TABLE E .1(i) BOILER EMISSIONS TO ATMOSPHERE · 2013-07-25 · Height above Ground (m): 22.0m above...
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TABLE E .1(i) BOILER EMISSIONS TO ATMOSPHERE Attach D.1.A: Table E.1 Page 1 of 104 Emission Point Ref. N o : UT1- 06 (BLR-11-11-1000) Location : Boiler Stack No. 4, New Utilities Building Grid Ref. (12 digit, 6E,6N): 178862E 63171N Vent Details Diameter: 900mm Height above Ground (m): 22.0m above ground, at EL 34.95m A.O.D. Date of commencement of emission: 1999 Characteristics of Emission on Natural gas: Boiler rating Steam Output: Thermal Input: 13,600 kg/hr 10.0 MW Boiler fuel Type: Maximum rate at which fuel is burned: % sulphur content: Natural Gas 750 kg/hr Nil NOx 200 mg/Nm 3 0 o C. 3% O2(Liquid or Gas), 6% O2(Solid Fuel) Maximum volume of emission 15,000 Nm 3 /hr Temperature 240 o C(max) o C(min) 160 o C(avg) (i) Period or periods during which emissions are made, or are to be made, including daily or seasonal variations (start-up/shutdown to be included): Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr** For inspection purposes only. Consent of copyright owner required for any other use. EPA Export 25-07-2013:20:19:13
Transcript of TABLE E .1(i) BOILER EMISSIONS TO ATMOSPHERE · 2013-07-25 · Height above Ground (m): 22.0m above...
TABLE E .1(i) BOILER EMISSIONS TO ATMOSPHERE
Attach D.1.A: Table E.1 Page 1 of 104
Emission Point Ref. No: UT1- 06 (BLR-11-11-1000)
Location : Boiler Stack No. 4, New Utilities Building
Grid Ref. (12 digit, 6E,6N): 178862E 63171N
Vent Details
Diameter: 900mm
Height above Ground (m): 22.0m above ground, at EL 34.95m A.O.D.
Date of commencement of emission:
1999
Characteristics of Emission on Natural gas:
Boiler rating Steam Output:
Thermal Input:
13,600 kg/hr
10.0 MW
Boiler fuel Type:
Maximum rate at which fuel is burned:
% sulphur content:
Natural Gas
750 kg/hr
Nil
NOx 200 mg/Nm3
0oC. 3% O2(Liquid or Gas), 6% O2(Solid Fuel)
Maximum volume of emission 15,000 Nm3/hr
Temperature 240 oC(max) oC(min) 160oC(avg)
(i) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up/shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr**
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TABLE E .1(i) BOILER EMISSIONS TO ATMOSPHERE
Attach D.1.A: Table E.1 Page 2 of 104
Characteristics of Emission on fuel oil:
Boiler rating Steam Output:
Thermal Input:
13,600 kg/hr
10.0 MW
Boiler fuel Type:
Maximum rate at which fuel is burned:
% sulphur content:
Fuel oil
850 kg/hr
<=0.2% on mass basis
SO2
NOx
320 mg/Nm3
350 mg/Nm3
0oC. 3% O2(Liquid or Gas),
Maximum volume of emission 15,000 Nm3/hr
Temperature 250 oC(max) oC(min) oC(avg)
(i) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up/shutdown to be included):
Periods of Emission (avg) As required day/yr**
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TABLE E .1(i) BOILER EMISSIONS TO ATMOSPHERE
Attach D.1.A: Table E.1 Page 3 of 104
Emission Point Ref. No: UT1- 07 (BLR-11-01-3000)
Location : Boiler Stack No. 6, Old Utilities Building
Grid Ref. (12 digit, 6E,6N): 78815E 63147N
Vent Details
Diameter: 450mm
Height above Ground (m): 19.5m above ground, at EL 32.8m A.O.D.
Date of commencement of emission:
2000
Characteristics of Emission :
Boiler rating Steam Output:
Thermal Input:
13,600 kg/hr
10.0 MW
Boiler fuel Type:
Maximum rate at which fuel is burned:
% sulphur content:
Natural Gas
750 kg/hr
Nil
NOx 200 mg/Nm3
0oC. 3% O2(Liquid or Gas), 6% O2(Solid Fuel)
Maximum volume of emission 15,000 m3/hr
Temperature 240 oC(max) oC(min) 160oC(avg)
(i) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up/shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr**
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TABLE E .1(i) BOILER EMISSIONS TO ATMOSPHERE
Attach D.1.A: Table E.1 Page 4 of 104
Characteristics of Emission on fuel oil:
Boiler rating Steam Output:
Thermal Input:
13,600 kg/hr
10.0 MW
Boiler fuel Type:
Maximum rate at which fuel is burned:
% sulphur content:
Fuel oil
850 kg/hr
<=0.2% on mass basis
SO2
NOx
320 mg/Nm3
350 mg/Nm3
0oC. 3% O2(Liquid or Gas),
Maximum volume of emission 15,000 m3/hr
0oC. 3% O2(Liquid or Gas), 6% O2(Solid Fuel)
Temperature 250 oC(max) oC(min) oC(avg)
(i) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up/shutdown to be included):
Periods of Emission (avg) As required day/yr**
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TABLE E .1(i) BOILER EMISSIONS TO ATMOSPHERE
Attach D.1.A: Table E.1 Page 5 of 104
Emission Point Ref. No: UT1- 08 (BLR-11-11-3000)
Location : Boiler Stack No. 4, New Utilities Building
Grid Ref. (12 digit, 6E,6N): 178865E 63159E
Vent Details
Diameter:
Height above Ground(m):
900mm
22m above ground at EL 35.0m A.O.D.
Date of commencement of
emission:
1999
Characteristics of Emission :
Boiler rating Steam Output:
Thermal Input:
13,600 kg/hr
10.0MW
Boiler fuel Type:
Maximum rate at which fuel is burned:
% sulphur content:
Natural Gas
750kg/hr
Nil
NOx 200 mg/Nm3
0oC. 3% O2(Liquid or Gas), 6% O2(Solid Fuel)
Maximum volume of emission 15,000 Nm3/hr
Temperature 240 oC(max) oC(min) 160oC(avg)
(i) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up/shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr**
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TABLE E .1(i) BOILER EMISSIONS TO ATMOSPHERE
Attach D.1.A: Table E.1 Page 6 of 104
Characteristics of Emission on fuel oil:
Boiler rating Steam Output:
Thermal Input:
13,600 kg/hr
10.0 MW
Boiler fuel Type:
Maximum rate at which fuel is burned:
% sulphur content:
Fuel oil
850 kg/hr
<=0.2% on mass basis
NOx 350 mg/Nm3
Maximum volume of emission 15,000 Nm3/hr
0oC. 3% O2(Liquid or Gas), 6% O2(Solid Fuel)
Temperature 250 oC(max) oC(min) oC(avg)
(i) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up/shutdown to be included):
Periods of Emission (avg) As required day/yr**
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TABLE E .1(i) BOILER EMISSIONS TO ATMOSPHERE
Attach D.1.A: Table E.1 Page 7 of 104
Emission Point Ref. No: UTI – 09 (BLR-11-11-2000)
Location : Boiler Stack No. 5, New Utilities Building
Grid Ref. (12 digit, 6E,6N): 178863E 063166N
Vent Details
Diameter:
Height above Ground(m):
900mm
22m above ground at EL 35.0m A.O.D.
