 ReactantRecovered Dimethyl Formamide
308.00Sell to authorized recycler
3 1,1’-Carbonyldiimidazole 78.20 Reagent Recovery
Loss 3.00 Solvent Loss
4 N,N-Dimethyl Formamide 311.00 Solvent Recovered
Acetic Acid 270.00Sell to authorized recycler
5 Acetic Acid (Glacial) 275.00 Reagent Recovery
Loss 5.00 Solvent Loss
6 Maleic Acid 74.50 ReagentRecovered Ethyl Acetate
7.00Sell to authorized recycler
7 Ethyl Acetate 2,954.00 Solvent Org. Mother Liquor 3,280.00
Sell to authorized recycler
Input Qty., kg Output Qty., kg
Intermediate (Stage III) 53.00 Acetone 1,256.00
Methane Sulfonic Acid 7.71
Acetone 42.00 Org. Mother Liquor 1,273.71
Recovered Acetone 30.00
Dabigatran Etexilate Mesylate 55.00
Total 1,358.71 Total 1,358.71
Drying
Finished Product
ProcessDabigatran Etexilate Mesylate (Stage-IV)
Reaction
Reaction
Centrifugation
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
S. No Input Kg/
Batch Remarks Output Kg/Batch Remarks
8 Ethanol 260.60 Solvent Aq. Effluent 5,892.90 To ETP
9 Sodium Carbonate 165.00 Washing media Loss 9.00 Atmospheric Loss
10 Sodium Chloride Solution 110.00 Washing media
11 Water 5,500.00 Wash water
Total Input 9,914.90 Total Output 9,914.90
Stage II (Intermediate)
S. No Input Kg/
Batch Remarks Output Kg/Batch Remarks
1 Intermediate (Stage I) 140.00 Reactant Intermediate
(Stage II) 85.00 Intermediate (Stage II)
2 Aluminium Carbonate 280.00 Reactant Recovered
Ethanol 2,300.00Sell to authorized recycler
3 Hydrochloric Acid 9.30 Reagent Recovery Loss 20.00 Solvent loss
4 Isopropyl Acetate 1,827.00 Solvent Recovered
Isopropyl Acetate 16.00Sell to authorized recycler
5 Ethanol 2,320.00 Solvent Org Mother Liquor 1,862.30
Sell to authorized recycler
Solid Waste 280.00 Inorganic HW (landfill)
Loss 13.00 Atmospheric Loss
Total Input 4,576.30 Total Output 4,576.30
Stage I (Product)
S. No Input Kg/
Batch Remarks Output Kg/Batch Remarks
1 Intermediate (Stage I) 85.00 Reactant Intermediate
(Stage III) 53.00 Intermediate Stage-I
2 n-Hexyl Chloroformate 31.32 Reactant Recovered
Tetrahydrofuran 1,440.00Sell to authorized recycler
3 Potassium Carbonate 65.75 Reagent Recovery Loss 72.00 Solvent Loss
4 Methylene Chloride 3,398.00 Solvent Recovered
MDC+THF 215.00Sell to authorized recycler
5 Tetrahydrofuran 1,740.00 Solvent Recovery Loss 9.00 Solvent Loss
6 Isopropyl Alcohol 1,316.00 Solvent Rec MDC 2,980.00 Sell to
authorized
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
S. No Input Kg/
Batch Remarks Output Kg/Batch Remarks
recycler
7 Methyl Isobutyl Ketone 707.20 Solvent Recovery Loss 150.00 Solvent Loss
8 Toluene 592.00 Solvent Rec MDC+ IPA 150.00Sell to authorized recycler
9 Activated Carbon 8.50 For
Decolorization Recovery Loss 3.00 Solvent Loss
10 Water 1,615.00 Wash water Recovered Toluene 150.00
Sell to authorized recycler
Recovery Loss 3.00 Solvent Loss
Recovered Toluene + MIBK 34.00
Sell to authorized recycler
Org Mother liquor 2,445.77
Sell to authorized recycler
Aq. Effluent 1,828.50 To ETP
Spent Carbon 8.50 Inorganic HW (landfill)
Loss 17.00 Atmospheric Loss
Total Input 9,558.77 Total Output 9,558.77
Stage II (Product)
S. No Input Kg/
Batch Remarks Output Kg/Batch Remarks
1 Intermediate (Stage II) 53.00 Reactant
Dabigatran Etexilate Mesylate
55.00 Finished Product
2 Methane Sulfonic Acid 7.71 Reagent Recovered
Acetone 30.00Sell to authorized recycler
3 Acetone 1,298.00 Solvent Org. Mother Liquor 1,273.71
Sell to authorized recycler
Total Input 1,358.71 Total Output 1,358.71
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
P2. LURASIDONE HCL
Stage I (Intermediate)Reduction of Cis-5-norbornene-exo-2, 3-dicarboxylic anhydride with hydrogen using
10% Palladium on carbon as a catalyst in present of tetrahydrofuran as solvent.
Resulting reaction mass filter on hyflow bed and remove Palladium on carbon. Remove
the solvent from filtrate by distillation. Give stripping with cyclohexane. Finally crystallize
the product in cyclohexane. Isolate solid by filtration. Dry the wet material to get Stage-
I.
Stage II (Intermediate)Lurasidone Amide Intermediate Stage-I is reacted with urea at higher temp to get the
Stage-II. After completion of reaction, Charge water and methylene chloride in reaction
mass. Product is extracted by methylene chloride. Remove the solvent from organic
layer by distillation. Precipitate the product by cyclohexane addition. Isolate solid by
filtration. Dry the wet material to get Stage-II.
Stage I (Product)Reduction of (1R, 2R)-cyclohexane-1, 2-dicarboxylic acid (KSM-I) using Vitride as
reducing agent in toluene, provide aq. HCl treatment to the reaction mass and extract
product with Methylene chloride. Wash MDC layer with aq. Sodium chloride solution
and then remove solvent by distillation. Precipitate and recrystallize the stage- I (Diol)
product using n-Heptane as a solvent.
Stage II (Product)Reaction of stage-I with methane sulphonyl chloride in presence of triethylamine in
Methylene chloride solvent gives stage-II. Provide aq. Sodium bicarbonate wash to the
reaction mass and remove solvent by distillation. This product is isolated using Methyl
tertiary butyl ether (MTBE).
Stage III (Product)Stage-II is condense with 3-(1-Piperazinyl)-1, 2-benzisothiazole (KSM-II) in the
presence of sodium carbonate in Dimethylformamide solvent gives stage-III. Isolate
inorganic salt by filtration and then remove solvent by distillation. The product is
isolated using n-hexane acetone mixture and in-situ purified in acetone.
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Stage IV (Product)Condensation of Stage-III with Lurasidone amide Intermediate in the presence of
potassium carbonate in Dimethylformamide solvent gives stage-IV (Lurasidone base).
The product is isolated using methanol as a solvent and purify in Acetone.
Stage V (Product)Dissolve stage-IV in Acetone and provide activated charcoal treatment. Lurasidone
hydrochloride is prepared in acetone using IPA-HCl.
b) Reaction Chemistry
Stage I (Intermediate)
Stage II (Intermediate)
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Stage I (Product)
Stage II (Product)
Stage III (Product)
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Stage IV (Product)
Stage V (Product)
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
c) Process Flow Diagram
Input Qty., kg Output Qty., kg
Exo-cis-5-norbornene-2,3-dicaroxylic anhydride 49.00
Tetrahydrofuran 174.00 Palladium on Carbon 0.49
Hydrogen Gas 0.49
Tetrahydrofuran 101.00 Solid Waste 0.05
Cyclohexane 98.00 Recovered Tetrahydrofuran 260.00 Recovery Loss 10.00 Rec THF+ Cyclohexane 40.00 Recovery Loss 1.50
Cyclohexane 98.00
Cyclohexane 36.00 Org Mother Liquor 194.50
Recovered Cyclohexane 5.30
Intermdediate Stage-I 45.63
Total 556.98 Total 556.98
Drying
Intermediate Stage I
Filtration
Lurasidone Amide Intermediate (Stage-I)
Reaction
Filtration
Distillation
Isolation
Process
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Input Qty., kg Output Qty., kg
Intermediate (Stage I) 45.63 CO2 Gas 7.20 Urea 9.90 Ammonia Gas 2.60
Water 46.00 Methylene Chloride 182.00
Aq. Effluent 46.00
Recovered Methylene Chloride 176.00 Recovery Loss 6.52
Cyclohexane 71.00
Cyclohexane 36.00 Org. Mother Liquor 102.58
Recovered Cyclohexane 4.00
Lurasidone Amide Intermediate 45.63
Total 390.53 Total 390.53
Intermediate (Stage II)
Lurasidone Amide Intermediate (Stage-II)
Reaction
Reaction
Layer Separation
Distilation
Isolation
Filtration
Drying
Process
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Input Qty., kg Output Qty., kg
Toluene 263.60 (1R,2R)-Cyclohexane-1,2-
Dicarboxylic acid 76.00
Vitride/Synhydrid 478.80 HPLCWater 608.00
Hydrochloric Acid 655.50
Toluene 131.78 Methylene Chloride 1,208.00 Aq. Effluent 2,812.40
Sodium Chloride 304.00 Water 760.00
Recovered Methylene Chloride & Toluene 1,550.00
n-Heptane 51.80 Recovery Loss 64.00 Recovered n-Heptane 50.00 Recovery Loss 2.20
n-Heptane 103.50
n-Heptane 38.80 Org. Mother Liqour 142.00 Filtration Loss 3.00
n-Heptane 103.50
n-Heptane 38.80 Org. MotherLliqour 142.00
Recovered n-Heptane 6.00
Intermediate (Stage I) 49.00
Methanol 60.12 Aq. Effluent 241.00 Water 228.00
Caustic flakes 11.40 Org. Mother Liquor 60.00
Total 5,121.60 Total 5,121.60
Lurasidone HCl (Stage-I)Process
Slurry wash
Intermediate
Decomposition of Vitride
Reaction
Quenching & Extraction
Distillation & stripping
Crystallization
Filtration
Filtration
Dryer
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Input Qty., kg Output Qty., kg
Intermediate (Stage I) 49.00 Methylene Chloride 324.63 HPLC
Triethyl Amine 110.05 Methane Sulfonyl Chloride 109.03
Water 735.00 Aq. Effluent 923.00 Methylene Chloride 129.85 Recovered Methylene Chloride 435.00 Sodium Bicabonate 12.25 Recovery Loss 19.00
Methyl Tertiary Butyl Ether 145.04
Methyl Tertiary Butyl Ether 108.78 Org. Mother Liqour 253.00 Filtration Loss 1.63
Recovered MTBE 10.00
Intermediate Stage-II 82.00
Total 1,723.63 Total 1,723.63
Reaction
Extraction and distillation
Crystallisation
Lurasidone HCl (Stage-II)Process
Filtrartion
Dryer
Intermediate
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Input Qty., kg Output Qty., kg
Dimethyl Formamide 774.10 Intermediate (Stage II) 82.00 3-(1-Piperazinyl)-1,2-
benzisothiazole 59.86 HPLC
Sodium Carbonate Anhydrous Powder 30.34
Dimethyl Formamide 164.00 Solid Waste 65.00
Recovered Dimethyl Formamide 925.00 Acetone 64.90 Recovery Loss 13.00
Recovered DMF + Acetone 63.70 Recovery Loss 1.20
Acetone 129.70 n-Hexane 108.10
Acetone 32.40 Org. Mother Liqour 316.30 n-Hexane 27.00 Filtration Loss 2.20
Acetone 194.60
Acetone 64.90 Org. Mother Liqour 256.00
Recovered Acetone 11.50
Intermediate (Stage III) 78.00
Total 1,731.90 Total 1,731.90
Drying
Intermediate
Lurasidone HCl (Stage-III)Process
Filtration
Reaction
Filtration
Distillation
Crystallization
Filtration
Slurry wash
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Input Qty., kg Output Qty., kg
Dimethyl Formamide 515.00 Intermediate (Stage III) 78.00
Lurasidone amide intermediate 45.63 Potassium Carbonate
(anhydrous) 50.93
Dimethyl Formamide 147.30 Solid Waste 85.00
Recovered Dimethyl formamide 650.00 Methanol 61.70 Recovery Loss 13.00
Recovered DMF + Methanol 59.00 Recovery Loss 1.70
Methanol 185.10
Methanol 123.40 Org. Mother Liqour 312.00 Filtration Loss 2.36
Acetone 185.10
Acetone 61.70 Org. Mother Liqour 245.00 Filtration Loss 1.80
Recovered Acetone 3.00
Intermediate (Stage-IV) 81.00
Total 1,453.86 Total 1,453.86
Process
Crystallization
Distillation
Filtration
Reaction
Lurasidone HCl (Stage-IV)
Intermediate
Drying
Filtration
Filtration
Slurry wash
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
d) Summary of Mass Balance
Capacity of Finished Product, TPM : 0.1
Working Days Per Month : 26
Stage I (Intermediate)
S. No Input Kg/
Batch Remarks Output Kg/Batch Remarks
1Exo-cis-5-norbornene-2,3-dicaroxylic anhydride
49.00 Reactant Intermediate Stage-I 45.63 Intermediate
(Stage-I)
2 Hydrogen Gas 0.49 Reactant Recovered Tetrahydrofuran 260.00
Sell to authorized recycler
3 Palladium on Carbon 0.49 Catalyst Recovery Loss 10.00 Solvent loss
4 Tetrahydrofuran 275.00 Solvent Rec THF+ Cyclohexane 40.00
Sell to authorized recycler
5 Cyclohexane 232.00 Solvent Recovery Loss 1.50 Solvent loss
Recovered Cyclohexane 5.30
Sell to authorized recycler
Input Qty., kg Output Qty., kg
Acetone 866.20 Intermediate (Stage IV) 81.00
Activated Carbon 4.05
Acetone 243.00 Spent Carbon (wet cake) 6.00
Isopropyl Alcohol HCl 41.37
Acetone 64.04 Org. Mother Liqour 1,205.00 Loss 5.66
Recovered Acetone 3.00
Lurasidone HCl 80.00
Total 1,299.66 Total 1,299.66
Dissolution & charcolisation
Lurasidone HCl (Stage-V)Process
Finished Product
Drying
Centrifugation
Crystallisation
Filtration
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
S. No Input Kg/
Batch Remarks Output Kg/Batch Remarks
Org Mother Liquor 194.50
Sell to authorized recycler
Solid Waste 0.05 Inorganic HW (landfill)
Total Input 556.98 Total Output 556.98
Stage II (Intermediate)
S. No Input Kg/
Batch Remarks Output Kg/Batch Remarks
1 IntermdediateStage-I 45.63 Reactant
Lurasidone Amide Intermediate
45.63Intermediate to be used in Stage IV of Lurasidone HCl
2 Urea 9.90 ReactantRecovered Methylene Chloride
176.00 Sell to authorized recycler
3 Methylene Chloride 182.00 Solvent Recovery Loss 6.52 Solvent loss
5 Cyclohexane 107.00 Solvent Recovered Cyclohexane 4.00 Sell to authorized
recycler
4 Water 46.00 Wash Water
Org. Mother Liquor 102.58 Sell to authorized
recyclerAq. Effluent 46.00 To MEECO2 Gas 7.20 To Atm.Ammonia Gas 2.60 To scrubber
Total Input 390.53 Total Output 390.53
Stage I (Product)
S. No Input Kg/
Batch Remarks Output Kg/Batch Remarks
1(1R,2R)-Cyclohexane-1,2-Dicarboxylic acid
76.00 Reactant Intermediate (Stage I) 49.00 Intermediate
(Stage I)
2 Vitride/Synhydrid 478.80 Reagent
Recovered Methylene Chloride & Toluene
1,550.00Sell to authorized recycler
3 Hydrochloric Acid 655.50 Reagent Recovery Loss 64.00 Solvent Loss
4 Caustic flakes 11.40 Reagent Recovered n-Heptane 56.00
Sell to authorized recycler
5 Toluene 395.38 Solvent Recovery Loss 2.20 Solvent Loss
6 Methylene Chloride 1,208.00 Solvent Org. Mother Liquor 344.00
Sell to authorized recycler
7 Methanol 60.12 Solvent Aq. Effluent 3,053.40 To MEE
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
S. No Input Kg/
Batch Remarks Output Kg/Batch Remarks
8 n-Heptane 336.40 Solvent Filtration Loss 3.00
9 Sodium Chloride 304.00 Salt for washing
10 Water 1,596.00 Washing media
Total Input 5,121.60 Total Output 5,121.60
Stage II (Product)
S. No Input Kg/
Batch Remarks Output Kg/Batch Remarks
1 Intermediate (Stage I) 49.00 Intermediate
stage-IIntermediate Stage-II 82.00 Intermediate
stage-II
2 Triethyl Amine 110.05 ReagentRecovered Methylene Chloride
435.00Sell to authorized recycler
3Methane Sulfonyl Chloride
109.03 Reactant Recovery Loss 19.00 solvent loss
5 Sodium Bicabonate 12.25 Reagent Recovered
MTBE 10.00Sell to authorized recycler
4 Methylene Chloride 454.48 Solvent Org. Mother
Liqour 253.00Sell to authorized recycler
6 Methyl Tertiary Butyl Ether 253.82 Solvent Aq. Effluent 923.00 To MEE
7 Water 735.00 Media Filtration Loss 1.63 solvent lossTotal Input 1,723.63 Total Output 1,723.63
Stage III (Product)
S. No Input Kg/
Batch Remarks Output Kg/Batch Remarks
1 Intermediate Stage-II 82.00 Inermediate
stage-IIIntermediate (Stage III) 78.00 Inermediate
stage-III
23-(1-Piperazinyl)-1,2-benzisothiazole
59.86 ReactantRecovered Dimethyl Formamide
925.00Sell to authorized recycler
3
Sodium Carbonate Anhydrous Powder
30.34 Reagent Recovery Loss 13.00 solvent loss
4 Dimethyl Formamide 938.10 Solvent
Recovered DMF + Acetone
63.70Sell to authorized recycler
5 Acetone 486.50 Solvent Recovery Loss 1.20 solvent loss
6 n-Hexane 135.10 Solvent Recovered Acetone 11.50 Sell to
authorized
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
S. No Input Kg/
Batch Remarks Output Kg/Batch Remarks
recycler
Org. Mother Liquor 572.30
Sell to authorized recycler
Solid Waste 65.00 Inorganic HW (Landfill)
Filtration Loss 2.20 solvent lossTotal Input 1,731.90 Total Output 1,731.90
Stage IV (Product)
S. No Input Kg/
Batch Remarks Output Kg/Batch Remarks
1 Intermediate (Stage III) 78.00 Intermediate
stage-IIIIntermediate (Stage-IV) 81.00 Intermediate
stage-III
2Lurasidone Amide Intermediate
45.63 ReactantRecovered Dimethyl formamide
650.00Sell to authorized recycler
3Potassium Carbonate (anhydrous)
50.93 Reagent Recovery Loss 13.00 solvent loss
4 Dimethyl Formamide 662.30 Solvent
Recovered DMF + Methanol
59.00Sell to authorized recycler
5 Methanol 370.20 Solvent Recovery Loss 1.70 solvent loss
6 Acetone 246.80 Solvent Recovered Acetone 3.00
Sell to authorized recycler
Org. Mother Liqour 557.00
Sell to authorized recycler
Solid Waste 85.00 Inorganic HW (Landfill)
Filtration Loss 4.16 solvent lossTotal Input 1,453.86 Total Output 1,453.86
Stage V (Product)
S. No Input Kg/Kg Remarks Output Kg/Kg Remarks
1 Intermediate (Stage-IV) 81.00 Intermediate
stage-IVLurasidone HCl 80.00 Finished
product
2 Acetone 1,173.24 Solvent Recovered Acetone 3.00
Sell to authorized recycler
3 Isopropyl Alcohol HCl 41.37 Reactant Org. Mother
Liqour 1,205.00Sell to authorized recycler
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
S. No Input Kg/Kg Remarks Output Kg/Kg Remarks
4 Activated Carbon 4.05 Decolourizing
agentSpent Carbon (wet cake) 6.00 Inorganic HW
(Landfill)Loss 5.66 solvent loss
Total Input 1,299.66 Total Output 1,299.66
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
P3. LACOSAMIDE
a) Manufacturing ProcessStage ID-serine is reacted with Benzyl chloroformate Benzyl chloroformate (50% in toluene) in
presence of aqueous Potassium carbonate and acetone. Separate the toluene from
reaction mass and wash the aqueous layer by toluene. Precipitate the product by
addition of hydrochlorid acid. Isolate the solid by filtration. Dry the wet material to get
stage-I product.
Stage IILacosamdie stage-I react with isobutyl chloroformate, N-methyl morpholine and Benzyl
amine in presence of tetrahydrofuran. Neutralize the reaction mass by aqueous sodium
bicarbonate solution. Remove aqueous layer by separation. Remove the solvent from
organic layer by distillation. Precipitate the product by adding water. Isolate the solid by
filtration. Dry the wet material to get stage-II product.
Stage IIILacosamide Stage-II react with hydrogen in presence of catalyst 10% palladium on
carbon and methanol at 4 to 6Kg/Cm2 hydrogen gas pressure to convert in to
lacosamid stage-III. Hydrogen is removed by flushing of nitrogen gas. Reaction mass
is filtered on hyflow bed to remove palladium carbon. Remove solvent from filtrate and
followed by toluene stripping. finally, product crystallize in toluene. Isolate the solid by
filtration. Dry the wet material to get stage-III product.
Stage IVLacosamide stage-III is react with triethyl amine and acetic anhydride in presence of
Methylene chloride and convert into stage-IV solid material. Isolate the solid by
filtration. Dry the wet material to get stage-IV product.
Stage VLacosamide stage-IV is react with Dimethyl sulphate in presence of catalyst Tetra butyl
ammonium bromide, Acetone and aqueous caustic solution to convert in to Stage-V.
Reaction mass neutralize by Acetic acid. Remove solvent by distillation. Charge water
to residue and extract product by methylene chloride from aqueous reaction mass. Give
the charcoal treatment to organic layer. Remove solvent from reaction mass. precipitate
the solid in Methyl tertiary butyl ether. Isolate the solid by filtration. Purify the wet
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
material in Methylene chloride and Methyl tertiary butyl ether by heating and followed
by cooling for precipitation. Isolate the solid by filtration. Dry the wet material to get
stage-V product.
