LIST OF ANNEXURES S. No Content...
Transcript of LIST OF ANNEXURES S. No Content...
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LIST OF ANNEXURES
S. No Content Annexure
1 List of Proposed Products & By-Products Annexure - I
2 Site Plan Annexure - II
3 Manufacturing Process Description Annexure - III
4 Water Consumption Details Annexure - IV
5 Solid & Hazardous Waste Generation And
Disposal Annexure -V
6 Stack Emission Details Annexure - VI
7 Process Emission Details Annexure -VII
8 List of Raw Materials Annexure - VIII
9 Waste water Details Annexure - IX
10 Consolidated Statement- Pollution Details Annexure –X
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ANNEXURE – I
LIST OF PROPOSED PRODUCTS
S
No Product name
Quantity in
Tonne /
Month
CAS no Therapeutic
category
1 Carvedilol 10 72956-09-3 Antihypertensive
2 Cyano diol hydrochloride 5 717133-25-0 Drug
intermediate
3 Dabigatran 5 211915-06-9 Anticoagulant
4 Fexofenadine hydrochloride 10 153439-40-8 Anti allergic
5 Fluconazole 10 88386-73-4 Antifungal
6 Folic acid 20 59-50-3 Hematinic (Vit-B)
7 Itraconazole 10 84625-61-6 Antifungal
8 Ketoconazole 10 65277-42-1 Antifungal
9 Levocetirizine dihydrochloride 5 130018-77-8 Antihistamine
10 Linagliptin 5 668270-12-0 Anti diabetic
11 Meropenem 5 119478-56-7 Antibacterial
12 Montelukast sodium 2 151767-02-1 Anti asthmatic
13 Rosuvastatin calcium 2 147098-20-2 Anti lipemic
agent
14 Sitagliptin Phosphate Monohydrate 5 654671-77-9 Anti Diabetic
15 Teneligliptin 5 760937-92-6 Anti Diabetic
16 Tri butyl tin chloride 5 1461-22-9 Organic Reagent
17 Valacyclovir Hydrochloride
Monohydrate 10 124832-27-5 Anti Viral
18 Vildagliptin 5 274901-16-5 Anti diabetic
Total 129
LIST OF BY-PRODUCTS
S.
No
Name of the Product
Name of the By-Product
Quantity
in Kg/Day
1
Itraconazole
Hydrochloric acid(17%) 6228
Ketoconazole
Fluconazole
Folic Acid
Fexofenadine Hydrochloride
Linagliptin
Levocetirizine Dihydrochloride
Dabigartan
Tri Butyl Tin Chloride
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S.
No
Name of the Product
Name of the By-Product
Quantity
in Kg/Day
Vildagliptin
Rosuvastatin Calcium
2
Itraconazole Hydrobromic acid(17%)
960
Ketoconazole
Linagliptin
Dabigartan
3
Fluconazole Aluminium chloride Solution
(Aluminum
hydroxide+water)(12%) 1652
Fexofenadine Hydrochloride
4 Fluconazole Triethyl amine hydrochloride 313 Levocetirizine Dihydrochloride
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ANNEXURE - II SITE PLAN
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ANNEXURE - III
MANUFACTURING PROCESS DESCRIPTION
1.CARVEDILOL
Process Description:
Stage-1
Phenyl hydrazine Hydrochloride reacts with 1, 3-Cyclohexanedione in the presence
of Methanol to give Stage-1 product.
Stage-2
Stage-1 product undergoes dehydrogenation by using Raney nickel as catalyst in
presence of Methanol to give Stage-2 product.
Stage-3
Stage-2 product reacts with Epichlorohydrin and sodium hydroxide in the presence
of methanol to give Stage-3 product.
Stage-4
Stage-3 product reacts with 2-(2-Methoxyphenoxy) ethyl amine in the presence of
Iso propyl alcohol to give Carvedilol product.
CARVEDILOL
Route of Synthesis:
Stage-1
NH NH2
HCl
Phenyl hydrazine Hydrochloride
C6H8N2.HCl
144.60
+ OO
1,3-Cyclohexanedione
C6H8O2
112.13
MethanolNH
O
1,2,3,9-Tetrahydro-carbazol-4-one
C12H11NO
185.22+ H2O
+
18.02
NH4Cl
.
53.49
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Stage-2
NH
O
1,2,3,9-Tetrahydro-carbazol-4-one
C12H11NO
185.22
NH
OH
4-Hydroxy carbazole
MethanolRaney Nickel
KOH
C12H9NO
183.21
+
56.11
+ HCl
36.46
+ KCl
74.55
+ H2O
18.02
+ H2
2.02
Stage-3
NH
OH
4-Hydroxy carbazole
C12H9NO
183.21
Epichlorohydrin
Cl O+
C3H5ClO
92.50
NH
O O
C15H13NO2
239.27
+ NaCl + H2O
58.44 18.02
Methanol+ NaOH
40.0
4-Oxiranylmethoxy-9H-carbazole
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Stage-4
NH
O O
C15H13NO2
239.27
NH2OO+
C9H13NO2
167.21
NH
O NH
OH
O
H3CO
Carvedilol
C24H26N2O4
404.48
Iso propyl alcohol
4-Oxiranylmethoxy-9H-carbazole
2-(2-Methoxy-phenoxy)-ethylamine
CARVEDILOL
Flow Chart: Phenyl hydrazine Hydrochloride1,3-CyclohexanedioneMethanolActivated carbonWater
Stage-1 Methanol RecoveryEffluent water
Stage-2Methanol RecoveryEffluent water
Stage-1Raney nickelMethanolPotassium hydroxide Hydrochloric acid Water
Stage-3Methanol RecoveryAcetone RecoveryEthyl acetate Recovery
Stage-2AcetoneEpichlorohydrinSodium hydroxideMethanolEthyl acetateWater
Stage-4 IPA RecoveryEthyl acetate Recovery
Stage-3Isopropyl alcohol2-(2-Methoxy phenoxy) ethylamineEthyl acetate
CARVEDILOL
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CARVEDILOL
Material Balance:
Material balance of Carvedilol Stage-1 Batch Size: 500.0.0 Kg
Name of the input Quantity in Kg
Name of the out put Quantity In Kg
Phenyl hydrazine Hydrochloride 209.00
Stage-1 260.00
1,3-Cyclohexanedione 162.00 Methanol Recovery 760.00
Methanol 800.00 Methanol Loss 16.00
Activated carbon 10.00 Effluent water 1103.35
Water 1000.00 (Water-1000 ,Ammonium chloride-77.30, Generated Water-26.05)
Spent carbon 10.00
Organic residue (process residue-7.65, Distillation Residue-24 (Methanol)
31.65
Total 2181 Total 2181
Material balance of Carvedilol Stage-2 Batch Size: 500.0.0 Kg
Name of the input Quantity in Kg
Name of the out put Quantity In Kg
Stage-1 260.00 Stage-2 244.00
Raney nickel 15.00 Methanol Recovery 950.00
Methanol 1000.00 Methanol Loss 20.00
Potassium hydroxide 79.00 Effluent water 1129.95
Hydrochloric acid 52.00 (Water-1000,Potasium chloride-
104.65, Generated Water -25.3)
Water 1000.00 Raney nickel Recovery 15.00
Process emission
(Hydrogen) 2.83
Organic residue (process residue-14.22 Distillation Residue-30 (Methanol)
44.22
Total 2406 Total 2406
Material balance of Carvedilol
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Stage-3 Batch Size: 500.0.0 Kg
Name of the input Quantity in Kg
Name of the out put Quantity In Kg
Stage-2 244.00 Stage-3 305.00
Acetone 500.00 Methanol Recovery 950.00
Epichlorohydrin 124.00 Methanol Loss 20.00
Sodium hydroxide 54.00 Acetone Recovery 475.00
Methanol 1000.00 Acetone Loss 10.00
Ethyl acetate 700.00 Ethyl acetate Recovery 665.00
Water 1000.00 Ethyl acetate Loss 14.00
Effluent water (Water-1000, Generated water-23.98, Sodium chloride-77.85)
1101.83
Organic residue (process residue-15.17 Distillation Residue-66 (Methanol-30,Acetone-15, Ethylacetate-21)
81.17
Total 3622 Total 3622
Material balance of Carvedilol Stage-4 Batch Size:500.0 Kg
Name of the input Quantity in Kg
Name of the out put Quantity In Kg
Stage-3 305.00 Carvedilol 500.00 Isopropyl alcohol 1000.00 Isopropyl alcohol Recovery 950.00 2-(2-Methoxy phenoxy) ethylamine
214.00 Isopropyl alcohol Loss 20.00
Ethyl acetate 1000.00 Ethyl acetate Recovery 950.00 Ethyl acetate Loss 20.00
Organic residue (process residue-19 Distillation Residue-60 (Isopropyl alcohol-30, Ethyl acetate-30)
79.00
Total 2519.00 Total 2519.00
2.CYANO DIOL HYDROCHLORIDE
Process Description:
Stage-1
5-Cyano pthalide undergoes condensation with P-Fluoromagnesium bromide and
Dimethyl amino magnesium chloride in presence of Toluene to give Stage-1 Product
Stage-2
Stage-1 Product reacts with Hydrochloric acid in presence of Toluene to give
Cyano Diol Hydrochloride product
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Route of synthesis:
Stage-1:
NC
O
O
5-Cyano pthalide
C9H5NO2
159.14
+
P-Fluoromagnesium bromide
F
MgBr
199.30
Dimethyl amino magnesium chloride
NH3C
H3CMgCl
+
145.91
OH
OHN
CH3
CH3
F
342.41
+ Mg(Br)OH +
121.21
Mg(Cl)OH
76.76
C6H4BrFMg C5H12ClMgN
+ 2 H2O
36.04
Toluene
4-Dimethylamino-1-(4-fluoro-phenyl)-1-(2-hydroxymethyl-
Cyano phenyl)-butan-1-ol
C20H23FN2O2
Magnesium hydroxy bromide
Magnesium hydroxy chloride
NC
Stage-2:
OH
OHN
CH3
CH3
F
342.41
4-Dimethylamino-1-(4-fluoro-phenyl)-1-(2-hydroxymethyl-Cyano
phenyl)-butan-1-ol
C20H23FN2O2
NC
+ HCl
36.46
OH
OHN
CH3
CH3
F
NC
HCl
C20H23FN2O2.HCl
378.87
Toluene
Cyano Diol Hydrochloride
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Flow chart:
Stage-1
Stage-2
5-Cyano pthalideP-Fluoromagnesium bromideDimethyl amino magnesium chlorideToluene Water
Toluene RecoveryEffluent Water
Stage-1 Hydrochloric acid Toluene Water
Toluene RecoveryEffluent Water
Cyano Diol Hydrochloride
Material Balance:
Material Balance of Cyano Diol Hydrochloride Stage-1 Batch Size: 100.0 Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
5-Cyano pthalide 42.00 Stage-1 85.00
P-Fluoromagnesium bromide 53.00 Toluene Recovery 190.00
Dimethyl amino magnesium chloride
39.00 Toluene Loss 4.00
Toluene 200.00 Effluent Water 342.72
Water 300.00 (Water-290.49, Magnesium hydroxybromide-31.98, Magnesium hydroxychloride-20.25)
Organic Residue (Process residue-6.28 Distillation Residue-6 (Toluene)
12.28
Total 634 Total 634
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Material Balance of Cyano Diol Hydrochloride Stage-2 Batch Size: 100.0 Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-1 85.00 Cyano Diol Hydrochloride 100.00
Hydrochloric acid 21.00 Toluene Recovery 190.00
Toluene 200.00 Toluene Loss 4.00
Water 300.00 Effluent Water 300.00
(Water-300)
Organic Residue (Process residue-6 Distillation Residue-6 (Toluene)
12.00
Total 606 Total 606
3. DABIGARTAN
Process Description
Stage-1
Pyridin-2-ylamine reacts with Ethyl acrylate, Ammonia and Hydrochloric acid in
presence of n-Hexane to give stage-1 product
Stage-2
Step-A
4-Chloro -3-nitro benzoic acid reacts with Methyl amine in presence of Isopropyl
Alcohol and Acetic to give step –A product
Step-B
Step-A product reacts with thinly chloride in presence of Methanol to give step-B of
stage of state-2 product
Stage-3
Stage-2 and Stage-1 condensed in presence of Tri ethyl amine, Toluene and Ethanol
to give stage-3product
Stage-4
Stage-3 product undergoes reduction with Iron powder in presence of Ammonium
formate, Toluene, Ethanol, Tetra hydro furan to give stage-3 product
Stage-5
4-Amino benzonitrile reacts with 2- Bromo acetic acid in presence of water to give
stage-5 product
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Stage-6
Stage-4 product reacts with stage -5 products in presence of DiChloro methane and
ethyl acetate to give stage-6 product
Stage-7
Stage-6 product reacts with Ammonium carbonate in presence of Ethanol and
Isopropyl Alcohol give stage-7 product
Stage-8
Stage-7 product reacts with Hexylchloroformate in presence of potassium carbonate
and Tetra hydro furan to give Dibgatran product
DABIGARTAN
Route of Synthesis:
Stage-1
N NH2
Pyridin-2-ylamine
C5H6N2
94.11
+
Ethyl acrylate
O
O
C5H8O2
100.12
N NH
O
O
3-(Pyridin-2-ylamino)-propionic acid ethyl ester
C10H14N2O2
194.23
n-Hexane+ NH3
17.03
+ HCl
36.46
+ NH4Cl
53.49
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Stage-2
Step-A
OH
O
O2N
Cl
4-Chloro-3-nitro-benzoic acid
C7H4ClNO4
201.56
+
Methyl Amine
H2N
CH5N
31.06
Acetic acid , Isopropylalcohol
OH
O
O2N
NH
4-Methylamino-3-nitro-benzoic acid
C8H8N2O4
196.16
+ HCl
36.46Water
Step-B
OH
O
O2N
NH
4-Methylamino-3-nitro-benzoic acid
C8H8N2O4
196.16
+ HCl
36.46+ SOCl2
118.97
Methanol
Cl
O
O2N
NH
C8H7ClN2O3
+
4-Methylamino-3-nitro-benzoyl chloride
214.61SO2
64.06
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Stage-3
Toluene , Ethanol
Cl
O
O2N
NH
C8H7ClN2O3
+4-Methylamino-3-nitro-
benzoyl chloride
214.61
N NH
O
O
3-(Pyridin-2-ylamino)-propionic acid ethyl ester
C10H14N2O2
194.23
+
Triethylamine
N
C6H15N
101.19
O
O2N
NH N
N O
O
3-[(4-Methylamino-3-nitro-benzoyl)-pyridin-2-yl-amino]-propionic acid ethyl ester
C18H20N4O5
372.38
+
Triethylamine hydrochloride
N
C6H16NCl
137.65
. HCl
Stage-4
Ammonium formate Toluene , Ethanol ,Tetrahydrofuran & Water
O
O2N
NH N
N O
O
3-[(4-Methylamino-3-nitro-benzoyl)-pyridin-2-yl-amino]-propionic acid ethyl ester
C18H20N4O5
372.38
+ Fe
55.84
O
H2N
NH N
N O
O
C18H22N4O3
342.39
+
3-[(3-Amino-4-methylamino-benzoyl)-pyridin-2-yl-amino]-propionic acid ethyl ester
Fe
55.84
+ O2
32.00
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Stage-5
4-Amino benzonitrile
N NH2
C7H6N2
118.14
2-bromoacetic acid
O
OHBr
+
C2H3BrO2
138.95
NHN
O
OH
Water
(4-Cyano-phenylamino)-acetic acid
C9H8N2O2
176.17
+ HBr
80.91
STAGE-6
Dichloromethane, Ethyl acetate
O
H2N
NH N
N O
O
C18H22N4O3
342.39
3-[(3-Amino-4-methylamino-benzoyl)-pyridin-2-yl-amino]-propionic acid ethyl ester
+N
HN
O
OH
(4-Cyano-phenylamino)-acetic acid
C9H8N2O2
176.17
N NH
O
N
N O
O
N
N
3-({2-[(4-Cyano-phenylamino)-methyl]-1-methyl-1H-benzoimidazole-5-carbonyl}-pyridin-2-yl-amino)-propionic acid ethyl ester
C27H26N6O3
482.53
+ 2 H2O
36.03
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Stage-7
N N O
O
O
N
N
HN
N N O
O
O
N
N
HN CN (NH4)2CO3
NH2
NH
C27H26N6O3
Mol. Wt.: 482.53
Ethyl 3-(2-((4-cyanophenylamino)methyl)-1-methyl-N-(pyridin-2-yl)-
1H-benzo[d]imidazole-5-carboxamido)propanoate
C27H29N7O3
Mol. Wt.: 499.56
Ethyl 3-(2-((4-amidinophenylamino)methyl)-1-methyl-N-(pyridin-2-
yl)-1H-benzo[d]imidazole-5-carboxamido)propanoate
CO2+
Ethano, IPA+
Ammonium carbonate
96.09
44.0
+ NH3
17.03
+ H2O
18.0
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Stage-8
N N O
O
O
N
N
HNNH2
NH
N N O
O
O
N
N
HNN
NH2
O
O
Dabigatran
Hexyl chloroformate
499.56
O
O
Cl
+
164.63
C34H41N7O5
627.73
C7H13Cl O2
3-({2-[(4-Carbamimidoyl-phenylamino)-methyl]-1-methyl-1H-benzoimidazole-5-
carbonyl}-pyridin-2-yl-amino)-propionic acid ethyl ester
C27H29N7O3
THF
+ K2CO3
138.21
+ KCl
74.55
CHKO2
84.12
+
Potassium formate
+ 0.5 O2
16.00
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Flow chart:
(pyridine-2-ylamine Ethyl acrylate Ammonia Hydrochloric acid n-Hexane Water
Stage-1
n-Hexane RecoveryEffluent water
Stage-2
Acetic acid RecoveryIsopropyl alcohol RecoveryMethanol RecoveryEffluent water
4-chloro-3-nitro-benzoic acid Methyl amine Acetic acid Isopropyl alcohol Thionyl chloride Methanol Water
Stage-3
Toluene RecoveryEthanol RecoveryEffluent water
Stage-1Stage-2Triethylamine Toluene Ethanol Water
Stage-4
Toluene RecoveryEthanol RecoveryTetra hydrofuran RecoveryEffluent water
Stage-3Iron Ammonium formate Toluene Ethanol Tetra hydrofuran Water
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Dabigartan
Stage-5 Effluent water
4-amino benzonitrile 2-bromoacetic acid Water
Stage-4Stage-5Dichloromethane Ethyl acetate Water
Stage-6
Dichloromethane RecoveryEthyl acetate RecoveryEffluent water
Stage-6Ammonium carbonate Ethanol Isopropyl alcohol Water
Stage-7
Ethanol RecoveryIsopropyl alcohol RecoveryEffluent water
Stage-7Hexyl chloro formate Potassium carbonate Tetrahydrofuran Water
Stage-8
Tetrahydrofuran RecoveryEffluent water
Material balance:
Material balance of Dabigartan Stage-1 Batch Size: 100.0Kg
Name of the input Quantity in Kg
Name of the out put Quantity In Kg
(pyridine-2-ylamine 23.00 Stage-1 45.00
Ethyl acrylate 25.00 n-Hexane Recovery 190.00
Ammonia 5.00 n-Hexane loss 4.00
Hydrochloric acid 9.00 Effluent water 313.10
n-Hexane 200.00 (Water-300 Ammonium chloride-13.10)
Water 300.00 Organic Residue 9.90
Process residue -3.9 Distillation Residue-6 (n-Hexane )
Total 562 Total 562
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Material balance of Dabigartan Stage-2 Batch Size: 100.0Kg
Name of the input Quantity in Kg
Name of the out put Quantity In Kg
4-chloro-3-nitro-benzoic acid 55.00 Stage-2 49.00
Methyl amine 9.00 Acetic acid Recovery 190.00
Acetic acid 200.00 Acetic acid loss 4.00
Isopropyl alcohol 200.00 Isopropyl alcohol Recovery 190.00
Thionyl chloride 31.00 Isopropyl alcohol loss 4.00
Methanol 200.00 Methanol Recovery 190.00
Water 300.00 Methanol loss 4.00
Effluent water 306.00
(Water-300 Isopropyl alcohol -6)
By product (Hydrochloric acid-19.04)
19.04
Process emission (Sulphur dioxide-16.25,
16.25
Organic Residue 22.71
Process residue -10.71 Distillation Residue-12 (Methanol-6, Acetic acid-6 )
Total 995 Total 995
Material balance of Dabigartan Stage-3 Batch Size: 100.0Kg
Name of the input Quantity in Kg
Name of the out put Quantity In Kg
Stage-1 45.00 Stage-3 78.00
Stage-2 49.00 Toluene Recovery 190.00
Triethylamine 24.00 Toluene loss 4.00
Toluene 200.00 Ethanol Recovery 190.00
Ethanol 200.00 Ethanol loss 4.00
Water 300.00 Effluent water 337.45
(Water-300 Toluene -6, Triethylamine hydrochloride-31.45)
Organic Residue 14.55
Process residue -8.55 Distillation Residue-6 (Ethanol -6)
Total 818 Total 818
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Material balance of Dabigartan Stage-4 Batch Size: 100.0Kg
Name of the input Quantity in Kg
Name of the out put Quantity In Kg
Stage-3 78.00 Stage-4 68.00
Iron 12.00 Toluene Recovery 190.00
Ammonium formate 20.00 Toluene loss 4.00
Toluene 200.00 Ethanol Recovery 190.00
Ethanol 200.00 Ethanol loss 4.00
Tetra hydrofuran 200.00 Tetra hydrofuran Recovery 190.00
Water 300.00 Tetra hydrofuran loss 4.00
Effluent water 337.70
(Water-300 Toluene -6, Iron -11.70, Ammonium formate-20)
Process emission (oxygen)
6.70
Organic Residue 15.6
Process residue -3.6 Distillation Residue-12 (Ethanol -6, Tetra hydrofuran-6)
Total 1010 Total 1010
Material balance of Dabigartan Stage-5 Batch Size: 100.0Kg
Name of the input Quantity in Kg
Name of the out put Quantity In Kg
4-amino benzonitrile 25.00 Stage-5 35.00
2-bromoacetic acid 30.00 Effluent water 300.00
Water 300.00 (Water-300)
Byproduct (Hydrobromic acid)
17.15
Organic Residue 2.85
Total 355 Total 355
Material balance of Dabigartan Stage-6 Batch Size: 100.0Kg
Name of the input Quantity in Kg
Name of the out put Quantity In Kg
Stage-4 68.00 Stage-6 89.00
Stage-5 35.00 Dichloromethane Recovery 190.00
Dichloromethane 200.00 Dichloromethane loss 4.00
Ethyl acetate 200.00 Ethyl acetate Recovery 190.00
Water 300.00 Ethyl acetate loss 4.00
Effluent water 313.15
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(Water-300 Ethyl acetate -6, Generated water -7.15
Organic Residue 12.85
Process residue -6.85 Distillation Residue-6 (Dichloromethane -6)
Total 803 Total 803
Material balance of Dabigartan Stage-7 Batch Size: 100.0Kg
Name of the input Quantity in Kg
Name of the out put Quantity In Kg
Stage-6 89.00 Stage-7 87.00
Ammonium carbonate 18.00 Ethanol Recovery 190.00
Ethanol 200 Ethanol loss 4.00
Isopropyl alcohol 200.00 Isopropyl alcohol Recovery 190.00
Water 300.00 Isopropyl alcohol loss 4.00
Effluent water 303.25
(Water-300 Generated water -3.35)
Process emission (Carbon dioxide-8.10, Ammonia-3.13),
11.23
Organic Residue 17.52
Process residue -5.52 Distillation Residue-12 (ethanol-6, Isopropyl alcohol-6 )
Total 807 Total 807
Material balance of Dabigartan Stage-8 Batch Size: 100.0Kg
Name of the input Quantity in Kg
Name of the out put Quantity In Kg
Stage-7 87.00 Dabigartan 100.00
Hexyl chloro formate 29.00 Tetrahydrofuran Recovery 190.00
Potassium carbonate 25.00 Tetrahydrofuran loss 4.00
Tetrahydrofuran 200.00 Effluent water 327.63
Water 300.00 (Water-300 , Potassium formate-14.65, potassium chloride-12.98)
Process emission (Oxygen)
2.78
Organic Residue 16.59
Process residue -10.59 Distillation Residue-6 (THF )
Total 641 Total 641
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4. FEXOFENADINE HYDROCHLORIDE
Process Description:
Stage-1
3-Chloro-2-methylprop-1-ene reacts with Sodium acetate in the presence of Dimethyl formamide to give Stage-1 product. Stage-2 Stage-1 product reacts with Aluminum chloride, Sodium hydroxide and Benzene in the presence of Toluene to give Stage-2 product. Stage-3 Stage-2 product reacts with 4-Chloro-butyryl chloride,in the presence of Dichloromehane to give Stage-3 product. Stage-4 Stage-3 product reacts with Sodium hydroxide in presence of Methanol to give Stage-4 product. Stage-5 Stage-4 product reacts with Hydrochloric acid and Potassium permanganate inpresence of water to give Stage-5 product. Stage-6 Stage-5 product reacts with Methanol and Hydrochloric acid in presence of Methanol to give Stage-6 product. Stage-7
Piperidine-4 -carboxylic acid reacts with Chloro benzene and Magnesium in
presence of THF and Toluene to give Azacyclonol.