Date of commencement of emission:
1999
Characteristics of Emission :
Boiler rating Steam Output:
Thermal Input:
13,600 kg/hr
10.0 MW
Boiler fuel Type:
Maximum rate at which fuel is burned:
% sulphur content:
Natural Gas
750 kg/hr
Nil
NOx 200 mg/Nm3
0oC. 3% O2(Liquid or Gas), 6% O2(Solid Fuel)
Maximum volume of emission 15,000 Nm3/hr
Temperature 240 oC(max) oC(min) 160oC(avg)
(i) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up/shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr**
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TABLE E .1(i) BOILER EMISSIONS TO ATMOSPHERE
Attach D.1.A: Table E.1 Page 8 of 104
Characteristics of Emission on fuel oil:
Boiler rating Steam Output:
Thermal Input:
13,600 kg/hr
10.0 MW
Boiler fuel Type:
Maximum rate at which fuel is burned:
% sulphur content:
Fuel oil
850 kg/hr
<=0.2% on mass basis
SO2
NOx
320 mg/Nm3
350 mg/Nm3
0oC. 3% O2(Liquid or Gas),
Maximum volume of emission 11,000 m3/hr
Temperature 250 oC(max) oC(min) oC(avg)
(i) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up/shutdown to be included):
Periods of Emission (avg) As required day/yr**
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TABLE E .1(ii) MAIN EMISSIONS TO ATMOSPHERE
Attach D.1.A: Table E.1 Page 9 of 104
Emission Point Ref. No: CB1 – 01 (Durr Thermal Oxidiser)
Source of Emission: Various from bulk plant header systems
Location : Outside Chemical Building No.1, South Side
Grid Ref. (12 digit, 6E,6N): 178896 E, 63209 N
Vent Details
Diameter:
Height above Ground(m):
1000mm
35m above ground at EL 45m A.O.D.
Date of commencement: September, 1994
Characteristics of Emission :
(i) Volume to be emitted:
Average/day 720,000 m3/d Maximum/day 720,000 m3/d
Maximum rate/hour 30,000 m3/h Min efflux velocity 13.8 m.sec-1
(ii) Other factors
Temperature 60 oC(max) 10 oC(min) oC(avg)
For Combustion Sources:
Volume terms expressed as : wet. dry. ____%O2
(iii) Briefly describe the treatment/abatement and give a reference for details elsewhere
in this application. A clearly labelled process flow diagram for each abatement system should be included in Attachment No 12A.
(iv) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up /shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr
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TABLE E .1(ii) MAIN EMISSIONS TO ATMOSPHERE
Attach D.1.A: Table E.1 Page 10 of 104
Emission Point Ref. No: CB1 – 02 (Carbon Absorber)
Source of Emission: Various sources from bulk plant header systems
Location : Outside Chemical Building No. 1, South Side
Grid Ref. (12 digit, 6E,6N): 178875 E, 63209 N
Vent Details
Diameter:
Height above Ground(m):
600mm
21m above ground at EL 34.0m A.O.D.
Date of commencement: 1995
Characteristics of Emission :
(i) Volume to be emitted:
Average/day 268,800 m3/d Maximum/day 268,800 m3/d
Maximum rate/hour 11,200 m3/h Min efflux velocity 19.6 m.sec-1
(ii) Other factors
Temperature <60 oC(max) 10 oC(min) oC(avg)
For Combustion Sources:
Volume terms expressed as : wet. dry. ________%O2
(iii) Briefly describe the treatment/abatement and give a reference for details elsewhere
in this application. A clearly labelled process flow diagram for each abatement system should be included in Attachment No 12A.
(iv) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up /shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr
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TABLE E .1(ii) MAIN EMISSIONS TO ATMOSPHERE
Attach D.1.A: Table E.1 Page 11 of 104
Emission Point Ref. No: CB1 – 03 (Scrubber Outlet)
Source of Emission: Various sources from bulk plant header systems
Location : Outside Chemical Building No. 1
Grid Ref. (12 digit, 6E,6N): 178893 E, 63246 N
Vent Details
Diameter:
Height above Ground(m):
750mm
20.0m above ground at EL 33.0m A.O.D.
Date of commencement: Future
Characteristics of Emission :
(i) Volume to be emitted:
Average/day 240,000 m3/d Maximum/day 240,000 m3/d
Maximum rate/hour 10,000 m3/h Min efflux velocity 6.3 m.sec-1
(ii) Other factors
Temperature 30 oC(max) 10 oC(min) oC(avg)
For Combustion Sources:
Volume terms expressed as : wet. dry. ________%O2
(iii) Briefly describe the treatment/abatement and give a reference for details elsewhere
in this application. A clearly labelled process flow diagram for each abatement system should be included in Attachment No 12A.
(iv) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up /shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr
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TABLE E .1(ii) MAIN EMISSIONS TO ATMOSPHERE
Attach D.1.A: Table E.1 Page 12 of 104
Emission Point Ref. No: DR1 - 03
Source of Emission: Drier Room Scrubber
Location : Outside Dryer House
Grid Ref. (12 digit, 6E,6N): 178820 E, 63183 N
Vent Details
Diameter:
Height above Ground(m):
600mm
11.0m above ground at EL 23.0m A.O.D.
Date of commencement: Prior to March 1989
Characteristics of Emission :
(i) Volume to be emitted:
Average/day 720,000 m3/d Maximum/day 720,000 m3/d
Maximum rate/hour 30,000 m3/h Min efflux velocity 29.5 m.sec-1
(ii) Other factors
Temperature 30 oC(max) 10 oC(min) 22 oC(avg)
For Combustion Sources:
Volume terms expressed as : wet. dry. ________%O2
(iii) Briefly describe the treatment/abatement and give a reference for details elsewhere
in this application. A clearly labelled process flow diagram for each abatement system should be included in Attachment No 12A.
(iv) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up /shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr
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TABLE E .1(ii) MAIN EMISSIONS TO ATMOSPHERE
Attach D.1.A: Table E.1 Page 13 of 104
Emission Point Ref. No: DR1 - 04
Source of Emission: Scrubber
Location : Outside Dryer House, West side
Grid Ref. (12 digit, 6E,6N): 178784 E, 63183 N
Vent Details
Diameter:
Height above Ground(m):
1000mm
10m above ground at EL 22.0m A.O.D.
Date of commencement: June, 1997
Characteristics of Emission :
(i) Volume to be emitted:
Average/day 1,440,000 m3/d Maximum/day 1,440,000m3/d
Maximum rate/hour 60,000 m3/h Min efflux velocity 21.2 m.sec-1
(ii) Other factors
Temperature 30oC(max) 10 oC(min) 22 oC(avg)
For Combustion Sources:
Volume terms expressed as : wet. dry. ________%O2
(iii) Briefly describe the treatment/abatement and give a reference for details elsewhere
in this application. A clearly labelled process flow diagram for each abatement system should be included in Attachment No 12A.