Stage VILacosamide stage-V is purify in ethyl acetate by heating and followed by cooling for
precipitation. Isolate the solid by filtration. Dry the wet material to get stage-VI finished
product.
b) Reaction Chemistry
Stage I
Stage II
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Stage III
Stage IV
Stage V
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Stage VI
c) Process Flow Diagram
Input Qty. kg Output Qty. kg
Purified Water 1,000.00 D-Serine 50.00
Potassium Carbonate 197.00 Acetone 79.00
Bezyal Chloroformate 212.00
Toluene 523.00 Org. Mother Liquor 630.00 2061.00
Hydrochloric Acid 295.00 Purified Water 250.00
Toluene 260.00 Aq. Effluent 1,850.00 Loss 20.00 Org. Mother liquor 241.00
Recovered Toluene 19.00
Intermediate (Stage-I) 106.00
Total 2,866.00 Total 2,866.00
Reaction
Intermediate
Centrifugation
Drying
Precipitation
Extration
Lacosamide Stage-I
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Input Qty., kg Output Qty., kg
Tetrahydrofuran 1,411.90 Intermediate (Stage I) 106.00
Isobutyl Chloroformate 63.60 N-Methyl Morpholine 46.64
Benzyl Amine 61.48
Purified Water 564.23 CO2 gas 19.50 Sodium Bicarbonate 28.71 Aq. Effluent 670.00
Purified Water 1,060.00 Recovered Tetrahydrofuran 1,303.00 Loss 25.00
Purified Water 212.00 Aq. Effluent 1,400.00 Methyl Tertiary Butyl
Ether 470.64 Org. Mother Liquor 458.70
Drying Recovered MTBE 25.00
Intermediate (Stage-II) 124.00
Total 4,025.20 Total 4,025.20
Reaction
Lacosamide Stage-II
Washing
Distillation & Precipitation
Centrifugation
Intermediate
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Input Qty., kg Output Qty., kg
Methanol 1,468.00 Intermediate (Stage II) 124.00
10 % Palladium on Carbon 2.48
Hydrogen Gas 0.50 CO2 gas 15.50
Hyflow 4.00 Solid Waste 9.00 Methanol 82.00
Clear filtrate
Recovered Methanol 1,434.00 Toluene 269.04 Loss 50.00
Recovered Toluene + mix solvent 60.00
Toluene 107.24 Org. Mother Liquor 406.00
Recovered Toluene 17.76
Intermediate (Stage-III) 65.00
Total 2,057.26 Total 2,057.26
Lacosamide Stage-III
Reaction
Filtration
Intermediate
Distillation and Precipitatio
Centrifugation
Drying
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Input Qty., kg Output Qty., kg
Methylene Chloride 858.00 Intermediate Stage III 65.00
Triethyl Amine 33.87 Acetic Anhydride 35.88
Methylene Chloride 171.60 Org. Mother Liquor 1,059.00
Recovered Methylene Chloride 47.35
Intermediate (Stage-IV) 58.00
Total 1,164.35 Total 1,164.35
Reaction
Centrifugation
Drying
Lacosamide Stage-IV
Intermediate
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Input Qty., kg Output Qty., kg
Acetone 1,147.00 Intermediate Stage IV 58.00
Tetrabutyl Ammonium Bromide 5.80
Dimethyl Sulfate 62.06 Caustic flakes 17.40 Purified Water 290.00 Recovered Acetone 1,080.00
Acetic Acid 36.54 Recovery Loss 40.60 Methylene Chloride 1,566.00 Aq. Effluent 340.00
Activated Carbon 5.80
Methylene Chloride 158.00 Spent Carbon 8.00
Methyl tert-butylether 504.55
Methylene Chloride 855.00 Recovered Methylene Chloride 1,640.00 Recovery Loss 58.00
Methyl tert-butylether 53.45 Org. Mother Liquor 1,493.00
Recovered Methyl tert-butylether 65.00
Intermediate (Stage-V) 35.00
Total 4,759.60 Total 4,759.60
Lacosamide Stage-V
Reaction, Distillation & Extraction
Filtration
Distillation and Precipitatio
Centrifugation
Drying
Intermediate
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
d) Summary of Mass Balance
Capacity of Finished Product, TPM : 0.5
Working Days Per Month : 26
Stage IS. No Input Kg/
batch Remarks Output Kg/batch Remarks
1 D-Serine 50.00 Reactant Intermediate (Stage-I) 106.00 Intermediate Stage-I
2 Benzyl Chloroformate 212.00 Reagent Org. Mother Liquor 871.00Sell to authorized recycler
3 Potassium Carbonate 197.00 Reagent Recovered Toluene 19.00Sell to authorized recycler
4 Hydrochloric Acid 295.00 Reagent Loss 20.00 Solvent loss
5 Acetone 79.00 Solvent Aq. Effluent 1,850.00 To MEE
6 Toluene 783.00 Solvent
7 Purified Water 1,250.00 Media
Total Input 2,866.00 Total Output 2,866.00
Input Qty., kg Output Qty., kg
Ethyl Acetate 192.50 Lacosamide Stage-V 35.00
Ethyl Acetate 28.00 Org. Mother Liquor 198.50
Recovered Ethyl Acetate 24.00
Lacosamide 33.00
Total 255.50 Total 255.50
Finished Product
Drying
Centrifugation
Purification
Lacosamide Stage-VI
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Stage IIS. No Input Kg/
batch Remarks Output Kg/batch Remarks
1 Intermediate (Stage-I) 106.00 Reactant Intermediate
(Stage-II) 124.00 Intermediate Stage-II
2 Isobutyl Chloroformate 63.60 Reactant Recovered
Tetrahydrofuran 1,303.00Sell to authorized recycler
3 N-Methyl Morpholine 46.64 Reagent Loss 25.00 Solvent loss
4 Benzyl Amine 61.48 Reagent Recovered MTBE 25.00Sell to authorized recycler
5 Sodium Bicarbonate 28.71 Reagent Org. Mother
Liquor 458.70Sell to authorized recycler
6 Methyl Tertiary Butyl Ether 470.64 Solvent Aq. Effluent 2,070.00 To ETP
7 Tetrahydrofuran 1,411.90 Solvent CO2 gas 19.50 Atmospheric Loss
8 Purified Water 1,836.23 MediaTotal Input 4,025.20 Total Output 4,025.20
Stage IIIS. No Input Kg/batch Remarks Output Kg/batch Remarks
1 Intermediate (Stage-II) 124.00 Reactant Intermediate
(Stage-III) 65.00 Intermediate Stage-II
2 Hydrogen Gas 0.50 Reagent Recovered Methanol 1,434.00
Sell to authorized recycler
3 Methanol 1,550.00 Solvent Loss 50.00 Solvent loss
4 Toluene 376.28 Solvent Recovered Toluene 17.76
Sell to authorized recycler
5 Hyflow 4.00 Filter media
Recovered Toluene + mix solvent
60.00Sell to authorized recycler
610 % Palladium on Carbon
2.48 Catalyst Org. Mother Liquor 406.00
Sell to authorized recycler
Solid Waste 9.00 Inorganic HW (landfill)
CO2 gas 15.50 Atmospheric Loss
Total Input 2,057.26 Total Output 2,057.26
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Stage IVS. No Input Kg/
batch Remarks Output Kg/batch Remarks
1 Intermediate (Stage-III) 65.00 Reactant Intermediate (Stage-IV) 58.00 Intermediate
Stage-IV
2 Triethyl Amine 33.87 ReagentRecovered Methylene Chloride
47.35Sell to authorized recycler
3 Acetic Anhydride 35.88 Reagent Org. Mother Liquor 1,059.00
Sell to authorized recycler
4 Methylene Chloride 1,029.60 SolventTotal Input 1,164.35 Total Output 1,164.35
Stage VS. No Input Kg/batch Remarks Output Kg/batch Remarks
1 Intermediate (Stage-IV) 58.00 Reactant Intermediate
(Stage-V) 35.00 Intermediate Stage-V
2 Caustic flakes 17.40 Reagent Recovered Acetone 1,080.00
Sell to authorized recycler
3 Dimethyl Sulfate 62.06 Reactant Recovery Loss 40.60 Solvent loss
4 Acetone 1,147.00 SolventRecovered Methylene Chloride
1,640.00Sell to authorized recycler
5Tetrabutyl Ammonium Bromide
5.80 Catalyst Recovery Loss 58.00 Solvent loss
6 Purified Water 290.00 MediaRecovered Methyl tert-butylether
65.00Sell to authorized recycler
7 Methylene Chloride 2,579.00 Solvent Org. Mother
Liquor 1,493.00Sell to authorized recycler
8 Methyl tert-butylether 558.00 Solvent Aq. Effluent 340.00 To ETP
9 Activated Carbon 5.80 For
Decolorization Spent Carbon 8.00 Inorganic HW (landfill)
10 Acetic Acid 36.54 ReagentTotal Input 4,759.60 Total Output 4,759.60
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Stage VIS. No Input Kg/
batch Remarks Output Kg/batch Remarks
1 Intermediate (Stage-V) 35.00 Product Lacosamide 33.00 Finished
product
2 Ethyl Acetate 220.50 Solvent Recovered Ethyl Acetate 24.00
Sell to authorized recycler
Org. Mother Liquor 198.50Sell to authorized recycler
Total Input 255.50 Total Output 255.50
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
P4. BENDAMUSTINE HCL
a) Manufacturing Process
Stage ICondensation of KSM-I (N-1-Methyl-4-nitrobenzene-1,2-diamine) with Glutaric
anhydride using sulphuric acid and IPA gave Stage-I.
Stage IISynthesis of Bendamustine Stage-II by catalytic hydrogenation of Stage-I using
Palladium on carbon in methanol as a solvent under H2 gas pressure.
Stage IIIBendamustine Stage-II react with 2-chloroethanol using DIPEA as a base in water and
product isolated by extraction with dichloromethane followed by distillation and isolation
using ethylacetate IPA mixture to get Stage-III.
Stage IVChlorination of stage-III with thionyl chloride using dichloromethane as a solvent.
Product isolated after work-up, solvent distillation and IPA addition to get pure stage-IV.
Stage VHydrolysis of stage-IV using Hydrochloric acid in water to get stage-V as monohydrate
Hydrochloride salt of Bendamustine Hydrochloride.
Stage VIPurifcation of Stage-V using acetonitre, acetone and and aquous HCl mixture to give
Bendamustine hydrochride
b) Reaction Chemistry
Stage I
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Stage II
Stage III
Stage IV
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Stage V
Stage VI
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
c) Process Flow Diagram
Input Qty., kg Process Output Qty., kg
N1-Methyl-4-nitrobenzene-1,2-diamine 7.370
Dihydro-2H-pyran-2,6(3H)-dione 6.279
Isopropyl Alcohol 110.550 CO2 emission 1.916
Sulphuric Acid 4.348
Water 412.720Potassium Carbonate 6.117
Aq. Mother liquor 515.849Filtration loss 19.167
n-Heptane 77.311Acetone 11.055 Aq. Mother liquor 83.064
Drying Loss 6.173
Stage-I Intermediate stage-I 9.581
Total 635.750 Total 635.750
Bendamustinen hydrochloride (Stage-I )
Reactor6-7 h at 80 0C
Reactor6-7 h at 45 0C
2 h Temp. 20 0C
Filtration 20 0C
Purify at 45 deg.for 2 hrs
Dryer45 0C for 8-10 hrs
Input Qty., kg Process Output Qty., kg
Intermediate (Stage II) 9.581Methanol 201.201 Solid waste 0.958
10% Palladium on Carbon 0.958
Org. Mother liquor 194.015Methanol 28.743 Filtration loss 18.204
Methanol 9.581 Aq. Effluent 95.810Water 95.810 Filtration loss 18.204
Drying Loss 11.976
Stage-II Intermediate stage-II 6.707
Total 345.874 Total 345.874
Dryer45 0C for 8-10 hrs
Filtration 35 deg C
Autoclave 10LStir for 3-4 h at
45 0C
Purify at 0-5 deg.for 2 hrs
Bendamustinen hydrochloride (Stage-II)
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Input Qty., kg Process Output Qty., kg
Intermediate stage-II 6.7072-chloroethanol 5.298
N,N-Di Isopropyl Ethyl Amine 9.389Water 53.654
Cool the reaction mass to RT
Methylene Dichloride 134.134
Methylene Dichloride 43.594
Methylene Dichloride 43.594Aq. Effluent 53.654
Recovered Methylene Dichloride 199.189
Solvent Loss 22.132
Ethyl Acetate 23.473 Strip out with EtOAC Org. Mother Liquor 23.473
Ethyl Acetate 33.534Isopropyl Alochol 3.353
Ethyl Acetate 3.353 Org. Mother Liquor 51.239Filtration Loss 3.186
Drying loss 3.186
Stage-III Intermediate Stage-III 4.024
Total 360.083 360.083
Bendamustinen hydrochloride (Stage-III )
Degassed it well for 1h at 40-45 deg
Stit at 0-5 deg for 3 h
Dryer45 0C for 8-10 hrs
ReactorStir for 4-5 h Temp. 80 °C
Stir the reaction mass for 40 mts. At rt
Separated off the Organic layer A
Stir Aqueous layer again with MDC and
separeted off the Organic layer B
Stir and separeted off the Organic layer C
Filtration
Distill off the filtrate u/V at 40 deg.
Temp. 25-30 0C
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Input Qty., kg Process Output Qty., kg
Intermediate Stage-III 4.024Methylene Dichloride 60.360
Thionyl Chloride 3.944 SO2 Gas 1.408
Cool the reaction mass to 15-20 deg.
Methylene Dichloride 60.360Water 40.260
Separate the Organic layer Aq. Effluent 43.762
Water 40.261Sodium Bicarbonate 2.011 Aq. Effluent 41.850
Activated Carbon 0.402
Solid waste 0.402
Recovered MDC 108.649Solvent Loss 12.072
Isopropyl Alcohol 4.024 Strip out with IPA
Isopropyl Alcohol 4.024
filtered off the solid
Isopropyl Alcohol 1.046 Org. Mother Liquor 8.422Filtration Loss 0.909
Drying loss 0.820
Stage-IV Intermediate Stage IV 2.422
Total 220.716 220.716
Bendamustinen hydrochloride (Stage-IV)
washed with IPA
Stir the reaction mass at 23-25 deg.
Distill off the filtrate u/V at 40 deg.
Temp. 35-40 0C
Degassed it well for 1h at 40-45 deg
Stit at 0-5 deg for 3 h
Dried u/V 45 0C for 8-10 hrs
Settle the layers
Stir for 30 mts. At 25 deg. Organic layer
ReactorStir for 4-5 h
Temp. 40-42 °C
Stir the reaction mass for 40 mts. At
Filter
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Input Qty., kg Process Output Qty., kg
Intermediate Stage IV 2.422Water 9.690
Hydrochloric Acid 9.690
Activated Carbon 0.242
Filter Solid waste 0.242
Water 2.422 wash the bed with hot water
Distillate 17.442
Water 7.267
Aq. Effluent 5.814Filtration Loss 5.110
Drying loss 1.453
Stage-V Intermediate Stage V 1.672
Total 31.733 Total 31.733
Bendamustinen hydrochloride (Stage-V)
Dryer45 0C for 8-10 hrs
Filtration
Stir the reaction mass for 40 mts. at
Stirred the reaction mass at 10-15 deg.
ReactorStir for 3-4 h Temp. 45 °C
Distilled off the filtrate u/v at 55 deg.
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
d) Summary of Mass Balance
Capacity of Finished Product, TPM : 0.01
Working Days Per Month : 26
Input Qty., kg Process Output Qty., kg
Intermediate (Stage V) 1.672Acetone 11.700
Acetonitrile 11.700Water 2.507
Hydrochloric Acid 0.251
Activated Carbon 0.167Stir the reaction
mass for 40 mts. at 40-45 deg.
Filtered it through Hyflow Solid waste 0.167
Acetonitrile 5.014 Recovered Solvent 14.035Solvent Loss 2.005
Acetonitrile 5.014 Recovered Solvent 14.035Solvent Loss 2.005
Acetonitrile 1.655Acetone 5.014
Org. Mother Liquor 8.020Filration Loss 2.205
Drying Loss 1.221
Total 44.696 Total 44.696
1.003
Bendamustinen hydrochloride (Stage-VI )
Finished Product Bendamustine HCl
strip out the residue with acetonitrile at 40-
Dryer45 0C for 8-10 hrs
ReactorStir for 15-20 mts.at
Temp. 45 °C
RM stirred for 2 hr at 2-5 deg.
Distilled off the solvent at 40-45 deg.
Filteration
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Stage IS. No Input Kg/
Batch Remarks Output Kg/Batch Remarks
1N1-Methyl-4-nitrobenzene-1,2-diamine
7.37 Reactant Intermediate stage-I 9.58 Intermediate
stage-I
2 Dihydro-2H-pyran-2,6(3H)-dione 6.28 Reactant CO2 emission 1.92 To atmosphere
throught vent
3 Sulphuric Acid 4.35 Reactant Aq. Mother liquor 598.91 To MEE
4 Isopropyl Alcohol 110.55 Solvent Filtration loss 19.17 Atmospheric Loss
6 Acetone 11.06 Solvent Drying Loss 6.17 Atmospheric Loss
7 n-Heptane 77.31 Solvent
8 Potassium Carbonate 6.12 Neutralization
9 Water 412.72Total Input 635.75 Total Output 635.75
Stage IIS. No Input Kg/
Batch Remarks Output Kg/Batch Remarks
1 Intermediate stage-I 9.58 Intermediate
stage-IIntermediate stage-II 6.71 Intermediate
stage-II
2 10% Palladium on Carbon 0.96 Catalyst Solid waste 0.96 For catalyst
regeneration
3 Methanol 239.53 Solvent Org. Mother liquor 194.02
Sell to authorized recycler
4 Water 95.81 Aq. Effluent 95.81 To MEEFiltration loss 36.41Drying Loss 11.98
Total Input 345.87 Total Output 345.87
Stage IIIS. No Input Kg/
Batch Remarks Output Kg/Batch Remarks
1 Intermediate stage-II 6.71 Intermediate
stage-IIIntermediate Stage-III 4.02 Intermediate
stage-III
2 2-chloroethanol 5.30 ReactantRecovered Methylene Dichloride
199.19Sell to authorized recycler
3 N,N-Di Isopropyl Ethyl Amine 9.39 Reactant Org. Mother
Liquor 74.71Sell to authorized recycler
5 Methylene Dichloride 221.32 Solvent Aq. Effluent 56.84 To MEE
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
S. No Input Kg/
Batch Remarks Output Kg/Batch Remarks
6 Isopropyl Alochol 3.35 Solvent Solvent Loss 22.13 Solvent loss
7 Ethyl Acetate 60.36 Solvent Drying loss 3.19 Atmospheric Loss
4 Water 53.65Total Input 360.08 Total Output 360.08
Stage IVS. No Input Kg/
Batch Remarks Output Kg/Batch Remarks
1 Intermediate Stage-III 4.02 Intermediate
stage-IIIIntermediate Stage IV 2.42 Intermediate
stage-IV
2 Thionyl Chloride 3.94 Reactant SO2 Gas 1.41
3 Methylene Dichloride 120.72 Solvent Solid waste 0.40 Inorganic HW
(landfill)
4 Isopropyl Alcohol 9.09 Solvent Recovered
MDC 108.65Sell to authorized recycler
5 Activated Carbon 0.40 Solvent Org. Mother
Liquor 8.42Sell to authorized recycler
6 Sodium Bicarbonate 2.01 Filtration Aid Aq. Effluent 85.61 To MEE
7 Water 80.52 Base Solvent Loss 12.07 Solvent loss
Filtration Loss 0.91 Atmospheric Loss
Drying loss 0.82 Atmospheric Loss
Total Input 220.72 Total Output 220.72
Stage VS. No Input Kg/
Batch Remarks Output Kg/Batch Remarks
1 Intermediate Stage IV 2.42 Intermediate
stage-IVIntermediate Stage V 1.67 Intermediate
stage-V
2 Hydrochloric Acid 9.69 Reactant Solid waste 0.24 Inorganic HW
(landfill)
3 Activated Carbon 0.24 Filtration Aid Aq. Effluent 10.92 To MEE
4 Water 19.38 Distillate 17.44
Drying loss 1.45 AtmosphericLoss
Total Input 31.73 Total Output 31.73
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Stage VIS. No Input Kg/Batch Remarks Output Kg/Batch Remarks
1 Intermediate Stage V 1.67 Intermediate
stage-VBendamustine HCl 1.00 Finished
product
2 Acetone 16.71 Solvent Solid waste 0.17 Inorganic HW (landfill)
3 Acetonitrile 23.38 Solvent Recovered Solvent 28.07
Sell to authorized recycler
4 Hydrochloric Acid 0.25 Acid Org. Mother
Liquor 8.02Sell to authorized recycler
5 Activated Carbon 0.17 Filtration Aid Filration Loss 2.21 To MEE
6 Water 2.51 Solvent Loss 4.01 Solvent loss
Drying Loss 1.22 Atmospheric Loss
Total Input 44.70 Total Output 44.70
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
P5. TRAZODONE HCL
a) Manufacturing ProcessStage I[1,2,4]Triazolo[4,3-a]pyridin-3(2H)-one (KSM-01) is reacted with aq. Caustic solution in
presence of IPA and convert in to Stage-I. Product precipitate by stirring the reaction
mass at lower temperature. Isolate the solid by filtration. Dry the wet material to get
stage-I product.
Stage II1-(3-Chlorophenyl)piperazine (KSM-02) is condensed with 3-Chloro-1-propanol in
presence of sodium iodide and triethyl amine in Toluene to give Stage-II. Give water
wash to the reaction mass and acidify organic layer with aq. HCl solution. Charolaise
the mass & filter thru hyflow bed. Crystallize solid stage-II by adjusting alkaline pH with
aq. caustic solution. Isolate the solid by filtration. Dry the wet material to get stage-I
product.
Stage IIITrazodone hydrochloride stage-II is reacted with methane sulfonyl chloride in presence
of Triethyl amine in presence of DMF to give mesyl TRZ-A. Filter the reaction mass and
isolate inorganic salt. Charge Stage-I in filtrate and stir the reaction mass to convert in
to stage-III. Remove solvent by distillation. Dissolve product in Methanol and precipice
the product by adding water. Isolate the solid by filtration. Dry the wet material to get
stage-III product.
Stage IVTrazodone hydrochloride stage-III is dissolve in methanol and provide charcoal
treatment. Filter the reaction mass to remove charcoal. Slowly add hydrochloride to
filtrate to convert in to trazodone hydrochloride salt. Isolate the solid by filtration. Dry the
wet material to get stage-IV product.
Stage VTrazodone hydrochloride stage-IV is purified with methanol to give Trazodone
hydrochloride. Precipitate the product by stirring the reaction mass at lower
temperature. Isolate the solid by filtration. Wet material dissolve in methanol. Filter the
clear reaction mass. Precipitate the material by cooling and stirring of reaction mass.