Stage-8
Stage-6 product undergoes condensation with Stage-7 product in presence of
Sodium bicarbonate, Methyl isobutyl ketone and Ethyl acetate to give Stage-8
Product
Stage-9
Stage-8 product reduction with Sodiumborohydride, Sodium hydroxide and Acetic
acid Methanol to give Stage-9 product .
Stage-10
Stage-9 product undergoes condensation with Hydrochloric acid in presence of Iso
propyl alcohol to give Fexofenadine Hydrochloride .
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FEXOFENADINE HYDROCHLORIDE
Route of Synthesis:
Stage-1:
CH3
H2C Cl + CH3COONa
+ NaCl
3-Chloro-2-methylprop-1-ene
2-methylprop-2-en-1-yl-acetate
90.55
C4H7Cl
82.03
C6H10O2
114.14
58.44
Dimethyl formamide
CH3
O
O
CH2
H3C
Stage-2:
2-methylprop-2-en-1-yl-acetate
C6H10O2
114.14
+ AlCl3
Benzene
C6H6
78.11
CH3
CH2OCOCH3H3C
C12H16O2
192.25
CH3
O
O
CH2
H3C
+
133.34
+ 3 H2O
54.05
Toluene
Acetic acid 2-methyl-2-phenyl-propyl ester
+ Al(OH)3
78.00
+ 3 HCl
109.38
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Stage-3:
CH3
CH2OCOCH3H3C
C12H16O2
192.25
+Cl
Cl
O
H3C CH2OCOCH3
CH3
+ HCl
2-Methyl-2-phenylpropyl acetate
C4H6Cl2O
141.0
C16H21ClO3
296.79
36.46
4-Chloro-butyryl chloride
Dichloromethane
Cl
O
Acetic acid 2-[4-(4-chloro-butyryl)-phenyl]-2-methyl-propyl ester
Stage-4:
H3C CH2OCOCH3
CH3
+
C16H21ClO3
296.79
Methanol
Cl
O
Acetic acid 2-[4-(4-chloro-butyryl)-phenyl]-2-methyl-propyl ester
H3C CH2OH
CH3
NaOH
40.0
C14H18O2
+ NaCl
58.44
218.29
+ CH3COOH
60.0
O
Cyclopropyl-[4-(2-hydroxy-1,1-dimethyl-ethyl)-phenyl]-methanone
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Stage-5:
+ HCl + KMnO4
MnO2 + KCl + H2O
86.9474.55 18.02
36.46 158.03
Water
H3C CH2OH
CH3
C14H18O2
218.29
O
Cyclopropyl-[4-(2-hydroxy-1,1-dimethyl-ethyl)-phenyl]-methanone
+
H3C COOH
CH3
O
Cyclopropyl-[4-(2-hydroxy-1,1-dimethyl-ethyl)-phenyl]-methanone
C14H16O3
232.28
Stage-6:
CH3OH + HCl
32.04 36.46
Methanol+
H3C COOH
CH3
O
Cyclopropyl-[4-(2-hydroxy-1,1-dimethyl-ethyl)-phenyl]-methanone
C14H16O3
232.28
+
H3C COOCH3
CH3
O
Cl
2-[4-(4-Chloro-butyryl)-phenyl]-2-methyl-propionic acid methyl ester
C15H19ClO3
282.76
H2O
18.02
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Stage-7:
Piperidine-4-carboxylic acid
NH
O OH
Chloro benzene
Cl
+
2
+ Mg
HO
NH
2
+ MgCl2 + MgO
Azacyclonol Magnesium chloride
C6H11NO2C6H5Cl
C18H21NO
129.162X112.56=225.12
2X24.3=48.6
267.3695.21
40.30
THF, Toluene
Stage-8:
H3C COOCH3
CH3
O
Cl
2-[4-(4-Chloro-butyryl)-phenyl]-2-methyl-propionic acid methyl ester
C15H19ClO3
282.76
+
Azacyclonol
C18H21NO
267.36
MIBK, Ethyl acetate+ NaHCO3
84.01
HN
OH
+ NaCl + CO2 + H2O
C33H39NO4
Mol. Wt.: 513.7
H3C
CH3
COOCH3
O
OH
2-(4-{4-[4-(Hydroxy-diphenyl-methyl)-piperidin-1-yl]-butyryl}-phenyl)-2-methyl
-propionic acid methyl ester
58.44 44.01 18.02
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Stage-9:
+
Methanol
H3C
CH3
COOCH3
O
N
OH
C33H39NO4
Mol. Wt.: 513.7
H3C
CH3
COOH
O
N
OH
2-(4-{4-[4-(Hydroxy-diphenyl-methyl)-piperidin-1-yl]-butyryl}-phenyl)-2-methyl-
propionic acid methyl ester
37.83
+ NaOH
40.00
+ 2 CH3COOH
120.10
+ 3 H2O
54.05
2-(4-{4-[4-(Hydroxy-diphenyl-methyl)-piperidin-1-yl]-butyryl}-phenyl)-2-
methyl-propionic acid
C32H37NO4
499.64
+ H3BO3
61.83
+ 2 CH3COONa
164.07
+ CH3OH
32.04
+ 4 H2
8.00
NaBH4
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Stage-10:
+ HCl
36.46
Iso propyl alcohol
.HCl
Fexofenadine Hydrochloride
C32H38NO3ClMol. Wt.: 536.10
C32H37NO4
Mol. Wt.:499.64
H3C
CH3
COOH
O
N
OH
H3C
CH3
COOH
O
N
OH
2-(4-{4-[4-(Hydroxy-diphenyl-methyl)-piperidin-1-yl]-butyryl}-phenyl)-
2-methyl-propionic acid
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FEXOFENADINE HYDROCHLORIDE
Flow Chart:
Stage-1
Stage-2
Stage-3
3-Chloro-2-methylprop-1-eneSodium acetateDMFWater
DMF RecoveryEffluent water
Stage-1TolueneBenzeneAluminum chlorideWater
Toluene RecoveryEffluentb water
Stage-24-Chlorobutanoyl chlorideDichloromethane Sodium sulphateWater
Dichloromethane RecoveryEffluent water
Stage-4
Stage-5
Stage-3Sodium hydroxideMethanolWater
Stage-4Hydrochloric AcidPotassium permanganateWater
Methanol RecoveryEffluent Water
Effluent Water
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Stage-6
Stage-7
Stage-8
THF RecoveryToluene RecoveryEffluent water
Ethyl Acetate RecoveryMIBK RecoveryEffluent water
Stage-9
Stage-10
Methanol RecoveryEffluent water
Isopropyl Alcohol Recovery
Stage-5MethanolHydrochloric AcidWater
Methanol RecoveryEffluent Water
Piperidine-4-carboxylic acidChloro benzeneMagnesiumTHFTolueneActivated CarbonWater
Stage-6Sodium BicarbonateStage-7Methyl isobutyl ketoneEthyl AcetateWater
Stage-8Sodium BorohydrideSodium HydroxideAcetic AcidActivated carbonMethanolWater
Stage-9Hydrochloric acidIsopropyl alcohol
FEXOFENADINE HYDROCHLORIDE
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FEXOFENADINE HYDROCHLORIDE
Material Balance:
Material Balance of Fexofenadine Hydrochloride Stage-1 Batch Size: 500Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
3-Chloro-2-methylprop-1-ene
108.00 Stage-1 131.00
Sodium acetate 98.00 DMF Recovery 475.00
DMF 500.00 DMF Loss 10.00
Water 300.00 Effluent water 374.70
(Water-300, Sodium chloride-69.7 DMF-5)
Organic Residue Process residue-5.3 Distillation residue-10 (DMF)
15.30
Total 1006 Total 1006
Material Balance of Fexofenadine Hydrochloride Stage-2 Batch Size: 500Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-1 131.00 Stage-2 215.00
Toluene 500.00 Toluene Recovery 475.00
Benzene 90.00 Toluene Loss 10.00
Aluminum chloride 153.00 By-Product
Aluminum chloride solution
(Aluminium hydroxide-89.5+Water-238)
Hydrochloric acid
327.50
125.52
Water 300.00 Organic Residue (process residue-5.98 Distillation residue-15 ( Toluene-15)
20.98
Total 1174 Total 1174
Material Balance of Fexofenadine Hydrochloride Stage-3 Batch Size: 500Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-2 215.00 Stage-3 321.00
4-Chlorobutanoyl chloride 158.00 Dichloromethane Recovery 475.00
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Dichloromethane 500.00 Dichloromethane Loss 10.00
Sodium sulphate 12.00 Effluent water 300.00
Water 300.00 (Water-300)
Inorganic solid waste (Sodium sulphate)
12.00
By product (Hydrochloric acid)
40.76
Organic Residue Process residue-11.24 Distillation Residue-15 (Dichloromethane)
26.24
Total 1185 Total 1185
Material Balance of Fexofenadine Hydrochloride Stage-4 Batch Size: 500Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-3 321.00 Stage-4 232.00
Sodium hydroxide 40.00 Methanol Recovery 475.00
Methanol 500.00 Methanol Loss 10.00
Water 300.00 Effluent Water 428.10
(Water-300,Acetic Acid-64.90 Sodium chloride-63.2)
Organic Residue (Process residue-0.9 Distillation residue-15 (Methanol)
15.90
Total 1161 Total 1161
Material Balance of Fexofenadine Hydrochloride Stage-5 Batch Size: 500Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-4 232.00 Stage-5 239.00
Hydrochloric Acid 39.00 Effluent Water (Water-300, Potassium Chloride-79.25, generated water-19.15, Manganese dioxide-90.3)
488.70
Potassium permanganate 168.00
Water 300.00 Organic Residue 11.30
Total 739 Total 739
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Material Balance of Fexofenadine Hydrochloride Stage-6 Batch Size: 500Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-5 239.00 Stage-6 285.00
Methanol 533.00 Methanol Recovery 475.00
Hydrochloric Acid 38.00 Methanol Loss 10.00
Water 300.00 Effluent Water 318.55
(Water-300, generated water-18.55)
Organic Residue Process residue-6.45 Distillation Residue-15 (Methanol)
21.45
Total 1110 Total 1110
Material Balance of Fexofenadine Hydrochloride Stage-7 Batch Size: 500Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Piperidine-4-carboxylic acid
139.00 Azacyclonol (Stage-7) 269.00
Chloro benzene 234.00 THF Recovery 475.00
Magnesium 51.00 THF Loss 10.00
THF 500.00 Toluene Recovery 475.00
Toluene 500.00 Toluene Loss 10.00
Activated Carbon 5.00 Effluent water 455.60
Water 300.00 (Water-300,Magnesium chloride-98.80,Magnesium oxide-41.80,THF-15
Spent Carbon 5.00
Organic Residue (Process residue-14.4 Distillation Residue-15 (Toluene)
29.40
Total 1729 Total 1729
Material Balance of Fexofenadine Hydrochloride Stage-8 Batch Size: 500Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-6 285.00 Stage-8 505.00
Sodium Bicarbonate 85.00 Ethyl Acetate Recovery 760.00
Stage-7 269.00 Ethyl Acetate Loss 16.00
Methyl isobutyl ketone 600.00 MIBK Recovery 570.00
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Ethyl Acetate 800.00 MIBK loss 12.00
Water 300.00 Effluent water 395.06
(Water-300, Sodium Chloride-58.90 generated water-18.16, MIBk-18)
Process Emission 44.35
(Carbon dioxide)
Organic residue- (Process residue-12.59 Distillation Residue-24 (Ethyl acetate)
36.59
Total 2339 Total 2339
Material Balance of Fexofenadine Hydrochloride Stage-9 Batch Size: 500Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-8 505.00 Stage-9 476.00
Sodium Borohydride 38.00 Methanol Recovery 760.00
Sodium Hydroxide 40.00 Methanol Loss 16.00
Acetic Acid 118.00 Effluent water 500.35
Activated carbon 5.00 (Water-446.85, Boric Acid-60.75, Sodium Acetate-161.25, Methanol-31.50)
Methanol 800.00 Spent Carbon 5.00
Water 300.00 Process Emissions 7.82
(Hydrogen)
Organic Residue Process residue-16.83 Distillation Residue-24 (Methanol)
40.83
Total 1806 Total 1806
Material Balance of Fexofenadine Hydrochloride Stage-10 Batch Size: 500Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-9 476.00 Fexofenadine Hydrochloride 500.00
Hydrochloric acid 35.00 Isopropyl Alcohol Recovery 285.00
Isopropyl alcohol 300.00 Isopropyl Alcohol Loss 6.00
Organic Residue Process residue-11 Distillation Residue-9 (Isp propyl alcohol)
20.00
Total 811 Total 811
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5.FLUCONAZOLE
Process Description
Stage-1
Step-A
1,3-Difluorobenzene reacts with Chloroacetyl Chloride in the presence of Aluminum
chloride and MDC to give step-A product .
Step-B
Step-A product reacts with 1,2,4-triazole in presence of Triethyl amine and
EthylAcetate to give DFTA(2,4-Difluoro-2-(1h- 1,2,4-Triazole-1-Yl)
Acetophenone)(Stage-1) product.
Stage-2
Stage-1 product reacts with Tri methyl sulfoxonium iodide in presence of potassium
hydroxide to give stage-4 product.
Stage-3
Stage-2 product reacts with 1, 2,4-triazole in presence of Potassium carbonate and
Toluene to get Fluconazole Technical product. Finally it is purified in Isopropyl
Alcohol pure Fluconazole
FLUCONAZOLE
Route of Synthesis:
Stage-1
Step-A
1,3-Difluorobenzene
F F +
Chloroacetyl chloride
O
ClCl
F F
Cl
O
2-Chloro-1-(2,4-difluorophenyl)ethanone
AlCl3
C6H4F2
114.09C2H2Cl2O
112.94
C8H5ClF2O
190.57
+
MDC+
133.34
+ 3H2O
54.06
Al(OH)3
78.00
4 HCl+
145.84
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Step-B
F F
Cl
O
2-Chloro-1-(2,4-difluorophenyl)ethanone
C8H5ClF2O190.57
N
NN
F F
O
1,2,4-triazole
+
. HCl
C2H3N3
69.07
C10H7F2N3O
223.18
NH
NN
Triethylamine
(2,4-Difluoro-2-(1h- 1,2,4-Triazole-1-Yl) Acetophenone)
(DFTA)
Ethyl Acetate,N+
C6H15N
101.19
Triethylamine hydrochlordie
N+
C6H16NCl
137.65
Stage-2
1-(2,4-difluorophenyl)-2-(1,2,4-triazol-1-yl)ethanone
N
NN
F F
O
C10H7F2N3O
223.18
+Trimethyl
sulfoxonium iodide
S+
O
H3C
CH3
CH3I-
+ KOH
1-[2-(2,4-di fluorophenyl)-2,3-epoxypropyl]-1H-1,2,4-Triazole
N N
N
O
F F
C3H9IOS
220.07
56.11
C11H9F2N3O
237.21
+ (CH3)2SO + KI + H2O
Dimethyl Sulfoxide
78.13
166.0 18.02
Toluene
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Stage-3
1-[2-(2,4-di fluorophenyl)-2,3-epoxypropyl]-1H-1,2,4-Triazole
N N
N
O
F F
C11H9F2N3O
237.21
1,2,4-Triazole
NH
NN
C2H3N3
69.07
+ + K2CO3
OH
N
N
N
NN
N
F F
Fluconazole
C13H12F2N6O
306.27
138.21
+ 2 HCl
2X36.5=73.0
+ 2 KCl + H2O + CO2
149.10 18.0 44.0
DMF, IPA, Activated Carbon
FLUCONAZOLE
Flow Chart: 1,3 Difluoro benzeneChloro Acetyl chlorideAluminium ChlorideMDC1,2,4-triazoleTriethyl AmineEthyl AcetateIso propyl alcohol DM Water
Mixed Solvent(MDC + Ethyl acetate)Recovery
Stage-1Tri methyl Sulfoxonium iodidePotassium HydroxideTolueneWater
Toluene RecoveryEffluent Water
Stage-21,2,4-TriazolePotassium carbonateDMFHydrochloric AcidIPAActivated CarbonSodium sulphate DM Water
DMF RecoveryIPA RecoveryEffluent water
FLUCONAZOLE
Stage-1
Stage-2
Stage-3
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FLUCONAZOLE
Material Balance:
Material Balance of Fluconazole
Stage-1 Batch Size: 100Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
1,3 Difluoro benzene 60.00 Stage-1 80.00
Chloro Acetyl chloride 60.00 Mixed Solvent(MDC + Ethyl acetate)Recovery
352.00
Aluminium Chloride 72.00 MDC Loss 12.00
MDC 250.00 Iso propyl alcohol Recovery 114.00
1,2,4-triazole 32.00
Triethyl Amine 46.00 Iso propyl alcohol loss 2.40
Ethyl Acetate 120.00 Ethyl Acetate loss 6.00
Iso propyl alcohol 120.00 By-Products
Aluminium chloride Solution (Aluminium hydroxide-41 +Water-389)
Triethyl amine hydrochloride
Hydrochloric acid
430.00
78.00 76.68
DM Water 400.00 Organic Residue Process residue-5.32 Distillation residue -3.6 (IPA)
8.92
Total 1160.00 Total 1160.00
Material Balance of Fluconazole
Stage-2 Batch Size: 100Kg
Name of the input Quantity
in Kg
Name of the out put Quantity
in Kg
Stage-1 80.00 Stage-2 85.00
Tri methyl Sulfoxonium iodide 80.00 Toluene Recovery 190.00
Potassium Hydroxide 20.00 Toluene Loss 4.00
Toluene 200.00 Effluent Water
(Water-400,
generated water-6.45,
Potassium iodide-59.5,
DMSO-28, Toluene-6) 499.95
Water 400.00
Organic Residue
Process residue-1.05
1.05
Total 780 Total 780
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Material Balance of Fluconazole
Stage-3 Batch Size: 100Kg
Name of the input Quantity
in Kg
Name of the out put Quantity
in Kg
Stage-2 85.00 Fluconazole 100.00
1,2,4-Triazole 26.00 DMF Recovery 190.00
Potassium carbonate 49.00 DMF Loss 4.00
DMF 200.00 IPA Recovery 190.00
Hydrochloric Acid 26.00 IPA Loss 4.00
IPA 200.00 Effluent Water
(Water-400,generated water-6.45,
Potassium chloride-53.42, DMF-6,
IPA- 3) 468.87
Activated Carbon 10.00
Sodium sulphate 25.00 Spent Carbon 10.00
DM Water 400.00 Process Emission
(Carbon dioxide) 15.76
Inorganic solid waste
(Sodium sulphate) 25.00
Organic Residue
Process residue -10.37
Distillation residue – 3
(IPA) 13.37
Total 1021 Total 1021
6.FOLIC ACID
Process description:
Stage-1:
4-Nitro-benzoic acid undergoes chlorination with Thionyl chloride in presence of
Toluene , Sodium hydroxide and Dimethyl formamide to give Stage-1 product.
Stage-2:
Stage-1 product reacts with monosodium glutamate in presence of Sulfuric acid and
toluene to give Stage-2 product .
Stage-3:
Stage-2 product undergoes Hydrogenation with Hydrogen gas in presence of
palladium carbon and toluene to give Stage-3 product
Stage-4:
Acetone reacts with Chlorine gas in presence of Water to give Stage-4 product.
Stage-5:
Stage-4 product reacts with Stage-2 product in presence of acetic acid to give Folic
acid Product.