(iv) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up /shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr
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TABLE E .1(ii) MAIN EMISSIONS TO ATMOSPHERE
Attach D.1.A: Table E.1 Page 14 of 104
Emission Point Ref. No: CB2 – 01 (Thermatrix Thermal Oxidiser with Scrubber)
Source of Emission: Various Sources from bulk plant header systems
Location : West Side of Chemical Building No. 2
Grid Ref. (12 digit, 6E,6N): 178914E, 63151N
Vent Details
Diameter:
Height above Ground(m):
1000mm
32m above ground at EL 45.0m A.O.D.
Date of commencement: 1999
Characteristics of Emission :
(i) Volume to be emitted:
Average/day 720,000 m3/d Maximum/day 720,000 m3/d
Maximum rate/hour 30,000 m3/h Min efflux velocity 10.6 m.sec-1
(ii) Other factors
Temperature 60 oC(max) 10 oC(min) oC(avg)
For Combustion Sources:
Volume terms expressed as : wet. dry. ________%O2
(iii) Briefly describe the treatment/abatement and give a reference for details elsewhere
in this application. A clearly labelled process flow diagram for each abatement system should be included in Attachment No 12A.
(iv) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up /shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr
(v) Tables 12(iii) and 12(iv) should be completed as appropriate for each emission point
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TABLE E .1(ii) MAIN EMISSIONS TO ATMOSPHERE
Attach D.1.A: Table E.1 Page 15 of 104
Emission Point Ref. No: CB2 – 18 General Scrubber
Source of Emission: Various Sources from bulk plant header systems
Location : Roof of Chemical Building No.2
Grid Ref. (12 digit, 6E,6N): 178941E, 63151N
Vent Details
Diameter:
Height above Ground(m):
750mm
30m above ground at EL 43.0m A.O.D.
Date of commencement: 1999
Characteristics of Emission :
(i) Volume to be emitted:
Average/day 240,000 m3/d Maximum/day 240,000 m3/d
Maximum rate/hour 10,000 m3/h Min efflux velocity 6.3 m.sec-1
(ii) Other factors
Temperature 30 oC(max) 10 oC(min) 22 oC(avg)
For Combustion Sources:
Volume terms expressed as : wet. dry. _______%O2
(iii) Briefly describe the treatment/abatement and give a reference for details elsewhere
in this application. A clearly labelled process flow diagram for each abatement system should be included in Attachment No 12A.
(iv) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up /shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr
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TABLE E .1(ii) OTHER EMISSIONS TO ATMOSPHERE
Attach D.1.A: Table E.1 Page 16 of 104
Emission Point Ref. No: TAB-01 HEPA filter
Source of Emission: Dust Collector 904
Location : Roof of Tabletting Building
Grid Ref. (12 digit, 6E,6N): 178876E, 63045N
Vent Details
Diameter:
Height above Ground(m):
325mm
26m above ground, at EL 39.0m A.O.D.
Date of commencement of
emission:
1999
Characteristics of Emission :
(i) Volume to be emitted:
Average/day 104,400 m3/d Maximum/day 104,400 m3/d
Maximum rate/hour 4350 m3/h Min efflux velocity 6.1 m.sec-1
(ii) Other factors
Temperature oC(max) oC(min) 25 oC(avg)
For Combustion Sources:
Volume terms expressed as : wet. dry. ________%O2
(iii) Briefly describe the treatment/abatement and give a reference for details elsewhere
in this application. A clearly labelled process flow diagram for each abatement system should be included in Attachment No 12A.
(iv) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up /shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr
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TABLE E .1(ii) OTHER EMISSIONS TO ATMOSPHERE
Attach D.1.A: Table E.1 Page 17 of 104
Emission Point Ref. No: TAB-02 HEPA filter
Source of Emission: Dust Collector 903
Location : Roof of Tabletting Building
Grid Ref. (12 digit, 6E,6N): 178898E, 63049N
Vent Details
Diameter:
Height above Ground(m):
325mm
26m above ground, at EL 39.0m A.O.D.
Date of commencement of
emission:
1999
Characteristics of Emission :
(i) Volume to be emitted:
Average/day 104,400 m3/d Maximum/day 104,400 m3/d
Maximum rate/hour 4350 m3/h Min efflux velocity 6.1 m.sec-1
(ii) Other factors
Temperature oC(max) oC(min) 25 oC(avg)
For Combustion Sources:
Volume terms expressed as : wet. dry. ________%O2
(iii) Briefly describe the treatment/abatement and give a reference for details elsewhere
in this application. A clearly labelled process flow diagram for each abatement system should be included in Attachment No 12A.
(iv) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up /shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr
(v) Tables 12(iii) and 12(iv) should be completed as appropriate for each emission point
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TABLE E .1(ii) OTHER EMISSIONS TO ATMOSPHERE
Attach D.1.A: Table E.1 Page 18 of 104
Emission Point Ref. No: TAB-03 HEPA Filter
Source of Emission: Dust Collector 906
Location : Roof of Tabletting Building
Grid Ref. (12 digit, 6E,6N): 178911E, 63063N
Vent Details
Diameter:
Height above Ground(m):
250mm
26m above ground, at EL 39m A.O.D.
Date of commencement of
emission:
1999
Characteristics of Emission :
(i) Volume to be emitted:
Average/day 104,400 m3/d Maximum/day 104,400 m3/d
Maximum rate/hour 4350 m3/h Min efflux velocity 6.1 m.sec-1
(ii) Other factors
Temperature oC(max) oC(min) 25 oC(avg)
For Combustion Sources:
Volume terms expressed as : wet. dry. ________%O2
(iii) Briefly describe the treatment/abatement and give a reference for details elsewhere
in this application. A clearly labelled process flow diagram for each abatement system should be included in Attachment No 12A.
(iv) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up /shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr
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TABLE E .1(ii) OTHER EMISSIONS TO ATMOSPHERE
Attach D.1.A: Table E.1 Page 19 of 104
Emission Point Ref. No: TAB-04 HEPA Filter
Source of Emission: Dust Collector 908
Location : Roof of Tabletting Building
Grid Ref. (12 digit, 6E,6N): 178908E, 63070N
Vent Details
Diameter:
Height above Ground(m):
300mm
26m above ground, at EL 39m A.O.D.
Date of commencement of
emission:
1999
Characteristics of Emission :
(i) Volume to be emitted:
Average/day 104,400 m3/d Maximum/day 104,400 m3/d
Maximum rate/hour 4350 m3/h Min efflux velocity 6.1 m.sec-1
(ii) Other factors
Temperature oC(max) oC(min) 25 oC(avg)
For Combustion Sources:
Volume terms expressed as : wet. dry. ________%O2
(iii) Briefly describe the treatment/abatement and give a reference for details elsewhere
in this application. A clearly labelled process flow diagram for each abatement system should be included in Attachment No 12A.