Isolate the solid by filtration. Dry the wet material to get stage-IV product.
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
b) Reaction Chemistry
Stage I
Stage II
Stage III
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Stage IV
Stage V
b) Process Flow Diagram
Input Qty., kg Process Out put Qty., kg
Purified Water 114.00 Caustic Flakes 12.40
Isopropyl Alcohol 506.30 [1,2,4]Triazolo[4,3-a]pyridin-
3(2H)-one 38.00
Isopropyl Alcohol 60.50 Org. Mother Liquor 681.20
Recovered Isopropyl Alcohol 8.00
Intermediate Stage I 42.00
Total 731.20 Total 731.20
Trazodone HCl Stage-I
Centrifugation
Drying
Stage-I
Reaction
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Input Qty., kg Process Out put Qty., kg
Toluene 119.60
1-(3-Chlorophenyl)-piperazine 46.00 3-Chloro -1-propanol 26.50
Triethyl Amine 30.80 Sodium Iodide 3.50
Purified Water 138.00 Aq. Effluent 175.00 364.40
Hydrochloric Acid 37.00 Purified Water 135.00 Recovered Toluene 119.60
Activated Carbon 2.30 Purified Water 23.00
Hyflow 5.00 Spent Carbon 2.30 Purified Water 122.00 Filtration Spent Hyflow 5.00
Caustic Flakes 13.10 Purified Water 108.00
Purified Water 230.00 Centrifugation Aq. Effluent 670.90
Drying Aq. Effluent 15.00
Intermediate Stage II 52.00 Total 1,039.80 Total 1,039.80
Reaction
pH adjustment and layer seperation
Charcoal treatment
pH adjustment
Trazodone HCl Stage-II
Stage-II
Reaction
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Input Qty., kg Process Out put Qty., kg
Intermediate Stage II 52.00 Dimethyl Formamide 147.30
Methane Sulfonyl Chloride 28.10 Triethyl Amine 26.80
Dimethyl Formamide 58.50 Solid Waste 25.00
Dimethyl Formamide 39.60 Intermediate (Stage I) 42.00
Recovered Dimethyl Formamid 245.00 Recovery Loss 0.40
Methanol 205.40 Purified Water 780.00
Purified Water 260.00 Centrifugation Aq. Effluent 1,281.30
Drying Aq. Effluent 20.00
Intermediate (Stage III) 68.00 Total 1,639.70 Total 1,639.70
Distillation
Stage-III
Precipitation
Reaction
Reaction
Filtration
Trazodone HCl Stage-III
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Input Qty., kg Process Out put Qty., kg
Intermediate (Stage III) 68.00 Methanol 212.50
Activated Carbon 3.40
Methanol 105.90 Spent Carbon 3.40
Hydrochloric Acid 26.30 Precipitation
Methanol 53.60 Centrifugation Org. Mother Liquor 396.60
Drying Recovered Methanol 7.20
Intermediate (Stage IV) 62.50 Total 469.70 Total 469.70
Reaction
Trazodone HCl Stage-IV
Filtration
Stage-IV
Input Qty., kg Process Out put Qty., kg
Intermediate (Stage IV) 62.50 PurificationMethanol 816.00
Distillation Recovered Methanol 670.00 Recovery Loss 7.00
Methanol 49.80 Centrifugation Org. Mother Liquor 188.30
Drying Recovered Methanol 6.00
Trazadone HCl 57.00 Total 928.30 Total 928.30
Finished Product
Trazodone HCl Stage-V
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
d) Summary of Mass Balance
Capacity of Finished Product, TPM : 4
Working Days Per Month : 26
Stage IS. No Input Kg/
batch Remarks Output Kg/batch Remarks
1 [1,2,4]Triazolo[4,3-a]pyridin-3(2H)-one 38.00 Reactant Intermediate
Stage I 42.00 Intermediate Stage-I
2 Caustic Flakes 12.40 ReagentRecovered Isopropyl Alcohol
8.00Sell to authorized recycler
3 Isopropyl Alcohol 566.80 Solvent Org. Mother Liquor 681.20
Sell to authorized recycler
4 Purified Water 114.00 Wash water
Total Input 731.20 Total Output 731.20
Stage II
S. No. Input Kg/
batch Remarks Output Kg/batch Remarks
11-(3-Chlorophenyl)-piperazine
46.00 Reactant Intermediate Stage II 52.00 Intermediate
stage-II
2 3-Chloro -1-propanol 26.50 Reactant Recovered
Toluene 119.60Sell to authorized recycler
3 Triethyl Amine 30.80 Reagent Aq. Effluent 860.90 To MEE
4 Sodium Iodide 3.50 Reagent Spent Carbon 2.30 Inorganic HW
(Landfill)
5 Hydrochloric Acid 37.00 Reagent Spent Hyflow 5.00 Inorganic HW
(Landfill)6 Caustic Flakes 13.10 Reagent
7 Toluene 119.60 Solvent
8 Activated Carbon 2.30 For
decolourization9 Hyflow 5.00 Filter aid10 Purified Water 756.00 Washing media
Total Input 1,039.80 Total Output 1,039.80
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Stage IIIS. No Input Kg/
batch Remarks Output Kg/batch Remarks
1 Intermediate (Stage I) 42.00 Intermediate Intermediate
(Stage III) 68.00 Intermediate product
2 Intermediate Stage II 52.00 Intermediate
Recovered Dimethyl Formamide
245.00Sell to authorized recycler
3Methane Sulfonyl Chloride
28.10 Reactant Recovery Loss 0.40 Solvent loss
4 Triethyl Amine 26.80 Reagent Aq. Effluent 20.00 To MEE
5 Dimethyl Formamide 245.40 Solvent Solid Waste 25.00 Inorganic HW
(Landfill)6 Methanol 205.40 Solvent Aq. Effluent 1,281.30 To MEE7 Purified Water 1,040.00 Wash media
Total Input 1,639.70 Total Output 1,639.70
Stage IVS.No Input Kg/
batch Remarks Output Kg/batch Remarks
1 Intermediate (Stage III) 68.00 Intermediate Intermediate
(Stage IV) 62.50 Intermediate Stage IV
2 Hydrochloric Acid 26.30 Reagent Recovered
Methanol 7.20Sell to authorized recycler
3 Methanol 372.00 Solvent Org. Mother Liquor 396.60
Sell to authorized recycler
4 Activated Carbon 3.40 For
Decolourization Spent Carbon 3.40 Inorganic HW (Landfill)
Total Input 469.70 Total Output 469.70
Stage VS. No Input Kg/
batch Remarks Output Kg/batch Remarks
1 Intermediate (Stage IV) 62.50 Intermediate Trazadone HCl 57.00 Finished Product
2 Methanol 865.80 Solvent Recovered Methanol 676.00 Sell to authorized
recyclerRecovery Loss 7.00 solvent lossOrg. Mother Liquor 188.30 Sell to authorized
recyclerTotal Input 928.30 Total Output 928.30
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
P6. GEMCITABINE HCL
a) Manufacturing ProcessStage IDi benzoyl lactum is react with Vitride in presence of Toluene, Methanol, and diluted
HCl solution. Organic layer is separated and solvent is removed under vacuum. It
further reacts with Methane sulphonyl chloride, Triethyl amine using Toluene. Solvent is
distill out under vacuum and the residue is Gemcitabine Hydrochloride Stage-I (In situ).
Stage IIN4 Acetyl cytosine, Hexamethyl disilazane ,Tri methyl silyl chloride, Tri methyl silyl
triflate are react with stage-I using Ethyl acetate as a media. Organic layer is separated,
and solvent is distilled out under vacuum. It further reacts with methanol, ammonia
solution by using purified water. Water is distilled out from Product layer under
vacuum. Product is crystallized by IPA, methanol and HCl. The product is filtered and
dried to get stage-II.
Stage IIIGemcitabine hydrochloride Stage-II is dissolved in purified water and re-precipitation of
pure Gemcitabine hydrochloride material is done by using Acetone. Slurry is cooled,
filtered and dried to get stage-III (pure gemcitabine hydrochloride)
Stage IVMother liquor (Methanol-ML) of stage-II (Process-II) having around higher percentage
of alpha anomer and it is neutralized with potassium hydroxide and reflux in highly
basic condition (Potassium hydroxide) in methanol solvent for 72 hours to obtain alpha
and beta anomers are in equal proportion.
Stage VCrude Gemcitabine hydrochloride is purifying in water & acetone.
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
b) Reaction Chemistry
Stage I
Stage II
Stage III
Stage IV
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Stage V
c) Process Flow Diagram
Input Qty., kg Process Output Qty., kg
Toluene 448.05 Dibenzoyl Lactum 75.00
Vitride 47.25 Methanol 8.93
579.23
Hydrochloric Acid 65.25 Toluene 65.25 Sodium
Bicarbonate 1.00 Effluent to ETP 725.00
Purified Water 551.00
536.73
Toluene 17.40 Recovered Toluene 520.00 Recovery Loss 10.00
24.13
Toluene 121.80 Methane Sulfonyl
Chloride 34.13 Effluent to ETP 413.00
Triethyl Amine 40.13 Purified Water 338.00
145.19
Ethyl Acetate 152.10 Toluene Recovery 120.00 Recovery Loss 2.69
Intermediate (Stage I) 174.60
Total 1,965.29 Total 1,965.29
Gemcitabine HCl (Stage-I) [Process I]
STAGE-I
Reaction and work up
Reaction
Distillation
work up
Distillation
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Input Qty., kg Process Output Qty., kg
Ethyl Acetate 810.00 N4 Acetyl Cytosine 45.75 Recovered Ethyl Acetate 348.00
Hexamethyl Disilazane 64.13 Recovery Loss 7.00
Trimethyl Silyl Chloride 1.88
Trimethyl Silyl Triflate 70.88
Stage-I 174.60 812.24
Purified Water 751.00 Effluent to ETP 1,126.10 Sodium
Bicarbonate 11.25
Ethyl Acetate 162.00
610.39
Methanol 468.47 Recovered Ethyl Acetate 640.00 Liquor Ammonia 165.00 Recovered Methanol 430.00
Isopropyl Alcohol 118.50 Recovered Isopropyl Alcohol 116.00
Recovery Loss 72.84
103.52
Methanol 23.70 ReactionHydrochloric Acid 34.78
162
Acetone 35.55 Organic Mother Liquor 177.75 Filtration Filtration Loss 11.80
8
Purified Water 48.00 Hydrochloric Acid 2.85 Purification
58.85
Acetone 28.44 Aq. Mother Liquor 45.00 Organic Mother Liquor 29.00 Filtration Loss 2.24
11.05Drying Recovered Acetone 1.30
Stage-II Intermediate (Stage II) 9.75
Total 3,016.78 Total 3,016.78
Filtration
Workup
Reaction & washing
Gemcitabine HCl (Stage-II) [Process I]
Reaction
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Input Qty., kg Process Output Qty., kg
Purified Water 69.00 Stage-II 9.75
Activated Carbon 0.98 Solid Waste 3.50 Hyflow 2.00
78.23
Acetone 639.90
718.13
Organic Mother liquor 695.00 Filtration loss 11.00 Recovered Acetone 3.73
Final product Gemcitabine HCl 8.40
Total 721.63 Total 721.63
Crystallisation
Filtration & Drying
Gemcitabine HCl (Stage-III) [Process I]
Charcolisation
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Input Qty., kg Process Output Qty., kg
Mother Liquor 177.75 Recovered Methanol + IPA 210.00
Potassium Hydroxide 31.88 Recovery loss 4.00
Methanol 177.75 173.38
Methanol 30.02 Inorganic Salt 36.70
166.7
Methanol (Flush) 142.20 Recovered Methanol 147.00
Isopropyl Alcohol 237.00 Recovered Isopropyl alcohol 232.00
Recovery loss 41.22 125.68
Methanol 283.61 Pottasium Hydroxide 37.50
Hydrochloric Acid (Cp Grade) 69.55
516.34
Methanol (Washing) 44.24 Inorganic salt 44.00
Methanol 15.80 532.38
Isopropyl Alcohol 237.00 Recovered Methanol 450.80 Recovered Isopropyl Alcohol 232.00
Recovery loss 5.00 81.58
Methanol 142.20 Hydrochloric Acid
(Cp Grade) 32.02
255.8
Acetone 30.02 Filtration Organic Mother Liquor 263.42 22.4
Purified Water 103.00 Hydrochloric Acid
(Cp Grade) 31.43
156.83
Acetone 60.04 Aq. Mother Liquor 140.49 Organic Mother Liquor 59.00 Filtration loss 8.50 Recovered Acetone 5.50
Stage-I Intermediate Stage IV 3.38
Total input 1,883.01 Total output 1,883.01
Purification
Filtration & Drying
Reaction
Filtration
Distillation
Reaction
Gemcitabine HCl (Stage-I) [Process II]
Reaction
Filtration
Distillation
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
d) Summary of Mass Balance
Capacity of Finished Product, TPM : 0.2
Working Days Per Month : 26
Stage IS.No Input Kg/
batch Remarks Output Kg/batch Remarks
1 Dibenzoyl Lactum 75.00 Reactant Intermediate
(Stage I) 174.60 Intermediate stage-I
2Methane Sulfonyl Chloride
34.13 Reactant Recovered Toluene 640.00
Sell to authorized recycler
3 Vitride 47.25 Reactant Recovery Loss 12.69 Solvent Loss
4 Methanol 8.93 Reagent Effluent 1,138.00 To MEE
5 Hydrochloric Acid 65.25 reagent
6 Triethyl Amine 40.13 Reactant
7 Sodium Bicarbonate 1.00 For
Neutralization8 Toluene 652.50 solvent9 Ethyl Acetate 152.10 Solvent
10 Purified Water 889.00 Water washTotal input 1,965.29 Total output 1,965.29
Input Qty., kg Process Output Qty., kg
Water 30.00 Stage-II 3.38
Activated Carbon 0.34 Solid Waste 2.34 Hyflow 2.00
78.23
Acetone 237.79
718.13
Organic Mother Liquor 265.00 Filtration loss 3.64 Drying loss -
Final product(Anomerized) Gemcitabine HCl 2.53
Total 273.51 Total 273.51
Filtration & Drying
Charcolisation
Gemcitabine HCl (Stage-II) [Process II]
Crystallisation
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Stage IIS.No Input Kg/
batch Remarks Output Kg/batch Remarks
1 Intermediate Stage I 174.60 Intermediate
stage-IIntermediate Stage II 9.75 Intermediate
stage-II
2 N4 Acetyl Cytosine 45.75 Reactant Organic Mother
Liquor 177.75 To be used in Stage IV
3 Hexamethyl Disilazane 64.13 Reactant Recovered
Ethyl Acetate 988.00Sell to authorized recycler
4 Trimethyl Silyl Chloride 1.88 Reactant Recovered
Methanol 430.00Sell to authorized recycler
5 Trimethyl Silyl Triflate 70.88 Reactant
Recovered Isopropyl Alcohol
116.00Sell to authorized recycler
7 Liquor Ammonia 165.00 Reactant Recovered
Acetone 1.30Sell to authorized recycler
8 Hydrochloric Acid 37.63 Reagent Recovery Loss 79.84 Solvent loss
6 Sodium Bicarbonate 11.25 For
neutralization Filtration Loss 14.04 Solvent loss
9 Ethyl Acetate 972.00 Solvent Effluent 1,126.10 To MEE
10 Isopropyl Alcohol 118.50 Solvent Aq. Mother
Liquor 45.00 To MEE
11 Methanol 492.17 Solvent Organic Mother Liquor 29.00
Sell to authorized recycler
12 Acetone 63.99 Solvent13 Purified Water 799.00 Water wash
Total input 3,016.78 Total output 3,016.78
Stage IIIS.
No. Input Kg/batch Remarks Output Kg/
batch Remarks
1 Intermediate Stage II 9.75 intermediate
stage-IIGemcitabine-HCl 8.40 Finished
product
2 Acetone 639.90 Solvent Recovered Acetone 3.73
Sell to authorized recycler
3 Hyflow 2.00 Filtration media Organic Mother liquor 695.00
Sell to authorized recycler
4 Activated Carbon 0.98 For
decolorization Filtration loss 11.00 Solvent loss
5 Purified Water 69.00 Water wash Solid Waste 3.50 Inorganic HW (landfill)
Total Input 721.63 Total Output 721.63
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Stage IVS.No Input Kg/
batch Remarks Output Kg/batch Remarks
1 Mother Liquor from Stage II 177.75
ML of intermediate stage-II
Intermediate Stage IV 3.38 Intermediate
stage-Iv
2 Isopropyl Alcohol 474.00 Solvent
Recovered Methanol + IPA
807.80Sell to authorized recycler
3 Methanol 835.82 SolventRecovered Isopropyl alcohol
464.00Sell to authorized recycler
4Hydrochloric Acid (Cp Grade)
133.00 reagent Recovered Acetone 5.50
Sell to authorized recycler
5 Acetone 90.06 Solvent Recovery loss 50.22 Solvent loss
6 PotassiumHydroxide 69.38 For
neutralization Filtration loss 8.50 Solvent loss
7 Purified Water 103.00 Aq. Mother Liquor 140.49 To MEE
Organic Mother Liquor 322.42
Sell to authorized recycler
Inorganic Salt 80.70 Inorganic HW (landfill)
Total input 1,883.01 Total output 1,883.01
Stage VS.No Input Kg/
batch Remarks Output Kg/batch Remarks
1 Intermediate Stage IV 3.38 Intermediate
stage-IvGemcitabine-HCl 2.53 Finished
product
2 Acetone 237.79 Solvent Org. Mother liquor 265.00
Sell to authorized recycler
3 Hyflow 2.00 Filtration media Filtration loss 3.64 Solvent loss
4 Activated carbon 0.34 For
Decolorization Solid waste 2.34 Inorganic HW (landfill)
5 Purified water 30.00 Wash waterTotal Input 273.51 Total Output 273.51
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
P7. CAPECITABINE
a) Manufacturing ProcessStage I5-Fluoro cytosine, Hexamethyl disilazane, Tri methyl silyl chloride reacts in presence of
toluene as a media to form Silyl compound. Silylated compound further reacts with 5-
Deoxy-1,2,3-tri-o-acetyl-D-ribofuranside in presence of Stannic chloride and Methylene
chloride. Neutralize the reaction mass with Sodium bicarbonate and purified water.
Organic layer is separated and wash with sodium bicarbonate solution followed by
drying over sodium sulphate. Remove solvent by vacuum distillation. Precipitate solid in
IPA, isolate solid by filtration and followed by drying. This is Capecitabine Stage-I.
Stage IICapecitabine Stage-I condense with n-Pentyl chloro formate in presence of pyridine
using MDC as a solvent. Add catalic amount Methanol to the reaction mass and then
washed it with purified water. MDC layer is dried over sodium sulphate and then
remove solvent by vacuum distillation. Resulting residue is Capecitabine Stage-II (In
situ).
Stage IIICapecitabine Stage-II is hydrolyze by aqueous sodium hydroxide (Caustic flakes)
solution using Methanol as a media, after reaction adjust pH ~5 of reaction mass with
HCl and extract product in MDC. Provide water washes to MDC layer and then give
Activated carbon treatment for the depolarization. Remove solvent by vacuum
distillation. Finally precipitate the product in Ethyl acetate, methanol and Hexane &
isolate solid by filtration. Dry the wet material to get Capecitabine Stage-III (Pure
Capecitabine).