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Route of Synthesis:
Stage-1:
COOH
NO2
4-Nitro-benzoic acid
C7H5NO4
167.12
+
Thionyl chloride
SOCl2
118.97
COCl
NO2
4-Nitro-benzoyl chlorideC7H4ClNO3
185.56
+ NaCl+ NaOH
40.058.44
+ H2O
18.02
+ SO2
64.06
DMF, Toluene
Stage-2:
COCl
NO2
4-Nitro-benzoyl chloride
C7H4ClNO3
185.56
+ HO
O O
ONaNH2
Monosodium glutamate
C5H8NNaO4
169.11
+ H2SO4
98.08
O2N
O
NH
COOH
COOHH
2-(4-Nitro-benzoylamino)-pentanedioic acid
C12H12N2O7
296.23
+ NaHSO4
120.06
+ HCl
36.46
Toluene
Stage-3:
O2N
O
NH
COOH
COOHH
2-(4-Nitro-benzoylamino)-pentanedioic acid
C12H12N2O7
296.23
+ H2H2N
O
NH
COOH
COOHH
2-(4-Amino-benzoylamino)-pentanedioic acid
C12H14N2O5
266.25
+ 2 H2O
36.0
3
6.0
Toluene
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Stage-4:
H3C
O
CH3
Acetone
C3H6O
58.08
+ Cl23
Chlorine Gas
3X70.91=212.73
O
Cl
Cl Cl
1,1,3-Trichloro-propan-2-one
+ 3 HCl
3X36.5=109.5
161.41
C3H3Cl3O
Water
Stage-5:
H2N
O
NH
COOH
COOHH
2-(4-Amino-benzoylamino)-pentanedioic acid
C12H14N2O5
266.25
O
Cl
Cl Cl
1,1,3-Trichloro-propan-2-one
161.41
C3H3Cl3O
+ +
N
N
NH2
NH2
OH
H2N H2SO4
2,5,6-Triamino-4,5-dihydro-pyrimidin-4-ol;
compound with sulfuric acid
C4H11N5O5S
241.23
N
NH
N
NNH
H2N
NH
O
COOH
OH COOH
Folic acid
C19H19N7O6
441.41
+H2O
3X18=54
+SO2
64.06
+ HCl
3X36.5=109.5
3 3
Acetic acid
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Flow Chart:
4-Nitro benzoic acidThionyl chlorideSodium hydroxideDimethyl formamideTolueneWater
Dimethyl Formamide RecoveryToluene RecoveryEffluent water
Stage-1
Toluene RecoveryEffluent WaterStage-2
Stage-1Monosodium glutamateSulfuric acidTolueneWater
Stage-2Catalyst(Iron Powder)Hydrogen GasTolueneSodium SulphateWater
AcetoneChlorine GasWater
Toluene RecoveryEffluent WaterStage-3
Effluent WaterStage-4
Acetic acid RecoveryEffluent WaterStage-5
Stage-3Stage-42,5,6-Triamino-4,5-dihydro-pyrimidin-4-ol ,Sulfuric acidAcetic acidWater
Folic Acid
Material Balance:
Material Balance of Folic Acid Stage-1 Batch Size: 200.0 Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
4-Nitro benzoic acid 100.00 Stage-1 105.00
Thionyl chloride 71.25 Dimethyl Formamide Recovery 380.00
Sodium hydroxide 44.00 Dimethyl formamide Loss 8.00
Dimethyl formamide 400.00 Toluene Recovery 380.00
Toluene 400.00 Toluene Loss 8.00
Water 1000.00 Effluent Water 1085.77
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(Water-1000, Generated water-10.8, sodium chloride-34.97, Toluene-10 Dimethyl formamide-10, Sodium hydroxide-20)
Process emissions 38.35
(sulfur dioxide)
Organic residue 10.13
(Organic Impurities-6.13, Distillation residue-4 (DMF-2, Toluene -2)
Total 2015.25 Total 2015.25
Material Balance of Folic Acid
Stage-2 Batch Size: 200.0 Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-1 105.00 Stage-2 153.00
Monosodium glutamate 96.00 Toluene Recovery 570.00
Sulfuric acid 56.00 Toluene Loss 12.00
Toluene 600.00 Effluent Water 778.00
Water 700.00 (Water-700, Sodium bisulfate-68, Toluene-10)
By -Product 20.65
(Hydrochloric acid )
Organic residue 23.35
(Organic Impurities-15.35, Distillation residue-8 (Toluene-8)
Total 1557 Total 1557
Material Balance of Folic Acid
Stage-3 Batch Size: 200.0 Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-2 153.00 Stage-3 130.00
Catalyst(Iron Powder) 10.00 Toluene Recovery 760.00
Hydrogen Gas 4.00 Toluene Loss 16.00
Toluene 800.00 Spent Catalyst 10.00
Sodium Sulphate 15.00 Effluent Water 1032.00
Water 1000.00 (Water-1000, Generated Water-20, Toluene-12)
Inorganic solid waste 15.00
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(Sodium sulphate)
Organic Residue 19.00
Process residue-7 Distillation Residue 12 (Toluene-12)
Total 1982 Total 1982
Material Balance of Folic Acid
Stage-4 Batch Size: 200.0 Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Acetone 30.00 Stage-4 79.00
Chlorine Gas 110.00 Effluent Water 800.00
Water 800.00 (Water-800)
By -Product 56.60
(Hydrochloric acid )
Organic Residue 4.40
Total 940 Total 940
Material Balance of Folic Acid
Stage-5 Batch Size: 200.0 Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-3 130.00 Folic acid 200.00
Stage-4 79.00 Acetic acid Recovery 475.00
2,5,6-Triamino-4,5-dihydro-pyrimidin-4-ol ,Sulfuric acid
118.00 Acetic acid Loss 10.00
Acetic acid 500.00 Effluent Water 835.36
Water 800.00 (Water-800, generated water-26.36, Acetic acid-9)
By –Product (Hydrochloric acid -53.47)
53.47
Process emission 31.28
(Sulfur dioxide-31.28)
Organic Residue 21.89
(Process residue-15.89, Distillation Residue-6 Acetic acid-6)
Total 1627 Total 1627
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7.ITRACONAZOLE
Process Description:
Stage-1:
1-(4-Methoxyphenyl) Piperazine undergoes condensation with p-Nitro Chloro
Benzene to give Stage-1 compound in presence of Potassium Carbonate and DMF.
Stage-2:
Stage-1 Compound Hydrogenation with Hydrogen to give Stage-2 compound in
presence of Palladium on carbon and DMF
Stage-3:
Stage-2 Compound undergoes condensation with Phenyl Chloro formate to give
Stage-3 Compound in presence of Sodium bicarbonate and MDC
Stage-4:
Stage-3 Compound reacts with Hydrazine Hydrate to give Stage-4 Compound in
presence of 1,4-Dioxane
Stage-5:
Stage-4 Compound reacts with Formamidine and Acetic Acid to give Stage-5
Compound in presence of DMF
Stage-6:
Stage-5 Compound reacts with 2-Bromobutane to give Stage-6 Compound in
presence of Potassium carbonate, DMF and Methanol.
Stage-7:
Stage-6 Compound reacts with Hydro bromic acid to give Stage-7 compound in
presence of Sodium Carbonate and Methanol.
Stage-8(preparation of Cis –Bromo benzoate)
Step-A
2,4-Dichloroacetophenone undergoes condensation with Glycerol and Bromine to
give Step-A compound in presence of Para toluene sulfuric acid and n-Butanol
Step-B
Step-A compound undergoes condensation with Benzoyl chloride to give Cis –
Bromo benzoate(Stage-8) in presence of Toluene
Stage-9:
Stage-8 Compound reacts with 1,2,4-Triazole to give Stage-9 compound in
presence of Potassium carbonate ,Sodium hydroxide and DMF
Stage-10:
Stage-9 compound reacts with Methane sulfonyl chloride to give Stage-10
compound in presence of Triethylamine and MDC
Stage-11
Stage-10 compound reacts with Stage-7 compound to give Itraconazole in presence
of Potassium hydroxide and Methanol.
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ITRACONAZOLE
Route of Synthesis:
Stage-1:
+
H3CO N N NO2
C11H16N2O
192.26
C6H4ClNO2
157.55
C17H19N3O3
313.35
+ 2 KCl + CO2 + H2O
149.10 44.01 18.02
HN N OCH3
1-(4-Methoxy-phenyl)-piperazine 1-Chloro-4-nitro-benzene
1-(4-Methoxy-phenyl)-4-(4-nitro-phenyl)-piperazine
Cl NO2 +DMF
WaterK2CO3
138.20
+ HCl
36.46
Stage-2:
H3CO N N NO2
C17H19N3O3
313.35
+ 3H2 pd/Catalyst
H3CO N N NH2
C17H21N3O
283.37
+ 2H2O
36.04
Hydrogen
6.05
DMF1-(4-Methoxy-phenyl)-4-(4-nitro-phenyl)-
piperazine
4-[4-(4-Methoxy-phenyl)-piperazin-1-yl]-phenylamine
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Stage-3:
H3CO N N NH2
C17H21N3O
283.37
+OCl
O+ NaHCO3
Phenyl chloro formate
C7H5ClO2
156.57
84.01
H3CO N N NHCOOPh
C24H25N3O3
403.47
+ NaCl + CO2 + H2O
58.44 44.01 18.02
4-[4-(4-Methoxy-phenyl)-piperazin-1-yl]-phenylamine
{4-[4-(4-Methoxy-phenyl)-piperazin-1-yl]-phenyl}-carbamic acid phenyl ester
MDC
Stage-4:
H3CO N N NHCOOPh
C24H25N3O3
403.47
+ N2H4.H2O
Hydrazine hydrate
50.06
1,4-Dioxane
H3CO N N NHCONHNH2
C18H23N5O2
341.41
+
OH
Phenol
C6H6O
94.11
+ H2O
18.02
{4-[4-(4-Methoxy-phenyl)-piperazin-1-yl]-phenyl}-carbamic acid phenyl ester
1,3-Dimethyl-7-{2-[(1-phenyl-2-propanyl)amino]ethyl}-3,7-dihydro-1H-purine-2,6-dione
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Stage-5:
H3CO N N NHCONHNH2
C18H23N5O2
341.41
+ H2N NH + 2CH3COOH
Formamidine
CH4N2
44.07
120.10
H3CO N N N
N
NH
O
C19H21N5O2
351.40
+
Ammonium acetate
2CH3COONH4
154.16
1,3-Dimethyl-7-{2-[(1-phenyl-2-propanyl)amino]ethyl}-3,7-dihydro-1H-purine-2,6-dione
2-{4-[4-(4-Methoxy-phenyl)-piperazin-1-yl]-phenyl}-2,4-dihydro-[1,2,4]triazol-3-one
Stage-6:
H3CO N N N
N
NH
O
C19H21N5O2
351.40
+ +
C4H9Br
137.02
69.10
Methanol
C23H29N5O2
407.51
+ KBr + 1/2CO2 + 1/2 H2O
119.0 22.0 9.01
2-{4-[4-(4-Methoxy-phenyl)-piperazin-1-yl]-phenyl}-2,4-dihydro-[1,2,4]triazol-3-one
H3CCH3
Br
2-Bromo-butane
1/2 K2CO3
H3CO N N NN
N
O
CH3
CH3
4-Isobutyl-2-{4-[4-(4-methoxy-phenyl)-piperazin-1-yl]-phenyl}-2,4-dihydro-[1,2,4]triazol-3-one
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Stage-7:
H3CO N N N
N
N
O
CH3
CH3
C23H29N5O2
407.51
+ 2HBr + Na2CO3
Hydrobromic acid
161.82
106.0
+ CH3OH + 2NaBr +
Methanol
C22H27N5O2
393.48
32.04 205.79 44.01
4-Isobutyl-2-{4-[4-(4-methoxy-phenyl)-piperazin-1-yl]-phenyl}-2,4-dihydro-[1,2,4]triazol-3-one
HO N N NN
N
O
CH3
CH3
2-{4-[4-(4-Hydroxy-phenyl)-piperazin-1-yl]-phenyl}-4-isobutyl-2,4-dihydro-[1,2,4]triazol-3-one
CO2
Stage-8
Step-A
Cl Cl
CH3
O
2,4-Dichloro acetophenone
+
Glycerol
HO OH
OH
+ Br2
C8H6Cl2O
189.04
C3H8O3
92.09
159.81
PTSA
n-Butanol
Cl Cl
O
O
Br
OH
C11H11BrCl2O3
342.01
+ +HBr
80.91
H2O
18.02[2-Bromomethyl-2-(2,4-dichloro-
phenyl)-[1,3]dioxolan-4-yl]-methanol
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Step-B
(Cis Bromo benzoate preparation)
Cl Cl
O
O
Br
OH
[2-Bromomethyl-2-(2,4-dichloro-phenyl)]-[1,3]dioxolan
-4-yl]-methanolC11H11BrCl2O3
342.01
+
Benzoyl chloride
O
Cl
C7H5ClO
140.57
Cl Cl
O
OOCOPh
Br
C18H15BrCl2O4
446.12
+
Benzoic acid 2-bromomethyl-2-(2,4-dichloro-phenyl)-[1,3]dioxolan
-4-ylmethyl ester
HCl
36.46
CIS-BROMO BENZOATE
Stage-9:
ClCl
O
O
Br
OOCC6H5
+ NN
HN
+ 1/2 K2CO3 + NaOHDMF
Water
Cis-bromo benzoate
C18H15BrCl2O4
446.12
1,2,4-Triazole
C2H3N3
69.1
Potassium carbonate
69.0
Sodium hydroxide
40.0
+
C13H13Cl2N3O3
330.17
COONa
Sodium benzoate
144.10
+ KBr + 1/2 CO2 +
119.0 22.0 9.01
O
OHO
NN
N
Cl Cl
[2-(2,4-Dichloro-phenyl)-2-[1,2,4]triazol-1-ylmethyl-[1,3]dioxolan-4-yl]-methanol
C7H5NaO2
1/2 H2O
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Stage-10:
ClCl
O
O
N
HO
N
N
C13H13Cl2N3O3
330.17
+ CH3SO2Cl + (C2H5)3NMDC
Water
C14H15Cl2N3O5S
408.26
+ (C2H5)3N.HCl
Methane sulfonyl chloride
114.55
Triethyl amine
101.19
Triethyl amine hydrochloride
137.65
[2-(2,4-Dichloro-phenyl)-2-[1,2,4]triazol-1-ylmethyl-[1,3]dioxolan-4-yl]-methanol
ClCl
O
O
N
O3SH3C
N
N
1-[2-(2,4-Dichloro-phenyl)-4-ethyl-[1,3]dioxolan-2-ylmethyl]-1H-[1,2,4]triazole;
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Stage-11:
ClCl
O
O
N
O3SH3C
N
N
C14H15Cl2N3O5S
408.26
C22H27N5O2
393.48
+ KOH
56.11
Potassium hydroxide
Methanol
CH3O2SOK + H2O
Methane sulfonate potassium
134.20
18.02
1-[2-(2,4-Dichloro-phenyl)-4-ethyl-[1,3]dioxolan
-2-ylmethyl]-1H-[1,2,4]triazole;(Stage-10)
+ HO N N NN
NO
CH3
CH3
2-{4-[4-(4-Hydroxy-phenyl)-piperazin-1-yl]-phenyl}-4-isobutyl-2,4-dihydro
-[1,2,4]triazol-3-one(Stage-7)
O N N NN
N
O
CH3
CH3Cl Cl
O
O
NN
N
+
C35H38Cl2N8O4
705.63
ITRACONAZOLE
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ITRACONAZOLE
Flow-Chart:
1-(4-Methoxy phenyl ) Piperazine1-Chloro-4-Nitro-benzeneDMFHydrochloric acidPotassium Carbonate
Stage-1DMF RecoveryEffluent water
Stage-1Palladium CarbonDMFHydrogen Gas
Stage-2DMF RecoveryEffluent water
Stage-2Phenyl Chloro formateMethylene DichlorideSodium Bicarbonate
Stage-3MDC RecoveryEffluent water
Stage-3Hydrazine Hydrate1,4-Dioxane
Stage-4 1,4-Dioxane Recovery
Stage-4FormamidineDimethyl FormamideAcetic Acid
Stage-5 DMF RecoveryEffluent water
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Stage-52-Bromo ButanePotassium CarbonateMethanolDimethyl Formamide
Stage-6DMF RecoveryMethanol Recovery
Stage-6Hydrogen BromideSodium CarbonateMethanol
Stage-7 Methanol Recovery
2,4 -DichloroacetophenoneGlycerolLiq Brominen-ButanolBenzoyl chlorideToluenep-Toluenesulfonic acid
Stage-8Toluene Recoveryn-Butanol recovery
Cis-Bromo Benzoate1,2,4-TriazoleSodium HydroxidePotassium CarbonateDimethyl Formamide
Stage-9 DMF Recovery
Stage-10
Stage-9Methane Sulfonyl ChlorideTriethylamineMethylene DichlorideIsopropyl Alcohol
MDC RecoveryIsopropyl Alcohol Recovery
Stage-11
Stage-7Stage-10Potassium HydroxideActivated CarbonDimethyl FormamideMethanol
DMF RecoveryMethanol Recovery
Itraconazole
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Material Balance:
Material Balance of Itraconazole Stage-1 Batch Size:200.00Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
1-(4-Methoxy phenyl ) Piperazine
57.00 Stage-1 92.00
1-Chloro-4-Nitro-benzene 46.30 DMF Recovery 95.00
DMF 100.00 DMF Loss 5.00
Hydrochloric acid 10.70 Effluent Water (Water3, gen.Water-5.4 Potassium chloride-44.2)
349.60
Potassium Carbonate 40.60
Water 300.00 Process Emissions (Carbon Dioxide)
13.00
Total 554.60 Total 554.60
Material Balance of Itraconazole
Stage-2 Batch Size:200.00Kg
Name of the input Quantity
in Kg
Name of the out put Quantity
in Kg
Stage-1 92.00 Stage-2 83.00
Palladium Carbon 5.00 DMF Recovery 95.00
DMF 100.00 DMF Loss 2.00
Hydrogen Gas 1.80 Effluent Water
(Water-300,gen.Water-10.6)
310.60
Water 300.00
Spent Catalyst
(Palladium Carbon Reuse)
5.00
Organic Residue
Process residue-0.2
Distillation Residue-3
(DMF)
3.20
Total 498.80 Total 498.80
Material Balance of Itraconazole
Stage-3 Batch Size:200.00Kg
Name of the input Quantity
in Kg
Name of the out put Quantity
in Kg
Stage-2 83.00 Stage-3 117.00
Phenyl Chloro formate 45.40 MDC Recovery 190.00
Methylene Dichloride 200.00 MDC Loss 10.00
Sodium Bicarbonate 24.40 Effluent Water 372.45
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Water 350.00 (Water-350,
gen.Water-5.3,
Sodium chloride-17.15 )
Process Emissions
(Carbon Dioxide)
12.90
Organic Residue
(Process residue-0.45
0.45
Total 702.80 Total 702.80
Material Balance of Itraconazole
Stage-4 Batch Size:200.00Kg
Name of the input Quantity
in Kg
Name of the out put Quantity
In Kg
Stage-3 117.00 Stage-4 99.00
Hydrazine Hydrate 14.55 1,4-Dioxane Recovery 190.00
1,4-Dioxane 200.00 1,4-Dioxane Loss 10.00
Water 300.00 Effluent Water
(Water-300, gen.Water-5.25)
305.25
Organic Residue
(process residue-27.3
(Phenol)
27.30
Total 631.55 Total 631.55
Material Balance of Itraconazole Stage-5 Batch Size:200.00Kg
Name of the input Quantity in Kg
Name of the out put Quantity In Kg
Stage-4 99.00 Stage-5 101.00
Formamidine 12.70 DMF Recovery 190.00
Dimethyl Formamide 200.00 DMF Loss 10.00
Acetic Acid 34.60 Effluent Water (Water-300, Ammonium acetate-44.70)
344.70
Water 300.00
Organic Residue Process residue-0.6
0.60
Total 646.30 Total 646.30
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Material Balance of Itraconazole
Stage-6 Batch Size:200.00Kg
Name of the input Quantity
in Kg
Name of the out put Quantity
in Kg
Stage-5 101.00 Stage-6 116.0
2-Bromo Butane 39.00 DMF Recovery 285.00
Potassium Carbonate 19.70 DMF Loss 6.00
Methanol 100.00 Methanol Recovery 95.00
Dimethyl Formamide 300.00 Methanol Loss 2.00
Water 300.00 Effluent Water
(Water-300, gen.Water-2.6,
Potassium bromide-34.2,
DMF-4)
340.80
Process Emissions
(Carbon Dioxide)
6.35
Organic Residue
(Process residue-0.55,
Distillation Residue-8
(Methanol-3, DMF-5)
8.55
Total 859.7 Total 859.7
Material Balance of Itraconazole Stage-7 Batch Size:200.00Kg
Stage-6 116.00 Stage-7 112.00
Hydrobromic acid 46.10 Methanol Recovery 190.00
Sodium Carbonate 30.20 Methanol Loss 4.00
Methanol 200.00 Effluent Water (Water-300, Sodium bromide-58.60, Methanol-9.10)
367.70
Water 300.00
Process Emissions (Carbon Dioxide)
12.60
Organic residue Distillation Residue-6 (Methanol)
6.00
Total 692.30 Total 692.30
Material Balance of Itraconazole Stage-8(Cis –Bromobenzoate) Batch Size:200.00Kg
2,4 -Dichloroacetophenone 55.00 Stage-8 (Cis –Bromobenzoate) 128.00
Glycerol 26.70 n-Butanol Recovery 190.00
Liq Bromine 46.30 n-Butanol Loss 4.00
n-Butanol 200.00 Toluene Recovery 190.00
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Benzoyl chloride 40.35 Toluene Loss 4.00
Toluene 200.00 By-Products (Hydrobromic acid-23.55, Hydrochloric acid -10.55, )
34.10
p-Toluenesulfonic acid 5.00
Water 300.00 Effluent water (Water-300, Generated water-5.25 p-Toluenesulfonic acid-5, n-Butanol-6)
316.25
Organic residue Process residue-1 Distillation Residue-6 (Toluene-6)
7.00
Total 1373.35 Total 1373.35
Material Balance of Itraconazole
Stage-9 Batch Size:200.00Kg
Name of the input Quantity in
Kg
Name of the out put Quantity
in Kg
Cis-Bromo Benzoate 128.00 Stage-9 94.00
1,2,4-Triazole 19.70 DMF Recovery 95.00
Sodium Hydroxide 19.65 DMF Loss 2.00
Potassium Carbonate 11.40 Effluent Water
(Water-300, gen.Water-2.60
Potassium Bromide-34.15,
Sodium Benzoate-41.35)
378.10
Dimethyl Formamide 100.00
Water 300.00 Process Emissions
(Carbon dioxide)
6.35
Organic residue
Process residue-0.3
Distillation Residue-3
(DMF)
3.30
Total 578.75 Total 578.75
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Material Balance of Itraconazole
Stage-10 Batch Size:200.00Kg
Name of the input Quantity
in Kg
Name of the out put Quantity
in Kg
Stage-9 94.00 Stage-10 116.00
Methane Sulfonyl Chloride 32.55 MDC Recovery 190.00
Triethylamine 28.80 MDC Loss 4.00
Methylene Dichloride 200.00 Isopropyl Alcohol Recovery 190.00
Isopropyl Alcohol 200.00 Isopropyl Alcohol Loss 4.00
Water 300.00 Effluent Water
(Water-300,Triethylamine
Hydrochloride-39.20, Isopropyl
Alcohol-6)
345.20
Organic Residue
Process residue-0.15
Distillation Residue-6
(MDC)
6.15
Total 855.35 Total 855.35
Material Balance of Itraconazole
Stage-11 Batch Size:200.00Kg
Name of the input Quantity
in Kg
Name of the out put Quantity
in Kg
Stage-7 112.00 Itraconazole 200.00
Stage-10 116.00 Dimethyl Formamide Recovery 190.00
Potassium Hydroxide 16.00 Dimethyl Formamide Loss 4.00
Activated Carbon 8.00 Methanol Recovery 190.00
Dimethyl Formamide 200.00 Methanol Loss 4.00
Methanol 200.00 Effluent Water
(Water-300
gen.Water-5.15,
DMF-6,
Potassium Methane Sulfonate-
38.15)
349.30
Water 300.00
Spent Carbon 8.00
Organic residue
Process residue-0.70
Distillation Residue-6
(Methanol-6)
6.70
Total 952 Total 952
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8. KETOCONAZOLE
Process Description:
Stage-1 (Preparation of Cis – Bromo benzoate)
Step-A
2, 4-Dichloroacetophenone reacts with Glycerol and Bromine in presence of
toluene,n-butanol and PTSA to give step-A product.