(iv) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up /shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr
For
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Attach D.1.A: Table E.1 Page 20 of 104
Emission Point Ref. No: TAB-05 HEPA Filter
Source of Emission: Dust Collector 907
Location : Roof of Tabletting Building
Grid Ref. (12 digit, 6E,6N): 178910E, 63067N
Vent Details
Diameter:
Height above Ground(m):
450mm
26m above ground, at EL 39m A.O.D.
Date of commencement of
emission:
1999
Characteristics of Emission :
(i) Volume to be emitted:
Average/day 187,200 m3/d Maximum/day 187,200 m3/d
Maximum rate/hour 7800 m3/h Min efflux velocity 7.7 m.sec-1
(ii) Other factors
Temperature oC(max) oC(min) 25 oC(avg)
For Combustion Sources:
Volume terms expressed as : wet. dry. ________%O2
(iii) Briefly describe the treatment/abatement and give a reference for details elsewhere
in this application. A clearly labelled process flow diagram for each abatement system should be included in Attachment No 12A.
(iv) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up /shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr
For
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Attach D.1.A: Table E.1 Page 21 of 104
Emission Point Ref. No: TAB-06 HEPA filter
Source of Emission: Dust Collector 905
Location : Roof of Tabletting Building
Grid Ref. (12 digit, 6E,6N): 178931E, 63089N
Vent Details
Diameter:
Height above Ground(m):
200mm
26m above ground, at EL 39m A.O.D.
Date of commencement of
emission:
1999
Characteristics of Emission :
(i) Volume to be emitted:
Average/day 104,400 m3/d Maximum/day 104,400 m3/d
Maximum rate/hour 4350 m3/h Min efflux velocity 6.1 m.sec-1
(ii) Other factors
Temperature oC(max) oC(min) 25 oC(avg)
For Combustion Sources:
Volume terms expressed as : wet. dry. ________%O2
(iii) Briefly describe the treatment/abatement and give a reference for details elsewhere
in this application. A clearly labelled process flow diagram for each abatement system should be included in Attachment No 12A.
(iv) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up /shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr
For
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.
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Attach D.1.A: Table E.1 Page 22 of 104
Emission Point Ref. No: TAB-10 HEPA filter
Source of Emission: Tablet Coater C-903
Location : Roof of Tabletting Building
Grid Ref. (12 digit, 6E,6N): 178882E, 63052N
Vent Details
Diameter:
Height above Ground(m):
400mm
27m above ground, at EL 39m A.O.D.
Date of commencement of
emission:
1999
Characteristics of Emission :
(i) Volume to be emitted:
Average/day 180,000 m3/d Maximum/day 180,000 m3/d
Maximum rate/hour 7500 m3/h Min efflux velocity 10.6 m.sec-1
(ii) Other factors
Temperature oC(max) oC(min) 50oC(avg)
For Combustion Sources:
Volume terms expressed as : wet. dry. ________%O2
(iii) Briefly describe the treatment/abatement and give a reference for details elsewhere
in this application. A clearly labelled process flow diagram for each abatement system should be included in Attachment No 12A.
(iv) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up /shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr
For
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Attach D.1.A: Table E.1 Page 23 of 104
Emission Point Ref. No: TAB-11 HEPA filter
Source of Emission: Tablet Coater C-902
Location : Roof of Tabletting Building
Grid Ref. (12 digit, 6E,6N): 178889E, 63054N
Vent Details
Diameter:
Height above Ground(m):
400mm
27m above ground, at EL 39m A.O.D.
Date of commencement of
emission:
1999
Characteristics of Emission :
(i) Volume to be emitted:
Average/day 180,000 m3/d Maximum/day 180,000 m3/d
Maximum rate/hour 7500 m3/h Min efflux velocity 10.6 m.sec-1
(ii) Other factors
Temperature oC(max) oC(min) 50oC(avg)
For Combustion Sources:
Volume terms expressed as : wet. dry. ________%O2
(iii) Briefly describe the treatment/abatement and give a reference for details elsewhere
in this application. A clearly labelled process flow diagram for each abatement system should be included in Attachment No 12A.
(iv) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up /shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr
For
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.
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Attach D.1.A: Table E.1 Page 24 of 104
Emission Point Ref. No: TAB-12 HEPA filter
Source of Emission: Tablet Coater C-901
Location : Roof of Tabletting Building
Grid Ref. (12 digit, 6E,6N): 178903E, 63056N
Vent Details
Diameter:
Height above Ground(m):
400mm
27m above ground, at EL 39m A.O.D.
Date of commencement of
emission:
1999
Characteristics of Emission :
(i) Volume to be emitted:
Average/day 180,000 m3/d Maximum/day 180,000 m3/d
Maximum rate/hour 7,500 m3/h Min efflux velocity 10.6 m.sec-1
(ii) Other factors
Temperature oC(max) oC(min) 50oC(avg)
For Combustion Sources:
Volume terms expressed as : wet. dry. ________%O2
(iii) Briefly describe the treatment/abatement and give a reference for details elsewhere
in this application. A clearly labelled process flow diagram for each abatement system should be included in Attachment No 12A.
(iv) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up /shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr
For
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.
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Attach D.1.A: Table E.1 Page 25 of 104
Emission Point Ref. No: TAB-13 HEPA filter
Source of Emission: Tablet Coater C-900
Location : Roof of Tabletting Building
Grid Ref. (12 digit, 6E,6N): 178906E, 63057N
Vent Details
Diameter:
Height above Ground(m):
400mm
27m above ground, at EL 39m A.O.D.
Date of commencement of
emission:
1999
Characteristics of Emission :
(i) Volume to be emitted:
Average/day 180,000 m3/d Maximum/day 180,000 m3/d
Maximum rate/hour 7,500 m3/h Min efflux velocity 10.6 m.sec-1
(ii) Other factors
Temperature oC(max) oC(min) 50oC(avg)
For Combustion Sources:
Volume terms expressed as : wet. dry. ________%O2
(iii) Briefly describe the treatment/abatement and give a reference for details elsewhere
in this application. A clearly labelled process flow diagram for each abatement system should be included in Attachment No 12A.
(iv) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up /shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr
For
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ectio
n pur
pose
s only
.
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Attach D.1.A: Table E.1 Page 26 of 104
Emission Point Ref. No: TAB-14 HEPA filter
Source of Emission: Tablet - Process Point
Location : Roof of Tabletting Building
Grid Ref. (12 digit, 6E,6N): 178868E, 63049N (Provisional)
Vent Details
Diameter:
Height above Ground(m):
500mm
27m above ground, at EL 39m A.O.D.
Date of commencement of
emission:
1999
Characteristics of Emission :
(i) Volume to be emitted:
Average/day 180,000 m3/d Maximum/day 180,000 3/d
Maximum rate/hour 7,500 m3/h Min efflux velocity 10.6 m.sec-1
(ii) Other factors
Temperature oC(max) oC(min) 50 oC(avg)
For Combustion Sources:
Volume terms expressed as : wet. dry. ________%O2
(iii) Briefly describe the treatment/abatement and give a reference for details elsewhere
in this application. A clearly labelled process flow diagram for each abatement system should be included in Attachment No 12A.