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
b) Reaction Chemistry
Stage I
Stage II
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Stage III
c) Process Flow Diagram
Input Qty., kg Output Qty., kg
5- Fluoro Cytosine 60.00 5-Deoxy-1,2,3-Tri-O-Acetyl-D-
Ribofuranos 125.00 Toluene 716.00
Hexamethyl Disilazane 75.00 Ammonia Gas To Scrubber 7.90 Tri Methyl Silyl Chloride 9.30 Recovered Toluene 709.00
Methylene Chloride 3,300.00 Solid Waste 75.00 Stannic Chloride 137.70 Co2 Gas To Vent 56.10
Sodium Bicarbonate 236.30 Inorganic Salt 400.00 Isopropyl Alcohol 99.00 Sodium Sulphate 63.30
Purified Water 80.00 3717.60
Purified Water 1,127.00 Aq. Effluent 1,086.00
3694.60
Recovered Methylene Chloride 3,135.00 Recovered Isopropyl Alcohol 97.00 Recovery Loss 173.00
289.60
Org. Mother Liquor 335.00 Isopropyl Alcohol 349.00 Recovered Isopropyl Alcohol 178.60
125.00
Intermediate (Stage I) 125.00
Total Input 6,377.60 Total Output 6,377.60
Stage-I
Distilation
Capecitabine (Stage-I)
Reaction
Washing
Filtration & Drying
Process
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Input Qty., kg Output Qty., kg
Intermediate Stage I 125.00 Methylene Chloride 1,964.00
Pyridine 62.50 N-Pentyl Chloroformate 126.30 Solid Waste 74.80
Methanol 6.00
2209.00
Purified Water 750.00 Aq. Effluent From Process 870.00 Sodium Sulphate 62.50
2151.50
Recovered Methylene Chloride 1,866.00 Recovery Loss 98.00
187.50
Intermediate (Stage II) 187.50
Total Input 3,096.30 Total Output 3,096.30
Capecitabine (Stage-II)
Reaction
Washing
Distilation
Process
Residue stage-II
Input Qty., kg Output Qty., kg
Capecitabine Stage-Ii 187.50 Methanol 346.00
Caustic Flakes 25.00 Hydrochloric Acid 73.75
Methylene Chloride 2,277.00 Purified Water 750.00
3659.25
Purified Water 1,500.00 Aq. Effluent 2,700.00 Activated Carbon 6.25 Solid Waste 25.00
2440.50
Ethyl Acetate 338.00 Recovered Methylene Chloride 2,162.00 Recovered Ethyl Acetate 332.00 Recovery Loss 121.00
163.50
Ethyl Acetate 315.00 Org. Mother Liquor 871.90 Methanol 16.00 Recovered Ethyl Acetate 15.00
Hexane 504.00 Drying Loss 10.00 101.60
Capecitabine 101.60
Total Input 6,338.50 Total Output 6,338.50
Finished Product
Distillation
Capecitabine (Stage-III)
Reaction
Washing
Filtration & Drying
Process
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
d) Summary of Mass Balance
Capacity of Finished Product, TPM : 6.0
Working Days Per Month : 26
Stage IS. No Input Kg/
batch Remarks Output Kg/batch Remarks
1 5- Fluoro Cytosine 60.00 Reactant Intermediate (Stage I) 125.00 Intermediate
(Stage I)
25-Deoxy-1,2,3-Tri-O-Acetyl-D-Ribofuranos
125.00 Reactant Recovered Toluene 709.00
Sell to authorized recycler
3 Toluene 716.00 SolventRecovered Isopropyl Alcohol
275.60Sell to authorized recycler
4 Isopropyl Alcohol 448.00 SolventRecovered Methylene Chloride
3,135.00Sell to authorized recycler
5 Methylene Chloride 3,300.00 Solvent Recovery Loss 173.00 Solvent
Loss
6 Hexamethyl Disilazane 75.00 Reagent Aq. Effluent 1,086.00 To MEE
7 Tri Methyl Silyl Chloride 9.30 Reagent Ammonia Gas
To Scrubber 7.90To vent through scrubber
8 Stannic Chloride 137.70 Reagent CO2 Gas 56.10To atmospheric vent
9 Sodium Bicarbonate 236.30 Neutralizat-
ion Solid Waste 75.00 Inorganic HW (landfill)
10 Sodium Sulphate 63.30 For Drying Inorganic Salt 400.00 Inorganic HW (landfill)
11 Purified Water 1,207.00 Wash water
Org. Mother Liquor 335.00
Sell to authorized recycler
Total Input 6,377.60 Total Output 6,377.60
Stage IIS.No Input Kg/
batch Remarks Output Kg/batch Remarks
1 Intermediate Stage I 125.00 Intermediate
(Stage I)Intermediate (Stage II) 187.50 Intermediate
(Stage II)
2 Pyridine 62.50 Reagent Recovery Loss 98.00 Solvent loss
3 N-Pentyl Chloroformate 126.30 Reactant
Recovered Methylene Chloride
1,866.00Sell to authorized recycler
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
S.No Input Kg/
batch Remarks Output Kg/batch Remarks
4 Methanol 6.00Reagent (to neutralize excess n-PCF)
Aq. Effluent From Process 870.00 To MEE
5 Methylene Chloride 1,964.00 Solvent Solid Waste 74.80 Inorganic HW
(Landfill)
6 Sodium Sulphate 62.50 For drying
7 Purified Water 750.00 Wash waterTotal input 3,096.30 Total output 3,096.30
Stage IIIS.No Input Kg/
batch Remarks Output Kg/batch Remarks
1 Capecitabine Stage-Ii 187.50 Intermediate
(Stage II) Capecitabine 101.60 Finished Product
2 Methanol 362.00 SolventRecovered Methylene Chloride
2,162.00Sell to authorized recycler
3 Caustic Flakes 25.00 Reagent Recovered
Ethyl Acetate 347.00Sell to authorized recycler
4 Hydrochloric Acid 73.75 Reagent Recovery Loss 121.00 Solvent Loss
5 Methylene Chloride 2,277.00 Solvent Org. Mother
Liquor 871.90Sell to authorized recycler
6 Ethyl Acetate 653.00 Solvent Aq. Effluent 2,700.00 To MEE
7 Activated Carbon 6.25 For
Decolorization Solid Waste 25.00 Inorganic HW (Landfill)
8 Hexane 504.00 For Crystalization Drying Loss 10.00 Atmospheric
Loss9 Purified Water 2,250.00 Wash water
Total input 6,338.50 Total output 6,338.50
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
P8. ERLOTINIB HCL
a) Manufacturing ProcessStage IEthyl 4,5-bis(2-methoxyethoxy)-2-aminobenzoate hydrochloride is react with
Ammonium formate in presence of Formamide as a media to form Erlotinib HCl stage-I,
Aqueous layer is separated with methylene chloride. Remove solvent by vacuum
distillation. Precipitate solid in IPA, isolate solid by filtration and washing followed by
drying. This is Stage-I.
Stage IIErlotinib HCl stage-I is reacted with oxalyl chloride in presence of methylene chloride
and Di methyl formamide as a media. Wash it with purified water and separate organic
layer. Activated charcoal is used to de-colorization of organic layer and distilled out
methylene chloride 7 to 10 volume of erlotinib HCl stage-I. Precipitate solid in n-
Heptane by distillate n-Heptane up to 70 to 75° C temperature reach atmospherically.
Isolate solid by filtration and washing followed by drying. This is stage-II.
Stage IIIErlotinib HCl stage-II is condensed with 3-ethnyl benzamine in presence of toluene and
isopropyl alcohol as media and isolate solid by filtration and washing followed by drying.
This is stae-III.
Stage IVErlotinib HCl stage-III is purified in isopropyl acetate and isolate solid by filtration and
washing followed by drying. This is stage-IV.
b) Reaction Chemistry
Stage I
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Stage II
Stage III
Stage IV
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
c) Process Flow Diagram
Input Qty., kg Process Output Qty., kg
Formamide 136.00 Ammonium Formate 21.63
Ethyl- 4,5-bis-(2-methoxyethoxy)-2-amino
benzoate hydrochloride (KSM1)
60.00
Purified Water 300.00 517.63
Methylene Chloride 1,425.60 Work up Aq. Effluent 472.60 1470.63
Recovered Methylene Chloride
1,355.00
Isopropyl Alcohol 94.80 Recovered Isopropyl Alcohol 92.80
Recovery Loss 72.60 45.03
Isopropyl Alcohol 355.50 Organic Mother Liquor 310.00 Filtration Loss 21.33
69.2
Drying Recovered Isopropyl Alcohol 25.00
Stage-I Intermediate Stage-I 44.20
Total input 2,393.53 Total output 2,393.53
Erlotinib HCl (Stage-I)
Reaction
Distillation
Filtration
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Input Qty., kg Process Output Qty., kg
Intermediate Stage I 44.20 Dimethyl Formamide 8.36
Oxalyl Chloride 28.60 Methylene Chloride 623.04
704.2
Purified Water (Chilled) 354.00 Work up Aq. Effluent 473.00 585.2
Methylene Chloride 233.64 Solid Waste 4.50 Activated Carbon 4.42
818.76
Recovered Methylene Chloride 475.00
n-Heptane 360.40 Recovered n-Heptane 95.00 Recovery Loss 210.50
398.66
n-Heptane 90.44 Organic Mother Liquor 392.00 Filtration Loss 33.00 Recoverd n-Heptane 22.10
Stage-II Intermediate Stage-II 42.00
Total input 1,747.10 Total output 1,747.10
Filtration & Drying
Erlotinib HCl (Stage-II)
Filtration
Reaction
Distillation
Input Qty., kg Process Output Qty., kg
Toluene 328.86 3-Ethynyl Benzamine 16.55
Activated Carbon 2.10 347.51
Hyflow 4.00 Recovered Toluene 17.40 Toluene 17.40 Solid Waste 6.80
344.71
Toluene 73.08 Isopropyl Alcohol 132.72
Intermediate Stage-II 42.00 592.51
Toluene 109.62 Organic Mother Liquor 615.00 Isopropyl Alcohol 33.18 Filtration Loss 32.81
87.5
Drying Recovered Isopropyl Alcohol 35.00
Stage-III Intermediate Stage III 52.50
Total input 759.51 Total output 759.51
Erlotinib HCl (Stage-III)
Filtration
Carbon filtration
Filtration
Reaction
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
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Manufacturing Process Details
b) Summary of Mass Balance
Capacity of Finished Product, TPM : 0.1
Working Days Per Month : 26
Stage I
S. No. Input Kg/
batch Remarks Output Kg/batch Remarks
1 Ammonium Formate 21.63 Reactant Intermediate Stage-I 44.20 Intermediate
(Stage I)
2
Ethyl- 4,5-bis-(2-methoxyethoxy)-2-amino benzoate hydrochloride (KSM1)
60.00 ReactantRecovered Methylene Chloride
1,355.00Sell to authorized recycler
3 Methylene Chloride 1,425.60 SolventRecovered Isopropyl Alcohol
117.80Sell to authorized recycler
4 Isopropyl Alcohol 450.30 Solvent Recovery Loss 72.60 Solvent Loss
5 Formamide 136.00 Solvent Aq. Effluent 472.60 To MEE
6 Purified Water 300.00 Wash water Filtration Loss 21.33 To MEE
7 Organic Mother Liquor 310.00
Sell to authorized recycler
Total Input 2,393.53 Total Output 2,393.53
Input Qty., kg Process Output Qty., kg
Intermediate Stage III 52.50 Isopropyl Acetate 685.56
Isopropyl Acetate 91.35 Organic Mother Liquor 710.00 Filtration Loss 36.50
Drying Recovered Isopropyl Acetate 34.35
Finished Product Erlotinib HCl 48.56
Total input 829.41 Total output 829.41
Purification
Filtration
Erlotinib HCl (Stage-IV)
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Stage IIS.
No. Input Kg/batch Remarks Output Kg/
batch Remarks
1 Intermediate Stage I 44.20 Intermediate
(Stage I)Intermediate Stage-II 42.00 Intermediate
(Stage II)
2 Oxalyl Chloride 28.60 Reactant
Recovered Methylene Chloride
475.00Sell to authorized recycler
3 Methylene Chloride 856.68 Solvent Recovered n-
Heptane 117.10Sell to authorized recycler
4 Dimethyl Formamide 8.36 Solvent Recovery Loss 210.50 Solvent Loss
5 n-Heptane 450.84 Solvent Aq. Effluent 473.00 To MEE
6 Activated Carbon 4.42 For
Decolorization Filtration Loss 33.00 To MEE
7Purified Water (Chilled)
354.00 Wash water Organic Mother Liquor 392.00
Sell to authorized recycler
8 Solid Waste 4.50 Inorganic HW (landfill)
Total Input 1,747.10 Total Output 1,747.10
Stage IIIS.
No. Input Kg/batch Remarks Output Kg/batch Remarks
1 Intermediate Stage-II 42.00 Intermediate
stage-IIIntermediate Stage III 52.50 Intermediate
stage-III
2 3-Ethynyl Benzamine 16.55 reactant Recovered
Toluene 17.40Sell to authorized recycler
3 Toluene 528.96 SolventRecovered Isopropyl Alcohol
35.00Sell to authorized recycler
4 Isopropyl Alcohol 165.90 Solvent Organic
Mother Liquor 615.00Sell to authorized recycler
5 Activated Carbon 2.10 Decoloriation Solid Waste 6.80 Inorganic HW
(landfill)
6 Hyflow 4.00 Filtration media Filtration Loss 32.81 To MEE
Total Input 759.51 Total Output 759.51
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Stage IVS.
No. Input Kg/batch Remarks Output Kg/
batch Remarks
1 Intermediate Stage III 52.50 Intermediate
stage-III Erlotinib HCl 48.56 Finished Product
2 Isopropyl Acetate 776.91 Solvent
Recovered Isopropyl Acetate
34.35Sell to authorized recycler
Filtration Loss 36.50 To MEE
Organic Mother Liquor 710.00
Sell to authorized recycler
Total Input 829.41 Total Output 829.41
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
P9. IMATINIB MESYLATE ALPHA
a) Manufacturing ProcessStage I & IIAcid compound react with 1,1'-carbonyldiimidazole (CDI) with dimethylformamide as a
solvent to form stage-I (Insitu) which is further react with amine compound to form
stage-II. Stage-I is isolated by adding purified water and adjusting pH with ammonia
solution followed by filtration and drying to get dry stage-II
Stage IIIStage-I is purified by charcolization in methanol solvent followed by crystallization in
methanol & Dimethyl sulfoxide solvent mixture. Wet cake is re-purified in methanol &
Dimethylsulfoxide solvent mixture followed by filtration and drying to get dry stage-II.
Stage IVStage-II react with methane sulfonic acid in presence of Methanol & Dimethylsulfoxide
solvent mixture to form stage-III (Imatinib mesylate). Dry Imatinib mesylate obtained by
filtration and drying.
b) Reaction Chemistry
Stage I
Stage II
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
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Stage III
Stage IV
c) Process Flow Diagram
Input Qty., kg Process Output Qty., kg
Acid Compound 33.20 Dimethyl Formamide 118.00 1-1' Carbonyl Di Imidazole 17.50
168.7Stage-IIAmine Compound 25.00 Ammonia Solution 25.00 Purified Water 475.00
693.7
Aq. Mother Liquor 605.00 Filtration Loss 25.30
63.4
Drying Loss 19.00
Intermediate (Stage II) 44.40
Total Input 693.70 Total Output 693.70
Stage-I insitu Reaction
Filtration
Imatinib Mesylate (Stage-I & II)
Reaction
Drying
Stage II
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Input Qty., kg Process Output Qty., kg
Intermediate Stage-II 44.40 Methanol 933.00 Solid Waste 4.40 Activated Carbon 4.40
977.40
Recovered Methanol 793.00 Recovery Loss 12.80
171.60
Isopropyl Alcohol 69.50 Org. Mother Liquor 262.10 Methanol 69.50 Filtration Loss 8.00
40.50
Drying Drying Loss 5.00
Stage III Intermediate (Stage-III) 35.50
Total Input 1,120.80 Total Output 1,120.80
Charcolisation and Filtration
Filtration & Washing
Distillation
Imatinib Mesylate (Stage-III)
Input Qty., kg Process Output Qty., kg
Intermediate (Stage III) 35.50 Isopropyl Alcohol 701.50 Methane Sulfonic Acid 6.85
743.85
Isopropyl Alcohol 112.00 Org. Mother Liquor 790.00 Filtration Loss 17.50
42.35
Isopropyl Alcohol 280.50 Purified Water 10.70
333.55
Isopropyl Alcohol 28.50 Org. Mother Liquor 310.00 Purified Water 1.07 Filtration Loss 8.52
Drying Drying Loss 12.00
Imatinib Mesylate 38.60
Total Input 1,176.62 Total Output 1,176.62
Finished Product
Filtration & Washing
IPA + Water Purification
Filtration & Washing
Reaction
Imatinib Mesylate (Stage-IV)
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
d) Summary of Mass Balance
Capacity of Finished Product, TPM : 0.5
Working Days Per Month : 26
Stage I & IIS.
No. Input Kg/batch Remarks Output Kg/
batch Remarks
1
4-(1(4-methylpiperaziynl)methyl) benzoic acid dihydrochloride(Acid Compound)
33.20 Reactant Intermediate (Stage II) 44.40 Intermediate
(stage-II)
21,1'-Carbonyldiimidazole
17.50 Reactant Aq. Mother Liquor 605.00 To MEE
3
N-(2-methyl-5-aminophenyl)-4-(3-pyridyl)-2-pyrimidine amine (amine compound)
25.00 Reactant Filtration Loss 25.30 To MEE
4 Ammonia Solution 25.00 Reagent Drying Loss 19.00 Atmospheric Loss
5 Dimethyl Formamide 118.00 Solvent
6 Purified Water 475.00 Wash waterTotal Input 693.70 Total Output 693.70
Stage IIIS.
No. Input Kg/batch Remarks Output Kg/
batch Remarks
1 Intermediate (Stage II) 44.40 Intermediate
(stage-II)Intermediate (Stage-III) 35.50 Intermediate
(stage-III)
2 Methanol 1,002.50 Solvent Recovered Methanol 793.00
Sell to authorized recycler
3 Isopropyl Alcohol 69.50 Solvent Recovery
Loss 12.80 Solvent Loss
4 Activated Carbon 4.40
For Decolorizat-ion
Org. Mother Liquor 262.10 Organic HW
(CHWIF)
Solid Waste 4.40 Inorganic HW (Landfill)
Filtration Loss 8.00 To MEE
Drying Loss 5.00 Atmospheric Loss
Total Input 1,120.80 Total Output 1,120.80
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Stage IVS.
No. Input Kg/batch Remarks Output Kg/
batch Remarks
1 Intermediate (Stage-III) 35.50 Intermediate
(stage-III) Imatinib Mesylate 38.60 Finished Product
2 Methane Sulfonic Acid 6.85 Reagent Org. Mother Liquor 1,100.00 Organic HW
(CHWIF)
3 Isopropyl Alcohol 1,122.50 solvent Filtration Loss 26.02 To MEE
4 Purified Water 11.77 Wash water Drying Loss 12.00 Atmospheric Loss
Total Input 1,176.62 Total Output 1,176.62
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
P10. NILOTINIB
a) Manufacturing ProcessStage ICondensation of Ethyl 3-guanidino-4-methylbenzoate nitrate (KSM-I) and 3-
(dimethylamino)-1-(pyridin-3-yl)prop-2-en-1-one (KSM-II) was done by using
dimethylformamide as solvent and sodium bicarbonate as base at 12 h at 120 0C. After
addition of water reaction mass was filtered and wet cake was dry u/v at 55-60 0C to
afforded stage-II.
Stage IIStage-I was hydrolyzed by sodium hydroxide (2M Aq. solution) using ethanol and water
as solvent for 5 h at 45-50 0C. Reaction mass was neutralized by using hydrochloric
acid (1N). After filtration, wet cake was dry u/v at 55-60 0C to afforded stage-II (Acid).
Stage IIIFirst converted acid (stage-II) to acid chloride (Intermediate) by using thionylchloride,
toluene and dimethyl formamide and stir for 5h at 60-65 0C. Acid chloride was
condensed with 3-(4-methyl-1H-imidazol-1-yl)-5-(trifluoromethyl)aniline (KSM-III) by
using THF as solvent and N,N-Diisopropylethylamine, 4-Dimethylaminopyridine as base
and stir for 12h at 25-30 0C. After addition of S
Stage IVNilotinib dihydrochloride dehydrate was prepared by using hydrochloric acid and water,
methanol as solvent. After addition of ethyl acetate as anti solvent stir for 48 h to
crystallize the product. Filter the reaction mass and dry u/v at 55-60 0C to afforded
stage-IV (Nilotinib Dihydrochloride Dihydrate).
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
b) Reaction Chemistry
Stage I
Stage II
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Stage III
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
c) Process Flow Diagram
Input Qty., kg Output Qty., kg
Dimethyl Formamide 59.10 Ethyl 3-guanidino-4-
methylbenzoate nitrate (KSM-I)
100.00
3-(dimethylamino)-1-(pyridin-
3-yl)prop-2-en-1-one62.00
Sodium Bicarbonate 60.00 CO2 Gas 15.48 265.62
CoolingTemp. 25 -30 0C
265.62
Purified Water 1,050.00 1315.62
Aqueous Mother liquor 1,220.00 Filtration Loss 10.00
85.62
0.62
85.00
Intermediate Intermediate Stage-I 85.00
Total 1,331.10 Total 1,331.10
Recovered Dimethyl Formamide
Nilotinib (Stage-I)
Dryer55-60 0C
ReactorStir for 12 h at
125 0C to 130 0C
Process
Stir for 4 h Temp. 25-30 0C
Filtration 25-30 0C
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Input Qty., kg Output Qty., kg
Intermediate Stage I 85.00 Ethanol 425.00
Purified Water 425.00 Sodium Hydroxide (aq) 25.42
960.42
960.42
Hydrochloric Acid 23.45 Reactor Stir for 1 h Temp. 25-30 °C
983.87
Org. Mother Liquor 490.67 Recovered Ethanol 382.50 Recovery Loss 42.50
68.20
68.20
68.20
Intermediate Stage-II 66.00 Recovered Ethanol 2.20
Total 983.87 Total 983.87
Dryer55-60 °C
CoolingTemp. 25 -30 °C
Nilotinib (Stage-II)Process
ReactorStir for 5 h
Temp. 45-50 °C
FiltrationTemp. 25-30 °C
Stage-II
Unload wet cack
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Input Qty., kg Output Qty., kg
Intermediate (Stage II) 66.00 Toluene 924.00 HCl gas 13.80
Dimethyl Formamide 6.30 Thionyl Chloride 25.63
1008.13
1008.13
3-(4-methyl-1H-imidazol-1-yl)-5-
(trifluoromethyl)aniline49.37
4-Dimethyl Amino Pyridine 1.05
N,N-Diisopropylethylamine 69.62
Tetrahydrofuran 660.00 1788.17
Sodium Bicarbonate (aq) 1,320.00 3108.17
Org. Mother Liquor 1,461.23 RecoveredToluene 831.60 Recovered Tetrahydrofurane 594.00
Solvent Loss 158.40 62.94
62.94
Intermediate (Stage III) 60.00 Recovered Toluene 2.94
Total 3,121.97 Total 3,121.97
Dryer55-60 0C
Process
Distilation U/VTemp. 60-65 °C
Stir for 8 hTemp. 25-30 0C
Stage-III
CoolingTemp 25-30 0C
Stir for 12 h
ReactorStir for 5 h
Temp. 60-65 °C
FiltrationTemp. 25-30 0C
Nilotinib (Stage-III)
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
d) Summary of Mass Balance
Capacity of Finished Product, TPM : 0.15
Working Days Per Month : 26
Stage IS. No Input Kg/
batch Remarks Output Kg/batch Remarks
1Ethyl 3-guanidino-4-methylbenzoate nitrate (KSM-I)
100.00 Reactant Intermediate Stage-I 85.00 Intermediate
stage-I
2
3-(dimethylamino)-1-(pyridin-3-yl)prop-2-en-1-one
62.00 ReactantRecovered Dimethyl Formamide
0.62 To MEE
3 Sodium Bicarbonate 60.00 For
neutralizationAqueous Mother liquor 1,220.00 To MEE
4 Dimethyl Formamide 59.10 Solvent Filtration Loss 10.00 To MEE
5 Purified Water 1,050.00 Wash water CO2 Gas 15.48To Atmospheric vent
Input Qty., kg Output Qty., kg
Intermediate (stage III) 60.00 Hydorchloric Acid 36.25
Purified Water 40.79 Methanol 1,200.00
1337.04
Ethyl Acetate 3,900.00
5237.04
Org. Mother Liquor 77.00 Recovered Methanol 1,080.00 Recovered Ethyl Acetate 3,510.00
Recovery Loss 510.00 60.04
60.04
Nilotinib 58.00 Recovered Methanol 2.04
Total 5,237.04 Total 5,237.04
ProcessNilotinib (Stage-IV)
Dryer55-60 0C
Finished Product
Stir for 48 hTemp. 25 -30 0C
ReactorStir for 5 h
Temp. 25-30 °C
FiltrationTemp. 25-30 0C
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
S. No Input Kg/
batch Remarks Output Kg/batch Remarks
Total Input 1,331.10 Total Output 1,331.10
Stage IIS. No Input Kg/
batch Remarks Output Kg/batch Remarks
1 Intermediate Stage-I 85.00 Intermediate
stage-IIntermediate Stage-II 66.00 Intermediate
stage-II
2 Sodium Hydroxide (aq) 25.42 Reactant Recovered
Ethanol 384.70Sell to authorized recycler
3 Ethanol 425.00 Solvent Recovery Loss 42.50 Solvent loss
4 Purified Water 425.00 Solvent Org. Mother Liquor 490.67
Sell to authorized recycler
5 Hydrochloric Acid 23.45 For
neutralizationTotal Input 983.87 Total Output 983.87
Stage IIIS. No Input Kg/
batch Remarks Output Kg/batch Remarks
1 Intermediate Stage-II 66.00 Intermediate
stage-IIIntermediate (Stage III) 60.00 Intermediate
stage-III
2 Thionyl Chloride 25.63 Reactant RecoveredToluene 834.54
Sell to authorized recycler
3
3-(4-methyl-1H-imidazol-1-yl)-5-(trifluoromethyl)aniline
49.37 Reactant Recovered Tetrahydrofurane 594.00
Sell to authorized recycler
4 4-Dimethyl Amino Pyridine 1.05 Reactant Solvent Loss 158.40 Solvent loss
5N,N-Diisopropylethylamine
69.62 Reagent Org. Mother Liquor 1,461.23Sell to authorized recycler
6 Dimethyl Formamide 6.30 Solvent HCl gas 13.80
To vent through scrubber
7 Toluene 924.00 Solvent8 Tetrahydrofuran 660.00 Solvent
9 Sodium Bicarbonate aq 1,320.00 For
neutralizationTotal Input 3,121.97 Total Output 3,121.97
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Stage IVS. No Input Kg/
batch Remarks Output Kg/batch Remarks
1 Intermediate (Stage III) 60.00 Intermediate
stage-III Nilotinib 58.00 Finished product
2 Hydorchloric Acid 36.25 Reactant Recovered
Methanol 1,082.04Sell to authorized recycler
3 Purified Water 40.79 Solvent Recovered Ethyl Acetate 3,510.00
Sell to authorized recycler
4 Methanol 1,200.00 Solvent Recovery Loss 510.00 Solvent loss
5 Ethyl Acetate 3,900.00 Solvent Org. Mother Liquor 77.00
Sell to authorized recycler
Total Input 5,237.04 Total Output 5,237.04
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
P11. DASATINIB
a) Manufacturing ProcessStage I2-amino-N-(2-chloro-6-methylphenyl)thiazole-5-carboxamide is reacted with 4,6-
dichloro-2-methylpyrimidine in presence of 20 % Sodium tertiary-butoxide in
tetrahydrofuran as solvent. Neutralize reaction mass using aqueous Hydrochloric acid
solution to give Dasatinib Stage – I. Isolate the solid by filtration. Purify the wet material
by water slurry. Finally isolate the solid by filtration. Dry the wet material to get
Dasatinib Stage-I
Stage IIDasatinib Stage – I is condensed with 2-(piperazin-1-yl)ethan-1-ol in presence of
Diisopropylethyl amine in n-butanol as solvent. Remove solvent by distillation.