Step-B
Step-A product reacts with benzoyl chloride in presence of toluene to give stage-1
cis bromo benzoate product.
Stage-2
Stage-1 reacts with 1H-Imidazole in presence of Sodium hydroxide, Methanol and
TBAB, DMF and toluene to give stage-2 product.
Stage-3
Stage-2 product reacts with p-Toluene Sulfonyl chloride in presence of sodium
carbonate, Activated carbon, Ethyl acetate and n-Hexane to give stage-3 product.
Stage-4
4-Chlorophenol undergoes condensation with Piperazine and Acetic acid in
presence of n-Butanol and Water to give stage-4 product.
Stage-5
Stage-5 compound undergoes condensation with Stgae-4 to give Ketoconazole in
presence of sodium methoxide, and Sodium hydroxide to give crude of
Ketoconazole. Further undergoes purification with Activated Carbon, Methanol and
Ethyl Acetate to give pure Ketoconazole
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Route of Synthesis:
Stage-1(Preparation of Cis –Bromo benzene)
Step-A
Cl Cl
CH3
O
2,4-Dichloro acetophenone
+
Glycerol
HO OH
OH
+ Br2
C8H6Cl2O
189.04
C3H8O3
92.09
159.81
PTSA
n-Butanol
Cl Cl
O
O
Br
OH
[2-Bromomethyl-2-(2,4-dichloro-phenyl)]-[1,3]dioxolan
-4-yl]-methanolC11H11BrCl2O3
342.01
+ +HBr
80.91
H2O
18.02
Step-B
Cl Cl
O
O
Br
OH
[2-Bromomethyl-2-(2,4-dichloro-phenyl)]-[1,3]dioxolan
-4-yl]-methanolC11H11BrCl2O3
342.01
+
Benzoyl chloride
O
Cl
C7H5ClO
140.57
Cl Cl
O
OOCOPh
Br
C18H15BrCl2O4
446.12
+
Benzoic acid 2-bromomethyl-2-(2,4-dichloro-phenyl)-[1,3]dioxolan
-4-ylmethyl ester
HCl
36.46
CIS-BROMO BENZOATE
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Stage-2
N
HN
+
1H-Imidazole
C3H4N2
68.08
+ NaOH
40.00
Cl Cl
O
OOH
N
N
H
C14H14Cl2N2O3
329.18
+
Cl Cl
O
OOCOPh
Br
C18H15BrCl2O4
446.12
Benzoic acid 2-bromomethyl-2-(2,4-dichloro-phenyl)-[1,3]dioxolan
-4-ylmethyl ester
OH
O
+
C7H6O2
122.12
Benzoic acid
NaBr
102.89Cis-2-(2,4-Dichlorophenyl)-2-(1H-imidazol-1-yl methyl)-1,3-dioxolane-4-Methanol
TBAB
Methanol
CIS-BROMO BENZOATE
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Stage-3
cis-2-(2,4-dichlorophenyl)-2-(1H-imidazol-1-ylmethyl)-1,3-dioxolane-4-methanol
O
O
N
N
Cl Cl
OH
para tolune sulfonyl chloride
S
O
O
ClH3C
Na2CO3+ +
(cis-Imidazole Alcohol)C14H14Cl2N2O3
329.18
C7H7ClO2S
190.65
O
O
N
N
Cl Cl
OS
O O
CH3
Toluene-4-sulfonic acid 2-(2,4-dichloro-phenyl)-2-imidazol-1-ylmethyl-[1,3]dioxolan-4-ylmethyl ester
cis-TosylateC21H20Cl2N2O5S
483.36
+ 2 NaCl + +
116.89
105.99
+ HCl
36.46
CO2
44.01
H2O
18.02
Stage-4
OH
Cl
4-Chloro-phenolC6H5ClO
128.56
+
HN NH
Piperazine
C4H10N2
86.14
+
H3C OH
O
Acetic acid
60.05
N N CH3
O
HO
1-Acetyl-4-(4-hydroxy phenyl)piperazine
C12H16N2O2
220.27
+ HCl + H2O
36.46 18.02
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Stage-5
O
O
N
N
Cl Cl
OS
O O
CH3
Toluene-4-sulfonic acid 2-(2,4-dichloro-phenyl)-2-imidazol-1-ylmethyl-[1,3]dioxolan-4-ylmethyl ester
cis-Tosylate
C21H20Cl2N2O5S
483.36
+ CH3ONa + NaOH
1-Acetyl-4-(4-hydroxyphenyl)
piperazine
+
C12H16N2O2
220.27
54.02
CH3
ONNOO
O
NN
Cl
Cl + CH3OH
CH3
+
Ketoconazole
531.43
C26H28Cl2N4O4
Toluene
C7H7
91.13
32.04
+ Na2SO4
142.04
O CH3
OH
40.00
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Flow Chart:
Stage-1
Stage-2
Stage-3
Stage-4
Stage-5
KETOCONAZOLE
2,4-Dichloro AcetophenoneGlycerolLiquid BromineBenzoyl chlorideMethanolToluene
Toluene RecMethanol RecEffluent water
Stage-1 (Cis -Bromo benzoate)ImidazoleSodium hydroxideMethanolTBAB
Methanol Rec
Stage-2(Cis-Imidazole alcohol)Para Toluene Sulfonyl ChlorideSodium CarbonateMethanolEthyl Acetate
Methanol RecEthyl acetate Rec
Stage-4Stage-3Sodium methoxideSodium hydroxideAcetoneMethanolEthyl Acetate
Methanol RecEthyl acetate RecAcetone Rec
4-ChlorophenolPiperazineAcetic acidn-Butanol
n-Butanol RecEffluent water
Material Balance:
Material Balance of Ketoconazole Stage-1(Cis –Bromo benzoate) Batch Size:100Kg
Name of the input Quantity in Kg
Name of the out put Quantity In Kg
2,4-Dichloro Acetophenone 43.00 Stage-1(Cis –Bromo benzoate) 93.00
Glycerol 21.00 Mixed solvents (Methanol+Toluene )Recovery
570.00
Liquid Bromine 36.00 Methanol Loss 15.00
Benzoyl chloride 31.00 Toluene Loss 15.00
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Methanol 300.00 n-Butanol Recovery 95.00
Toluene 300.00 n-Butanol Loss 2.00
ParaToluene Sulphonic acid 7.50 Effluent water 411.51
n-Butanol 100.00 (Water-400, Generated water-4.01, PTSA-7.5 )
Water 400.00 By-Products 25.87
(Hydrobromic acid-18.04, Hydrochloric acid-7.83)
Organic residue (Process rersidue-8.12 Distillation Residue-3 ( Butanol-3)
11.12
Total 1238.5 Total 1238.5
Material Balance of Ketoconazole
Stage-2 Batch Size:100Kg
Name of the input Quantity
in Kg
Name of the out put Quantity
in Kg
Stage-1 (Cis –Bromo benzoate) 93.00 Stage-2(Cis-Imidazole alcohol) 66.00
Imidazole 15.00 Methanol Recovery 285.00
Sodium hydroxide 9.00 Methanol loss 6.00
Methanol 300.00 Effluent water 466.50
TBAB 20.00 (water-400,
Sodium bromide-21.26,
TBAB-20, Benzoic acid-25.24)
Water 400.00 Organic residue 13.50
Process residue-4.50
Distillation Residue-9
(Methanol)
Total 837 Total 837
Material Balance of Ketoconazole Stage-3 Batch Size:100Kg
Name of the input Quantity in Kg
Name of the out put Quantity In Kg
Stage-2(Cis-Imidazole alcohol)
66.00 Stage-3(Cis –Tosylate) 94.00
Para Toluene Sulfonyl Chloride
39.00 Methanol Recovery 190.00
Sodium Carbonate 22.00 Methanol Loss 10.00
Methanol 200.00 Methylene DichlorideRecovery 190.00
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Methylene Dichloride 200.00 Methylene Dichloride Loss 10.00
Hydrochloric Acid 8.00 Ethyl Acetate Recovery 285.00
Ethyl Acetate 300.00 Ethyl Acetate loss 6.00
n-Hexane 300.00 n-Hexane Recovery 285.00
Activated Carbon 2.50 n-Hexane Loss 6.00
DM Water 400.00 Effluent Water 441.04
(Water-400, generated water-3.61, Sodium chloride-23.43,Ethyl acetate-9 Hexane-5)
Spent Carbon 2.50
Process emission 8.82
(Carbon dioxide)
Organic residue (Process residue-5.14, Distillation Residue-4 ( Hexane-4)
9.14
Total 1537.5 Total 1537.5
Material Balance of Ketoconazole Stage-4 Batch Size:100Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
4-Chlorophenol 26.00 Stage-4 43.00
Piperazine 18.00 n-Butanol Recovery 285.00
Acetic acid 12.00 n-Butanol Loss 6.00
n-Butanol 300.00 Effluent water 408.60
Water 400.00 (Water-400, Generated water-3.6, Butanol-5)
By-product 7.29
(Hydrochloric acid)
Organic residue Process Residue-2.11, Distillation Residue-4 (Butanol)
6.11
Total 756. Total 756
Material Balance of Ketoconazole Stage-5 Batch Size:100Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-3 94.00 Ketoconazole 100.00
Stage-4 43.00 Acetone Recovery 285.00
Sodium methoxide 11.00 Acetone Loss 6.00
Sodium hydroxide 8.00 Methanol Recovery 228.00
Acetone 300.00 Methanol Loss 5.00
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Methanol 240.00 Ethyl Acetate Recovery 313.00
Ethyl Acetate 330.00 Ethyl Acetate Loss 7.00
Activated Carbon 3.00 Effluent Water 423.89
DM Water 400.00 (Water-400, Toluene-17.68, Methanol-6.21)
Inorganic solid waste (Sodium sulphate)
27.55
Spent Carbon 3.00
Organic Residue (Process residue-4.56 Distillation Residue-26 (Acetone-9,Methanol-7,Ethyl acetate-10)
30.56
Total 1429 Total 1429
9.LEVO CETIRIZINE DI HYDROCHLORIDE
Process Description
Stage-1
Step-A
P-Chlorobenzo phenone undergoes Amination with Ammonium formate in presence
of Toluene to give Step-A product.
Step-B
Step-A product undergoes salt formation with HCl inpresence of Methanol to give
Stage-1 Product..
Stage-2
Step-A
Stage-1product undergoes resolution with tartaric acid in presence of Sodium
hydroxide to give Step-A product
Step-B
Step-A product undergoes Hydrolysis with Sodium hydroxide in presence of
Methanol and HCl to give Stage-2 Product.
Stage-3
PTSC undergoes condensation with n,n-bis(2-chloroethyl)amine Hydrochloride in
presence of MDC and sodium htdroxide to give Stage-3 Product.
Stage-4
Stage-3 Product react with (L)-(4-chloro-phenyl)-c-phenyl-methylamine-1-methane
sulfonyl-4-methyl-benzene(2-ethyl-methyl-amine) in presence of methanol to give
Stage-4 Product.
Stage-5
Stage-4 product undergoes hydrolysis with HBr and Acetic Acid in presence of
Toluene to give Stage-5 product.
Stage-6
Stage-5 product reacts with Chloro ethanol in presence of Triethyl amine and
Toluene to give stage-6 product
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Stage-7
Step-A
Stage-6 product undergoes condensation with Sodium monochloro acetate in
presence of DMF, Acetone and HCl to give Levocetrizine dihydrochloride crude.
Step-B
Levocetrizine dihydrochloride crude purified in Dichloromethane, Activated carbon &
Acetone to give Levocetrizine dihydrochloride
LEVOCETIRIZINE DIHYDROCHLORIDE Route of Synthesis:
Stage-1
Step-A
O
Cl
p-chloro benzophenone
Ammonium formate
63.06
+ Toluene Cl
NH2
C-(4-Chloro-phenyl)-C-phenyl-
methylamine
+ CO2 + H2O
44.00 18.02
NH4HCO2
C13H9ClO
216.66C13H12ClN
217.69
Step-B
Cl
NH2
+
C-(4-Chloro-phenyl)-C-phenyl-methylamine
HCl
36.46
MethanolCl
NH2
C-(4-Chloro-phenyl)-C-phenyl-methylamine Hydrochloride
HCl
C13H12ClN
217.69C13H13Cl2N
254.19
.
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Stage-2(Resolution)
Step-A
Cl
NH2
C-(4-Chloro-phenyl)-C-phenyl-methylamine Hydrochloride
HCl
C13H13Cl2N
254.19 X 2=508.38
.
+
Tartaric acid
OH
OHO
OH
O
OH
C4H6O6
150.09
+ 2 NaOH
80.00
Cl
NH2 OH
OHO
OH
O
OH.
C-(4-Chloro-phenyl)-C-phenyl-methylamin 2,3-dihydroxy-succinic acid
C17H18ClNO6
367.78
+
Isomer
Cl
NH2
C13H12ClN
217.69
+ 2 NaCl
116.88
+ 2 H2O
36.02
2
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Step-B (Hydrolysis)
Cl
NH2 OH
OHO
OH
O
OH.
C-(4-Chloro-phenyl)-C-phenyl-methylamin 2,3-dihydroxy-succinic acid
C17H18ClNO6
367.78
+
Cl
NH2
C13H12ClN
217.69
NaOH
40.00
+ HCl
36.46
C-(4-Chloro-phenyl)-C-phenyl-methylamine
OH
OHO
OH
O
OH
+
Tartric acid
C4H6O6
150.09
+ NaCl
58.44
+ H2O
18.02
Stage-3
para toluene sulphonyl chloride
n,n-bis( 2-chloro ethyl) amine
Hydrochloride
80.001-Methanesulfonyl-4-methyl-
benzene,(2-chloro-ethyl)-chloromethyl-
amine
CH3
SO2Cl +HN
Cl
ClHCl
+ 2NaOHMDC
CH3
SO2N
Cl
Cl
C11H15Cl2NO2S
296.21
+ 2NaCl
116.89
+ 2H2O
36.0
C7H7ClO2S
190.65
C4H10Cl3N
178.5
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Stage-4
1-Methanesulfonyl-4-methyl-benzene,
(2-chloro-ethyl)-chloromethyl-amine
CH3
SO2 N
Cl
Cl
C11H15Cl2NO2S
296.21
Cl
NH2
+
(L)_(4-Chloro-phenyl)-C-phenyl-methylamine-1-methane sulfonyl
-4-methyl-benzene(2-ethyl-methyl-amine
C13H12ClN
217.69
N
Cl
N S
O
O
CH3
1-[(4-Chloro-phenyl)-phenyl-methyl]-4-(toluene-4-sulfonyl)-piperazine
+
C24H25ClN2O2S
440.99
MeOH
2HCl
72.92
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Stage-5
N
Cl
N S
O
O
CH3
1-[(4-Chloro-phenyl)-phenyl-methyl]-4-(toluene-4-sulfonyl)-piperazine
C24H25ClN2O2S
440.99
+ HBr + CH3COOH
Hydrobromic acid
80.91
Acetic acid
60.05
N
HN
Cl
1-[(4-Chloro-phenyl)-phenyl-methyl]-piperazine
+ CH3COOBr +
SO2H
CH3
C17H19ClN2
286.80
Bromo acetate
138.95
pTSA
156.20
C7H8O2S
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Stage-6
N
HN
Cl
1-[(4-Chloro-phenyl)-phenyl-methyl]-piperazine
C17H19ClN2
286.80
+
Chloro ethanol
C2H5ClO80.51
C19H23ClN2O
330.85
CH3
OH
Cl
1-{4-[(4-Chloro-phenyl)-phenyl-methyl]-piperazin-1-yl}-ethanol
CH3
NN
Cl
OH
+ HCl
+
Triethylamine
N
C6H15N
101.19
N .
Triethylamine Hydrogen chloride
C6H16ClN
137.65
Stage-7
C19H23ClN2O
330.85
1-{4-[(4-Chloro-phenyl)-phenyl-methyl]-piperazin-1-yl}-ethanol
CH3
NN
Cl
OH
Sodium monochloro acetate
Na+
O
O-Cl + 2HCl
DMF, MDC, Acetone, Activated Carbon ,
C2H2ClNaO2
116.48
Hydrochloric acid
2x36.46=72.92
NaCl
levocetirizine dihydrochlorideSodium chloride
58.44C21H25ClN2O3.2HCl
461.81
+
CH3
O
OO
N
N
Cl2 HCl
+
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Flow Chart:
Stage - 1
Stage - 2
Stage - 3
Stage - 4
Stage - 5
p-chloro benzo phenoneAmmonium formateHydrochloric acidTolueneActivated carbonWater
Effluent waterToluene Recovery
Stage-1Sodium hydroxideTartaric acidMDCHydrochloric acidWater
MDC RecoveryEffluent Water
para toluene sulphonyl chloriden,n-bis( 2-chloro ethyl)amine HClSodium HydroxideMDCWater
MDC RecoveryEffluent Water
Stage-3Stage-2Ethyl di isopropyl amineMethanol
Methanol RecoveryEthyl di isopropyl amine Reuse
Stage-4Hydro bromic acidAcetic acidTolueneWater
Toluene RecoveryEffluent Water
Stage - 6
Stage-5Chloro ethanolTriethyl amineTolueneWater
Toluene RecoveryEffluent Water
Stage - 7
Stage-6Sodium mono chloro acetateHydrochloric acidDi methyl formamideMDCActivated CarbonAcetoneWater
MDC RecoveryAcetone RecoveryDMF RecoveryEffluent Water
LevocetirizineDi Hydrochloride
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Material Balance:
Material balance of Levo Cetrizine di Hydrochloride
Stage-1 Batch Size: 100Kg
Name of the input Quantity
in kg
Name of the out put Quantity
in Kg
p-chloro benzo phenone 125.00 Stage-1 136.00
Ammonium formate 37.00 Toluene Recovery 760.00
Hydrochloric acid 21.00 Toluene Loss 16.00
Toluene 800.00 Effluent Water 422.32
Activated carbon 5.00 (Water-400,
generated water-10.32,
Toluene-12)
Water 400.00 Spent carbon 5.00
Process Emission 25.21
(Carbon dioxide)
Organic residue 23.47
(Process residue-11.47
Distillation Residue-12
(Toluene-12)
Total 1388.00 Total 1388.00
Material balance of Levocetirizine Dihydrochloride
Stage-2 Batch Size: 100Kg
Name of the input Quantity
in kg
Name of the out put Quantity
in Kg
Stage-1 136.00 Stage-2 55.00
Sodium hydroxide 33.00 MDC Recovery 665.00
Tartaric acid 40.00 MDC Loss 14.00
MDC 700.00 Effluent Water 560.42
Hydrochloric acid 10.00 (Water-500,
generated water-14.23,
Sodium Chloride-46.19)
Water 500.00 Organic Residue 124.58
(Process Residue-103.58
(Isomer-58, Tartaric acid-
38.74)
Distillation Residue-21
(MDC-21)
Total 1419.00 Total 1419.00
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Material balance of Levocetirizine Dihydrochloride
Stage-3 Batch Size: 100Kg
Name of the input Quantity
in kg
Name of the out put Quantity
in Kg
para toluene sulphonyl chloride 50.00 Stage-3 74.00
n,n-bis( 2-chloro ethyl)
amine HCl
46.00 MDC Recovery 665.00
Sodium Hydroxide 21.00 MDC Loss 14.00
MDC 700.00 Effluent Water 439.37
Water 400.00 (Water-400,
generated water-9.27,
Sodium chloride-30.1)
Organic Residue 24.63
(Process Residue-3.63,
Distillation Residue-21
(MDC-21)
Total 1217.00 Total 1217.00
Material balance of Levocetirizine Dihydrochloride
Stage-4 Batch Size: 100Kg
Name of the input Quantity
in kg
Name of the out put Quantity
in Kg
Stage-3 74.00 Stage-4 107.00
Stage-2 55.00 Methanol Recovery 380.00
Ethyl di isopropyl amine 28.00 Methanol Loss 8.00
Methanol 400.00 Ethyl di isopropyl amine Reuse 28.00
By -product 18.24
(Hydrochloric acid)
Organic Residue 15.76
(Process Residue-3.76,
Distillation Residue-12
(Methanol-12)
Total 557.00 Total 557.00
Material balance of Levocetirizine Dihydrochloride
Stage-5 Batch Size: 100Kg
Name of the input Quantity
in kg
Name of the out put Quantity
in Kg
Stage-4 107.00 Stage-5 67.00
Hydro bromic acid 20.00 Toluene Recovery 380.00
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Acetic acid 15.00 Toluene Loss 8.00
Toluene 400.00 Effluent Water 177.07
Water 100.00
(Water-100,
Bromoacetate-33.46,
PTSA-37.61,Toluene-6)
Organic Residue 9.93
(Process Residue-3.93,
Distillation Residue-6
(Toluene-6)
Total 642.00 Total 642.00
Material balance of Levocetirizine Dihydrochloride
Stage-6 Batch Size: 100Kg
Name of the input Quantity
in kg
Name of the out put Quantity
in Kg
Stage-5 67.00 Stage-6 74.00
Chloro ethanol 19.00 Toluene Recovery 380.00
Triethyl amine 24.00 Toluene Loss 8.00
Toluene 400.00 Effluent Water 306.00
Water 300.00 (Water-300,Toluene-6)
By –Products
(Triethyl amine hydrogen
chloride) 31.74
Organic Residue 10.26
(Process Residue-4.26,
Distillation Residue-6
(Toluene-6)
Total 810.00 Total 810.00
Material balance of Levocetirizine Dihydrochloride
Stage-7 Batch Size: 100Kg
Name of the input Quantity
in kg
Name of the out put Quantity
in Kg
Stage-6 74.00 Levocetirizine Dihydrochloride 100.00
Sodium mono chloro acetate 26.00 MDC Recovery 237.00
Hydrochloric acid 17.00 MDC Loss 5.00
Di methyl formamide 100.00 Acetone Recovery 95.00
MDC 250.00 Acetone Loss 2.00
Activated Carbon 5.00 DMF Recovery 95.00
Acetone 100.00 DMF Loss 2.00
Water 200.00 Effluent Water 216.04
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(Water-200,
Sodium chloride-13.04,
DMF-3)
Spent Carbon 5.00
Organic Residue 14.96
Process Residue-3.96,
Distillation Residue-11
(MDC-8, Acetone-3
Total 772 Total 772
10. LINAGLIPTIN
Process Description:
Stage-1
8-Bromo-7-but-2-ynyl-3-methyl -3,7-dihydro-purine-2,6-dione reacts with 2-
(chloromethyl)-4-methyl quinazoline in presence of DMSO, water and Ethanol to give
Stage-1 Product.