(iv) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up /shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr
For
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ectio
n pur
pose
s only
.
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Attach D.1.A: Table E.1 Page 27 of 104
Emission Point Ref. No: TAB-15 HEPA filter
Source of Emission: Fluid Bed Dryer D-400
Location : Roof of Tabletting Building
Grid Ref. (12 digit, 6E,6N): 178883E, 63056N
Vent Details
Diameter:
Height above Ground(m):
400 mm
27m above ground, at EL 39m A.O.D.
Date of commencement of
emission:
1999
Characteristics of Emission :
(i) Volume to be emitted:
Average/day 192,000 m3/d Maximum/day 192,000 m3/d
Maximum rate/hour 8,000 m3/h Min efflux velocity 14.4 m.sec-1
(ii) Other factors
Temperature oC(max) oC(min) 50 oC(avg)
For Combustion Sources:
Volume terms expressed as : wet. dry. ________%O2
(iii) Briefly describe the treatment/abatement and give a reference for details elsewhere
in this application. A clearly labelled process flow diagram for each abatement system should be included in Attachment No 12A.
(iv) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up /shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr
For
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ectio
n pur
pose
s only
.
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Attach D.1.A: Table E.1 Page 28 of 104
Emission Point Ref. No: TAB-16 HEPA Filter
Source of Emission: Fluid Bed Dryer D-300
Location : Roof of Tabletting Building
Grid Ref. (12 digit, 6E,6N): 178888E 63057N
Vent Details
Diameter:
Height above Ground(m):
400 mm
27m above ground, at EL 39m A.O.D.
Date of commencement of
emission:
1999
Characteristics of Emission :
(i) Volume to be emitted:
Average/day 192,000 m3/d Maximum/day 192,000 m3/d
Maximum rate/hour 8,000 m3/h Min efflux velocity 14.4 m.sec-1
(ii) Other factors
Temperature oC(max) oC(min) 50 oC(avg)
For Combustion Sources:
Volume terms expressed as : wet. dry. ________%O2
(iii) Briefly describe the treatment/abatement and give a reference for details elsewhere
in this application. A clearly labelled process flow diagram for each abatement system should be included in Attachment No 12A.
(iv) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up /shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr
For
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pose
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.
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Attach D.1.A: Table E.1 Page 29 of 104
Emission Point Ref. No: TAB-17 HEPA Filter
Source of Emission: Fluid Bed Dryer D-200
Location : Roof of Tabletting Building
Grid Ref. (12 digit, 6E,6N): 178897E 63058N
Vent Details
Diameter:
Height above Ground(m):
400 mm
27m above ground, at EL 39m A.O.D.
Date of commencement of
emission:
1999
Characteristics of Emission :
(i) Volume to be emitted:
Average/day 192,000 m3/d Maximum/day 192,000 m3/d
Maximum rate/hour 8,000 m3/h Min efflux velocity 14.4 m.sec-1
(ii) Other factors
Temperature oC(max) oC(min) 50 oC(avg)
For Combustion Sources:
Volume terms expressed as : wet. dry. ________%O2
(iii) Briefly describe the treatment/abatement and give a reference for details elsewhere
in this application. A clearly labelled process flow diagram for each abatement system should be included in Attachment No 12A.
(iv) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up /shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr
For
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ectio
n pur
pose
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.
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Attach D.1.A: Table E.1 Page 30 of 104
Emission Point Ref. No: TAB-18 HEPA Filter
Source of Emission: Fluid Bed Dryer D-100
Location : Roof of Tabletting Building
Grid Ref. (12 digit, 6E,6N): 178903E, 63060N
Vent Details
Diameter:
Height above Ground(m):
400 mm
27m above ground, at EL 39m A.O.D.
Date of commencement of
emission:
1999
Characteristics of Emission :
(i) Volume to be emitted:
Average/day 192,000 m3/d Maximum/day 192,000 m3/d
Maximum rate/hour 8,000 m3/h Min efflux velocity 14.4 m.sec-1
(ii) Other factors
Temperature oC(max) oC(min) 50oC(avg)
For Combustion Sources:
Volume terms expressed as : wet. dry. ________%O2
(iii) Briefly describe the treatment/abatement and give a reference for details elsewhere
in this application. A clearly labelled process flow diagram for each abatement system should be included in Attachment No 12A.
(iv) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up /shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr
For
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ectio
n pur
pose
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.
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Attach D.1.A: Table E.1 Page 31 of 104
Emission Point Ref. No: TAB-19 HEPA Filter
Source of Emission: Tablet - Process Point
Location : Roof of Tabletting Building
Grid Ref. (12 digit, 6E,6N): 178874E, 63043N (Provisional)
Vent Details
Diameter:
Height above Ground(m):
500 mm
27m above ground, at EL 39m A.O.D.
Date of commencement of
emission:
1999
Characteristics of Emission :
(i) Volume to be emitted:
Average/day 104,000 m3/d Maximum/day 104,000 m3/d
Maximum rate/hour 4,350 m3/h Min efflux velocity 6.1 m.sec-1
(ii) Other factors
Temperature oC(max) oC(min) 25oC(avg)
For Combustion Sources:
Volume terms expressed as : wet. dry. ________%O2
(iii) Briefly describe the treatment/abatement and give a reference for details elsewhere
in this application. A clearly labelled process flow diagram for each abatement system should be included in Attachment No 12A.
(iv) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up /shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr
For
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ectio
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pose
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.
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Attach D.1.A: Table E.1 Page 32 of 104
Emission Point Ref. No: TAB-20 HEPA Filter
Source of Emission: Tablet - Process Point
Location : Roof of Tabletting Building
Grid Ref. (12 digit, 6E,6N): 178873E, 63050N (Provisional)
Vent Details
Diameter:
Height above Ground(m):
500 mm
27m above ground, at EL 39m A.O.D.
Date of commencement of
emission:
1999
Characteristics of Emission :
(i) Volume to be emitted:
Average/day 180,000 m3/d Maximum/day 180,000 m3/d
Maximum rate/hour 7,500 m3/h Min efflux velocity 10.6 m.sec-1
(ii) Other factors
Temperature oC(max) oC(min) 50 oC(avg)
For Combustion Sources:
Volume terms expressed as : wet. dry. ________%O2
(iii) Briefly describe the treatment/abatement and give a reference for details elsewhere
in this application. A clearly labelled process flow diagram for each abatement system should be included in Attachment No 12A.
(iv) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up /shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr
For
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ectio
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pose
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.
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Attach D.1.A: Table E.1 Page 33 of 104
Emission Point Ref. No: TAB-21 HEPA Filter
Source of Emission: Fluid Bed Dryer D-500
Location : Roof of Tabletting Building
Grid Ref. (12 digit, 6E,6N): 178871E, 63053N
Vent Details
Diameter:
Height above Ground(m):
400 mm
27m above ground, at EL 39m A.O.D.