Precipitate the solid by n-Butanol. Isolate the solid by filtration. Purify the Wet material
by preparing slurry in water. Again isolate solid by filtration. Dry wet material to get
Dasatininb Stage-II.
Stage IIIDasatinib Stage – II is purified by using Ethanol and Purified water mixture as solvent.
Recrystallise the product by adding water. Isolate solid by filtration. Dry wet material to
get Dasatininb Stage-III.
Stage IVPrepare solution of formic acid in ethanol and charge Dasatinib Stage – III. Stage-III is
reacted with Fumaric to convert into Dasatinib Stage – IV. Isolate solid by filtration. Dry
wet material to get Dasatininb Stage-IV.
Stage VDasatinib Stage – IV is dissolved in purified water and filter the mass on hyflow bed.
Resulting reaction mass neutralized by using Ammonium carbonate solution in Purified
water to give Dasatinib. Isolate the solid by filtration. Purify the Wet material by
preparing slurry in water. Again isolate solid by filtration. Dry wet material to get
Dasatininb.
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
b) Reaction ChemistryStage I
Stage II
Stage III
Stage IV
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Stage V
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
c) Process Flow Diagram
Input Qty., kg Output Qty., kg
2-amino-N-(2-chloro-6-methylphenyl)-5-
thiazolecarboxamide 86.20
Tetrahydrofuran 1,120.70 4,6-dichloro-2-methyl
pyrimidine 62.90
Sodium Tertiary Butoxide solution (20%)
in THF 543.10
Hydrochloric Acid 86.20 Purified Water 258.60
Aq. Mother Liquor 390.50 Tetrahydrofuran 172.40 Org. Mother Liquor 1,836.20
Purified Water 431.00
Purified Water 172.40 Aq. Mother Liquor 594.80
Aq. Effluent 8.60
Intemediate (Stage-I) 103.40
Total 2,933.50 Total 2,933.50
Dastinib (Stage-I)Process
Reaction
Filtration
Reaction
Reactor
Filtration
Purification
Drying
Dasatinib Stage - I
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Input Qty., kg Output Qty., kg
Intermediate (Stage I) 103.40 2-(piperazin-1-yl)ethan-1-
ol 239.00
N,N-Diisopropylethylamine 67.80
n-Butanol 827.60
Recovered n-butanol 676.00
Recovery Loss 13.50
n-Butanol 103.40 Org. Mother Liquor 537.80
Purified Water 517.20
Purified Water 103.40 Aq. Mother Liquor 605.20
Aq. Effluent 15.50
Intermediate (Stage-II) 113.80
Total 1,961.80 Total 1,961.80
Dastinib (Stage-II)Process
Dasatinib Stage - II
Reaction
Filtration
Purification
Distilation
Dryer
Filtration
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Input Qty., kg Output Qty., kg
Intermediate Stage II 113.80 Ethanol 2,275.90
Purified Water 569.00
Purified Water 910.30
Ethanol (aq) for washing 113.80 Aq. & Org. Mix ML 3,889.70
Aq. Effluent 13.80
Intermediate (Stage-III) 79.30
Total 3,982.80 Total 3,982.80
Dastinib (Stage-III)
Purification
Crystallisation
Filtration
Drying
Dasatinib Stage III
Process
Input Qty., kg Output Qty., kg
Ethanol 1,586.20 Fumaric Acid 54.70
Intermediate (Stage III) 79.30
Ethanol 79.30 Org. Mother Liquor 1,714.10
Recovered Ethanol 13.80
Intermediate Stage-IV 71.60
Total 1,799.50 Total 1,799.50
Filtration
Drying
Dasatinib Stage - IV
Preparation of solution
Reaction
Dastinib (Stage-IV)Process
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
d) Summary of Mass Balance
Capacity of Finished Product, TPM : 0.05
Working Days Per Month : 26
Input Qty., kg Output Qty., kg
Intermediate Stage IV 71.60 Purified Water 3,148.30
Purified Water 143.10 Purified Water 143.10 -
Carbon dioxide gas 10.50
Ammonia gas 4.30
Ammonium Carbonate 21.40 Purified Water 357.80
Purified Water 71.60 Aq. Mother liquor 3,857.00
Purified Water 858.60
Purified Water 143.10 Aq. Mother liquor 1,026.50
Aq. Effluent 10.30
Dasitinib 50.00
Total 4,958.60 Total 4,958.60
Finished Product
Filtration
Reaction
Purification
Dastinib (Stage-V)Process
Dryer
Filtration
Water slurry
Filtration
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Stage I
S. No Input Kg/
batch Remarks Output Kg/batch Remarks
12-amino-N-(2-chloro-6-methylphenyl)-5-thiazolecarboxamide
86.20 Reactant Intemediate (Stage-I) 103.40 Intermediate
(Stage-I)
2 4,6-dichloro-2-methyl pyrimidine 62.90 Reactant Org. Mother
Liquor 1,836.20Sell to authorized recycler
3 Hydrochloric Acid 86.20 Reactant Aq. Mother Liquor 985.30 To MEE
4 Tetrahydrofuran 1,293.10 Solvent Aq. Effluent 8.60 To MEE
5Sodium Tertiary Butoxide solution (20%) in THF
543.10 Catalyst
6 Purified Water 862.00 Media
Total Input 2,933.50 Total Output 2,933.50
Stage II
S. No Input Kg/
batch Remarks Output Kg/batch Remarks
1 Intermediate (Stage I) 103.40 Intermediate (Stage I)
Intermediate (Stage-II) 113.80 Intermediate
(Stage-II)
3 2-(piperazin-1-yl)ethan-1-ol 239.00 Reactant Recovered
n-butanol 676.00Sell to authorized recycler
2 n-Butanol 931.00 Solvent Recovery Loss 13.50 Solvent loss
4 N,N-Diisopropylethylamine 67.80 Solvent Org. Mother
Liquor 537.80Sell to authorized recycler
5 Purified Water 620.60 Media Aq. Mother Liquor 605.20 To MEE
Aq. Effluent 15.50
Total Input 1,961.80 Total Output 1,961.80
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Stage III
S. No Input Kg/
batch Remarks Output Kg/batch Remarks
1 Dasatinib Stage – II 113.80 Intermediate
(Stage II)Intermediate (Stage-III) 79.30 Intemediate
(Stage-III)
2 Ethanol 2,389.70 Solvent Aq. & Org. Mix ML 3,889.70
Sell to authorized recycler
3 Purified Water 1,479.30 Media Aq. Effluent 13.80 To MEE
Total Input 3,982.80 Total Output 3,982.80
Stage IV
S. No Input Kg/
batch Remarks Output Kg/batch Remarks
1 Intermediate (Stage III) 79.30 Reactant Intermediate
Stage-IV 71.60 Intermediate Stage-IV
2 Fumaric Acid 54.70 Reactant Recovered Ethanol 13.80 Sell to authorized
recycler
3 Ethanol 1,665.50 Solvent Org. Mother Liquor 1,714.10 Sell to authorized
recyclerTotal Input 1,799.50 Total Output 1,799.50
Stage V
S. No Input Kg/
batch Remarks Output Kg/batch Remarks
1 Intermediate Stage-IV 71.60 Reactant Dasitinib 50.00 Finished
product
2 Ammonium Carbonate 21.40 Reactant Aq. Mother liquor 4,883.50 To MEE
3 Purified Water 4,865.60 Media Aq. Effluent 10.30 To MEEAmmonia gas 4.30 To scrubber
Carbon dioxide gas 10.50
Toatmosphere through vent
Total Input 4,958.60 Total Output 4,958.60
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
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Manufacturing Process Details
P12. PAZOPANIB HCl
a) Manufacturing ProcessStage I2,3-dimethyl-2H-indazol-6-amine hydrochloride (KSM-I) and 2,4-dichloropyrimidine
(KSM-II) are reacting in presence of sodium bicarbonate and methanol to give
Pazopanib stage – I. After reaction, isolate solid by filtration. Wet material is purified in
methanol. Precipitate the product in water. isolate solid by filtration. Dry the wet material
to get Pazopanib stage – I.
Stage IIPazopanib Stage – I react with dimethylcarbonate using anhydrous potassium
carbonate as base in Dimethyl formamide as solvent to give Pazopanib stage – II.
Crystallize product by water and methanol. Isolate the solid by filtration. Dry the wet
material to get Pazopanib stage – II.
Stage IIIPazopanib Stage – II is purified by carbon treatment in methanol solvent. Filter the
reaction mass on hyflow bed and remove carbon. Resulted filtrate is cooled and
precipitate the solid. Isolate the solid by filtration. Dry the wet material to get Pazopanib
stage – III.
Stage IVPazopanib Stage – III and 5-amino-2-methylbenzenesulfonamide (KSM-III) are reacted
in presence of catalytic amount of Conc. Hydrochloric acid in methanol to convert into
Pazopanib Stage – IV. Precipitate the product by stirring. Isolate the solid by filtration.
Dry the wet material to get Pazopanib stage – III.
Stage VPazopanib Stage – IV is converted to hydrated form by dissolving and crystallized in
acetonitrile & water mixture. Precipitate the product by cooling the reaction mass.
Isolate the solid by filtration. Purify the wet material by ethanol. Isolate the solid by
filtration. Dry the wet material. After drying hydrated form again converted in anhydrate
form Pazopanib HCl.
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
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b) Reaction ChemistryStage I
Stage II
Stage III
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Stage IV
Stage V
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
c) Process Flow Diagram
Input Qty., kg Output Qty., kg
Methanol 923.10 2,3-dimethyl-2H-indazol-6-amine
hydrochloride (Indazol HCl)
76.90 Carbon Dioxide Gas 33.80
Sodium Bicarbonate 98.10 2,4-dichloropyrimidine 92.80
Org. Mother Liqour 1,072.20
Methanol 307.70
Methanol 153.90 Org. Mother Liqour 461.50
Water 769.20
Water 269.20 Aq. Mother Liqour 1,092.30 Methanol 76.90
Recovered Methanol 23.40
Intermediate (Stage-I) 84.60
Total 2,767.80 Total 2,767.80
Pazopanib HCl (Stage-I)Process
Reaction
Reaction
Stage-I
Filtration
Filtration
Reaction
Filtration
Drying
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
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Manufacturing Process Details
Input Qty., kg Output Qty., kg
Dimethyl Formamide 304.60 Intermediate Stage-I 84.60 Carbon Dioxide Gas 12.30
Potassium Carbonate (anhydrous) 128.50
Dimethyl Carbonate 152.30
Water 1,353.90
Water 169.20 Aq. Mother Liqour 2,173.10 Methanol 84.60
Aq. Effluent 20.00
Intermediate (Stage-II) 72.30
Total 2,277.70 Total 2,277.70
Reaction
Crystallisation
Filtration
Drying
Stage-II
Pazopanib HCl (Stage-II)Process
Input Qty., kg Output Qty., kg
Methanol 1,446.20 Intermediate Stage II 72.30
Activated Carbon 3.60
Hyflow 5.00 Solid waste (Hyflow + Carbon) 9.00
Methanol 144.60
Methanol 72.30 Org. Mother Liquor 1,664.20
Recovered Methanol 15.40
Intermediate (Stage-III) 55.40
Total 1,744.00 Total 1,744.00
Purification
Pazopanib HCl (Stage-III)Process
Filtration
Drying
Stage-III
Crystallisation
Filtration
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Input Qty., kg Output Qty., kg
Methanol 1,384.60 Intermediate Stage-III 55.40
5-amino-2-methylbenzenesulfona
mide36.50
Hydrochloric Acid 3.90
Methanol 110.80 Org. Mother Liquor 1,500.00
Recovered Methanol 16.60
Intermediate (Stage-IV) 74.60
Total 1,591.20 Total 1,591.20
Drying
Stage-IV
Reaction
Filtration
Pazopanib HCl (Stage-IV)Process
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
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Manufacturing Process Details
d) Summary of Mass Balance
Capacity of Finished Product, TPM : 0.06
Working Days Per Month : 26
Stage IS. No Input Kg/
batch Remarks Output Kg/batch Remarks
1
2,3-dimethyl-2H-indazol-6-amine hydrochloride (Indazol HCl)
76.90 Reactant Intermediate (Stage-I) 84.60 Intermediate
(Stage-I)
2 2,4-dichloropyrimidine 92.80 Reactant Recovered
Methanol 23.40Sell to authorized recycler
Input Qty., kg Output Qty., kg
Acetonitrile 370.00 Water 205.40
Intermediate Stage IV 74.60
Acetonitrile 33.10 Water 18.50
Acetonitrile 67.70 Org. Mother Liquor 731.00 Water 37.70
Ethanol 320.80
Ethanol 74.60 Org. Mother Liquor 392.00
Recovered Ethanol 19.40
Pazopanib HCl 60.00
Total 1,202.40 Total 1,202.40
Cystallisation
Filtration
Reaction
Finished Product
Drying
Purification
Filtration
Pazopanib HCl (Stage-V)Process
Filtration
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
S. No Input Kg/
batch Remarks Output Kg/batch Remarks
3 Sodium Bicarbonate 98.10 Reagent Org. Mother
Liqour 1,533.70Sell to authorized recycler
4 Methanol 1,461.60 Solvent Aq. Mother Liqour 1,092.30 To MEE
5 Water 1,038.40 Media Carbon Dioxide Gas 33.80
To atmospheric vent
Total Input 2,767.80 Total Output 2,767.80
Stage II
S. No Input Kg/
batch Remarks Output Kg/batch Remarks
1 Intermediate (Stage-I) 84.60 Reactant Intermediate
(Stage-II) 72.30 Intermediate stage-II
2Potassium Carbonate (anhydrous)
128.50 Reagent Aq. Mother Liqour 2,173.10 To MEE
3 Dimethyl Carbonate 152.30 Reactant Aq. Effluent 20.00 To MEE
4 Methanol 84.60 Solvent Carbon Dioxide Gas 12.30 To atmospheric
vent
5 Dimethyl Formamide 304.60 Solvent
6 Water 1,523.10 MediaTotal Input 2,277.70 Total Output 2,277.70
Stage III
S. No Input Kg/
batch Remarks Output Kg/batch Remarks
1 Intermediate (Stage-II) 72.30 Reactant Intermediate
(Stage-III) 55.40 Intermediate Stage-III
2 Activated Carbon 3.60
For decolouriza-tion
RecoveredMethanol 15.40
Sell to authorized recycler
3 Hyflow 5.00 Filter aidSolid waste (Hyflow + Carbon)
9.00 Inorganic HW (landfill)
4 Methanol 1,663.10 Solvent Org. Mother Liquor 1,664.20
Sell to authorized recycler
Total Input 1,744.00 Total Output 1,744.00
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Stage IV
S. No Input Kg/batch Remarks Output Kg/batch Remarks
1 Intermediate (Stage-III) 55.40 Reactant Intermediate
(Stage-IV) 74.60 Intermediate (Stage-IV)
25-amino-2-methylbenzenesulfonamide
36.50 Reactant Recovered Methanol 16.60
Sell to authorized recycler
3 Hydrochloric Acid 3.90 Reagent Org. Mother
Liquor 1,500.00Sell to authorized recycler
4 Methanol 1,495.40 SolventTotal Input 1,591.20 Total Output 1,591.20
Stage V
S. No Input Kg/batch Remarks Output Kg/batch Remarks
1Intermediate (Stage-IV) 74.60 Reagent Pazopanib
HCl 60.00 Finished product
2 Acetonitrile 470.80 Solvent Recovered Ethanol 19.40
Sell to authorized recycler
3 Water 261.60 Media Org. Mother Liquor 1,123.00
Sell to authorized recycler
4 Ethanol 395.40 SolventTotal Input 1,202.40 Total Output 1,202.40
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
P13. SORAFENIB
a) Manufacturing ProcessStage IA mixture of 4-chloro-pyridine-2-carboxylic acid methyl amide hydrochloride, 4-
aminophenol and aqueous potassium hydroxide in Tetrahydrofuran was stirred at 65oC.
Product is isolated as hydrochloride salt. Thus obtained salt is dissolved in purified
water and neutralized using 10% NaOH solution to obtain crude Stage-I which is
crystalize in Isopropanol to get Stage-I.
Stage IIStage-II is prepared by reacting Stage-I with 4-chloro-3-(trifluoromethyl) phenyl
isocyanate in methylene chloride and dimethyl formamide at lower temperature.
Stage IIISorafenib base crude is purified by acetone and Dimethyl formamide
Stage IVSorafenib tosylate is prepared from Stage-III and PTSA in Methanol. Wet material is
dried to get API.
b) Reaction Chemistry
Stage I
Stage II
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Stage III
Stage IV
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
c) Process Flow Diagram
Input Qty., kg Process Output Qty., kg
Tetrahydrofuran 392.23 Paracetamol 48.27
Purified Water 32.65 Potassium Hydroxide 85.92 Potassium Carbonate 2.91 Tetrabutyl Ammonium
Bromide (TBAB) 17.16
4-chloro-pyridine-2-
carboxylic acid methyl amide
hydrochloride (Amide KSM)
44.12
Hydrochloric Acid 199.51
Tetrahydrofuran 156.89 Org. Mother Liquor 948.29 Filtration Loss (Org ML 10.00
Purified Water 441.20
Purified Water 44.12 Solid Waste 0.04
Caustic flakes 23.82 Purified Water 301.78
Purified Water 88.24 Aq. Mother Liquor 867.34 Filtration Loss 8.00
Isopropyl Alcohol 101.04
Isopropyl Alcohol 20.21 Org. Mother Liquor 121.39 Filtration Loss 17.65
Recovered Isopropyl Alcohol 5.30
Intermediate stage-I 22.06
Total input 2,000.07 Total output 2,000.07
Filtration
Sorafenib Tosylate (Stage-I)
Filtrate/Cooling
Filteration
Reaction Mass/Heating
Wet Cake
Reaction Mass/Heating
Filteration
Reaction
Cool Reaction Mass
Reaction
Intermediate
Wet Cake/Heating
Cooling
Filtration
Drying
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Input Qty., kg Process Output Qty., kg
Intermediate Stage I 22.06 Methylene Chloride 97.95
Dimethyl Formamide 13.88
4-chloro-3-(trifluoromethyl) phenyl
isocyanate(Isocyanate KSM)
34.13
Methylene Chloride 48.75 Dimethyl Formamide 6.93
Methylene Chloride 117.36 Org. Mother Liquir 285.00 Purified Water 88.24 Filtration Loss (org ML 14.30
Aq. Mother Liquor 87.25 Filtration Loss 1.00
Recovered MDC 5.00
Intermediate Stage-II 36.75
Total input 429.300 Total output 429.300
Sorafenib Tosylate (Stage-II)
Drying
Intermediate
Filtration
Reaction Mass
Reaction Mass/Cooling/
Stirring
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Input Qty., kg Process Output Qty., kg
Intermediate Stage II 36.75 Acetone 641.95
Dimethyl Formamide 6.94
Activated carbon 1.83
Acetone 58.36 Solid Waste 1.83
Recovered Acetone 555.00 Recovery loss 4.96
Acetone 29.18 Org. Mother Liquor 167.95 Filtration loss 14.90
Recovered Acetone 2.00
Intermediate Stage-III 28.37
Total input 775.01 Total output 775.01
Reaction Mass/Heating
Reaction Mass
Sorafenib Tosylate (Stage-III)
Sparkler Filtration
Distillation/Cooling
Filtration
Drying
Intermediate
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
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Manufacturing Process Details
d) Summary of Mass Balance
Capacity of Finished Product, TPM : 0.1
Working Days Per Month : 26
Input Qty., kg Process Output Qty., kg
Intermediate Stage III 28.37Methanol 89.88
Methanol 44.944-methyl benzene sulfonic acid monohydrate (PTSA) 12.18
Methanol 44.94 Org. Mother Liquor 166.00Filtration Loss 4.32
Recovered Methanol 15.00
Sorafenib Tosylate 34.99
Total 220.31 Total 220.31
Finished Product
Reaction Mass
Reaction Mass
Cooling
Filtration
Drying
Sorafenib Tosylate (Stage-IV)
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Stage IS. No Input Kg/
batch Remarks Output Kg/batch Remarks
1
4-chloro-pyridine-2-carboxylic acid methyl amide hydrochloride (Amide KSM)
44.12 Reactant Intermediate stage-I 22.06 Intermediate
stage-I
2 Paracetamol 48.27 ReactantRecovered Isopropyl Alcohol
5.30Sell to authorized recycler
3Tetrabutyl Ammonium Bromide (TBAB)
17.16 Reactant Org. Mother Liquor 1,069.68
Sell to authorized recycler
4 Potassium Hydroxide 85.92 Reactant Aq. Mother
Liquor 867.34 To MEE
5 Potassium Carbonate 2.91 Reactant Filtration
Loss 8.00 To MEE
6 Hydrochloric Acid 199.51 Reagent Solid Waste 0.04 Inorganic HW (landfill)
7 Tetrahydrofuran 549.12 SolventFiltration Loss (Org ML)
27.65
8 Isopropyl Alcohol 121.25 Solvent
9 Caustic flakes 23.82 Neutralizing agent
10 Purified Water 907.99 Wash waterTotal Input 2,000.07 Total Output 2,000.07
Stage IIS. No Input Kg/
batch Remarks Output Kg/batch Remarks
1 Intermediate stage-I 22.06 Intermediate stage-I
Intermediate Stage-II 36.75 Intermediate
stage-II
2 Methylene Chloride 264.06 Solvent Recovered MDC 5.00
Sell to authorized recycler
3 Dimethyl Formamide 20.81 Solvent Org. Mother Liquir 285.00
Sell to authorized recycler
4
4-chloro-3-(trifluoromethyl) phenyl isocyanate(Isocyanate KSM)
34.13 Reactant Aq. Mother Liquor 87.25 To MEE
5 Purified Water 88.24 Wash waterFiltration Loss (org ML)
15.30 To MEE
Total Input 429.30 Total Output 429.30
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Stage IIIS. No Input Kg/
batch Remarks Output Kg/batch Remarks
1 Intermediate Stage-II 36.75 Intermediate
stage-IIIntermediate Stage-III 28.37 Intermediate
stage-III
2 Acetone 729.49 Solvent Recovered Acetone 557.00
Sell to authorized recycler
3 Dimethyl Formamide 6.94 Solvent Recovery loss 4.96 Solvent loss
4 Activated carbon 1.83 For
DecolorizationOrg. Mother Liquor 167.95
Sell to authorized recycler
Filtration loss 14.90 To MEE
Solid Waste 1.83 Inorganic HW (landfill)
Total Input 775.01 Total Output 775.01
Stage IVS. No Input Kg/batch Remarks Output Kg/batch Remarks
1 Intermediate Stage-III 28.37 Intermediate
stage-IIISorafenib Tosylate 34.99 Finished
Product
2
4-methyl benzene sulfonic acid monohydrate (PTSA)
12.18 Reactant Recovered Methanol 15.00
Sell to authorized recycler
3 Methanol 179.76 Solvent Org. Mother Liquor 166.00
Sell to authorized recycler
Filtration Loss 4.32 To MEE
Total Input 220.31 Total Output 220.31
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
P14. N-BZ-BIS-LACTAM
a) Manufacturing Process1,5-bis[di isopropyl-(+)- 4’phenyl -2’-azetidinone-3’- hydroxyl-silyl] pentane reacts with
benzoyl chloride in presence of methylene chloride, 4- dimethyl amino pyridine and
triethyl amine. After completion of reaction, reaction mass washed with aqueous
solution of sodium bicarbonate and followed by aqueous sodium chloride solution. Give
Sodium sulphate treatment to organic layer. Romove methylene chloride by distillation.