Stage-2
Stage-1 Product reacts with Boc-3 Amino Piperidine in presence of DMSO, Iso
propyl ether and Ethyl acetate to give Stage-2 Product.
Stage-3:
Stage-2 Product undergoes Hydrolysis with water in presence of MDC, Methanol
and Ethanol to give Stage-3 Product.
Stage-4
Stage-3 Product undergoes Purification in Methanol ,IPA and Activated Carbon to
give Linagliptin.
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LINAGLIPTIN
Route of Synthesis:
Stage-1
N
NN
HN
O
O
CH3
CH3
Br
N
N
CH3
Cl
2-(chloromethyl)-4-methyl quinazoline
N
NN
N
O
N
N
CH3 CH3
CH3
Br
8-bromo-7-(but-2-yn-1yl)-3-methyl-1-[(4-methyl quinazolin-2-yl)methyl]-3,4,5,7-
tetrahydro-1H-purine-2,6-dione
C20H19BrN6O2
455.31
O
DMSO ,Ethanol
8-Bromo-7-but-2-ynyl-3-methyl-3,7-dihydro-purine-2,6-dione
C10H9BrN4O2
297.11
+
C10H9ClN2
192.64
+ H2O
18.02
+ HCl
36.46
+ 0.5 O2
16.00
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Stage-2
N
NN
N
O
N
N
CH3 CH3
CH3
Br
8-bromo-7-(but-2-yn-1yl)-3-methyl-1-[(4-methyl quinazolin-2-yl)methyl]-3,4,5,7-
tetrahydro-1H-purine-2,6-dione
C20H19BrN6O2
455.31
O
Boc-3-Amino piperidine
NHNH
O
O+
C10H20N2O2
200.28
N
NN
N
O
N
N
CH3 CH3
CH3O
HN
N
O
O
CH3
CH3
CH3
N-BOC-Linagliptin
C30H36N8O4
572.66
(R)-tert-butyl (1-(7-(but-2-yn-1-yl)-3-methyl-1-((4-methylquinazolin-2-yl)methyl)-2,6-dioxo-2,3,6,7-tetrahydro-1H-purin-8-yl)piperidin-3-yl)carbamate
+ HBr
80.91
+ H2
2.02
DMSO, Iso propyl ether, Ethyl acetate
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Stage-3
N
NN
N
O
N
N
CH3 CH3
CH3O
HN
N
O
O
CH3
CH3
CH3
N-BOC-Linagliptin
C30H36N8O4
572.66
(R)-tert-butyl (1-(7-(but-2-yn-1-yl)-3-methyl-1-((4-methylquinazolin-2-yl)methyl)-2,6-dioxo-2,3,6,7-tetrahydro-1H-purin-8-yl)piperidin-3-yl)carbamate
MDC, Methanol Ethanol
N
NN
N
O
N
N
CH3 CH3
CH3O
H2N
N
(R)-8-(3-aminopiperidin-1-yl)-7-(but-2-yn-1-yl)-3-methyl-1-((4-methylquinazolin-2-yl)methyl)
-1H-purine-2,6(3H,7H)-dione
C25H28N8O2
472.54
O
O
CH3
CH3
CH3
HO
Carbonic acid mono-tert-butyl ester
+
C5H10O3
118.13
+ H2O
18.02
Stage-4:
N
NN
N
O
N
N
CH3 CH3
CH3O
H2N
N
(R)-8-(3-aminopiperidin-1-yl)-7-(but-2-yn-1-yl)-3-methyl-1-((4-methylquinazolin-2-yl)methyl)
-1H-purine-2,6(3H,7H)-dione
C25H28N8O2
472.54
Methanol, IPA, Activated Carbon
N
NN
N
O
N
N
CH3 CH3
CH3O
H2N
N
Linagliptin
C25H28N8O2
472.54
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LINAGLIPTIN
Flow chart:
8-Bromo-7-but-2-ynyl-3-methyl-3,7-dihydro-purine-2,6-dione2- Chloromethyl-4- methyl quinazolineDimethyl sulfoxideEthanolWater
Stage-1Boc-3- amino piperidineDimethyl sulfoxideIsopropyl etherEthyl acetateActivated carbonWater
Dimethyl sulfoxide RecoveryIsopropyl ether recoveryEthyl acetate recoveryEffluent water
Stage-2Sodium sulphateEthanolMethanolMethylene chlorideWater
Methylene chloride Recovery Ethanol RecoveryMethanol RecoveryEffluent water
Stage-1
Stage-2
Stage-3
Dimethy sulfoxide Recovery Ethanol RecoveryEffluent water
Stage-3Isopropyl AlcoholActivated CarbonMethanol
Isopropyl Alcohol RecoveryMethanol Recovery
Stage-4
Linagliptin
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Material Balance:
Material balance of Linagliptin Stage-1 Batch size : 100kg
Name of the input Quantity
in kg
Name of the out put Quantity
in kg
8-Bromo-7-but-2-ynyl-3-methyl-3,7-dihydro-purine-2,6-dione
72.00 Stage-I 107.00
2- Chloromethyl-4- methyl quinazoline
47.00 Dimethy sulfoxide Recovery 190.00
Dimethyl sulfoxide 200.00 Dimethy sulfoxide Loss 10.00
Ethanol 200.00 Ethanol Recovery 190.00
Water 300.00 Ethanol Loss 4.00
EffulentWater 295.64
(Water -295.64)
By- Product (Hydrochloric acid-8.83)
8.83
Process emission 3.87
(Oxygen-3.87)
Organic Residue 9.66
Process Residue-3.66 Distillation Residue-6 ( Ethanol-6)
Total 819 Total 819
Material balance of Linagliptin
Stage-2 Batch size : 100kg
Name of the input Quantity
in kg
Name of the out put Quantity
in kg
Stage-1 107.00 Stage-2 130.00
Boc-3- amino piperidine 47.00 Dimethyl sulfoxide Recovery 190.00
Dimethyl sulfoxide 200.00 Dimethyl sulfoxide loss 10.00
Isopropyl ether 200.00 Isopropyl ether recovery 190.00
Ethyl acetate 200.00 Isopropyl ether loss 10.00
Activated carbon 5.00 Ethyl acetate recovery 190.00
Water 300.00 Ethyl acetate loss 4.00
Effluent water
(Water-300)
300.00
By –product
(Hydrobromic acid-19.01)
19.01
Spent Carbon 5.00
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Process emission 0.47
(Hydrogen-0.47)
Organic Residue 10.52
Process Residue-4.52,
Distillation Residue-6
(Ethyl acetate-6)
Total 1059 Total 1059
Material balance of Linagliptin
Stage-3 Batch size : 100kg
Name of the input Quantity
in kg
Name of the out put Quantity
in kg
Stage-2 130.00 Stage-3 104.00
Sodium sulphate 25.00 Methylene chloride Recovery 190.00
Ethanol 200.00 Methylene chloride Loss 10.00
Methanol 200.00 Ethanol Recovery 190.00
Methylene chloride 200.00 Ethanol Loss 10.00
Water 300.00 Methanol Recovery 190.00
Methanol Loss 10.00
Effluent water 322.72
(Water-295.9, Carbonic
acidmono-tert-butylester-26.82)
Inorganic solid waste 25.00
(Sodium sulphate)
Organic Residue 3.28
Total 1055 Total 1055
Material balance of Linagliptin
Stage-4 Batch size : 100kg
Name of the input Quantity
in kg
Name of the out put Quantity
in kg
Stage-3 104.00 Linagliptin 100.00
Isopropyl Alcohol 300.00 Isopropyl Alcohol Recovery 285.00
Activated Carbon 5.00 Isopropyl Alcohol Loss 6.00
Methanol 300.00 Methanol Recovery 285.00
Methanol Loss 6.00
Spent Carbon 5.00
Organic Residue 22.00
Process Residue-4,
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Distillation Residue-18
(Methanol-9,IPA-9)
Total 709 Total 709
11. MEROPENEM
Process Description:
Stage-1
3-(Diphenoxy-phosphoroloxy)-6-(1-hydroxy-ethyl)-4-methyl-7-oxo-1-aza-bicycle[3.2.0 ] hept-2-ene-2-carboxylic acid 4-nitro-benzyl ester reacts with 2- Dimethylcarbamoyl-4-mercapto-pyrrolidine-1-carboxylic acid 4-nitro-benzyl ester in presence of Sodium Hydroxide, TEA and MDC to give stage-1 product.
Stage-2
Stage-1 product undergoes Hydrogenation with Hydrogen in presence of Palladium
carbon , Iso propyl alcohol , n-Hexane and Ethyl acetate to give Meropenem.
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Route of Synthesis:
Stage-1
O
O
N
NO2
O
H3C
OH
H HCH3
O P
O
OPh
OPh
3-(Diphenoxy-phosphoryloxy)-6-(1-hydroxy-ethyl)-4-methyl-7-oxo-1-aza-bicyclo[3.2.0]hept-2-ene-2-
carboxylic acid 4-nitro-benzyl ester
C29H27N2O10P
594.51
+
ON
OMe2N
SH
O
NO2
2-Dimethylcarbamoyl-4-mercapto-pyrrolidine-1-carboxylic acid
4-nitro-benzyl ester
C15H19N3O5S
353.39
+
Triethylamine
N
C6H15N
101.19
NaOH
40.00
+ 2 HCl
72.92
O
O
N
NO2
O
H3C
OHH H CH3
S
+
O
N
O
Me2N
O NO2
3-[5-Dimethylcarbamoyl-1-(4-nitro-benzyloxycarbonyl)-pyrrolidin-
3-ylsulfanyl]-6-(1-hydroxy-ethyl)-4-methyl-7-oxo-1-aza-bicyclo[3.2.0]
hept-2-ene-2-carboxylic acid 4-nitro-benzyl ester
C32H35N5O11S
697.71
HO P
O
OPh
OPh
Phosphoric acid diphenyl ester
+
C12H11O4P
250.19
+
137.65
+ NaCl
58.44
+ H2O
18.02Triethyl amine Hydrochloride
Acetonitrile , Dichloromethane
N HCl
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Stage-2
O
O
N
NO2
O
H3C
OHH H CH3
S
O
N
O
Me2N
O NO2
3-[5-Dimethylcarbamoyl-1-(4-nitro-benzyloxycarbonyl)-pyrrolidin-3-yl
sulfonyl]-6-(1-hydroxy-ethyl)-4-methyl-7-oxo-1-aza-bicyclo[3.2.0]
hept-2-ene-2-carboxylic acid 4-nitro-benzyl ester
C32H35N5O11S
697.71
Ethyl acetate,Pd/C, Iso propyl alcohol
& n-Hexane
OH
O
N
O
H3C
OH
H HCH3
S NH
O
Me2N CH3
NO2
O
O NO2H
1-Methyl-4-nitro-benzeneMeropenem
C17H25N3O5S
383.46
+
C8H7NO4
181.15
+
C7H7NO2
137.14
Formic acid 4-nitro-benzyl ester
+ 2 H2
4.03
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Flow Chart:
3-(Diphenoxy-phosphoryloxy)-6- (1-hydroxy-ethyl)-4-methyl-7-oxo- 1-aza-bicyclo[3.2.0]hept-2-ene-2- carboxylic acid 4-nitro-benzyl ester2-Dimethylcarbamoyl-4-mercapto- pyrrolidine-1-carboxylic acid 4-nitro-benzyl esterTriethyl amineSodium hydroxide Hydrochloric acid Acetonitrile Dichloromethane Water
Stage-1
Stage-2
Acetonitrile RecoveryDichloromethane RecoveryEffluent Water
Stage-1Hydrogen Ethyl acetate Iso propyl alcohol n-Hexane Palladium on carbon Water
Ethyl acetate RecoveryIso propyl alcohol Recoveryn-Hexane RecoveryPalladium on carbon Recovery Effluent Water
Meropenem
Material balance:
Material Balance of Meropenem Stage-1 Batch Size: 250Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
3-(Diphenoxy-phosphoryloxy)-6- (1-hydroxy-ethyl)-4-methyl-7-oxo- 1-aza-bicyclo[3.2.0]hept-2-ene-2- carboxylic acid 4-nitro-benzyl ester
430.00 Stage-I 479.00
2-Dimethylcarbamoyl-4-mercapto- pyrrolidine-1-carboxylic acid 4-nitro-benzyl ester
256.00 Acetonitrile Recovery 475.00
Triethyl amine 74.00 Acetonitrile Loss 10.00
Sodium hydroxide 29.00 Dichloromethane Recovery 475.00
Hydrochloric acid 53.00 Dichloromethane Loss 10.00
Acetonitrile 500.00 Effluent Water 570.29
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Dichloromethane 500.00 (Water-500,Sodium chloride-42.26, Generated water-13.03, Acetonitrie-15)
Water 500.00 Organic Solid Waste (Process residue-307.71 Phosphoric acid diphenyl ester-180.95, triethylaminehydrochloride-99.56, Organic impurities-27.2) ]Distillation Residue-15 (Dichloromethan-15)
322.71
Total 2342 Total 2342
Material Balance of Meropenem Stage-2 Batch Size: 250Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-1 479.00 Meropenem 250.00
Hydrogen 3.00 Ethyl acetate Recovery 570.00
Ethyl acetate 600.00 Ethyl acetate Loss 12.00
Iso propyl alcohol 500.00 Iso propyl alcohol Recovery 475.00
n-Hexane 500.00 Iso propyl alcohol Loss 10.00
Palladium on carbon 10.00 n-Hexane Recovery 475.00
Water 500.00 n-Hexane Loss 10.00
Palladium on carbon Recovery 10.00
Effluent Water (Water-500, n-Hexane-15)
515.00
Organic Solid Waste (Process residue-232 Formic acid 4-nitrobenzyl ester -124.36, 1-methyl 4-nitro-benzene-94.15, Organic impurities-13.49) Distillation Residue-33 (Ethyl acetate-18, Iso propyl alcohol-15)
265.00
Total 2592 Total 2592
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12.MONTELUKAST SODIUM
Process Description:
Stage-1
Step-A
1-{3-[2-(7-Chloro-quinolin-2-yl)-vinyl]-phenyl}-3-[2-(1-hydroxy-1-methyl-ethyl)-phenyl]
propan-1-ol reacts with Methane sulfonyl chloride and Diisopropylethylamine in
presence of Toluene & n-Hexane to give Step-A product.
Step-B
Step-A reacts with (1-Mercaptomethyl cyclopropyl)acetic acid and Tert Butylamine in
presence of Toluene & n-Hexane to give Stage-1 product.
Stage-2
Stage -1 product undergoes reacts with Acetic acid in presence of Methanol & MDC
to give Stage-2 product.
Stage-3
Stage-2 product reacts with Sodium hydroxide in presence of Methanol to give
Montelukast sodium product.
Route of Synthesis:
Stage-1:
Step-A
NCl
OH
H3C
OHH3C
1-{3-[2-(7-Chloro-quinolin-2-yl)-vinyl]-phenyl}-3-[2-(1-hydroxy-1-methyl-
ethyl)-phenyl]-propan-1-ol
C29H28ClNO2
457.99
+
Methane sulfonyl chloride
CH3SO2Cl +
Diisopropylethyl amine
N
CH3
CH3H3C
CH3
114.55C8H19N
129.24
NCl
O
H3C
OHH3C
SO O
CH3
C30H30ClNO4S
536.08
Methanesulfonic acid 1-{3-[2-(7-chloro-quinolin-2-yl)-vinyl]-phenyl}-3-[2-(1-hydroxy-1-methyl-
ethyl)-phenyl]-propyl ester
+
Diisopropylamine Hydrochloride
HCl
C8H19N.HCl
165.70
Toluene & n-Hexane
CH3
N
CH3
CH2H3C
CH3
CH3
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Step-B
+
H3CH3C
H3C
NH2
tert-Butylamine
C4H11N
73.14
NCl
O
H3C
OHH3C
SO O
CH3
C30H30ClNO4S
536.08
Methanesulfonic acid 1-{3-[2-(7-chloro-quinolin-2-yl)-vinyl]-phenyl}-3-[2-(1-hydroxy
-1-methyl-ethyl)-phenyl]-propyl ester
+
(1-Mercaptomethyl cyclopropyl)acetic acid
HOOC
HS
C6H10O2S
146.20
NCl
S
H3C
OHH3C
COOH
CH3SO3Na
+
C39H47ClN2O3S
659.32
Toluene & n-Hexane
(1-{1-{3-[2-(7-Chloro-quinolin-2-yl)-vinyl]-phenyl}-3-[2-(1-hydroxy-1-methyl-ethyl)-phenyl]-propylsulfanylmethyl}-
cyclopropyl)-acetic acid
+ CH3ONa
54.02
Sodium Methane Sulfonate
118.09
+CH3OH
32.04
H3CH3C
H3C
NH2
Na+
SO O
O-
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Stage-2:
NCl
S
H3C
OHH3C
COOH
C39H47ClN2O3S
659.32
(1-{1-{3-[2-(7-Chloro-quinolin-2-yl)-vinyl]-phenyl}-3-[2-(1-hydroxy-1-methyl-ethyl)-phenyl]-propylsulfanylmethyl}-cyclopropyl)-
acetic acid
H3C
H3C
H3C
NH2
+ H3C OH
O
Acetic acid
60.05
Methanol
MDC
H3C
H3C
H3C
NH2H3C OH
ONCl
S
H3C
OHH3C
COOH
(1-{1-{3-[2-(7-Chloro-quinolin-2-yl)-vinyl]-phenyl}-3-[2-(1-hydroxy-1-methyl-ethyl)-phenyl]-propylsulfanylmethyl}-
cyclopropyl)-acetic acid
C35H36ClNO3S
586.18
133.19
Tert Butylamine salt of Acetic acid
+
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Stage-3:
NCl
S
H3C
OHH3C
COOH
(1-{1-{3-[2-(7-Chloro-quinolin-2-yl)-vinyl]-phenyl}-3-[2-(1-hydroxy-1-methyl-ethyl)-phenyl]-propylsulfanylmethyl}-
cyclopropyl)-acetic acid
C35H36ClNO3S
586.18
+ NaOH
40.00
Methanol
NCl
S
H3C
OHH3C
COONa
C35H35ClNNaO3S
608.17
Montelukast Sodium
+ H2O
18.00
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MONTELUKAST SODIUM
Flow Chart:
Stage-1
1-{3-[2-(7-Chloro-quinolin-2-yl)-vinyl]-phenyl}-3-[2-(1-hydroxy-1-methyl-ethyl)-phenyl]-propan-1-ol TolueneMethane sulfonyl chlorideDiisopropyl ethyl amineSodium methoxide Tert . butyl amine (1-Mercaptomethyl cyclopropyl)acetic acid n-Hexane Water
n-Hexane RecoveryToluene RecoveryEffluent water
MONTELUKAST SODIUM
Stage-3Stage-2MethanolSodium hydroxideActivated carbonn-HeptaneWater
Methanol Recoveryn-Heptane RecoveryEffluent water
Stage-2Stage-1DichloromethaneAcetic acidMethanolActivated carbonWater
Dichloromethane RecoveryMethanol RecoveryEffluent water
Material Balance:
Material balance of Montelukast sodium Stage-1 Batch Size: 100.0Kg
Name of the input Quantity in Kg
Name of the out put Quantity In Kg
1-{3-[2-(7-Chloro-quinolin-2-yl)-
vinyl]-phenyl}-3-[2-(1-hydroxy-1-
methyl-ethyl)-phenyl]-propan-1-ol
(MON10)
90.00 Stage-1 119.00
Toluene 500.00 n-Hexane Recovery 285.00
Methane sulfonyl chloride 23.00 n-Hexane Loss 6.00
Diisopropyl ethyl amine 26.00 Toluene Recovery 475.00
Sodium methoxide 10.50 Toluene Loss 10.00
Tert . butyl amine 14.00 Effluent water
(Water-500,Diisopropylamine hydrochloride-32.55, n-Hexane-9,
584.82
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Toluene-15, Sodium methane sulfonate -22.25, Methanol-6.02)
(1-Mercaptomethyl
cyclopropyl)acetic acid
28.00 Organic residue 11.68
n-Hexane 300.00
Water 500.00
Total 1491.5 Total 1491.5
Material balance of Montelukast sodium Stage-2 Batch Size: 100.0Kg
Name of the input Quantity in Kg
Name of the out put Quantity In Kg
Stage-1 119.00 Stage-2 101.00
Dichloromethane 500.00 Dichloromethane Recovery 475.00
Acetic acid 11.00 Dichloromethane Loss 10.00
Methanol 500.00 Methanol Recovery 475.00
Activated carbon 5.00 Methanol Loss 10.00
Water 500.00 Effluent water 524.03
(Water-500,Tert butylamine salt of acetic acid-24.03)
Spent carbon 5.00
Organic Residue 34.97
Process residue-4.97 Distillation Residue-30 (Methanol-15, Dichloromethane-15)
Total 1635 Total 1635
Material balance of Montelukast sodium Stage-3 Batch Size:100.0Kg
Name of the input Quantity in Kg
Name of the out put Quantity In Kg
Stage-2 101.00 Montelukast sodium 100.00
Methanol 300.00 Methanol Recovery 285.00
Sodium hydroxide 7.00 Methanol Loss 6.00
Activated carbon 3.00 n-Heptane Recovery 285.00
n-Heptane 300.00 n-Heptane Loss 6.00
Water 500.00 Effluent water (Water-500, Generated water-3.10)
503.10
Spent carbon 3.00
Organic Residue 22.90
Process residue-4.9 Distillation residue-18 (Methanol-9, n-Heptane-9)
Total 1211 Total 1211
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13.ROSUVASTATIN CALCIUM
Process Description
Stage-1
4-Fluoro-Benzadehyde reacts with 4-Methyl-3-oxo-pentanoic acid ethyl ester,
Potassium hydroxide in presence of Methanol to give Stage-1 product.