Date of commencement of
emission:
1999
Characteristics of Emission :
(i) Volume to be emitted:
Average/day 156,000 m3/d Maximum/day 156,000 m3/d
Maximum rate/hour 6,500 m3/h Min efflux velocity 14.4 m.sec-1
(ii) Other factors
Temperature oC(max) oC(min) 50 oC(avg)
For Combustion Sources:
Volume terms expressed as : wet. dry. ________%O2
(iii) Briefly describe the treatment/abatement and give a reference for details elsewhere
in this application. A clearly labelled process flow diagram for each abatement system should be included in Attachment No 12A.
(iv) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up /shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr
For
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ectio
n pur
pose
s only
.
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Attach D.1.A: Table E.1 Page 34 of 104
Emission Point Ref. No: TAB-22 HEPA Filter
Source of Emission: Tablet - Dust Collector
Location : Roof of Tabletting Building
Grid Ref. (12 digit, 6E,6N): 178854E, 063049N (Provisional)
Vent Details
Diameter:
Height above Ground(m):
500mm
27m above ground, at EL 39m A.O.D.
Date of commencement of
emission:
1999
Characteristics of Emission :
(i) Volume to be emitted:
Average/day 43,200 m3/d Maximum/day 43,200 m3/d
Maximum rate/hour 1,800 m3/h Min efflux velocity 5.2 m.sec-1
(ii) Other factors
Temperature oC(max) oC(min) 50 oC(avg)
For Combustion Sources:
Volume terms expressed as : wet. dry. ________%O2
(iii) Briefly describe the treatment/abatement and give a reference for details elsewhere
in this application. A clearly labelled process flow diagram for each abatement system should be included in Attachment No 12A.
(iv) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up /shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr
(v) Tables 12(iii) and 12(iv) should be completed as appropriate for each emission point
For
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ectio
n pur
pose
s only
.
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Attach D.1.A: Table E.1 Page 35 of 104
Emission Point Ref. No: TAB-23 HEPA Filter
Source of Emission: Tablet - Dust Collector
Location : Roof of Tabletting Building
Grid Ref. (12 digit, 6E,6N): 178852E, 63050N
Vent Details
Diameter:
Height above Ground(m):
600 mm
27m above ground, at EL 39m A.O.D.
Date of commencement of
emission:
1999
Characteristics of Emission :
(i) Volume to be emitted:
Average/day 187,200 m3/d Maximum/day 187,200 m3/d
Maximum rate/hour 7,800 m3/h Min efflux velocity 7.7 m.sec-1
(ii) Other factors
Temperature oC(max) oC(min) 25 oC(avg)
For Combustion Sources:
Volume terms expressed as : wet. dry. ________%O2
(iii) Briefly describe the treatment/abatement and give a reference for details elsewhere
in this application. A clearly labelled process flow diagram for each abatement system should be included in Attachment No 12A.
(iv) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up /shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr
For
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ectio
n pur
pose
s only
.
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Attach D.1.A: Table E.1 Page 36 of 104
Emission Point Ref. No: TAB-24 HEPA Filter
Source of Emission: Tablet - Dust Collector
Location : Roof of Tabletting Building
Grid Ref. (12 digit, 6E,6N): 178853E, 63062N
Vent Details
Diameter:
Height above Ground(m):
450 mm
27m above ground, at EL 39m A.O.D.
Date of commencement of
emission:
1999
Characteristics of Emission :
(i) Volume to be emitted:
Average/day 88,800 m3/d Maximum/day 88,800 m3/d
Maximum rate/hour 3,700 m3/h Min efflux velocity 6.5 m.sec-1
(ii) Other factors
Temperature oC(max) oC(min) 25 oC(avg)
For Combustion Sources:
Volume terms expressed as : wet. dry. ________%O2
(iii) Briefly describe the treatment/abatement and give a reference for details elsewhere
in this application. A clearly labelled process flow diagram for each abatement system should be included in Attachment No 12A.
(iv) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up /shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr
(v) Tables 12(iii) and 12(iv) should be completed as appropriate for each emission point
For
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ectio
n pur
pose
s only
.
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EPA Export 25-07-2013:20:19:16
TABLE E .1(ii) OTHER EMISSIONS TO ATMOSPHERE
Attach D.1.A: Table E.1 Page 37 of 104
Emission Point Ref. No: TAB-25 HEPA Filter
Source of Emission: Tablet - Coater Vent
Location : Roof of Tabletting Building
Grid Ref. (12 digit, 6E,6N): 178848E, 63045N
Vent Details
Diameter:
Height above Ground(m):
500 mm
27m above ground, at EL 39m A.O.D.
Date of commencement of
emission:
1999
Characteristics of Emission :
(i) Volume to be emitted:
Average/day 180,000 m3/d Maximum/day 180,000 m3/d
Maximum rate/hour 7,500 m3/h Min efflux velocity 10.6 m.sec-1
(ii) Other factors
Temperature oC(max) oC(min) 50oC(avg)
For Combustion Sources:
Volume terms expressed as : wet. dry. ________%O2
(iii) Briefly describe the treatment/abatement and give a reference for details elsewhere
in this application. A clearly labelled process flow diagram for each abatement system should be included in Attachment No 12A.
(iv) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up /shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr
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EPA Export 25-07-2013:20:19:16
TABLE E .1(ii) OTHER EMISSIONS TO ATMOSPHERE
Attach D.1.A: Table E.1 Page 38 of 104
Emission Point Ref. No: TAB-26 HEPA Filter
Source of Emission: Tablet - Coater Vent
Location : Roof of Tabletting Building
Grid Ref. (12 digit, 6E,6N): 178844E, 63037N
Vent Details
Diameter:
Height above Ground(m):
500 mm
27m above ground, at EL 39m A.O.D.
Date of commencement of
emission:
1999
Characteristics of Emission :
(i) Volume to be emitted:
Average/day 180,000 m3/d Maximum/day 180,000 m3/d
Maximum rate/hour 7,500 m3/h Min efflux velocity 10.6 m.sec-1
(ii) Other factors
Temperature oC(max) oC(min) 50 oC(avg)
For Combustion Sources:
Volume terms expressed as : wet. dry. ________%O2
(iii) Briefly describe the treatment/abatement and give a reference for details elsewhere
in this application. A clearly labelled process flow diagram for each abatement system should be included in Attachment No 12A.
(iv) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up /shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr
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EPA Export 25-07-2013:20:19:16
TABLE E .1(ii) OTHER EMISSIONS TO ATMOSPHERE
Attach D.1.A: Table E.1 Page 39 of 104
Emission Point Ref. No: TAB-27 HEPA Filter
Source of Emission: Fluid bed dryer
Location : Roof of Tabletting Building
Grid Ref. (12 digit, 6E,6N): 178844E, 63041N
Vent Details
Diameter:
Height above Ground(m):
400 mm
27m above ground, at EL 39m A.O.D.
Date of commencement of
emission:
1999
Characteristics of Emission :
(i) Volume to be emitted:
Average/day 156,000 m3/d Maximum/day 156,000 m3/d
Maximum rate/hour 6,500 m3/h Min efflux velocity 14.4 m.sec-1
(ii) Other factors
Temperature oC(max) oC(min) 50 oC(avg)
For Combustion Sources:
Volume terms expressed as : wet. dry. ________%O2
(iii) Briefly describe the treatment/abatement and give a reference for details elsewhere
in this application. A clearly labelled process flow diagram for each abatement system should be included in Attachment No 12A.