Dilute the reaction mass with hexane. Product 1,5-bis[di isopropyl-(+)-(3’R,4’S)-1’-
benzoyl-4’-phenyl-2’-azetidinone-3’- hydroxyl -silyl] pentane (N-BZ bis lactam) is
seperated by column chromatography. Wash crometography with diethyl ether.
Remove the solvent by distillation. Strip out the reaction mass with Tetrahydrofuran.
Distillied out the solvent by distillation to get finished product.
b) Reaction Chemistry
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
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Manufacturing Process Details
c) Process Flow Diagram
Input Qty., kg Out put Qty., kg
1,5-bis[di isopropyl-(+)- 4’phenyl -2’-azetidinone-3’- hydroxyl-
silyl]pentane5.00
Methylene Chloride 66.00 4-Dimethyl Amino Pyridine 0.10
Triethyl Amine 3.26 Benzoyl Chloride 2.42
Benzoyl Chloride 0.61
Water 15.00 Aq. Effluent 21.69 Sodium Bicarbonate 0.30
Water 30.00 Sodium Chloride 4.50 Aq. Effluent 34.50 Sodium Sulphate 5.00 Solid Waste (Sodium Sulfate) 5.00
Methylene Chloride 26.40
Recovered Methylene Chloride 89.00 Recovery Loss 3.40
Hexane 13.08
Silica Gel 140.00 Hexane 2,275.92
Diethyl Ether 242.42
Recovered Hexane + Diethyl Ether 2,480.42 RecoveryLoss 51.00 Solid Waste (Silica gel) 141.00
Diethyl Ether 7.13 Recovered Diethyl Ether 7.00 Tetrahydrofuran 35.56 Recovery Loss 0.13
Recovered Tetrahydrofuran 34.50 Recovery Loss 1.06
N-BZ-BIZ Lactam 4.00
Total 2,872.70 Total 2,872.70
ProcessProduct: N-BZ-BIS-LACTAM Stage-I
Organic layer
Organic layer Distillation
Residue
Column Chromatography
Reaction mass
Reaction mass
Reaction mass
Column Effluent
Distillation
Rotavapor
Paclitaxel
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
d) Summary of Mass Balance
Capacity of Finished Product, TPM : 0.05
Working Days Per Month : 26
S. No Input Kg/
batch Remarks Output Kg/batch Remarks
1
1,5-bis[di isopropyl-(+)- 4’phenyl -2’-azetidinone-3’-hydroxyl-silyl]pentane
5.00 Reactant N-BZ-BIZ Lactam 4.00 Finished
Product
2 4-Dimethyl Amino Pyridine 0.10 Reagent
Recovered Methylene Chloride
89.00Sell to authorized recycler
3 Triethyl Amine 3.26 Reagent Recovery Loss 3.40 Solvent loss
4 Benzoyl Chloride 3.03 ReactantRecovered Hexane + Diethyl Ether
2,480.42Sell to authorized recycler
5 Diethyl Ether 249.55 Solvent RecoveryLoss 51.00 Solvent loss
6 Hexane 2,289.00 Solvent Recovered Diethyl Ether 7.00
Sell to authorized recycler
7 Tetrahydrofuran 35.56 Solvent Recovery Loss 0.13 Solvent loss
8 Methylene Chloride 92.40 Solvent Recovered Tetrahydrofuran 34.50
Sell to authorized recycler
9 Sodium Bicarbonate 0.30 Washing
media Recovery Loss 1.06 Solvent loss
10 Sodium Chloride 4.50 Washing media Aq. Effluent 56.19 To MEE
11 Sodium Sulphate 5.00 Drying agent
Solid Waste (Sodium Sulfate) 5.00
Inorganic HW (landfill)
12 Silica Gel 140.00Absorbing agent for column
Solid Waste (Silica gel) 141.00
Inorganic HW (landfill)
13 Water 45.00 Media
Total Input 2,872.70 Total Output 2,872.70
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
P15. N-BOC-BIS-LACTAM
a) Manufacturing Process
1,5-bis[di isopropyl-(+)- 4’phenyl -2’-azetidinone-3’- hydroxyl-silyl] pentane reacts with
ditertiary butyl di carbonate in presence of methylene chloride, 4- dimethyl amino
pyridine and triethyl amine. After completion of reaction, reaction mass washed with
aqueous solution of sodium bicarbonate and followed by aqueous sodium chloride
solution. Give Sodium sulphate treatment to organic layer. Remove methylene chloride
by distillation. Dilute the reaction mass with hexane. Product 1,5-bis[di isopropyl-(+)-
(3’R,4’S)-1’-tert butoxycarbonyl-4’-phenyl-2’azetidinone – 3’- hydroxyl -silyl]pentane (N-
Boc bis lactam) is separated by column chromatography. Wash crometography with
diethyl ether. Remove the solvent by distillation. Strip out the reaction mass with
Tetrahydrofuran. Distil out the solvent by distillation to get finished product.
b) Reaction Chemistry
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
c) Process Flow Diagram
Input Qty., kg Output Qty., kg
1,5-bis[di isopropyl-(+)- 4’phenyl -2’-azetidinone-3’-
hydroxyl-silyl]pentane2.50
Methylene Chloride 72.60
4-Dimethyl Amino Pyridine 0.25
Ditertiary Butyl Dicarbonate 3.50
Methanol 1.60
Water 26.00 Aq. Effluent 26.25
Water 12.00 Sodium Chloride 3.75 Aq. Effluent 15.75
Sodium Sulphate 2.50 Solid Waste (Sodium Sulphate) 2.50
Methylene Chloride 19.80
Recovered Methylene Chloride + Methanol 90.70
Recovery Loss 3.30
Hexane 6.60
Silica Gel 50.00 Hexane 521.40
Ethyl Acetate 90.00
Recovered Hexane + Ethyl Acetate 605.50
Recovery Loss 12.50 Solid Waste (Silica Gel) 54.00
Recovered Tetrahydrofuran 22.00
Tetrahydrofuran 22.50 Recovery Loss 0.50
N-BOC-BIS Lactam 2.00
Total 835.00 Total 835.00
N-Boc-Bis-LactamProcess
Reaction mass
Reaction mass
Reaction mass
Residue
Organic layer Distillation
Column Chromatography
Colum Effluent
Distillation
Rotavapor
Finished Product
Organic layer
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
d) Summary of Mass Balance
Capacity of Finished Product, TPM : 0.05
Working Days Per Month : 26
S. No Input Kg/batch Remarks Output Kg/batch Remarks
1
1,5-bis[di isopropyl-(+)-4’phenyl -2’-azetidinone-3’-hydroxyl-silyl]pentane
2.50 Reactant N-BOC-BIS Lactam 2.00 Finished
product
2 4-Dimethyl Amino Pyridine 0.25 Reactant
Recovered Methylene Chloride + Methanol
90.70Sell to authorized recycler
3 Ditertiary Butyl Dicarbonate 3.50 Reagent Recovery Loss 3.30 Solvent
loss
4 Methylene Chloride 92.40 Solvent
Recovered Hexane + Ethyl Acetate
605.50Sell to authorized recycler
5 Methanol 1.60 Solvent Recovery Loss 12.50 Solvent loss
6 Ethyl Acetate 90.00 Solvent Recovered Tetrahydrofuran 22.00
Sell to authorized recycler
7 Hexane 528.00 Solvent Recovery Loss 0.50 Solvent loss
8 Tetrahydrofuran 22.50 Solvent Aq. Effluent 42.00 To MEE
9 Sodium Chloride 3.75 Washing media
Solid Waste (Sodium Sulphate)
2.50Inorganic HW (landfill)
10 Sodium Sulphate 2.50 Drying agent
Solid Waste (Silica Gel) 54.00
Inorganic HW (landfill)
11 Silica Gel 50.00Absorbing agent for column
12 Water 38.00 MediaTotal input 835.00 Total Output 835.00
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
P16. 5-(4-(4-(5-CYANO-1H-INDOL-3-YL)-BUTYL)-PIPERAZIN-1-YL)BENZOFURAN-2-CARBOXAMIDE
a) Manufacturing ProcessEthyl-5-(4-(5-Cyno-1H-indol-3-yl)butyl)piprazin-1-yl)benzfuran-2-carboxylate
hydrochloride reacts with ammonia gas in presence of di methyl fromamide. After
reaction filter the reaction mass and remove inorganic salt. Charge water in to filtrate
and isolate the product by filtration. Dry the wet material to get product.
b) Reaction Chemistry
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
c) Process Flow Diagram
d) Summary of Mass Balance
Capacity of Finished Product, TPM : 0.05
Working Days Per Month : 26
S. No Input Kg/
batch Remarks Output Kg/batch Remarks
1
Ethyl 5-(4-(4-(5-cyano-1H-indol-3-yl)butyl)piperazin-1-yl) benzofuran-2-carboxylate hydrochloride
43.50 Reactant Intermediate of Vilazodone 26.00 Finished
product
2 Ammonia Gas 6.71 Reactant Aq. Effluent 4,428.21 To MEE
3 Dimethyl Formamide 2,613.00 Solvent Solid Waste 40.00Inorganic HW (landfill)
4 Purified Water 1,831.00 MediaTotal Input 4,494.21 Total Output 4,494.21
Input Qty., kg Process Out put Qty., kg
Ethyl 5-(4-(4-(5-cyano-1H-indol-3-yl)butyl)piperazin-1-yl)
benzofuran-2-carboxylate hydrochloride
43.50
Ammonia Gas 6.71 Dimethyl Formamide 2,000.00
Dimethyl Formamide 613.00 Solid Waste 40.00
Purified Water 1,831.00 Aq. Effluent 4,428.21
Vilazodone 26.00
Total 4,494.21 Total 4,494.21
5-(4-(4-(5-Cyano-1H-indol-3-yl)-butyl)-piperazin-1-yl)benzofuran-2-carboxamide
Ammination Reaction
Crystallisation & Filtration
Finished Product
Filtration
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
P17. 2-ACETAMIDO-2-PHENETHYLPROPANE-1,3-DIYL-DIACETATE
a) Manufacturing ProcessStage IPhenyl ethyl bromide react with diethyl acetamido malonate in presence of cesium
carbonate and dimethyl sulphoxide, resulting reaction mix was quenched with purified
water and precipitated product was collected with filtration. Wet cake crude compound
was purified with ethyl acetate: methyl tertiary butyl ether to get pure stage-I. Solid
material isolated by filtration. Wet material dried to get stage-I
Stage IIStage-I is reduced with sodium borohydride and calcium chloride in presence of ethanol
to give hydroxy intermediate. Reaction mass quenched in acetic acid solution. Remove
solvent by distillation. Extract product by Methylene chloride from residue. Wash the
organic layer with solution of sodium metabisulphate and followed by sodium chloride
solution. Remove the solvent by distillation from organic layer. Resulting reaction mass
further acylated with acetic anhydride and triethyl amine in presence of methylene
chloride to gave stage-II. Reaction mass quenched in acetic acid solution and extract
product by methylene chloride. Remove the solvent by distillation. Purify the Crude
compound with ethyl acetate: methyl tertiary butyl ether to gave pure stage-II. Solid
material isolated by filtration. Wet material dried to get stage-II.
b) Reaction Chemistry
Stage I
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Stage II
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
c) Process Flow Diagram
Input Qty., kg Out put Qty., kg
Dimethyl Sulphoxide 206.25 Cesium Carbonate 57.20
Diethyl Acetamidomalonate 29.25 Phenyl Ethyl Bromide 12.50
Water 625.00
Water 25.00 Aq. Mother Liquor 935.87
Ethyl Acetate 11.20
Methyl Tertiary Butyl Ether 27.75
Methyl Tertiary Butyl Ether 4.62 Org. Mother Liquor 46.00
Recovered MTBE 3.50
Intemediate Stage-I 13.40
Total 998.77 Total 998.77
Reaction
Process2-ACETAMIDO-2-PHENETHYLPROPANE-1,3-DIYL-DIACETATE STAGE I
Precipitation
Centrifuge
Drying
Intermediate
Reaction
Centrifugation
Wet Cake
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
Input Qty., kg Out put Qty., kg
Ethanol 105.30 Intermediate Stage I 13.40
Calcium chloride dihydrate 15.31 Sodium Borohydride 9.43
Water 66.75
Acetic Acid 21.02 Water 113.50
Sodium Chloride 8.00
Mix Solvent 101.00 Recovery Loss 2.00
Water 26.70 Methylene Chloride 98.48 Aq. Mother Liquor 190.00
Sodium Metabisulphite 8.01 Sodium Bicarbonate 3.34
Recovered Methylene Chloride 190.00
Recovery Loss 6.96
Triethyl Amine 9.70 Acetic Anhydride 9.35
4-Dimethyl Amino Pyridine 1.00
Water 26.70 Methylene Chloride 98.48 Aq. Mother Liquor 44.00
Acetic Acid 7.04
Ethyl Acetate 13.35 Methyl Tertiary Butyl Ether 29.60
Methyl Tertiary-butyl Ether 9.88 Org. Mother Liquor 148.20
Recovered MTBE 2.60
Fingolimod HCl 9.58
Total 694.34 Total 694.34
2-ACETAMIDO-2-PHENETHYLPROPANE-1,3-DIYL-DIACETATE STAGE IIProcess
Reaction
Finished Product
Quenching
Distillation
Work up
Distillation
Reaction mass
Work up
Drying
Purification
Centrifuge
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
d) Summary of Mass Balance
Capacity of Finished Product, TPM : 0.05
Working Days Per Month : 26
Stage IS. No Input Kg/
batch Remarks Output Kg/batch Remarks
1 Phenyl Ethyl Bromide 12.50 Reactant Intermediate Stage-I 13.40 Intermediate
(Stage-I)
2 Diethyl Acetamidomalonate 29.25 Reactant Recovered
MTBE 3.50Sell to authorized recycler
3 Cesium Carbonate 57.20 Reagent Org. Mother Liquor 46.00
Sell to authorized recycler
4 Dimethyl Sulphoxide 206.25 Solvent Aq. Mother Liquor 935.87 To MEE
5 Methyl Tertiary Butyl Ether 32.37 Solvent
6 Ethyl Acetate 11.20 Solvent7 Water 650.00 Media
Total Input 998.77 Total Output 998.77
Stage IIS. No Input Kg/
Batch Remarks Output Kg/Batch Remarks
1 Intermediate Stage-I 13.40 Reactant Intermediate of
Fingolimod HCl 9.58 Finished Product
2 Sodium Borohydride 9.43 Reagent Recovered MTBE 2.60
Sell to authorized recycler
3 Calcium chloride dihydrate 15.31 Reagent Mix Solvent 101.00
Sell to authorized recycler
6 Acetic Acid 28.06 Reagent Recovery Loss 2.00 Solvent Loss
7 Acetic Anhydride 9.35 ReagentRecovered Methylene Chloride
190.00Sell to authorized recycler
8 Triethyl Amine 9.70 Reagent Recovery Loss 6.96 Solvent Loss
9 4-Dimethyl Amino Pyridine 1.00 Reagent Aq. Mother Liquor 234.00 To MEE
10 Methyl Tertiary Butyl Ether 39.48 Solvent Org. Mother
Liquor 148.20Sell to authorized recycler
11 Ethyl Acetate 13.35 Solvent12 Ethanol 105.30 Solvent
13 Methylene Chloride 196.96 Solvent
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
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Manufacturing Process Details
S. No Input Kg/
Batch Remarks Output Kg/Batch Remarks
14 Sodium Chloride 8.00 Washing media
15 Sodium Metabisulphite 8.01 Washing
media
16 Sodium Bicarbonate 3.34 Washing
media17 Water 233.65 Media
Total Input 694.34 Total Output 694.34
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Manufacturing Process Details
E4 SODIUM METHOXIDE
a) Manufacturing Process
By using sodium hydroxide and methanol, prepare solution and distil out solvent and
water by distillation column and finally get desired mass. Reaction of sodium methoxide
with methanol will give sodium methoxide and water. Remove excess methanol and
water by column distillation. Remaining mass will be dry sodium methoxide.
b) Reaction Chemistry
c) Process Flow Diagram
Sodium Hydroxide + Methanol Sodium methoxide +
M.F : NaOH MF : CH3OH M.F : CH3NaOM.W : 40 M.W : 32 M.W : 54
Water
M.F : H2OM.W : 18
Input Qty., kg Out put Qty., kg
Sodium hydroxide 500.0 Methanol 1,580.0
2080 kgMethanol recovery 2,997.0
Methanol 4,000.0 Methanol loss 158.0 Water 225.0
Sodium Methoxide 2,700.0
Total Input 6,080.0 Total Output 6,080.0
ProcessSodium Methoxide
Reaction
Column distillation
Sodium methoxide in Methanol 25 %
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
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Manufacturing Process Details
d) Summary of Mass Balance
Capacity of Finished Product, TPM : 275
Working Days Per Month : 26
S. No Input Kg/
batch Remarks Output Kg/batch Remarks
1 Sodium hydroxide 500.0 Reactant Sodium
Methoxide 2,700.0 Finished Product
2 Methanol (Fresh) 2,583.0 Solvent Methanol
recovery 2,997.0 Sell to authorized recycler OR Reuse
3 Methanol (Recovered) 2,997.0 Recovered
SolventMethanol loss 158.0 Sell to authorized
recyclerEffluent 225.0 To MEE
Total Input 6,080.0 Total Output 6,080.0
Bendamustine stage-I:Condensation of KSM-I (N-1-Methyl-4-nitrobenzene-1,2-diamine) with Glutaric anhydride using sulphuric acid and IPA gave Stage-I.
Bendamustine stage-II:Synthesis of Bendamustine Stage-II by catalytic hydrogenation of Stage-I using Palladium on carbon in methanol as a solvent under H2 gas pressure.
Bendamustine stage-III:Bendamustine Stage-II react with 2-chloroethanol using DIPEA as a base in water and
product isolatied by extraction with dichloromethane followed by distillation and isolation using ethylacetate IPA mixture to get Stage-III.
Bendamustine stage-IV:Chlorination of stage-III with thionyl chloride using dichloromethane as a solvent. Product isolated after work-up, solvent distillation and IPA addition to get pure stage-IV.
Bendamustine stage-V:Hydrolysis of stage-IV using Hydrochloric acid in water to get stage-V as monohydrate Hydrochloride salt of Bendamustine Hydrochloride.