Stage-2
Stage-1 product reacts with S-Methyl iso thio urea and 2, 3Dichloro-5, 6-dicyano benzo quinone in presence of HMPA and MDC to give stage-2 product. Stage-3 Stage-2 product reacts with meta-chloro peroxy benzoic acid in presence of MDC to give Stage-3 as product. Stage-4 Stage-3 product reacts with methyl amine in presence of Ethanol and Methanol to give Stage-4 product. Stage-5 Stage-4 product reacts with Methane sulfonyl chloride in presence of Dimethoxy ethane to give Stage-5 product. Stage-6 Stage-5 product undergoes reduction with Diisobutylaluminium in presence of Toluene to give Stage-6 product. Stage-7 Stage-6 product reacts with methyl (3R)-3-(ert-butyldimethylsilyloxy)-5-oxo-6-triphenylphosphoranylidene hexanoate in presence of DMF to give Stage-7 product Stage-8 Stage-7 product reacts with Hydrogen fluoride in presence of THF and Ethyl acetate to give Stage-8 as product. Stage-9 Stage-8 product undergoes reduction with Hydrogen in presence of Sodium Boro hydride, THF and Dimethoxy borene to give Sage-9 product. Stage-10
Stage-9 product reacts with Calcium chloride undergoes saponification in presence
of Toluene and Ethyl acetate to give Rosuvastatin Calcium as product.
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ROSUVASTATIN CALCIUM Route of Synthesis:
Stage-1
F
CHO
4-Fluoro-benzaldehyde
+
4-Methyl-3-oxo-pentanoic acid ethyl ester
FCOOC2H5
CH3
O
H2O
2-(4-Fluoro-benzylidene)-4-methyl-3-oxo-pentanoic acid ethyl ester
C7H5F0
124.11
C8H14O3
158.19
C15H17FO3
264.29
18.0
C CH2
O
CHH3C
H3CCOOC2H5
CH3
MeOH
+
Stage-2
FCOOC2H5
CH3
O
2-(4-Fluoro-benzylidene)-4-methyl-3-oxo-pentanoic acid ethyl ester
C15H17FO3
264.29
S-methylisothiourea
NH
SH2NCH3
+
2,3-Dichloro-5,6-dicyano-p-benzoquinone
O
O
Cl
Cl
NC
NC
+
FCOOC2H5
N N
CH3
CH3
SCH3
OH
OH
Cl
Cl
NC
NC
4-(4-Fluoro-phenyl)-6-isopropyl-2-methylsulfanyl-pyrimidine
-5-carboxylic acid ethyl ester
HMPA
+
C2H6N2S
90.15
C8Cl2N2O2
227.0
C17H19FN2O2S
334.41
2,3-Dichloro-5,6-dicyano-p-benzoquinol
+ H2O
C8H2Cl2N2O2
229.02
18.0
CH3
MDC
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Stage-3
FCOOC2H5
N N
CH3
CH3
SCH3
4-(4-Fluoro-phenyl)-6-isopropyl-2-methylsulfanyl-pyrimidine
-5-carboxylic acid ethyl ester
C17H19FN2O2S
334.41
FCOOC2H5
N N
CH3
CH3
SO2CH3
meta-Chloroperoxybenzoic acid
O
O
OH
Cl
+
+
meta-Chlorobenzoic acid
O
HO
Cl
4-(4-Fluoro-phenyl)-6-isopropyl-2-methanesulfonyl-pyrimidine-5
-carboxylic acid ethyl ester
C17H19FN2O4S
366.41
2
C7H5ClO2
2x156.57=313.14
C7H5ClO3
2
2x172.57=345.14
MDC
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Stage-4
FCOOC2H5
N N
CH3
CH3
SO2CH3
4-(4-Fluoro-phenyl)-6-isopropyl-2-methanesulfonyl-pyrimidine-5
-carboxylic acid ethyl ester
C17H19FN2O4S
366.41
CH3
SO OH
Methanesulfonic acid
+
Methylamine
H2N CH3
FCOOC2H5
N N
CH3
CH3
NHCH3
Ethanol
4-(4-Fluoro-phenyl)-6-isopropyl-2-methylamino-pyrimidine-5-carboxylic acid ethyl ester
+
C17H20FN3O2
317.36
CH5N
31.06
CH4O2S
80.11
MeOH
Stage-5
FCOOC2H5
N N
CH3
CH3
NHCH3
4-(4-Fluoro-phenyl)-6-isopropyl-2-methylamino-pyrimidine-5-carboxylic acid ethyl ester
C17H20FN3O2
317.36
Methane sulfonyl chloride
CH3
SO O
Cl
CH3ClO2S
114.55
FCOOC2H5
N N
CH3
CH3
N
SO2CH3
CH3
4-(4-Fluoro-phenyl)-6-isopropyl-2-(methanesulfonyl-methyl
-amino)-pyrimidine-5-carboxylic acid ethyl ester
C18H22FN3O4S
395.45
HCl
36.5
Dimethoxy ethane
++
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Stage-6
FCOOC2H5
N N
CH3
CH3
N
SO2CH3
CH3
4-(4-Fluoro-phenyl)-6-isopropyl-2-(methanesulfonyl-methyl
-amino)-pyrimidine-5-carboxylic acid ethyl ester
C18H22FN3O4S
395.45
FCHO
N N
CH3
CH3
N
SO2CH3
CH3
+
N-[4-(4-Fluoro-phenyl)-5-formyl-6-isopropyl-pyrimidin-2-yl]-N-methyl
-methanesulfonamide
C16H18FN3O3S
351.40
TolueneAl
H
Diisobutylaluminium hydride
142.22
+Al
OC2H5
Diisobutylaluminiumethoxide
186.27
Stage-7
FCHO
N N
CH3
CH3
N
SO2CH3
CH3
N-[4-(4-Fluoro-phenyl)-5-formyl-6-isopropyl-pyrimidin-2-yl]-N-methyl
-methanesulfonamide
C16H18FN3O3S
351.40
Methyl (3R)-3-(tert-butyldimethylsilyloxy)-5-oxo-6-triphenylphosphoranylidenehexanoate
O
O
P
O
O
Si CH3H3CH3C
H3CCH3
CH3
+
C31H39O4PSi
534.70
F
N
N
CH3
CH3NH3CO2S
CH3
COOCH3
O O
Si
CH3
CH3
CH3
CH3
CH3
3-(tert-Butyl-dimethyl-silanyloxy)-7-[4-(4-fluoro-phenyl)-6-isopropyl-2-(methanesulfonyl-methyl-amino)
-pyrimidin-5-yl]-5-oxo-hept-6-enoic acid methyl ester
C29H42FN3O6SSi
607.81
+ O P
Triphenylphosphine oxide
C18H15OP
278.28
TEA
N,N-DMFKI
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Stage-8
F
N
N
CH3
CH3NH3CO2S
CH3
COOCH3
O O
Si
CH3
CH3
CH3
CH3
CH3
3-(tert-Butyl-dimethyl-silanyloxy)-7-[4-(4-fluoro-phenyl)-6-isopropyl-2-(methanesulfonyl-methyl-amino)
-pyrimidin-5-yl]-5-oxo-hept-6-enoic acid methyl ester
C29H42FN3O6SSi
607.81
+ HFTHF/Ethyl acetate
Hydrogen fluoride
20.01
F
N
N
CH3
CH3NH3CO2S
CH3
COOCH3
O OHSi
CH3
CH3
CH3
CH3
CH3
7-[4-(4-Fluoro-phenyl)-6-isopropyl-2-(methanesulfonyl-methyl-amino)-pyrimidin-5-yl]-3-hydroxy
-5-oxo-hept-6-enoic acid methyl ester
+ F
tert-Butyl-fluoro-dimethyl-silane
C23H28FN3O6S
493.55
C6H15FSi
134.27
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Stage-9
F
N
N
CH3
CH3NH3CO2S
CH3
COOCH3
O OH
7-[4-(4-Fluoro-phenyl)-6-isopropyl-2-(methanesulfonyl-methyl-amino)-pyrimidin-5-yl]-3-hydroxy
-5-oxo-hept-6-enoic acid methyl esterC23H28FN3O6S
493.55
NaBH4
F
N
N
CH3
CH3NH3CO2S
CH3
COOCH3
OH OH
7-[4-(4-Fluoro-phenyl)-6-isopropyl-2-(methanesulfonyl-methyl-amino)-pyrimidin-5-yl]-3,5-dihydroxy-
hept-6-enoic acid methyl ester
C23H30FN3O6S
495.56
+
37.83
+ HCl
36.5
+ NaCl
58.44
+ H3BO3
Diethyl methoxy borane
THF
61.83
+ 3 H2O
3X18=54.0
+ 3 H2
6.05
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Stage-10
F
N
N
CH3
CH3NH3CO2S
CH3
COOCH3
OH OH
7-[4-(4-Fluoro-phenyl)-6-isopropyl-2-(methanesulfonyl-methyl-amino)-pyrimidin-5-yl]-3,5-dihydroxy-
hept-6-enoic acid methyl ester
C23H30FN3O6S
2x495.56=991.12
+2
110.98
Water
F
N
N
CH3
CH3NH3CO2S
CH3
COO-
OH OH
2 Ca 2+
Rosuvastatin calcium
(C22H27FN3O6S)Ca
1001.14
+ 2 CH3Cl
Calcium chloride
100.98
Methyl chloride
C2H6Cl2
CaCl2Toluene,Ethyl acetate
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ROSUVASTATIN CALCIUM
Flow-Chart:
Stage-1
Stage-2
Stage-3
4-Fluoro benzaldehyde4-Methyl-3-oxo-pentanoic acid ethyl esterMethanolWater
Methanol RecoveryEffluent water
Stage-1S-Methyl iso thio urea2,3-Dichloro-5,6-dicyano benzoquinoneHMPAMDCWater
MDC RecoveryHMPA RecoveryEffluent water
Stage-2Meta chloro peroxy benzoic acidMDCWater
MDC RecoveryEffluent water
Stage-4
Stage-5
Stage-3Methyl amineEthanolMethanolWater
Ethanol RecoveryMethanol RecoveryEffluent water
Stage-4Methane sulfonyl chlorideDi methoxy ethane
Di methoxy ethane Recovery
Stage-5Diisobutylaluminium hydride Toluene
Toluene RecoveryStage-6
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Stage-7
Stage-8
Stage-9
N,N-Dimethyl formamide RecoveryEffluent water
Stage-7Hydrogen fluorideTHFEthyl acetate
THF RecoveryEthyl acetate Recovery
Stage-8Sodium boro hydrideDiethyl methoxy boraneEthyl acetateHydrochloric acidTHFWater
Ethyl acetate RecoveryTHF RecoveryEffluent water
Stage-10
Stage-9Calcium chlorideTolueneEthyl acetateWater
Toluene RecoveryEthyl acetate RecoveryEffluent water
Stage-6Methyl(3R)-3-(tert butyl di methyl silyloxy)-5-oxo-6-triphenyl phosphoranylidene hexanoateTriethyl amineN,N-Dimethyl formamideWater
ROSUVASTATIN CALCIUM
Material Balance:
Material Balance of Rosuvastatin Calcium Stage-1 Batch Size: 100.0 Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
4-Fluoro benzaldehyde 41.00 Stage-1 85.00
4-Methyl-3-oxo-pentanoic acid ethyl ester
53.00 Methanol Recovery 238.00
Methanol 250.00 Methanol Loss 5.00
Water 300.00 Effluent water 305.95
(Water-300,gen water-5.95)
Organic Residue Process residue-3.05 Distillation Residue-7 (Methanol)
10.05
Total 644 Total 644
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Material Balance of Rosuvastatin Calcium Stage-2 Batch Size: 100.0 Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-1 85.00 Stage-2 105.50
S-Methyl iso thio urea 29.00 MDC Recovery 285.00
2,3-Dichloro-5,6-dicyano benzoquinone
73.00 MDC Loss 6.00
HMPA 100.00 HMPA Recovery 95.00
MDC 300.00 HMPA Loss 2.00
Water 300.00 Effluent water 379.44
(Water-300,gen water-5.79, , 2,3-Dichloro-5,6-Dicyano-benzoquinol-73.65)
Organic Residue 14.06
(Process residue-2.06 Distillation Residue-12 (HMPA-3, MDC-9)
Total 887 Total 887
Material Balance of Rosuvastatin Calcium Stage-3 Batch Size: 100.0 Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-2 105.50 Stage-3 96.00
Meta chloro peroxy benzoic acid
109.00 MDC Recovery 285.00
MDC 300.00 MDC Loss 6.00
Water 300.00 Effluent water 398.78
(Water-300, Meta chlorobenzoic acid-98.78 )
Organic Residue 28.72
(Process residue-19.72, Distillation Residue-9 (MDC))
Total 814.50 Total 814.50
Material Balance of Rosuvastatin Calcium Stage-4 Batch Size: 100.0 Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-3 96.00 Stage-4 81.00
Methyl amine 9.00 Ethanol Recovery 238.00
Ethanol 250.00 Ethanol Loss 5.00
Methanol 300.00 Methanol Recovery 285.00
Water 300.00 Methanol Loss 9.00
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Effluent water 317.70
(Water-300,Methane sulfonic acid-17.7)
Organic Residue Process residue-3.3 Distillation Residue-16 (Ethanol-7, Methanol-9)
19.30
Total 955 Total 955
Material Balance of Rosuvastatin Calcium Stage-5 Batch Size: 100.0 Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-4 81.00 Stage-5 95.00
Methane sulfonyl chloride 30.00 Di methoxy ethane Recovery 285.00
Di methoxy ethane 300.00 Di methoxy ethane Loss 6.00
By - Product 9.30
(Hydrochloric acid)
Organic Residue Process residue-6.7 Distillation Residue-9 (Di methoxy ethane)
15.70
Total 411 Total 411
Material Balance of Rosuvastatin Calcium Stage-6 Batch Size: 100.0 Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-5 95.00 Stage-6 82.00
Diisobutylaluminium hydride 35.00 Toluene Recovery 285.00
Toluene 300.00 Toluene Loss 6.00
Organic Residue 57.00
(Process residue-48 Organic Impurities-3 diisobutylaluminium ethoxide-45 Distillation Residue-9 (Toluene)
Total 430 Total 430
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Material Balance of Rosuvastatin Calcium Stage-7 Batch Size: 100.0 Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-6 82.00 Stage-7 136.00
Methyl(3R)-3-(tert butyl di methyl silyloxy)-5-oxo-6-triphenyl phosphoranylidene hexanoate
125.00 N,N-Dimethyl formamide Recovery
285.00
Triethyl amine 10.00 N,N-Dimethyl formamide Loss 6.00
N,N-Dimethyl formamide 300.00 Effluent water 319.00
Water 300.00 (Water-300, Triethyl amine-10, DMF-9)
Organic Residue 71.00
(Process residue- Organic Impurities-6, Triphenyl phosphine oxide-65)
Total 817 Total 817
Material Balance of Rosuvastatin Calcium Stage-8 Batch Size: 100.0 Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-7 136.00 Stage-8 107.00
Hydrogen fluoride 4.50 THF Recovery 285.00
THF 300.00 THF Loss 6.00
Ethyl acetate 300.00 Ethyl acetate Recovery 285.00
Ethyl acetate Loss 6.00
Organic Residue 51.50
(Process residue-33.5 Organic Impurities-3.5, Tert-butyl-fluoro-dimethyl silane-30) Distillation Residue-18 (THF-9, Ethyl acetate-9)
Total 740.5 Total 740.5
Material Balance of Rosuvastatin Calcium Stage-9 Batch Size: 100.0 Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-8 107.00 Stage-9 102.00
Sodium boro hydride 8.20 Ethyl acetate Recovery 285.00
Diethyl methoxy borane 20.00 Ethyl acetate Loss 6.00
Ethyl acetate 300.00 THF Recovery 285.00
Hydrochloric acid 8.00 THF Loss 6.00
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THF 300.00 Effluent water 343.34
Water 300.00 (water-288.28, Sodium chloride-12.66 Dimethoxy borane-20, Boric acid-13.40, THF-9)
Process Emissions 1.31
(Hydrogen)
Organic Residue Process residue-5.55 Distillation Residue-9 (Ethyl acetate-9)
14.55
Total 1043.2 Total 1043.2
Material Balance of Rosuvastatin Calcium Stage-10 Batch Size: 100.0 Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-9 102.00 Rosuvastatin Calcium 100.00
Calcium chloride 11.50 Toluene Recovery 285.00
Toluene 300.00 Toluene Loss 6.00
Ethyl acetate 300.00 Ethyl acetate Recovery 285.00
Water 300.00 Ethyl acetate Loss 6.00
Effluent water 309.00
(Water-300, Toluene-9)
Process emission ((Chloromethane)
10.39
Organic Residue 12.11
(Process residue-3.11 Distillation Residue-9 (Ethyl acetate-9)
Total 1013.5 Total 1013.5
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14.SITAGLIPTIN PHOSPHATE MONOHYDRATE Process Description
Stage-1
Step-A
(2, 4, 5-Trifluoro-phenyl) acetic acid undergoes Chlorination with Thionyl chloride
and Meldrums acid in presence of Sodium Hydroxide, MDC, Methanol and Ethyl
acetate to give Step-A product
Step-B
Step-A product reacts with 3-(Trifluoro methyl) 5, 6, 7, 8-tetra hydro-[1,2,4]triazolo
(4, 3-a) pyrazine hydrochloride in presence of Methane sulphonic acid , Sodium
carbonate, Methanol, Toluene and IPA to give Stage-1 product
Stage-2
Stage-1 compound reacts with Hydroxy-phenyl acetic acid and sodium borohydride
in presence of acetic acid, MDC and IPA to give stage-2 product
Stage-3
Stage-2 compound reacts with sodium hydroxide, phosphoric acid and water in
presence of Toluene, MDC and IPA to give Sitagliptin Phosphate Monohydrate.