(iv) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up /shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr
(v) Tables 12(iii) and 12(iv) should be completed as appropriate for each emission point
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EPA Export 25-07-2013:20:19:16
TABLE E .1(ii) OTHER EMISSIONS TO ATMOSPHERE
Attach D.1.A: Table E.1 Page 40 of 104
Emission Point Ref. No: TAB-28 HEPA Filter
Source of Emission: Dust Collector 934
Location : Roof of Tabletting Building
Grid Ref. (12 digit, 6E,6N): 178896E, 63049N
Vent Details
Diameter:
Height above Ground(m):
400 mm
27m above ground, at EL 39m A.O.D.
Date of commencement of
emission:
1999
Characteristics of Emission :
(i) Volume to be emitted:
Average/day 104,000 m3/d Maximum/day 104,000 m3/d
Maximum rate/hour 4,350 m3/h Min efflux velocity 6.1 m.sec-1
(ii) Other factors
Temperature oC(max) oC(min) 25oC(avg)
For Combustion Sources:
Volume terms expressed as : wet. dry. ________%O2
(iii) Briefly describe the treatment/abatement and give a reference for details elsewhere
in this application. A clearly labelled process flow diagram for each abatement system should be included in Attachment No 12A.
(iv) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up /shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr
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EPA Export 25-07-2013:20:19:16
TABLE E .1(ii) OTHER EMISSIONS TO ATMOSPHERE
Attach D.1.A: Table E.1 Page 41 of 104
Emission Point Ref. No: TAB-29 HEPA Filter
Source of Emission: Tablet - Fluid bed dryer
Location : Roof of Tabletting Building
Grid Ref. (12 digit, 6E,6N): 178840E, 63049N (Provisional)
Vent Details
Diameter:
Height above Ground(m):
400 mm
27m above ground, at EL 39m A.O.D.
Date of commencement of
emission:
1999
Characteristics of Emission :
(i) Volume to be emitted:
Average/day 156,000 m3/d Maximum/day 156,000 m3/d
Maximum rate/hour 6,500 m3/h Min efflux velocity 14.4 m.sec-1
(ii) Other factors
Temperature oC(max) oC(min) 50 oC(avg)
For Combustion Sources:
Volume terms expressed as : wet. dry. ________%O2
(iii) Briefly describe the treatment/abatement and give a reference for details elsewhere
in this application. A clearly labelled process flow diagram for each abatement system should be included in Attachment No 12A.
(iv) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up /shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr
(v) Tables 12(iii) and 12(iv) should be completed as appropriate for each emission point
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EPA Export 25-07-2013:20:19:16
TABLE E .1(ii) OTHER EMISSIONS TO ATMOSPHERE
Attach D.1.A: Table E.1 Page 42 of 104
Emission Point Ref. No: TAB-30 HEPA Filter
Source of Emission: Tablet – Process Point
Location : Roof of Tabletting Building
Grid Ref. (12 digit, 6E,6N): 178831E, 63043N (Provisional)
Vent Details
Diameter:
Height above Ground(m):
500 mm
27m above ground, at EL 39m A.O.D.
Date of commencement of
emission:
1999
Characteristics of Emission :
(i) Volume to be emitted:
Average/day 180,000 m3/d Maximum/day 180,000 m3/d
Maximum rate/hour 7,500 m3/h Min efflux velocity 10.6 m.sec-1
(ii) Other factors
Temperature oC(max) oC(min) 50oC(avg)
For Combustion Sources:
Volume terms expressed as : wet. dry. ________%O2
(iii) Briefly describe the treatment/abatement and give a reference for details elsewhere
in this application. A clearly labelled process flow diagram for each abatement system should be included in Attachment No 12A.
(iv) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up /shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr
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EPA Export 25-07-2013:20:19:16
TABLE E .1(ii) OTHER EMISSIONS TO ATMOSPHERE
Attach D.1.A: Table E.1 Page 43 of 104
Emission Point Ref. No: TAB-31 HEPA Filter
Source of Emission: Fluid bed dryer
Location : Roof of Tabletting Building
Grid Ref. (12 digit, 6E,6N): 178830E, 63047N (Provisional)
Vent Details
Diameter:
Height above Ground(m):
400 mm
27m above ground, at EL 39m A.O.D.
Date of commencement of
emission:
1999
Characteristics of Emission :
(i) Volume to be emitted:
Average/day 156,000 m3/d Maximum/day 156,000 m3/d
Maximum rate/hour 6,500 m3/h Min efflux velocity 14.4 m.sec-1
(ii) Other factors
Temperature oC(max) oC(min) 50 oC(avg)
For Combustion Sources:
Volume terms expressed as : wet. dry. ________%O2
(iii) Briefly describe the treatment/abatement and give a reference for details elsewhere
in this application. A clearly labelled process flow diagram for each abatement system should be included in Attachment No 12A.
(iv) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up /shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr
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TABLE E .1(ii) OTHER EMISSIONS TO ATMOSPHERE
Attach D.1.A: Table E.1 Page 44 of 104
TABLE 12A(ii) MAIN EMISSIONS TO ATMOSPHERE Emission Point: Emission Point Ref. No: TAB-32 HEPA Filter
Source of Emission: Dust Collector 910
Location : Roof of Tabletting Building
Grid Ref. (12 digit, 6E,6N): 178912E, 63057N
Vent Details
Diameter:
Height above Ground(m):
400 mm
26m above ground, at EL 39m A.O.D.
Date of commencement of
emission:
1999
Characteristics of Emission :
(i) Volume to be emitted:
Average/day 104,000 m3/d Maximum/day 104,000 m3/d
Maximum rate/hour 4,350 m3/h Min efflux velocity 6.1 m.sec-1
(ii) Other factors
Temperature oC(max) oC(min) 25oC(avg)
For Combustion Sources:
Volume terms expressed as : wet. dry. ________%O2
(iii) Briefly describe the treatment/abatement and give a reference for details elsewhere
in this application. A clearly labelled process flow diagram for each abatement system should be included in Attachment No 12A.
(iv) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up /shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr
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EPA Export 25-07-2013:20:19:16
TABLE E .1(ii) OTHER EMISSIONS TO ATMOSPHERE
Attach D.1.A: Table E.1 Page 45 of 104
Emission Point Ref. No: TAB-33 HEPA Filter
Source of Emission: Coater C-904
Location : Roof of Tabletting Building
Grid Ref. (12 digit, 6E,6N): 178872E, 63051N
Vent Details
Diameter:
Height above Ground(m):
400 mm
27m above ground, at EL 39m A.O.D.