Bendamustine stage-VI:Purifcation of Stage-V using acetonitre,acetone and and aquous HCl mixture to give Bendamustine hydrochride
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ANNEXURE 3 DETAILS OF RAW MATERIALS
REQUIREMENT
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Details of Raw Material Requirement
DETAILS OF RAW MATERIAL REQUIREMENT
Sr. No. Name of Raw Material Product
Code kg/kgRequirement, TPM
Product Wise Total
1 (1R,2R)-Cyclohexane-1,2-Dicarboxylic acid P2 0.950 0.10 0.10
2 [1,2,4]Triazolo[4,3-a]pyridin-3(2H)-one P5 0.667 2.67 2.67
3 1-(3-Chlorophenyl)-piperazine P5 0.807 3.23 3.23
4 1,1’-CarbonyldiimidazoleP1 1.422 1.14
1.36P9 0.45 0.23
5 1,5-bis[di isopropyl-(+)- 4’phenyl -2’-azetidinone-3’- hydroxyl-silyl]pentane
P14 1.25 0.060.13
P15 1.25 0.06
6 10 % Palladium on CarbonP3 0.075 0.04
0.05P4 0.96 0.01
7 2-((4-cyanophenyl)amino) Acetic Acid P1 1.393 1.11 1.11
8 2-(piperazin-1-yl)ethan-1-ol P11 4.78 0.24 0.24
9 2,3-dimethyl-2H-indazol-6-amine hydrochloride (Indazol HCl) P12 1.28 0.08 0.08
10 2,4-dichloropyrimidine P12 1.55 0.09 0.09
11 2-amino-N-(2-chloro-6-methylphenyl)-5-thiazolecarboxamide P11 1.72 0.09 0.09
12 2-chloroethanol P4 5.28 0.05 0.05
13 3-(1-Piperazinyl)-1,2-benzisothiazole P2 0.748 0.07 0.07
14 3-(4-methyl-1H-imidazol-1-yl)-5-(trifluoromethyl)aniline P10 0.85 0.13 0.13
15 3-(dimethylamino)-1-(pyridin-3-yl)prop-2-en-1-one P10 1.07 0.16 0.16
16 3-Chloro -1-propanol P5 0.465 1.86 1.86
17 3-Ethynyl Benzamine P8 0.34 0.03 0.03
184-(1(4-methylpiperaziynl)methyl) benzoic acid dihydrochloride(Acid Compound)
P9 0.86 0.43 0.43
19 4,6-dichloro-2-methyl pyrimidine P11 1.26 0.06 0.06
20 4-chloro-3-(trifluoromethyl) phenyl isocyanate(Isocyanate KSM) P13 0.98 0.10 0.10
214-chloro-pyridine-2-carboxylic acid methyl amide hydrochloride (Amide KSM)
P13 1.26 0.13 0.13
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Details of Raw Material Requirement
Sr. No. Name of Raw Material Product
Code kg/kgRequirement, TPM
Product Wise Total
22 4-Dimethyl Amino Pyridine
P10 0.02 0.0027
0.015P14 0.03 0.0013
P15 0.13 0.01
P17 0.10 0.01
23 4-methyl benzene sulfonic acid monohydrate (PTSA) P13 0.35 0.03 0.03
24 5- Fluoro Cytosine P7 0.44 2.67 2.67
25 5-amino-2-methylbenzenesulfonamide P12 0.61 0.04 0.04
26 5-Deoxy-1,2,3-Tri-O-Acetyl-D-Ribofuranos P7 0.93 5.56 5.56
27 Acetic Acid (Glacial)
P1 5.000 4.00
4.70P3 1.107 0.55
P17 2.93 0.15
28 Acetic AnhydrideP3 1.087 0.54
0.59P17 0.98 0.05
29 Acetone
P1 23.600 18.88
61.08
P2 23.832 2.38
P3 37.152 18.58
P4 27.69 0.28
P6 94.40 18.88
P13 20.85 2.08
30 AcetonitrileP4 23.32 0.23
0.70P12 7.85 0.47
31 Activated Carbon
P1 0.155 0.12
1.01
P2 0.051 0.01
P3 0.176 0.09
P4 0.81 0.01
P5 0.100 0.40
P6 0.12 0.02
P7 0.05 0.28
P8 0.13 0.01
P9 0.11 0.06
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Details of Raw Material Requirement
Sr. No. Name of Raw Material Product
Code kg/kgRequirement, TPM
Product Wise Total
P12 0.06 0.00
P13 0.05 0.01
32 Aluminium Carbonate P1 5.091 4.07 4.07
33 Ammonia Gas P16 0.26 0.01 0.01
34 Ammonia SolutionP9 0.65 0.32
3.34P6 15.10 3.02
35 Ammonium Carbonate P11 0.43 0.02 0.02
36 Ammonium Formate P8 0.45 0.04 0.04
37 Benzoyl Chloride P14 0.76 0.04 0.038
38 Benzyl Amine P3 1.863 0.93 0.93
39 Bezyal Chloroformate P3 6.424 3.21 3.21
40 Calcium chloride dihydrate P17 1.60 0.08 0.08
41 Caustic flakes
P2 0.143 0.01
3.25
P3 0.527 0.26
P5 0.447 1.79
P7 0.19 1.11
P13 0.68 0.07
42 Cesium Carbonate P17 5.97 0.30 0.30
43 Cyclohexane P2 4.238 0.42 0.42
44 Dibenzoyl Lactum P6 6.86 1.37 1.37
45 Diethyl Acetamidomalonate P17 3.05 0.15 0.15
46 Diethyl Ether P14 62.39 3.12 3.12
47 Dihydro-2H-pyran-2,6(3H)-dione P4 6.26 0.06 0.063
48 Dimethyl Carbonate P12 2.54 0.15 0.15
49 Dimethyl Formamide
P2 20.005 2.00
26.35
P5 4.305 17.22
P8 0.17 0.02
P9 3.06 1.53
P10 1.13 0.17
P12 5.08 0.30
P13 0.79 0.08
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Details of Raw Material Requirement
Sr. No. Name of Raw Material Product
Code kg/kgRequirement, TPM
Product Wise Total
P16 100.50 5.03
50 Dimethyl Sulfate P3 1.881 0.94 0.94
51 Dimethyl Sulphoxide P17 21.53 1.08 1.08
52 Ditertiary Butyl Dicarbonate P15 1.75 0.09 0.09
53 D-Serine P3 1.515 0.76 0.76
54 Ethanol
P1 46.920 37.54
43.64
P10 7.33 1.10
P11 81.10 4.06
P12 6.59 0.40
P17 10.99 0.55
55Ethyl 3-(3-amino-4-(methylamino)-N-(pyridin-2-yl)benzamido) propanoate [DAP]
P1 2.000 1.60 1.60
56 Ethyl 3-guanidino-4-methylbenzoate nitrate (KSM-I) P10 1.72 0.26 0.26
57Ethyl- 4,5-bis-(2-methoxyethoxy)-2-amino benzoate hydrochloride (KSM1)
P8 1.24 0.12 0.12
58Ethyl 5-(4-(4-(5-cyano-1H-indol-3-yl)butyl)piperazin-1-yl) benzofuran-2-carboxylate hydrochloride
P16 1.67 0.08 0.08
59 Ethyl Acetate
P1 53.709 42.97
108.97
P3 6.682 3.34
P4 60.19 0.60
P6 102.85 20.57
P7 4.84 29.02
P10 67.24 10.09
P15 45.00 2.25
P17 2.56 0.13
60 Exo-cis-5-norbornene-2,3-dicaroxylic anhydride P2 0.613 0.06 0.06
61 Formamide P8 2.80 0.28 0.28
62 Fumaric Acid P11 1.09 0.05 0.05
63 Hexamethyl Disilazane P6 5.87 1.17 4.51
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Details of Raw Material Requirement
Sr. No. Name of Raw Material Product
Code kg/kgRequirement, TPM
Product Wise Total
P7 0.56 3.33
64 Hexane
P7 3.73 22.40
64.21P14 572.25 28.61
P15 264.00 13.20
65 Hydrochloric Acid
P1 0.169 0.14
18.37
P2 8.194 0.82
P3 8.939 4.47
P4 9.91 0.10
P5 1.111 4.44
P6 21.58 4.32
P7 0.55 3.28
P10 1.03 0.15
P11 1.72 0.09
P12 0.07 0.00
P13 5.70 0.57
66 Hydrogen GasP2 0.006 0.001
0.01P3 0.015 0.01
67 Hyflow
P3 0.121 0.06
0.50
P5 0.088 0.35
P6 0.37 0.07
P8 0.08 0.01
P12 0.08 0.01
68 Isobutyl Chloroformate P3 1.927 0.96 0.96
69 Isopropyl AcetateP1 33.218 26.57
28.17P8 16.00 1.60
70 Isopropyl Alcohol
P1 23.927 19.14
107.95
P4 122.64 1.23
P5 9.944 39.78
P6 54.21 10.84
P7 3.32 19.91
P8 12.69 1.27
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Details of Raw Material Requirement
Sr. No. Name of Raw Material Product
Code kg/kgRequirement, TPM
Product Wise Total
P9 30.88 15.44
P13 3.47 0.35
71 Isopropyl Alcohol HCl P2 0.517 0.05 0.05
74 Maleic Acid P1 1.355 1.08 1.08
75 Methane Sulfonic AcidP1 0.140 0.11
0.20P9 0.18 0.09
76 Methane Sulfonyl ChlorideP2 1.363 0.14
2.73P5 0.493 1.97P6 3.12 0.62
77 Methanol
P1 15.47 12.38
592.69
P2 19.867 1.987
P3 86.061 43.030
P4 638.87 6.39
P5 25.319 101.28
P6 349.49 69.90
P7 7.54 45.24
P8 23.36 2.34
P9 51.88 25.94
P10 34.48 5.17
P11 3.45 0.17P12 97.65 5.86P13 28.00 2.80
P14 31.25 1.56
P15 78.30 3.92
P16 3.85 0.19
P17 29.10 1.46
E4 0.957 263.08
78 Methyl Isobutyl Ketone P1 12.858 10.29 10.29
79 Methyl Tertiary Butyl EtherP2 3.173 0.32
16.28P3 31.171 15.59P17 7.50 0.38
80 Methylene Chloride P1 61.782 49.43 454.92
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Details of Raw Material Requirement
Sr. No. Name of Raw Material Product
Code kg/kgRequirement, TPM
Product Wise Total
P2 23.056 2.31P3 109.352 54.68
P4 341.05 3.41
P7 55.86 335.16
P8 47.00 4.70P13 7.55 0.75P14 23.10 1.16
P15 46.20 2.31
P17 20.56 1.03
81N-(2-methyl-5-aminophenyl)-4-(3-pyridyl)-2-pyrimidine amine (amine compound)
P9 0.65 0.32 0.32
82 N,N-Di Isopropyl Ethyl Amine
P4 9.36 0.09
0.34P10 1.20 0.18
P11 1.36 0.07
83 N,N-Dimethyl Formamide P1 5.655 4.52 4.52
84 N1-Methyl-4-nitrobenzene-1,2-diamine P4 7.35 0.07 0.073
85 N4 Acetyl Cytosine P6 4.19 0.84 0.84
86 n-Butanol P11 18.62 0.93 0.93
87 n-Heptane
P2 4.205 0.42
2.12P4 77.09 0.77
P8 9.28 0.93
88 n-Hexane P2 1.689 0.17 0.17
89 n-Hexyl Chloroformate P1 0.569 0.46 0.46
90 N-Methyl Morpholine P3 1.413 0.71 0.71
91 N-Pentyl Chloroformate P7 0.94 5.61 5.61
92 Oxalyl Chloride P8 0.59 0.06 0.06
93 Palladium on Carbon P2 0.006 0.001 0.001
94 Paracetamol P13 1.38 0.14 0.14
95 Phenyl Ethyl Bromide P17 1.30 0.07 0.07
96 Potassium CarbonateP1 1.195 0.96
4.20P2 0.637 0.06
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Details of Raw Material Requirement
Sr. No. Name of Raw Material Product
Code kg/kgRequirement, TPM
Product Wise Total
P3 5.970 2.98
P4 6.10 0.06
P12 2.14 0.13
P13 0.08 0.01
97 Potassium HydroxideP6 6.35 1.27
1.52P13 2.46 0.25
98 Pyridine P7 0.46 2.78 2.78
99 Silica GelP14 35.00 1.75
3.00P15 25.00 1.25
100 Sodium Bicabonate
P2 0.153 0.02
11.47
P3 0.870 0.43
P4 2.01 0.02
P6 1.12 0.22
P7 1.75 10.50
P10 1.03 0.16
P12 1.64 0.10
P14 0.08 0.00
P17 0.35 0.02
101 Sodium Bicarbonate (aq) P10 22.76 3.41 3.41
102 Sodium Borohydride P17 0.98 0.05 0.05
103 Sodium CarbonateP1 3.000 2.40
2.44P2 0.379 0.04
104 Sodium Chloride
P2 3.800 0.38
2.17P14 1.13 0.06
P15 1.88 0.09P17 0.84 0.04P1 2.000 1.60
105 Sodium hydroxideE4 0.185 50.93
50.99P10 0.44 0.07
106 Sodium Iodide P5 0.061 0.25 0.25
107 Sodium Metabisulphite P17 0.84 0.04 0.04
108 Sodium Sulphate P7 0.93 5.59 5.72
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Details of Raw Material Requirement
Sr. No. Name of Raw Material Product
Code kg/kgRequirement, TPM
Product Wise Total
P14 1.25 0.06
P15 1.25 0.06
109 Sodium Tertiary Butoxide solution (20%) in THF P11 10.86 0.54 0.54
110 Stannic Chloride P7 1.02 6.12 6.12
111 Sulphuric Acid P4 4.34 0.04 0.043
112 Tetrabutyl Ammonium BromideP3 0.176 0.09
0.14P13 0.49 0.05
113 Tetrahydrofuran
P1 31.636 25.31
52.62
P2 3.438 0.34
P3 42.785 21.39
P10 11.38 1.71
P11 25.86 1.29
P13 15.69 1.57
P14 8.89 0.44
P15 11.25 0.56
114 Thionyl ChlorideP4 3.93 0.04
0.11P10 0.44 0.07
115 Toluene
P1 10.764 8.61
82.30
P2 4.942 0.49
P3 35.130 17.56
P5 2.098 8.39
P6 59.70 11.94
P7 5.30 31.82
P8 10.89 1.09
P10 15.93 2.39
116 Trimethyl Silyl ChlorideP6 0.17 0.03
0.45P7 0.07 0.41
117 Triethyl Amine
P2 1.376 0.14
5.52P3 1.026 0.51
P5 1.011 4.04
P6 3.67 0.73
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Details of Raw Material Requirement
Sr. No. Name of Raw Material Product
Code kg/kgRequirement, TPM
Product Wise Total
P14 0.82 0.04
P17 1.01 0.05
118 Trimethyl Silyl Triflate P6 6.48 1.30 1.30
119 Urea P2 0.124 0.01 0.012
120 Vitride/SynhydridP6 4.32 0.86
1.46P2 5.985 0.60
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ANNEXURE 4 DETAILS OF STORAGE OF PRODUCTS
& RAW MATERIALS
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Details of Product & Raw Materials Storage
DETAILS OF PRODUCTS & RAW MATERIAL STORAGE
� DETAILS OF PRODUCT STORAGE
Sr. No.
Name of Raw Material CAS Nos. Physical
FormType Of
Packing / Storage
Storage tank/ Container Max.
Storagecapacity
(MT)
Storage Pressure
Storage Temp Market Mode of
TransportSize (MT) Nos.
P1 Dabigatran Etexilate Mesylate 872728-81-9 Solid HDPE Drum 0.025 32 0.800 Atmosphere 2 to
8° CDomestic/
Export Road/Air/Sea
P2 LurasidoneHCl 367514-88-3 Solid HDPE Drum 0.025 4 0.100 Atmosphere NMT 25° C
Domestic/Export Road/Air/Sea
P3 Lacosamide 175481-36-4 Solid HDPE Drum 0.025 20 0.500 Atmosphere NMT 25° C
Domestic/Export Road/Air/Sea
P4 BendamustineHCl 3543-75-7 Solid HDPE Drum 0.010 1 0.010 Atmosphere NMT 25° C
Domestic/Export Road/Air/Sea
P5 Trazodone HCl 25332-39-2 Solid HDPE Drum 0.025 160 4.000 Atmosphere NMT 25° C
Domestic/Export Road/Air/Sea
P6 Gemcitabine HCl 12211-03-9 Solid HDPE Drum 0.025 8 0.200 Atmosphere NMT 25° C
Domestic/Export Road/Air/Sea
P7 Capecitabine 154361-50-9 Solid HDPE Drum 0.025 240 6.000 Atmosphere NMT 25° C
Domestic/Export Road/Air/Sea
P8 Erlotinib HCl 183319-69-9 Solid HDPE Drum 0.025 4 0.100 Atmosphere NMT 25° C
Domestic/Export Road/Air/Sea
P9 Imatinib Mesylate Alpha 220127-57-1 Solid HDPE Drum 0.025 25 0.500 Atmosphere NMT
25° CDomestic/
Export Road/Air/Sea
P10 Nilotinib 641571-10-0 Solid HDPE Drum 0.025 6 0.150 Atmosphere NMT 25° C
Domestic/Export Road/Air/Sea
P11 Dasatinib 302962-49-8 Solid HDPE Drum 0.025 2 0.050 Atmosphere NMT 25° C
Domestic/Export Road/Air/Sea
P12 Pazopanib HCl 635702-64-6 Solid HDPE Drum 0.025 3 0.060 Atmosphere NMT 25° C
Domestic/Export Road/Air/Sea
P13 Sorafenib 475207-59-1 Solid HDPE Drum 0.025 4 0.100 Atmosphere NMT 25° C
Domestic/Export Road/Air/Sea
P14 N-BZ-Bis-Lactam -- Viscous Liquid HDPE Drum 0.005 10 0.050 Atmosphere 2 to 8°
CDomestic/
Export Road/Air/Sea
P15 N-BOC-Bis-Lactam -- Viscous Liquid HDPE Drum 0.005 10 0.050 Atmosphere 2 to 8°
CDomestic/
Export Road/Air/Sea
P16
5-(4-(4-(5-Cyano-1H-indol-3-yl)-butyl)-piperazin-1-yl)benzofuran-2-carboxamide [Intermediate for Vilazodone]
-- Liquid HDPE Drum 0.200 01 0.050 Atmosphere NMT 25° C
Domestic/Export Road/Air/Sea
P17
2-acetamido-2-phenethylpropane-1,3-diyl-diacetate [Intermediate for Fingolimod]
-- Solid HDPE Drum 0.025 2 0.050 Atmosphere NMT 25° C
Domestic/Export Road/Air/Sea
� DETAILS OF RAW MATERIAL STORAGE
Sr. No.
Name of Raw Material CAS Nos. Physical
FormType Of
Packing / Storage
Storage tank/ Container Max.
Storage capacity
(MT)
Storage Pressure
Storage Temp Source Mode of
TransportSize (MT) Nos.
1 (1R,2R)-Cyclohexane-1,2- Dicarboxylic acid 2305-32-0 Solid Carboy 0.025 4 0.100 Atm. Ambient Import Air / Sea /
Road
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Details of Product & Raw Material Storage
Sr. No.
Name of Raw Material CAS Nos. Physical
FormType Of
Packing / Storage
Storage tank/ Container Max.
Storage capacity
(MT)
Storage Pressure
Storage Temp Source Mode of
TransportSize (MT) Nos.
2 [1,2,4]Triazolo[4,3-a]pyridin-3(2H)-one 6969-71-7 Solid HDPE Drum 0.100 10 1.000 Atm. Ambient Domestic Road
3 1-(3-Chlorophenyl)-piperazine 13078-15-4 Solid HDPE Drum 0.100 10 1.000 Atm. Ambient Domestic Road
4 1,1’-Carbonyldiimidazole 530-62-1 Solid Fiber Drum 0.025 20 0.500 Atm. Ambient Domestic Road
5
1,5-bis[di isopropyl-(+)-4’phenyl -2’-azetidinone-3’-hydroxyl-silyl]pentane
-- Liquid HDPE Container 0.005 10 0.050 Atm. 2 - 8 °C Domestic Air / Sea /
Road
6 10 % Palladium on Carbon
Carbon: 7440-40-0Palladium: 7440-05-3
Solid Carboy 0.005 3 0.015 Atm. Ambient Domestic Road
72-((4-cyanophenyl)amino) Acetic Acid
42288-26-6 Solid Fiber Drum 0.025 16 0.400 Atm. Ambient Domestic Road
8 2-(piperazin-1-yl)ethan-1-ol 103-76-4 Liquid HDPE Drum 0.050 5 0.250 Atm. 23-27
°CDomestic / Import
Air / Sea / Road
9
2,3-dimethyl-2H-indazol-6-amine hydrochloride (IndazolHCl)
635702-60-2 Solid HDPE Container 0.025 1 0.025 Atm. 23-27
°C Domestic Road
10 2,4-dichloropyrimidine 3934-20-1 Solid HDPE Container 0.025 1 0.025 Atm. 2 - 8 °C Domestic Road
112-amino-N-(2-chloro-6-methylphenyl)-5-thiazolecarboxamide
302964-24-5 Solid HDPE Container 0.050 2 0.100 Atm. 23-27
°CDomestic / Import
Air / Sea / Road
12 2-chloroethanol 107-07-3 0.050 1 0.050
13 3-(1-Piperazinyl)-1,2-benzisothiazole 87691-87-0 Solid HDPE Drum 0.025 1 0.025 Atm. 23-27
°C Domestic Road
143-(4-methyl-1H-imidazol-1-yl)-5-(trifluoromethyl)aniline
-- Solid HDPE Container 0.050 1 0.050 Atm. 23-27
°C Domestic Road
153-(dimethylamino)-1-(pyridin-3-yl)prop-2-en-1-one
123367-26-0 Solid HDPE Container 0.050 1 0.050 Atm. 23-27
°C Domestic Road
16 3-Chloro -1-propanol 627-30-5 Liquid HDPE Drum 0.050 1 0.050 Atm. Ambient Domestic Road
17 3-Ethynyl Benzamine 54060-30-9 Solid Carboy 0.005 8 0.040 Atm. Ambient Imported Air / Sea / Road
18
4-(1(4-methylpiperaziynl)methyl) benzoic acid dihydrochloride(Acid Compound)
-- Solid Fiber Drum 0.100 5 0.500 Atm. Ambient Imported Air / Sea / Road
19 4,6-dichloro-2-methyl pyrimidine 1780-26-3 Solid HDPE
Container 0.020 1 0.020 Atm. 23-27°C Domestic Air / Sea /
Road
20
4-chloro-3-(trifluoromethyl) phenyl isocyanate(Isocyanate KSM)
327-78-6 Solid HDPE Container 0.010 4 0.040 Atm. 2 - 8 °C Domestic Road
21
4-chloro-pyridine-2-carboxylic acid methyl amide hydrochloride (Amide KSM)
-- Solid Drum 0.010 5 0.050 Atm. Ambient Domestic Road
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Details of Product & Raw Materials Storage
Sr. No.
Name of Raw Material CAS Nos. Physical
FormType Of
Packing / Storage
Storage tank/ Container Max.
Storage capacity
(MT)
Storage Pressure
Storage Temp Source Mode of
TransportSize (MT) Nos.