SITAGLIPTIN PHOSPHATE MONOHYDRATE
Route of synthesis
Stage-1
Step-A F
F
F
OH
O
(2,4,5-Trifluoro-phenyl)-acetic acid
C8H5F3O2
190.12
+ SOCl2
118.97
+
O O
OO
CH3H3C
Meldrums acid
C6H8O4
144.13
+ 2 NaOH
80.00
F
F
FOH
O
O
O
OCH3
C14H11F3O5
316.23
+ SO2 + 2 NaCl
64.06 2X58.4=116.8
+ 2H2O
36.02
CH3
5-[1-Hydroxy-2-(2,4,5-trifluoro-phenyl)-ethylidene]-2,2-dimethyl-[1,3]
dioxane-4,6-dione
MDC, Methanol, Ethyl acetate
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Step-B
F
F
FOH
O
O
O
OCH3
C14H11F3O5
316.23
CH3
5-[1-Hydroxy-2-(2,4,5-trifluoro-phenyl)-ethylidene]-2,2-dimethyl-[1,3]
dioxane-4,6-dione
+
HN
NN
N
CF3
HCl
C6H8ClF3N4
228.60
+
3-Trifluoromethyl-5,6,7,8-tetrahydro-[1,2,4]triazolo[4,3-a]
pyrazine Hydrochloride
+CH3SO3H
96.11
NaHCO3
+ NH3
17.03
84.01
F
F
FNH2 O
N
NN
N
CF3
3-Amino-1-(3-trifluoromethyl-5,6-dihydro-8H-[1,2,4]triazolo[4,3-a]pyrazin-7-yl)-4-(2,4,5-
trifluoro-phenyl)-but-2-en-1-one
C16H13F6N5O
405.30
+
NaCl
58.44
+ SO2
64.06
+ O2
32.00
Propanetriol
OHHO
HO
C3H8O3
92.09
+
Lactic acid
OH
OOH
C3H6O3
90.08
+
Methanol, Toluene, IPA
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Stage-2
F
F
FNH2 O
N
NN
N
CF3
3-Amino-1-(3-trifluoromethyl-5,6-dihydro-8H-[1,2,4]triazolo[4,3-a]pyrazin-7-yl)-4-(2,4,5-
trifluoro-phenyl)-but-2-en-1-one
C16H13F6N5O
405.30
+ NaBH4
37.83
+ CH3COOH
60.05
+
O
OH
OH
Hydroxy-phenyl-acetic acid
C8H8O3
152.15
F
F
FNH2 O
N
NN
N
CF3
O
OH
OH
3-Amino-1-(3-trifluoromethyl-5,6-dihydro-8H-[1,2,4]triazolo[4,3-a]pyrazin-7-yl)-4-
(2,4,5-trifluoro-phenyl)-but-2-en-1-one Hydroxy phenyl acetate
C24H23F6N5O4
559.46
+ CH3COONa
82.03
+
+ H3BO3
61.83
3 H2O
54.05
+ 4 H2
8.00
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Stage-3
F
F
FNH2 O
N
NN
N
CF3
O
OH
OH
3-Amino-1-(3-trifluoromethyl-5,6-dihydro-8H-[1,2,4]triazolo[4,3-a]pyrazin-7-yl)-4-
(2,4,5-trifluoro-phenyl)-but-2-en-1-one Hydroxy phenyl acetate
C24H23F6N5O4
559.46
+ NaOH
40.00
+ H3PO4
98.00
H3PO4 H2O
Sitagliptin Phosphate monohydrate
C16H20F6N5O6P
523.32
O
OH
ONa
+
Sodium mandelate
C8H7NaO3
174.13
F
F
F
NH2
N
N
N
N
CF3
O
MDC, IPA
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Flow Chart
2,4,5-Trifluro phenyl acetic acid3-(trifluoromethyl)-5,6,7,8-tetrahydro(1,2,4)triazole(4,3,-a)Pyrazine hydrochlorideMethane sulfonic acidThionyl chlorideMeldrum acidSodium hydroxideSodium sulphateSodium bicarbonateMethylene dichlorideAmmonia Ethyl acetateMethanolWater
Stage-1Sodium borohydrateHydroxyl phenyl acetic acidAcetic acidIsopropyl alcoholTolueneMethylene chlorideWater
Methylene dichloride RecoveryToluene RecoveryIsopropyl alcohol RecoveryEffluent water
Methylene dichloride RecoveryIsopropyl alcohol RecoveryEffluent water
Stage-1
Stage-2
Stage-3
Methylene dichloride RecoveryEthyl acetate RecoveryMethanol RecoveryEffluent water
Stage-2Sodium hydroxidePhosphoric acidSodium sulphateMethylene chlorideIsopropyl alcoholWater
Sitagliptin Phosphate Monohydrate
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Material Balance
Material balance of Sitagliptin Phosphate Monohydrate
Stage-1 Batch size : 100kg
Name of the input Quantity
in kg
Name of the out put Quantity
in kg
2,4,5-Trifluro phenyl acetic acid 41.00 Stage-1 82.00
3-(trifluoromethyl)-5,6,7,8-
tetrahydro(1,2,4)triazole(4,3,-
a)Pyrazine hydrochloride
48.00 Methylene dichloride
Recovery
190.00
Methane sulfonic acid 20.00 Methylene dichloride Loss 4.00
Thionyl chloride 26.00 Ethyl acetate Recovery 190.00
Meldrum acid 31.10 Ethyl acetate Loss 4.00
Sodium hydroxide 17.50 Methanol Recovery 190.00
Sodium sulphate 10.00 Methanol Loss 4.00
Sodium bicarbonate 18.00 Effluent water 389.21
Methylene dichloride 200.00 (Water-300,
Generated water-7.8,
Sodium chloride-37.4,
Lactic acid-18.8,
Propanetriol-19.21,
Ethyl acetate-6)
Ammonia 3.60 Inorganic solid waste 10.00
Ethyl acetate 200.00 (Sodium sulphate)
Methanol 200.00 Process emission 33.84
Water 300.00 (Sulphur dioxide-27.17,
Oxygen-6.67)
Organic residue 18.15
Process residue -6.15
Distillation residue- 12
(MDC-6, Methanol-6)
Total 1115.2 Total 1115.2
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Material balance of Sitagliptin Phosphate Monohydrate
Stage-2 Batch size : 100kg
Name of the input Quantity
In kg
Name of the out put Quantity
In kg
Stage-1 82.00 Stage-2 110.00
Sodium borohydrate 8.00 Mixed Solvents(Methylene
dichloride+ Toluene)
Recovery
380.00
Hydroxyl phenyl acetic acid 31.00 Methylene dichloride Loss 10.00
Acetic acid 12.20 Toluene Loss 10.00
Isopropyl alcohol 200.00 Isopropyl alcohol Recovery 190.00
Toluene 200.00 Isopropyl alcohol Loss 4.00
Methylene chloride 200.00 Effluent water 318.10
Water 300.00 (Water-289, Sodium acetate-
16.6, Boric acid-12.5)
Process emission 1.61
(Hydrogen)
Organic residue 9.49
Process residue-3.49
Distillation residue - 6
( IPA-6)
Total 1033.2 Total 1033.20
Material balance of Sitagliptin Phosphate Monohydrate
Stage-3 Batch size : 100kg
Name of the input Quantity
In kg
Name of the out put Quantity
In kg
Stage-2 110.00 Sitagliptin Phosphate
Monohydrate
100.00
Sodium hydroxide 8.00 Methylene dichloride
Recovery
190.00
Phosphoric acid 20.00 Methylene dichloride Loss 10.00
Sodium sulphate 10.00 Isopropyl alcohol Recovery 190.00
Methylene chloride 200.00 Isopropyl alcohol Loss 4.00
Isopropyl alcohol 200.00 Effluent water 206.00
Water 200.00 (Water-200,IPA-6)
Inorganic solid waste 10.00
(Sodium sulphate)
Organic residue 38.00
Process residue -38
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(Sodium mandelate-34.25,
Organic impurities-3.75)
Total 748 Total 748
15.TENELIGLIPTIN HYDROBROMIDE HYDRATE
Process Description:
Stage-1
1-(3-Methyl-1-phenyl-1H-Pyrazol-5-yl) piperazine reacts with 4-Benzenesulfonyloxy-
2-(thiazolidine-3-carbonyl)-pyrrolidine-1-carboxylic acid tert-butyl ester in presence of
DMF and Ethyl acetate to give Stage-1 Product.
Stage-2
Stage-1 Product reacts with Trifluoro acetic acid in presence of MDC to give
Teneligliptin.
Stage-3
Teneligliptin undergoes salt formation with Hydrobromide hydrate in presence of
MDC, Ethyl acetate and IPA to give Teneligliptan Penta Hydrobromide Hydrate.
Route oh Synthesis:
Stage-1
N
O
O
O
S
N
SO
OO
N
HN
N N
1-(3-Methyl-1-phenyl-1H-pyrazol-5-
yl)piperazine
C14H18N4
242.32
+
4-Benzenesulfonyloxy-2-(thiazolidine-3-carbonyl)-pyrrolidine-1-carboxylic acid
tert-butyl ester
C19H26N2O6S2
442.55
N
O
O
O
S
N
NN
NN
C27H38N6O3S526.69
(2S,4S)-tert-butyl 4-(4-(3-methyl-1-phenyl-1H-pyrazol-5-yl)piperazin-1-
yl)-2-(thiazolidine-3-carbonyl)pyrrolidine-1-carboxylate
SO
OOH
Benzenesulfonic acid
C6H6O3S
158.18
+
DMF, Ethy acetate
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Stage-2
N
O
O
O
SN
NNNN
C27H38N6O3S526.69
(2S,4S)-tert-butyl 4-(4-(3-methyl-1-phenyl-1H-pyrazol-5-yl)piperazin-1-
yl)-2-(thiazolidine-3-carbonyl)pyrrolidine-1-carboxylate
Tri Fluoro Acetic acid
O
OH
Formic acid tert-butyl ester
NH
O
SN
NNNN
Teneligliptin
C22H30N6OS
426.58
+
C5H10O2102.13
MDC
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Stage-3
MDC, Ethyl acetate, IPA
NH
O
SN
NNNN
Teneligliptin
C22H30N6OS
426.58 X 2=853.16
Hydrobromide hydrate
+
NH
O
SN
NNNN
5 HBr H2O
[C22H30N6OS ]2 5HBr H2O
422.57
Teneligliptin Penta hydrobromide hydrate
2
2
HBr5
H2O
1275.74
x
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TENELIGLIPTIN PENTA HYDROBROMIDE HYDRATE
Flow chart
1-(3-methyl-1-phenyl-1H-pyrazo-5-yl) piperazine4-Benzenesulfonyloxy-2-(thiazolidine -3-carbonyl)-pyrrolidine-1-carboxylic acidtert-butyl esterDimethyl form amideEthyl acetateWater
Ethyl acetate RecoveryDimethyl formamide RecoveryEffluent water
Stage-1
Methylene chloride RecoveryEffluent water
Stage-2
Methylene chloride RecoveryEthyl acetate RecoveryIsopropyl alcohol RecoverySpent carbon Effluent water
Stage-3
Stage-1Sodium sulphateTrifluoro acetic acidMethylene chlorideWater
Stage-2Aqueous hydrobromic acid Isopropyl alcoholEthyl acetateMethylene chlorideActivated carbonWater
Teneligliptin Hydrobromide Hydrate
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TENELIGLIPTIN HYDROBROMIDE HYDRATE
Material balance:
Material balance of Teneligliptin Hydrobromide Hydrate
Stage-1 Batch size : 100.00kg
Name of the input Quantity
In kg
Name of the out put Quantity
In kg
1-(3-methyl-1-phenyl-1H-pyrazo-
5-yl) piperazine
42.00 Stage-1 88.00
4-Benzenesulfonyloxy-2-
(thiazolidine -3-carbonyl)-
pyrrolidine-1-carboxylic acid tert-
butyl ester
77.00 Ethyl acetate Recovery 95.00
Dimethyl form amide 200.00 Ethyl acetate Loss 5.00
Ethyl acetate 100.00 Dimethyl formamide
Recovery
190.00
Water 200.00 Dimethyl formamide Loss 4.00
Effluent water 206.00
(Water- 200, DMF-6)
Organic residue 31.00
Process residue-14
(benzene sulfonic acid-
27.45, Organic impurities-
3.55)
Total 619 Total 619
Material balance of Teneligliptin Hydrobromide Hydrate
Stage-2 Batch size : 100kg
Name of the input Quantity
in kg
Name of the out put Quantity
in kg
Stage-1 88.00 Stage-2 69.00
Sodium sulphate 20.00 Methylene chloride Recovery 190.00
Trifluoro acetic acid 5.00 Methylene chloride Loss 10.00
Methylene chloride 200.00 Inorganic solid waste 20.00
Water 200.00 (Sodium sulphate-20)
Effluent Water 205.00
(Water-200, Trifluoro acetic acid-5)
Organic residue 19.00
Process residue19
(Formic acid tert-butylester-17.10,
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Organic impurities-1.9)
Total 513 Total 513
Material balance of Teneligliptin Hydrobromide Hydrate
Stage-3 Batch size : 100.00kg
Name of the input Quantity
In kg
Name of the out put Quantity
In kg
Stage-2 69.00 Teneligliptin hydrobromide hydrate 100.00
Aqueous hydrobromic acid 35.00 Methylene chloride Recovery 190.00
Isopropyl alcohol 200.00 Methylene chloride Loss 10.00
Ethyl acetate 200.00 Ethyl acetate Recovery 190.00
Methylene chloride 200.00 Ethyl acetate Loss 4.00
Activated carbon 10.00 Isopropyl alcohol Recovery 190.00
Water 200.00 Isopropyl alcohol Loss 4.00
Spent carbon 10.00
Effluent water 212.00
(Water-200, Isopropyl alcohol-6, Ethyl
acetate-6)
0
Organic residue 4.00
Total 914 Total 914
16.TRI BUTYL TIN CHLORIDE
Process description:
Stage-1
n-Butyl chloride undergoes Grignard reaction with Magnesium and Tin Chloride in
presence of Diethyl ether to give Tri Butyl tin Chloride product.
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Route of Synthesis:
Stage-1
n-Butyl Chloride
CH3Cl
C4H9Cl
92.57X3=277.71
+ SnCl2
189.62
+ Mg
24.31
Diethyl ether3
ClSn CH3
CH3
H3C
Tri Butyl Tin Chloride
+ H2O
18.02
C12H27ClSn
325.51
+ MgCl2
95.21
+ 2 HCl
72.92
+ 0.5 O2
16.00
Flow chart:
n-Butyl ChlorideTin(II) chlorideMagnesium Diethyl ether Toluene Ammonium chloride IodineEthylene di bromideWater
Mixed Solvents(Diethyl ether +Toluene ) RecoveryEffluent water
Stage-1
Tri Butyl Tin ChlorideMaterial Balance:
Material balance of Tri Butyl Tin Chloride Stage-1 Batch Size: 500.0.0 Kg
Name of the input Quantity in Kg
Name of the out put Quantity In Kg
n-Butyl Chloride 450.00 Tri Butyl Tin Chloride 500.00
Tin(II) chloride 308.00
Mixed Solvents (Diethyl ether +Toluene ) Recovery
713.00
Magnesium 40.00 Toluene loss 30.00
Diethyl ether 150.00 Diethyl ether loss 7.00
Toluene 600.00 Effluent water 1374.47
Ammonium chloride 50.00 (Water-1170 ,Ammonium chloride-50, Magnesium chloride-154.27, Iodine-0.1, Ethylene
0
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dibromide-0.1)
Iodine 0.100 Process emission (Oxygen-25.92)
25.92
Ethylene di bromide 0.100 By –product (Hydrochloric acid -118.15)
118.15
Water 1200.00 Organic residue 29.66
Total 2798.2 Total 2798.2
17.VALACYCLOVIR HYDROCHLORIDE MONOHYDRATE
Process Description:
Stage-1
Acetic acid 2-(2-acetylamino-6- oxo-1,6-dihydro-purin-9-ylmethoxy)-ethyl ester
undergoes condensation with 3-Methyl-2-(phenoxycarbonyl methyl-amino)-butyric
acid in presence of Dimethylformamide, Dimethyl amine , Acetone & ehanol to give
Stage-1
Product.
Stage-2
Stage-1 product undergoes reduction with Hydrogen Gas in presence of palladium
on carbon as catalysed and further Reacted with Hydrochloric acid and water to give
Valcyclovir Hydrochloride monohydrate.
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VALACYCLOVIR HYDROCHLORIDE MONOHYDRATE
Route of Synthesis:
Stage-1
C12H15N5O5
309.28
3-Methyl-2-(phenoxycarbonylmethyl-amino)-butyric acid
C13H17NO4
251.28
+
Dimethyl formamide , Dimethylamine ,
Acetone & Ethanol
2-Benzyloxycarbonylamino-3-methyl-butyric acid 2-(2-amino-6-oxo-1,6-dihydro-purin-9-yl
methoxy)-ethyl ester
C21H26N6O6
458.47
+ 2CH3COOH
120.10
+ H2O
18.0
HN
N N
N
OO CH3
O
O
NH
H3C
O
Acetic acid 2-(2-acetylamino-6-oxo-1,6-dihydro-purin-9-ylmethoxy)-ethyl ester
H3C
O
OH
NCH3O
O
CH3
HN
N N
N
OO
O
O
H2NHN
O
O
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Stage-2
Palladium on Carbon, Methanol & Ethanol
2-Benzyloxycarbonylamino-3-methyl-butyric acid 2-(2-amino-6-oxo-1,6-dihydro-purin-9-yl
methoxy)-ethyl ester
C21H26N6O6
458.47
HN
N N
N
OO
O
O
H2NHN
O
O
+
Valcyclovir Hydrochloride Monohydrate
C13H23ClN6O5
378.81
C8H8O2
136.15
+ HCl
36.46
+ H2O
18.02
+ H2
2.02
HN
N N
N
OO
O
O
H2NNH2
O
O
Formic acid benzyl ester
. H2O . HCl
Flow Chart:
Stage-1
Stage-2
Dimethyl amine RecoveryDimethyl formamide RecoveryAcetone RecoveryEthanol RecoveryEffluent Water
Stage-IPalladium on CarbonHydrochloric acid MethanolEthanolHydrogenActivated carbonDM Water
Methanol RecoveryEthanol RecoveryPalladium on Carbon RecoveryEffluent Water
Acetic acid 2-(2-acetylamino-6- oxo-1,6-dihydro-purin-9-ylmethoxy)-ethyl ester3-Methyl-2-(phenoxy carbonyl methylamino)-butyric acidDimethyl amineDimethyl formamideAcetoneEthanolSodium sulphate Water
Valcyclovir Hydrochloride Monohydrate
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Material Balance
Material Balance of Valcyclovir Hydrochloride Monohydrate Stage-1 Batch Size: 500Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Acetic acid 2-(2-acetylamino-6- oxo-1,6-dihydro-purin-9-ylmethoxy)-ethyl ester
453.00 Stage-I 637.00
3-Methyl-2-(phenoxy carbonyl methylamino)-butyric acid
368.00 Dimethyl amine Recovery 190.00
Dimethyl amine 200.00 Dimethyl amine Loss 4.00
Dimethyl formamide 500.00 Dimethyl formamide Recovery 475.00
Acetone 500.00 Dimethyl formamide Loss 10.00
Ethanol 500.00 Acetone Recovery 475.00
Sodium sulphate 25.00 Acetone Loss 10.00
Water 500.00 Ethanol Recovery 475.00
Ethanol Loss 10.00
Effluent Water 670.51
(Water-473.61, Acetic acid-175.90, Dimethylamine-6 Dimethyl formamide-15)
Inorganic solid waste (Sodium sulphate)
25.00
Organic Solid Waste (Process residue-34.49 Distillation Residue-30 (Acetone -15, Ethanol-15)
64.49
Total 3046 Total 3046
Material Balance of Valcyclovir Hydrochloride Monohydrate
Stage-2 Batch Size: 500Kg
Name of the input Quantity
in Kg
Name of the out put Quantity in
Kg
Stage-I 637.00 Valcyclovir Hydrochloride
Monohydrate
500.00
Palladium on Carbon 15.00 Methanol Recovery 475.00
Hydrochloric acid 51.00 Methanol Loss 10.00
Methanol 500.00 Ethanol Recovery 475.00
Ethanol 500.00 Ethanol Loss 10.00
Hydrogen 3.00 Palladium on Carbon
Recovery
15.00
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Activated carbon 5.00 Effluent Water 475.00
DM Water 500.00 (Water-475)
Spent Carbon 5.00
Organic residue-
Process residue-216
(Formic acid methyl ester -
189.16, Organic impurities-
26.84)
Distillation residue-30
(Methanol-15, ethanol-15
246.00
Total 2211 Total 2211
18.VILDAGLIPTIN
Process Description:
Stage-1
Pyrrolidine-2-carboxylic acid reacts with chloro-acetyl chloride in presence of MDC
and IPA to give Stage-1 Product.
Stage-2
Stage-1 product reacts with Ammonium carbonate in presence of MDC and IPA to
give stage-2 Product.
Stage-3
Stage-2 product reacts with Trifluoro acetic anhydride in presence of MDC and IPA
to give Stage-3 Product.
Stage-4
Stage-3 Product reacts with 3-Amoino- adam -1-ol in presence of MDC and Acetone
to give Vildagliptin.
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VILDAGLIPTIN
Route of Synthesis:
Stage-1
+
Chloro-acetyl chloride
C2H2Cl2O
112.94
C5H9NO2
115.13
MDC, IPA
HN
O
OH
Pyrrolidine-2-carboxylic acid
ClCl
O N O
OH
(S)-1-(2-chloroacetyl)pyrrolidine
-2-carboxylic acid
C7H10ClNO3
191.61
O
Cl
+ HCl
36.46
Stage-2
MDC, IPA
N O
OH
(S)-1-(2-chloroacetyl)pyrrolidine
-2-carboxylic acid
C7H10ClNO3
191.61
O
Cl
+ (NH4)2CO3
96.09
N O
NH2
(S)-1-(2-chloroacetyl)pyrrolidine-2-carboxamide
ClO
C7H11ClN2O2
190.63
+ CO2
44.01
+ NH3
17.03
H2O+
36.02
2
Stage-3
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N O
NH2
(S)-1-(2-chloroacetyl)pyrrolidine-2-carboxamide
ClO
C7H11ClN2O2
190.63
+
Tri fluoro acetic anhydride
F3C O CF3
O O
C4F6O3
210.03
N
ClO
CN
1-(2-chloroacetyl)pyrrolidine
-2-carbonitrile
C7H9ClN2O
172.61
+
Tri fluoro acetic acid
OO F
FF
C2HF3O2
114.02 X2=228.04
+ 3 H2
6.06
2
IPA, MDC
Stage-4
N
ClO
CN
C7H9ClN2O
172.61
OHH2N
1-(2-Chloro-acetyl)-pyrrolidine
-2-carbonitrile
3-Amino-adamantan-1-ol
N
O
CN
OH
C17H25N3O2
303.40
NH
+
C10H17NO
167.25
Vildagliptin
MDC, Acetone+ HCl
36.46
Flow Chart:
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Pyrrolidine -2-carboxlic acidChloro acetyl chlorideSodium sulphateSodium chlorideIsopropyl etherMethylene dichloride
Stage-1Ammonium bicarbonateIsopropyl alcoholMethylene dichloride Isopropyl ether
Methylene dichloride recoveryIsopropyl alcohol recoveryIsopropyl ether recovery
Stage-33- amino-1- adamantanolePotassium carbonatePotassium iodideActivated carbonHyflowSodium sulphateSodium chlorideMethylene chlorideAcetone
Tetrahydrofuran RecoveryMethylene chloride RecoveryIsopropyl alcohol Recovery
Stage-1
Stage-2
Stage-3
Methylene dichloride recoveryIsopropyl ether recovery
Stage-4
Stage-2Trifluoro acetic anhydrideAmmonium bicarbonateSodium chlorideSodium sulphateIsopropyl alcoholTetrahydrofuranMethylene chloride
Vildagliptin
Acetone Recovery Methylene chloride Recovery
VILDAGLIPTIN
Material Balance:
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Material balance of Vildagliptin
Stage-1 Batch size : 100kg
Name of the input Quantity
In kg
Name of the out put Quantity
In kg
Pyrrolidine -2-carboxlic acid 44.00 Stage-1 71.00
Chloro acetyl chloride 44.00 Methylene dichloride
Recovery
190.00
Isopropyl ether 0200.00 Methylene dichloride Loss 10.00
Methylene dichloride 200.00 Isopropyl ether Recovery 190.00
Water 200.00 Isopropyl ether Loss 10.00
Effluent water 200.00
(Water-200)
By -product 13.93
(Hydrochloric acid)
Organic residue 3.07
Total 688 Total 688
Material balance of Vildagliptin
Stage-2 Batch size : 100kg
Name of the input Quantity
In kg
Name of the out put Quantity
In kg
Stage-1 71.00 Stage2 68.00
Ammonium bicarbonate 36.00 Methylene dichloride
recovery
190.00
Isopropyl alcohol 100.00 Methylene dichloride Loss 10.00
Methylene dichloride (MDC) 200.00 Isopropyl alcohol Recovery 95.00
Isopropyl ether 200.00 Isopropyl alcohol Loss 5.00
Isopropyl ether Recovery 190.00
Isopropyl ether Loss 10.00
Generated water 13.35
Process emission 22.60
(Carbon dioxide-16.3,
Ammonia-6.3)
Organic residue 3.05
Total 607 Total 607
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Material balance of Vildagliptin Stage-3 Batch size : 100kg
Name of the input Quantity In kg
Name of the out put Quantity In kg
Stage-2 68.00 Stage-3 57.00
Trifluoro acetic anhydride 75.00 Tetrahydrofuran Recovery 190.00
Isopropyl alcohol 200.00 Tetrahydrofuran Loss 4.00
Tetrahydrofuran 200.00 Methylene chloride Recovery 190.00
Methylene chloride 200.00 Methylene chloride Loss 10.00
Water 200.00 Isopropyl alcohol Recovery 190.00
Isopropyl alcohol Loss 4.00
Effluent water 287.35
(Water -200, THF-6, Tri fluoroacetic acid -81.35)
Process emission (Hydrogen)
2.15
Organic residue 8.50
Process Residue-2.5 Distillation residue- 6 (Isopropyl alcohol -6)
Total 943 Total 943
Material balance of Vildagliptin Stage-4 Batch size :100kg
Name of the input Quantity In kg
Name of the out put Quantity In kg
Stage-3 59.00 Vildagliptin 100.00
3- amino-1- adamantanole 58.00 Acetone Recovery 190.00
Activated carbon 5.00 Acetone Loss 4.00
Methylene chloride 200.00 Methylene chloride Recovery
190.00
Acetone 200.00 Methylene chloride Loss 10.00
Water 300.00 Effluent water 300.00
(Water -300)
Spent carbon 5.00
By product 12.46
(Hydrochloric acid )
Organic Residue 10.54
Process residue-4.54 Distillation residue-6 (Acetone-6)
Total 822 Total 822
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ANNEXURE – IV
WATER CONSUMPTION DETAILS
S.No Purpose Water input KLD
1 Process 52
2 Washings 5
3 Boiler make up 42
4 Cooling towers make up 79
5 Scrubbing system 7
6 Domestic 4
7 Gardening 5
Total 194
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ANNEXURE -V
SOLID & HAZARDOUS WASTE GENERATION AND DISPOSAL
S. No Name of the
Hazardous Waste Quantity Kg/Day
Disposal Method
1 Organic Solid Waste 1657
Sent to Cement Industries
2 Spent Carbon 145
3 Solvent distillation residue
1091
4 Organic Evaporate liquid from MEE stripper
640
5 Mixed Solvents 3945 Sent to paint industries
6 ETP Sludge 1000 Sent to TSDF 7 Inorganic solid waste 359
8 MEE Salts 3151
9 Used Oils 500 Ltrs/Annum SPCB Authorized Agencies for Reprocessing/Recycling
10 Detoxified Containers 500 No’s/Month After Detoxification sent back to suppliers/sent to outside Parties
11 Used Lead Acid Batteries 2 No’s/Year Send back to suppliers for buyback of New Batteries
Solid Waste Details
12 Fly ash from boiler 7700
Kg/Day Sent to Brick Manufacturers
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ANNEXURE - VI
STACK EMISSION DETAILS FOR PROPOSED BOILER
Particulars Units 3.0TPH Coal Fired Boiler
4.0TPH Coal Fired Boiler
Type of Fuel -- Indian Coal Indian Coal
Coal /Fuel Consumption TPD 12 16
Ash Content % 35 35
Sulphur Content % 0.4 0.4
No. of Stacks No 1 1
Height of stack M 30 32
Diameter of Stack M 0.5 0.6
Temperature of Flue Gas oC 200 220
Velocity of Flue Gas m/s 12 14
Particulate Matter at outlet of Bag filter
gm/sec 0.50 0.75
Sulphur dioxide emission gm/sec 0.78 1.04
Oxides of Nitrogen emission
gm/sec 2.05 2.74
Pollution control equipments
Cyclone separator followed by suitable pack of Bag filters
STACK EMISSION DETAILS FOR DG SETS
Capacity In KVA
Emission of SPM in mg/Nm3
Emission Of SO2 in mg/Nm3
Emission of NOx
in mg/Nm3
Stack dia. in m
Flue Gas Temp. in
OC
Stack Height in m
Flue gas Velocity in m/sec.
750 KVA 80.0 190.0 235.0 0.30 225 10 15
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ANNEXURE -VII
PROCESS EMISSION DETAILS
S. No Name of the Gas Quantity
in Kg/Day Treatment Method
1 Carbon dioxide 280 Dispersed into the atmosphere
2 Oxygen 42 Dispersed into the atmosphere
3 Ammonia 16 Scrubbed by using Chilled water media
4 Sulfur dioxide 305 Scrubbed by using C.S.Lye Solution
5 Hydrogen 15 Diffused by using Nitrogen through Flame arrestor
6 Chloro methane 7 Scrubbed by using C.S.Lye Solution
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ANNEXURE - VIII
LIST OF RAW MATERIALS
1. CARVEDILOL
S. No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
1 Phenyl hydrazine Hydrochloride 209.00 139.33
2 1,3-Cyclohexanedione 162.00 108.00 3 2-(2-Methoxy phenoxy)
ethylamine 214.00 142.67
4 Acetone 500.00 333.33 5 Activated carbon 10.00 6.67 6 Epichlorohydrin 124.00 82.67 7 Ethyl acetate 1700.00 1133.33 8 Hydrochloric acid 52.00 34.67 9 Isopropyl alcohol 1000.00 666.67 10 Methanol 2800.00 1866.67 11 Potassium hydroxide 79.00 52.67 12 Raney nickel 15.00 10.00 13 Sodium hydroxide 54.00 36.00
2.CYANO DIOL HYDROCHLORIDE
S. No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
1 5-Cyano pthalide 42.00 70.00
2 Dimethyl amino magnesium chloride
39.00 65.00
3 Hydrochloric acid 21.00 35.00
4 P-Fluoromagnesium bromide
53.00 88.33
5 Toluene 400.00 666.67
3. DABIGARTAN
S. No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
1 Pyridine -2-ylamine 23.00 38.33 2 2-bromoacetic acid 30.00 50.00
3 4-amino benzonitrile 25.00 41.67 4 4-chloro-3-nitro-benzoic
acid 55.00
91.67 5 Acetic acid 200.00 333.33 6 Ammonia 5.00 8.33 7 Ammonium carbonate 18.00 30.00 8 Ammonium formate 20.00 33.33
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S. No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
9 Dichloromethane 200.00 333.33 10 Ethanol 600.00 1000.0 11 Ethyl acetate 200.00 333.33 12 Ethyl acrylate 25.00 41.67 13 Hexyl chloro formate 29.00 48.33 14 Hydrochloric acid 9.00 15.00 15 Iron 12.00 20.00 16 Isopropyl alcohol 400.00 666.67 17 Methanol 200.00 333.33 18 Methyl amine 9.00 15.00
19 n-Hexane 200.00 333.33 20 Potassium carbonate 25.00 41.67
21 Tetra hydrofuran 400.00 666.67 22 Thionyl chloride 31.00 51.67 23 Toluene 400.00 666.67 24 Triethylamine 24.00 40.00
4.FEXOFENADINE HYDROCHLORIDE
S. No.
Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
1 3-Chloro-2-methylprop-1-ene
108.00 72.00
2 4-Chlorobutanoyl chloride 158.00 105.33 3 Acetic Acid 118.00 78.67 4 Activated Carbon 10.00 6.67 5 Aluminum chloride 153.00 102.00 6 Benzene 90.00 60.00 7 Chloro benzene 234.00 156.00
8 Dichloromethane 500.00 333.33 9 Dimethyl formamide 500.00 333.33 10 Ethyl Acetate 800.00 533.33 11 Hydrochloric Acid 112.00 74.66 12 Isopropyl alcohol 300.00 200.00 13 Magnesium 51.00 34.00 14 Methanol 1033.00 688.67 15 Methyl isobutyl ketone 600.00 400.00 16 Methyl isobutyl ketone 600.00 400.00 17 Piperidine-4-carboxylic
acid 139.00
92.67 18 Potassium permanganate 168.00 112.00 19 Sodium acetate 98.00 65.33 20 Sodium Bicarbonate 85.00 56.67
21 Sodium Borohydride 38.00 25.33 22 Sodium hydroxide 80.00 53.33 23 Sodium sulphate 12.00 8.00
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S. No.
Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
24 THF 500.00 333.33 25 Toluene 1000.00 666.67
5.FLUCONAZOLE
S. No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
1 1,3 Difluoro benzene 60.00 200.00 2 1,2,4-triazole 58.00 193.33 3 Activated Carbon 10.00 33.33
4 Aluminium Chloride 72.00 240.00 5 Chloro Acetyl chloride 60.00 200.00 6 DMF 200.00 666.67 7 Ethyl Acetate 120.00 400.00
8 Hydrochloric Acid 26.00 86.67 9 Iso propyl alcohol 320.00 1066.67 10 MDC 250.00 833.33 11 Potassium carbonate 49.00 163.33 12 Potassium Hydroxide 20.00 66.67 13 Sodium sulphate 25.00 83.33 14 Toluene 200.00 666.67 15 Tri methyl Sulfoxonium
iodide 80.00 266.67 16 Triethyl Amine 46.00 153.33
6.FOLIC ACID
S. No.
Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
1 4-Nitro benzoic acid 100.00 333.33 2 2,5,6-Triamino-4,5-
dihydro-pyrimidin-4-ol ,Sulfuric acid
118.00
393.33
3 Acetic acid 500.00 1666.67 4 Acetone 30.00 100.00 5 Catalyst(Iron Powder) 10.00 33.33 6 Chlorine Gas 110.00 366.67 7 Dimethyl formamide 400.00 1333.33 8 Hydrogen Gas 4.00 13.33 9 Monosodium glutamate 96.00 320.00 10 Sodium hydroxide 44.00 146.67 11 Sodium Sulphate 15.00 50.00 12 Sulfuric acid 56.00 186.67 13 Thionyl chloride 71.25 237.50 14 Toluene 1800.00 6000.00
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7.ITRACONAZOLE
S. No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
1 1-(4-Methoxy phenyl ) Piperazine 57.00 95.00
2 1,2,4-Triazole 19.70 32.83 3 1,4-Dioxane 200.00 333.33
4 1-Chloro-4-Nitro-benzene 46.30 77.17 5 2,4 -
Dichloroacetophenone 55.00 91.67 6 2-Bromo Butane 39.00 65.00
7 Acetic Acid 34.60 57.66 8 Activated Carbon 8.00 13.33 9 Benzoyl chloride 40.35 67.25 10 Cis-Bromo Benzoate 128.00 213.33 11 Dimethyl Formamide 700.00 1166.67 12 Formamidine 12.70 21.17 13 Glycerol 26.70 44.50 14 Hydrazine Hydrate 14.55 24.25 15 Hydrochloric acid 10.70 17.83 16 Hydrobromic acid 46.10 76.83 17 Hydrogen Gas 1.80 3.00
18 Liq Bromine 46.30 77.17 19 Methane Sulfonyl Chloride 32.55 54.25 20 Methanol 500.00 833.33 21 Methylene Dichloride 400.00 666.67 22 n-Butanol 200.00 333.33 23 Palladium Carbon 5.00 8.33 24 Phenyl Chloro formate 45.40 75.67 25 Potassium Carbonate 71.70 119.50 26 Potassium Hydroxide 16.00 26.67 27 p-Toluenesulfonic acid 5.00 8.33 28 Sodium Bicarbonate 24.40 40.67 29 Sodium Carbonate 30.20 50.33 30 Sodium Hydroxide 19.65 32.75
31 Toluene 200.00 333.33 32 Triethylamine 28.80 48.00
8.KETOCONAZOLE
S. No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
1 2,4-Dichloro Acetophenone 43.00 143.33
2 4-Chlorophenol 26.00 86.67 3 Acetic acid 12.00 40.00
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S. No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
4 Acetone 300.00 1000.00 5 Activated Carbon 5.50 18.33 6 Benzoyl chloride 31.00 103.33
7 Ethyl Acetate 630.00 2100.00 8 Glycerol 21.00 70.00 9 Hydrochloric Acid 8.00 26.67 10 Imidazole 15.00 50.00 11 Liquid Bromine 36.00 120.00 12 Methanol 740.00 2466.67 13 Methanol 300.00 1000.00
14 Methylene Dichloride 200.00 666.67 15 n-Butanol 100.00 333.33 16 n-Butanol 300.00 1000.00 17 n-Hexane 300.00 1000.00 18 Para Toluene Sulfonyl
Chloride 39.00 130.00 19 ParaToluene Sulphonic
acid 7.50 25.00 20 Piperazine 18.00 60.00
21 Sodium Carbonate 22.00 73.33 22 Sodium hydroxide 17.00 56.67 23 Sodium methoxide 11.00 36.67 24 TBAB 20.00 66.67 25 Toluene 300.00 1000.00
9.LEVO CETIRIZINE DI HYDROCHLORIDE
S. No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
1 p-chloro benzo phenone 125.00 208.33 2 Acetic acid 15.00 25.00 3 Acetone 100.00 166.67
4 Activated carbon 10.00 16.67 5 Ammonium formate 37.00 61.67 6 Chloro ethanol 19.00 31.67 7 Di methyl formamide 100.00 166.67 8 Ethyl di isopropyl amine 28.00 46.67 9 Hydro bromic acid 20.00 33.33 10 Hydrochloric acid 48.00 80.00
11 MDC 1650.00 2750.00 12 Methanol 400.00 666.67 13 n,n-bis( 2-chloro ethyl)
amine HCl 46.00 76.67 14 para toluene sulphonyl
chloride 50.00 83.33
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S. No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
15 Sodium hydroxide 33.00 55.00 16 Sodium Hydroxide 21.00 35.00 17 Sodium mono chloro
acetate 26.00 43.33
18 Tartaric acid 40.00 66.67 19 Toluene 1600.00 2666.67 20 Triethyl amine 24.00 40.00
10.LINAGLIPTIN
S. No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
1 8-Bromo-7-but-2-ynyl-3-methyl-3,7-dihydro-purine-2,6-dione 72.00 120.00
2 2- Chloromethyl-4- methyl quinazoline 47.00 78.33
3 Activated carbon 5.00 8.33 4 Activated Carbon 5.00 8.33 5 Boc-3- amino piperidine 47.00 78.33 6 Dimethyl sulfoxide 400.00 666.66 7 Ethanol 400.00 666.66 8 Ethyl acetate 200.00 333.33 9 Isopropyl Alcohol 300.00 500.00
10 Isopropyl ether 200.00 333.33 11 Methanol 500.00 833.33 12 Methylene chloride 200.00 333.33 13 Sodium sulphate 25.00 41.67
11.MEROPENEM
S. No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
1 3-(Diphenoxy-phosphoryloxy)-6- (1-hydroxy-ethyl)-4-methyl-7-oxo- 1-aza-bicyclo[3.2.0]hept-2-ene-2- carboxylic acid 4-nitro-benzyl ester 430.00 286.67
2 2-Dimethylcarbamoyl-4-mercapto- pyrrolidine-1-carboxylic acid 4-nitro-benzyl ester 256.00 170.67
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S. No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
3 Acetonitrile 500.00 333.33 4 Dichloromethane 500.00 333.33 5 Ethyl acetate 600.00 400.00
6 Hydrochloric acid 53.00 35.33 7 Hydrogen 3.00 2.00 8 Iso propyl alcohol 500.00 333.33 9 n-Hexane 500.00 333.33 10 Palladium on carbon 10.00 6.67 11 Sodium hydroxide 29.00 19.33 12 Triethyl amine 74.00 49.33
12.MONTELUKAST SODIUM
S. No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
1 1-{3-[2-(7-Chloro-quinolin-2-yl)-vinyl]-phenyl}-3-[2-(1-hydroxy-1-methyl-ethyl)-phenyl]-propan-1-ol (MON10) 90.00 60.00
2 (1-Mercaptomethyl cyclopropyl)acetic acid 28.00 18.67
3 Acetic acid 11.00 7.33 4 Activated carbon 8.00 5.33 5 Dichloromethane 500.00 333.33 6 Diisopropyl ethyl amine 26.00 17.33 7 Methane sulfonyl chloride 23.00 15.33 8 Methanol 800.00 533.33 9 n-Heptane 300.00 200.00
10 n-Hexane 300.00 200.00 11 Sodium hydroxide 7.00 4.67 12 Sodium methoxide 10.50 7.00
13 Tert . butyl amine 14.00 9.33 14 Toluene 500.00 333.33
13.ROSUVASTATIN CALCIUM
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S. No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
1 4-Fluoro benzaldehyde 41.00 27.33 2 2,3-Dichloro-5,6-dicyano
benzoquinone 73.00 48.67 3 4-Methyl-3-oxo-pentanoic
acid ethyl ester 53.00 35.33
4 Calcium chloride 11.50 7.67 5 Di methoxy ethane 300.00 200.00 6 Diethyl methoxy borane 20.00 13.33 7 Diisobutylaluminium
hydride 35.00 23.33 8 Ethanol 250.00 166.67 9 Ethyl acetate 900.00 600.00 10 HMPA 100.00 66.67 11 Hydrochloric acid 8.00 5.33 12 Hydrogen fluoride 4.50 3.00 13 MDC 600.00 400.00 14 Meta chloro peroxy
benzoic acid 109.00 72.67 15 Methane sulfonyl chloride 30.00 20.00 16 Methanol 550.00 366.67 17 Methyl amine 9.00 6.00
18 Methyl(3R)-3-(tert butyl di methyl silyloxy)-5-oxo-6-triphenyl phosphoranylidene hexanoate 125.00 83.33
19 N,N-Dimethyl formamide 300.00 200.00 20 S-Methyl iso thio urea 29.00 19.33 21 Sodium boro hydride 8.20 5.47 22 THF 600.00 400.00 23 Toluene 600.00 400.00 24 Triethyl amine 10.00 6.67
14.SITAGLIPTIN PHOSPHATE MONOHYDRATE
S. No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
1 2,4,5-Trifluro phenyl acetic acid 41.00 68.33
2 3-(trifluoromethyl)-5,6,7,8-tetrahydro(1,2,4)triazole(4,3,-a)Pyrazine hydrochloride 48.00 80.00
3 Acetic acid 12.20 20.33 4 Ammonia 3.60 6.00 5 Ethyl acetate 200.00 333.33
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S. No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
6 Hydroxyl phenyl acetic acid 31.00 51.67 7 Isopropyl alcohol 400.00 666.67 8 Meldrum acid 31.10 51.83
9 Methane sulfonic acid 20.00 33.33 10 Methanol 200.00 333.33 11 Methylene chloride 400.00 666.67 12 Methylene dichloride 200.00 333.33 13 Phosphoric acid 20.00 33.33 14 Sodium bicarbonate 18.00 30.00 15 Sodium borohydrate 8.00 13.33
16 Sodium hydroxide 25.50 42.50 17 Sodium sulphate 20.00 33.33 18 Thionyl chloride 26.00 43.33 19 Toluene 200.00 333.33
15.TENELIGLIPTIN HYDROBROMIDE HYDRATE
S. No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
1 1-(3-methyl-1-phenyl-1H-pyrazo-5-yl) piperazine 42.00 70.00
2 4-Benzenesulfonyloxy-2-(thiazolidine -3-carbonyl)-pyrrolidine-1-carboxylic acid tert-butyl ester 77.00 128.33
3 Activated carbon 10.00 16.67 4 Aqueous hydrobromic acid 35.00 58.33
5 Dimethyl form amide 200.00 333.33 6 Ethyl acetate 300.00 500.00 7 Isopropyl alcohol 200.00 333.33 8 Methylene chloride 400.00 666.67 9 Sodium sulphate 20.00 33.33
10 Trifluoro acetic acid 5.00 8.33
16.TRI BUTYL TIN CHLORIDE
S. No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
1 n-Butyl Chloride 450.00 150.00 2 Ammonium chloride 50.00 16.67 3 Diethyl ether 150.00 50.00 4 Ethylene di bromide 0.100 0.03 5 Iodine 0.100 0.03 6 Magnesium 40.00 13.33
Additional Information SRR Laboratories
Prepared By Rightsource Industrial Solutions Pvt. Ltd Page 150
S. No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
7 Tin(II) chloride 308.00 102.67 8 Toluene 600.00 200.00
17.VALACYCLOVIR HYDROCHLORIDE MONOHYDRATE
S. No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
1 Acetic acid 2-(2-acetylamino-6- oxo-1,6-dihydro-purin-9-ylmethoxy)-ethyl ester 453.00 302.00
2 3-Methyl-2-(phenoxy carbonyl methylamino)-butyric acid 368.00 245.33
3 Acetone 500.00 333.33 4 Activated carbon 5.00 3.33 5 Dimethyl amine 200.00 133.33 6 Dimethyl formamide 500.00 333.33 7 Ethanol 1000.00 666.67 8 Hydrochloric acid 51.00 34.00
9 Hydrogen 3.00 2.00 10 Methanol 500.00 333.33 11 Palladium on Carbon 15.00 10.00 12 Sodium sulphate 25.00 16.67
18.VILDAGLIPTIN
S. No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
1 Pyrrolidine -2-carboxlic acid 44.00 73.33
2 3- amino-1- adamantanole 58.00 96.67
3 Acetone 200.00 333.33
4 Activated carbon 5.00 8.33
5 Ammonium bicarbonate 36.00 60.00
6 Chloro acetyl chloride 44.00 73.33
7 Isopropyl alcohol 300.00 500.00
8 Isopropyl ether 200.00 333.33
9 Isopropyl ether 200.00 333.33
10 Methylene chloride 400.00 666.67
11 Methylene dichloride 400.00 666.67
12 Tetrahydrofuran 200.00 333.33
13 Trifluoro acetic anhydride 75.00 125.00
ANNEXURE – IX
Additional Information SRR Laboratories
Prepared By Rightsource Industrial Solutions Pvt. Ltd Page 151
WASTE WATER DETAILS
S.No Purpose Effluent Water KLD
1 Process 55
2 Washings 5
3 Boiler Blow down 6
4 Cooling towers Blow down 11
5 Scrubbing system 2
6 Domestic 3.8
Total 82.8
HTDS & LTDS DETAILS
S. No
Purpose HTDS KLD
LTDS KLD
Total Effluent in
KLD
Disposal Method
1 Process 30 25 55
ZLD System
2 Washings 0 5 5
3 Boiler Blow down 0 6 6
4 Cooling towers blow down
0 11 11
5 Scrubbing system 2 0 2
6 Domestic 0 3.8 3.8
Total 32 50.8 82.8
Additional Information SRR Laboratories
Prepared By Rightsource Industrial Solutions Pvt. Ltd Page 152
ANNEXURE – X
CONSOLIDATED STATEMENT- POLLUTION DETAILS
Additional Information SRR Laboratories
Prepared By Rightsource Industrial Solutions Pvt. Ltd Page 153
LIST OF ENCLOSURES
S. No Content Enclosures
1 Sale Agreement Enclosure - I
2
Topomap Showing Inter-State Booundary[
Telangana State – Andhra Pradesh Interstate
Boundary – 400 meters (NE)] Within 5 Kms
Radius
Enclosure - II