22 4-Dimethyl Amino Pyridine 1122-58-3 Solid HDPE
Container 0.025 1 0.015 Atm. Ambient Domestic Road
234-methyl benzene sulfonic acid monohydrate (PTSA)
6192-52-5 Solid Bag 0.005 2 0.010 Atm. Ambient Domestic Road
24 5- Fluoro Cytosine 2022-85-7 Solid Fiber Drum 0.025 1 0.025 Atm. 2 - 8 °C Imported Air / Sea / Road
255-amino-2-methylbenzenesulfonamide
3934-20-1 Solid HDPE Container 0.015 1 0.015 Atm. 23-27
°C Domestic Road
26 5-Deoxy-1,2,3-Tri-O-Acetyl-D-Ribofuranos 6974-32-9 Solid HDPE
Container 1.000 5 5.000 Atm. 2 - 8 °C Domestic / Import
Air / Sea / Road
27 Acetic Acid (Glacial) 64-19-7 Liquid Carboy 0.250 6 1.500 Atm. Ambient Domestic Road
28 Acetic Anhydride 108-24-7 Liquid HDPE Carboy 0.050 4 0.200 Atm. Ambient Domestic Road
29 Acetone 67-64-1 Liquid MS Drum 2 5 10.000 Atm. Ambient Domestic Road
30 Acetonitrile 75-05-8 Liquid Drum 0.200 1 0.200 Atm. Ambient Domestic Road
31 Activated Carbon 7440-44-0 Solid Bag 0.050 6 0.300 Atm. Ambient Domestic Road
32 Aluminium Carbonate 1339-92-0 Solid Bag 0.500 3 1.500 Atm. Ambient Domestic Road
33 Ammonia Gas 7664-41-7 Gas Cylinder 0.001 5 0.005 Atm. Ambient Domestic Road
34 Ammonia Solution 7664-41-7 Liquid Carboy 0.200 6 1.200 Atm. Ambient Domestic Road
35 Ammonium Carbonate 506-87-6 Solid HDPE Container 0.005 2 0.010 Atm. Ambient Domestic Road
36 Ammonium Formate 540-69-2 Solid Fiber Drum 0.015 1 0.015 Atm. Ambient Domestic Road
37 Benzoyl Chloride 98-88-4 Liquid Bottle 0.015 1 0.015 Atm. Ambient Domestic Road
38 Benzyl Amine 100-46-9 Liquid Carboy 0.100 4 0.400 Atm. Ambient Domestic Road
39 Bezyal Chloroformate 501-53-1 Liquid HDPE Drum 0.600 2 1.200 Atm. 2 - 8 °C Domestic Road
40 Calcium chloride dihydrate 10035-04-8 Solid HDPE
Container 0.025 1 0.025 Atm. Ambient Domestic Road
41 Caustic flakes 1310-73-2 Solid Bag 0.100 10 1.000 Atm. Ambient Domestic Road
42 Cesium Carbonate 534-17-8 Solid HDPE Container 0.025 4 0.100 Atm. Ambient Domestic Road
43 Cyclohexane 110-82-7 Liquid HDPE Drum 0.150 1 0.150 Atm. Ambient Domestic Road
44 Dibenzoyl Lactum 122111-01-7 Solid HDPE COntainer 0.050 10 0.500 Atm. Ambient Imported Air / Sea /
Road
45 Diethyl Acetamidomalonate 1068-90-2 Solid HDPE
Container 0.025 2 0.050 Atm. Ambient Domestic Air / Sea / Road
46 Diethyl Ether 60-29-7 Liquid Drum 0.200 5 1.000 Atm. Ambient Domestic Road
47 Dihydro-2H-pyran-2,6(3H)-dione 108-55-4 Solid Drum 0.020 1 0.020 Atm. Ambient Domestic Road
48 Dimethyl Carbonate 616-38-6 Liquid Carboy 0.050 1 0.050 Atm. Ambient Domestic Road
49 Dimethyl Formamide 68-12-2 Liquid HDPE Drum 2.000 5 10.000 Atm. Ambient Domestic Road
50 Dimethyl Sulfate 77-78-1 Liquid HDPE Drum 0.200 2 0.400 Atm. Ambient Domestic Road
51 Dimethyl Sulphoxide 67-68-5 Liquid HDPE Drum 0.200 2 0.400 Atm. Ambient Domestic Road
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Details of Product & Raw Material Storage
Sr. No.
Name of Raw Material CAS Nos. Physical
FormType Of
Packing / Storage
Storage tank/ Container Max.
Storage capacity
(MT)
Storage Pressure
Storage Temp Source Mode of
TransportSize (MT) Nos.
52 Ditertiary Butyl Dicarbonate 24424-99-5 Liquid Bottle 0.015 2 0.030 Atm. 2 - 8 °C Domestic Road
53 D-Serine 312-84-5 Solid HDPE Drum 0.050 16 0.800 Atm. Ambient Imported Air / Sea / Road
54 Ethanol 64-17-5 Liquid HDPE Drum 5.000 2 10.000 Atm. Ambient Domestic Road
55
Ethyl 3-(3-amino-4-(methylamino)-N-(pyridin-2-yl)benzamido) propanoate [DAP]
212322-56-0 Solid Fiber Drum 0.050 12 0.600 Atm. Ambient Domestic Road
56Ethyl 3-guanidino-4-methylbenzoate nitrate (KSM-I)
641569-96-2 Solid HDPE Container 0.025 4 0.100 Atm. 23-27
°C Domestic Road
57
Ethyl- 4,5-bis-(2-methoxyethoxy)-2-amino benzoate hydrochloride (KSM1)
183322-17-0 Solid Fiber Drum 0.025 6 0.150 Atm. Ambient Imported Air / Sea / Road
58
Ethyl 5-(4-(4-(5-cyano-1H-indol-3-yl)butyl)piperazin-1-yl) benzofuran-2-carboxylate hydrochloride
163521-11-7 Solid Bag 0.025 1 0.025 Atm. Ambient Domestic Road
59 Ethyl Acetate 141-78-6 Liquid HDPE Drum 5.000 5 25.000 Atm. Ambient Domestic Road
60Exo-cis-5-norbornene-2,3-dicaroxylic anhydride
129-64-6 Solid Fiber Drum 0.025 2 0.050 Atm. Ambient Imported Air / Sea / Road
61 Formamide 75-12-7 Liquid Drum 0.100 1 0.100 Atm. Ambient Domestic Road
62 Fumaric Acid 110-17-8 Solid HDPE Container 0.020 1 0.020 Atm. Ambient Domestic Road
63 Hexamethyl Disilazane 999-97-3 Liquid HDPE Container 0.250 6 1.500 Atm. Ambient Domestic Road
64 Hexane 110-54-3 Liquid Drum 2.000 6 12.000 Atm. Ambient Domestic Road
65 Hydrochloric Acid 7647-01-0 & 7732-18-5 Liquid Drum 2.000 4 8.000 Atm. Ambient Domestic Road
66 Hydrogen Gas 1333-74-0 Gas Cylinder 0.00100 5.0 0.005 Atm. Ambient Domestic Road
67 Hyflow 14464-46-1 Solid Bag 0.050 4 0.200 Atm. Ambient Domestic Road
68 Isobutyl Chloroformate 543-27-1 Liquid Carboy 0.025 12 0.300 Atm. 2 - 8 °C Domestic Road
69 Isopropyl Acetate 108-21-4 Liquid HDPE Drum 2.000 5 10.000 Atm. Ambient Domestic Road
70 Isopropyl Alcohol 67-63-0 Liquid MS Drum 5.000 4 20.000 Atm. Ambient Domestic Road
71 Isopropyl Alcohol HCl 7647-01-0 Liquid Carboy 0.020 1 0.020 Atm. 23-27°C Domestic Road
72 Maleic Acid 110-16-7 Solid Bag 0.025 10 0.250 Atm. Ambient Domestic Road
73 Methane Sulfonic Acid 75-75-2 Liquid Carboy 0.050 1 0.050 Atm. Ambient Domestic Road
74 Methane Sulfonyl Chloride 124-63-0 Liquid HDPE Drum 0.250 4 1.000 Atm. Ambient Domestic Road
75 Methanol 67-56-1 Liquid MS Tank 20.000 4 80.000 Atm. Ambient Domestic Road
76 Methyl Isobutyl Ketone 108-10-1 Liquid MS Drum 1.000 4 4.000 Atm. Ambient Domestic Road
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment ReportProposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Details of Product & Raw Materials Storage
Sr. No.
Name of Raw Material CAS Nos. Physical
FormType Of
Packing / Storage
Storage tank/ Container Max.
Storage capacity
(MT)
Storage Pressure
Storage Temp Source Mode of
TransportSize (MT) Nos.
77 Methyl Tertiary Butyl Ether 1634-04-4 Liquid MS Drum 2.000 3 6.000 Atm. Ambient Domestic Road
78 Methylene Chloride 75-09-2 Liquid HDPE Tank 20.000 5 100.000 Atm. Ambient Domestic Road
79
N-(2-methyl-5-aminophenyl)-4-(3-pyridyl)-2-pyrimidine amine (amine compound)
152460-10-1 Solid Fiber Drum 0.040 10 0.400 Atm. Ambient Imported Air / Sea / Road
80 N,N-Di Isopropyl Ethyl Amine 7087-68-5 Liquid HDPE
Container 0.025 4 0.100 Atm. 23-27°C Domestic Road
81 N,N-Dimethyl Formamide 68-12-2 Liquid HDPE Drum 0.150 10 1.500 Atm. Ambient Domestic Road
82N1-Methyl-4-nitrobenzene-1,2-diamine
41939-61-1 Solid Drum 0.010 3 0.030 Atm. Ambient Domestic Road
83 N4 Acetyl Cytosine 14631-20-0 Solid Drum 0.250 4 1.000 Atm. Ambient Imported Air / Sea / Road
84 n-Butanol 71-36-3 Liquid HDPE Drum 0.150 2 0.300 Atm. Ambient Domestic Road
85 n-Heptane 142-82-5 Liquid MS Drum 0.100 5 0.500 Atm. Ambient Domestic Road
86 n-Hexane 110-54-3 Liquid MS Drum 0.020 3 0.060 Atm. Ambient Domestic Road
87 n-Hexyl Chloroformate 6092-54-2 Liquid Carboy 1.500 0 0.150 Atm. 23-27°C Domestic Road
88 N-Methyl Morpholine 109-02-4 Liquid Carboy 0.050 5 0.250 Atm. Ambient Domestic Road
89 N-Pentyl Chloroformate 638-41-5 Liquid HDPE
Container 1.000 2 2.000 Atm. 23-27°C Domestic Road
90 Oxalyl Chloride 79-37-8 Solid Drum 0.025 1 0.025 Atm. Ambient Domestic Road
91 Palladium on Carbon
Carbon: 7440-40-0Palladium: 7440-05-3
Solid Drum 0.0001 2 0.000 Atm. Ambient Domestic Road
92 Paracetamol 103-90-2 Solid Drum 0.025 2 0.050 Atm. 23-27°C Domestic Road
93 Phenyl Ethyl Bromide 103-63-9 Liquid HDPE Carboy 0.025 3 0.075 Atm. Ambient Domestic
/ Import Road
94 Potassium Carbonate 584-08-7 Solid Bag 0.500 3 1.500 Atm. Ambient Domestic Road
95 Potassium Hydroxide 1310-58-3 Solid Bag 0.200 3 0.600 Atm. Ambient Domestic Road
96 Pyridine 110-86-1 Liquid Drum 0.250 4 1.000 Atm. Ambient Domestic Road
97 Silica Gel 63231-67-4 Solid Fiber Drum 0.250 4 1.000 Atm. Ambient Domestic Road
98 Sodium Bicarbonate 144-55-8 Solid HDPE Container 0.500 10 5.000 Atm. Ambient Domestic Road
99 Sodium Bicarbonate (aq) 144-55-8 Liquid Drum 0.300 5 1.500 Atm. Ambient Domestic Road
100 Sodium Borohydride 16940-66-2 Solid HDPE Container 0.020 1 0.020 Atm. Ambient Domestic Road
101 Sodium Carbonate 497-19-8 Solid Bag 0.250 4 1.000 Atm. Ambient Domestic Road
102 Sodium Chloride 7647-14-5 Solid Bag 0.050 4 0.200 Atm. Ambient Domestic Road
103 Sodium hydroxide 1310-73-2 Solid HDPE Container 5.000 4 20.000 Atm. Ambient Domestic Road
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Intas Pharmaceuticals Ltd., Valia-BharuchEnvironmental Impact Assessment Report
Proposed Expansion Project for Manufacturing of Synthetic Organic Chemicals
Details of Product & Raw Material Storage
Sr. No.
Name of Raw Material CAS Nos. Physical
FormType Of
Packing / Storage
Storage tank/ Container Max.
Storage capacity
(MT)
Storage Pressure
Storage Temp Source Mode of
TransportSize (MT) Nos.
104 Sodium Iodide 7681-82-5 Solid Fiber Drum 0.025 4 0.100 Atm. Ambient Domestic Road
105 Sodium Metabisulphite 7681-57-4 Solid HDPE Container 0.015 1 0.015 Atm. Ambient Domestic Road
106 Sodium Sulphate 7757-82-6 Solid HDPE Drum 0.500 5 2.500 Atm. Ambient Domestic Road
107Sodium Tertiary Butoxide solution (20%) in THF
109-99-9 Liquid HDPE Drum 0.200 1 0.200 Atm. 23-27°C Domestic Road
108 Stannic Chloride 7646-78-8 Liquid PTFE Container 0.500 4 2.000 Atm. Ambient Domestic Road
109 Sulphuric Acid 7664-93-9 Liquid MS Drum 0.010 1 0.010 Atm. Ambient Domestic Road
110 Tetrabutyl Ammonium Bromide 1643-19-2 Solid HDPE
Container 0.025 2 0.050 Atm. Ambient Domestic Road
111 Tetrahydrofuran 109-99-9 Liquid HDPE Drum 2.000 5 10.000 Atm. Ambient Domestic Road
112 Thionyl Chloride 7719-09-7 Liquid MS Container 0.025 1 0.025 Atm. Ambient Domestic Road
113 Toluene 108-88-3 Liquid MS Drum 5.000 4 20.000 Atm. Ambient Domestic Road
114 Trimethyl Silyl Chloride 75-77-4 Liquid Drum 0.100 2 0.200 Atm. Ambient Domestic Road
115 Triethyl Amine 121-44-8 Liquid MS Drum 0.500 4 2.000 Atm. Ambient Domestic Road
116 Trimethyl Silyl Triflate 27607-77-8 Solid Drum 0.250 4 1.000 Atm. Ambient Domestic / Import Road
117 Urea 57-13-6 Solid Bag 0.005 1 0.005 Atm. Ambient Domestic Road
118 Vitride / Synhydrid 22722-98-1 Solid Container 0.200 2 0.400 Atm. 23-27°C Domestic Road
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ANNEXURE 5 LAYOUT PLAN
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100.0 0.0
10.0
20.0
30.0
40.0
50.0
60.0
70.0
80.0
90.0
100.0
110.0
120.0
130.0
140.0
150.0
160.0
170.0
180.0
190.0
200.0
210.0
220.0
230.0
240.0
250.0
260.0
270.0
280.0
290.0
0.0
10.0
HOUSE
20.0
30.0
40.0
50.0
60.0
70.0
80.0
90.0
110.0
120.0
130.0
140.0
150.0
genation
Security Cabin
UG TANK
VILLAGE ROAD
Blo
ck B
BOILER
UTILITY BLOCK
Tra
nsf
orm
er
area
Blo
ck C
19.3
0
IPL-01DRG.NO.-
REM
ARKS
INTAS PHARMACEUTICALS LTD.N
SCALE : 1 CM=5 M
Hydro
shedshed
PROPOSED BLOCK-I
55X34
CERAMATIC BLOCK-D
METHAONALDAY TANK
STORE FOR DAYDTOCK
28X16
PROPOSED WAREHOUSE
45X33
SOLVANT STORAGE( ABOVE GROUND)
25X25
HOUSE
BOILER
FUEL STORAGE
DA
Y S
TO
RE
FO
RE
BL
OC
K C
& P
P
45X17
PROPOSED BLOCK
ST
OR
AG
E F
OR
S
MO
SCRAPE YARD
FIRE HYDRAUNT POINT
PROPOSED ADMIN,
QA & QC
20 X 32
PROPOSED SITE PLAN @ VALIA .
PROPOSED BLOCK
PROPOSED BLOCK
UG TANK
(FIRE HYDRAUNT)
BLOCK-A
FIRE HYDRAUNT LINE
LEGEND DESCRIPTION
GENERAL PARKING
GA
TE
1
GA
TE
2
SURVEY NO. 128
SURVEY NO. 130
SURVEY NO. 129
SURVEY NO. 121
SURVEY NO. 122
TRANSPORT VEHICLE
PARKING
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ANNEXURE 6 ACKNOWLEDGEMENT OF CGWA
APPLICATION SLIP
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RECEIPTTransaction Ref.No. 0611170001166 Dated: Nov 4 2017 8:11PM
Received from M/S. INTAS PHARMACEUTICALS LTD with Transaction Ref.No. 0611170001166 Dated Nov 4 2017 8:11PM the sum of INR 1000 (One Thousand Only ) through Internet basedOnline payment in the account of PROCESSING FEE OF FRESH NOC FOR GROUND WATER EXTRACTION, , APPLICATION NO - 21-4/2635/GJ/IND/2017.Disclaimer:- This is a system generated electronic receipt, hence no physical signature is required for the purpose of authentication
Printed On: 06-11-2017 03:9:09
Courtesy :- Controller General of Accounts
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ANNEXURE 7 COPY OF MEMBERSHIP
(NECL, BEIL) & LOI (RSPL)
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ANNEXURE 8 DETAILS OF FLY ASH GENERATION
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ANNEXURE 9 COPIES OF CONSENT TO
ESTABLISH
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Outward NNNNo:42225555577771111111111,,,,1111177777////1111100000/////222220000011117
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Outward No:42577771111111111,1111177777/////1111100000/////2222200000111117
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Outward No:425711,177777///10/2017
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Outwarrrrd No:3777777444445555511111,,,0000077777/////1111122222/////22222000001111166666
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Outward No:37777444445555511111,,,,,0000077777/////1111122222/////22222000001111166666
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Outward No:377451,07/12/2016
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A-197
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A-200
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A-201
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Outward NNNNNoo:::::4444411111144442222266666,04///0000055555/////2222000001111177777
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Outward No:411426,04/05/201111777
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In exercise of the power conferred under section-25 of the Water (Prevention and Control of Pollution) Act-1974, under section-21 of the Air (Prevention and Control of Pollution)Act-1981 and Authorization under rule 3(c)& 5(5)of the Hazardous Waste (Management, Handling and Transboundary Movement)Rules’2008 framed under the E(P)Act-1986.
/Survey No.44-B,, Village : Naldhari,Ta: Valia,City : Naldhari,Dist : Ankleshwar, Tal : Valia, SIDC : Not In GidcPhone : 270389
Besides streamlining and simplifying of regulatory regime,Gujarat Pollution Control Board has taken initiative in from of introduction of Consolidated Consent and Authorization (CC&A) which provides for a one shot application and clearance of the consents under Water Act,Air Act and Authorization under Hazardous Wastes Rules for a period of 5 years.
CConsolidated Consent and Authorisation
CCONSENT AND AUTHORISATION :
And whereas Board has received consolidated Application No.(CtO:CCA-Ammendment) 116333 and Dated 21/12/2016 for the consolidated consent and authorization(CC&A) of this Board under the provisions / rules of the aforesaid Acts Consent & Authorization is hereby granted as under.
Board issues consolidated consent and Authorization to an industrial unit for operation of plant/carrying out industrial activity specifying following conditions.
(under the provisions / rules of the aforesaid environmental acts)
Consented CETP: Not Linked to any CETP
2.
( Member Secretary )
For and on behalf ofGujarat Pollution Control Board
PPCB Id:15887Application : CtO:CCA-Ammendment, No. 116333 Dt. 21/12/2016, Granted On: 10/04/2017
3. GENERAL CONDITIONS :-a) This order is provisional order and detailed order is considered as final.b) All the conditions & provisions under the Water Act 1974, the Air Act 1981 and the Environment (Protection) Act – 1986 and the rules made there under shall be complied with *.c) All the conditions & provisions under the Hazardous Waste (Management, Handling and Trans boundary Movement) Rules 2008 as amended shall be compliedd) The applicant shall provide portholes, ladder, platform etc at chimney(s) for monitoring the air emissions and the same shall be open for inspection to/and for use of Board’s staff. The chimney(s) vents attached to various sources of emission shall be designed by numbers such as S-1, S-2, etc. and these shall be painted/ displayed to facilitate identification.e) The industry shall take adequate measures for control of noise levels from its own sources within the premises so as to maintain ambient air quality standards in respect of noise to less than 75dB(A) during day time and 70dB(A) during night time. Daytime is reckoned in between 6 a.m. and 10 p.m. and nighttime is reckoned between 10 p.m. and 6 a.m.f) In case of change of ownership/management the name and address of the new owners/ partners/ directors/ proprietor or equipment or working conditions as mentioned in the consents form / order should immediately be intimated to the Board.g) Industry shall have to display data outside the main factory gate with regard to quantity and nature of hazardous chemicals being handled in the plant, including waste water and air emissions and solid hazardous wastes generated within the factory premises.h) The CCA shall be produced for inspection at the request of an officer authorized by the Gujarat Pollution Control Board.i) Any unauthorized change in personnel, equipment or working conditions as mentioned in the CCA order by CCA holder shall constitute a breach of this CCA.j) Adequate plantation shall be carried out all along the periphery of the industrial premises in such a way that the density of plantation is atleast 1000 trees per acre of land and a green belt of 5 meters width is developed.K) The applicant shall have to submit the returns in prescribed form regarding water consumption and shall have to make payment of water cess to the Board under the Water Cess Act- 1977.
Consented TSDF: B.E.I.L, Ankleshwar [14983]
*** Note : ACT-Specific, Industry-specific, Area-specific Conditions alongwith Product, Waste water effluent details shall be precisely mentioned in the DETAILED Consent Order.
*** Note :This is only provisional communication. The final Consent/Authorization in hard copy with duly signed by competent authority shall the final and valid Consent/Authorization.
M/s. Intas Pharmaceuticals Ltd Formerly Zora Pharma Limited,To,
All Conditions under the AIR ACT-1981 WATER ACT-1974 HAZARDOUS ACT-2008 shall be Applicable to you as mentioned in the detailed Consent Order ***
Consent Order No:1. AWH-85219 Valid Upto: 01/11/2017
Computer generated Order thru XGN, does NOT require Physical Signature N CIPrinted On : 10/04/2017
Gujarat Pollution Control BoardParyavaran Bhavan, Sector-10/A,
Gandhinagar - 382010Tele : 23222756
Consent No. AWH-85219 Valid upto: 01/11/2017
Provisional Consent Order (CCA)
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