Date of commencement of
emission:
1999
Characteristics of Emission :
(i) Volume to be emitted:
Average/day 180,000 m3/d Maximum/day 180,000 m3/d
Maximum rate/hour 7,500 m3/h Min efflux velocity 10.6 m.sec-1
(ii) Other factors
Temperature oC(max) oC(min) 50oC(avg)
For Combustion Sources:
Volume terms expressed as : wet. dry. ________%O2
(iii) Briefly describe the treatment/abatement and give a reference for details elsewhere
in this application. A clearly labelled process flow diagram for each abatement system should be included in Attachment No 12A.
(iv) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up /shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr
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EPA Export 25-07-2013:20:19:16
TABLE E .1(ii) OTHER EMISSIONS TO ATMOSPHERE
Attach D.1.A: Table E.1 Page 46 of 104
Emission Point Ref. No: TAB-34 HEPA Filter
Source of Emission: Tablet – Process Point
Location : Roof of Tabletting Building
Grid Ref. (12 digit, 6E,6N): 178826E, 63046N
Vent Details
Diameter:
Height above Ground(m):
400 mm
27m above ground, at EL 39m A.O.D.
Date of commencement of
emission:
1999
Characteristics of Emission :
(i) Volume to be emitted:
Average/day 156,000 m3/d Maximum/day 156,000 m3/d
Maximum rate/hour 6,500 m3/h Min efflux velocity 14.4 m.sec-1
(ii) Other factors
Temperature oC(max) oC(min) 50oC(avg)
For Combustion Sources:
Volume terms expressed as : wet. dry. ________%O2
(iii) Briefly describe the treatment/abatement and give a reference for details elsewhere
in this application. A clearly labelled process flow diagram for each abatement system should be included in Attachment No 12A.
(iv) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up /shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr
(v) Tables 12(iii) and 12(iv) should be completed as appropriate for each emission point
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EPA Export 25-07-2013:20:19:16
TABLE E .1(ii) OTHER EMISSIONS TO ATMOSPHERE
Attach D.1.A: Table E.1 Page 47 of 104
Emission Point Ref. No: TAB-35 HEPA Filter
Source of Emission: IBC Wash W901
Location : Roof of Tabletting Building
Grid Ref. (12 digit, 6E,6N): 178962E, 63063N
Vent Details
Diameter:
Height above Ground(m):
450 mm
22m above ground, at EL 39m A.O.D.
Date of commencement of
emission:
1999
Characteristics of Emission :
(i) Volume to be emitted:
Average/day 180,000 m3/d Maximum/day 180,000 m3/d
Maximum rate/hour 7,500 m3/h Min efflux velocity 10.6 m.sec-1
(ii) Other factors
Temperature oC(max) oC(min) 50 oC(avg)
For Combustion Sources:
Volume terms expressed as : wet. dry. ________%O2
(iii) Briefly describe the treatment/abatement and give a reference for details elsewhere
in this application. A clearly labelled process flow diagram for each abatement system should be included in Attachment No 12A.
(iv) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up /shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr
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EPA Export 25-07-2013:20:19:16
TABLE E .1(ii) OTHER EMISSIONS TO ATMOSPHERE
Attach D.1.A: Table E.1 Page 48 of 104
Emission Point Ref. No: TAB-36 HEPA Filter
Source of Emission: IBC Wash W902
Location : Roof of Tabletting Building
Grid Ref. (12 digit, 6E,6N): 178964E, 63063N
Vent Details
Diameter:
Height above Ground(m):
450 mm
22m above ground, at EL 39m A.O.D.
Date of commencement of
emission:
1999
Characteristics of Emission :
(i) Volume to be emitted:
Average/day 180,000 m3/d Maximum/day 180,000 m3/d
Maximum rate/hour 7,500 m3/h Min efflux velocity 10.6 m.sec-1
(ii) Other factors
Temperature oC(max) oC(min) 50oC(avg)
For Combustion Sources:
Volume terms expressed as : wet. dry. ________%O2
(iii) Briefly describe the treatment/abatement and give a reference for details elsewhere
in this application. A clearly labelled process flow diagram for each abatement system should be included in Attachment No 12A.
(iv) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up /shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr
(v) Tables 12(iii) and 12(iv) should be completed as appropriate for each emission point
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EPA Export 25-07-2013:20:19:16
TABLE E .1(ii) OTHER EMISSIONS TO ATMOSPHERE
Attach D.1.A: Table E.1 Page 49 of 104
Emission Point Ref. No: TAB-37 HEPA Filter
Source of Emission: Dust Collector
Location : Roof of Tabletting Building
Grid Ref. (12 digit, 6E,6N): 178818E, 63032N
Vent Details
Diameter:
Height above Ground(m):
500 mm
27m above ground, at EL 39m A.O.D.
Date of commencement of
emission:
1999
Characteristics of Emission :
(i) Volume to be emitted:
Average/day 104,000 m3/d Maximum/day 104,000 m3/d
Maximum rate/hour 4,350 m3/h Min efflux velocity 6.1 m.sec-1
(ii) Other factors
Temperature oC(max) oC(min) 25oC(avg)
For Combustion Sources:
Volume terms expressed as : wet. dry. ________%O2
(iii) Briefly describe the treatment/abatement and give a reference for details elsewhere
in this application. A clearly labelled process flow diagram for each abatement system should be included in Attachment No 12A.
(iv) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up /shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr
(v)
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EPA Export 25-07-2013:20:19:16
TABLE E .1(ii) OTHER EMISSIONS TO ATMOSPHERE
Attach D.1.A: Table E.1 Page 50 of 104
Emission Point Ref. No: TAB-38 HEPA Filter
Source of Emission: Central Vacuum DC Exhaust X949
Location : Roof of Tabletting Building
Grid Ref. (12 digit, 6E,6N): 178909E, 63054N
Vent Details
Diameter:
Height above Ground(m):
150 mm
26m above ground, at EL 39m A.O.D.
Date of commencement of
emission:
1999
Characteristics of Emission :
(i) Volume to be emitted:
Average/day 180,000 m3/d Maximum/day 180,000 m3/d
Maximum rate/hour 7,500 m3/h Min efflux velocity 10.6 m.sec-1
(ii) Other factors
Temperature oC(max) oC(min) 50 oC(avg)
For Combustion Sources:
Volume terms expressed as : wet. dry. ________%O2
(iii) Briefly describe the treatment/abatement and give a reference for details elsewhere
in this application. A clearly labelled process flow diagram for each abatement system should be included in Attachment No 12A.
(iv) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up /shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr
(v)
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TABLE E .1(ii) OTHER EMISSIONS TO ATMOSPHERE
Attach D.1.A: Table E.1 Page 51 of 104
Emission Point Ref. No: TAB-39 HEPA Filter
Source of Emission: Tablet – Process Point
Location : Roof of Tabletting Building
Grid Ref. (12 digit, 6E,6N): 178975E, 63094N
Vent Details
Diameter:
Height above Ground(m):
200 mm
27m above ground, at EL 39m A.O.D.
Date of commencement of
emission:
1999
Characteristics of Emission :
(i) Volume to be emitted:
Average/day 10,200 m3/d Maximum/day 10,200 m3/d
Maximum rate/hour 425 m3/h Min efflux velocity 3.8 m.sec-1
(ii) Other factors
Temperature oC(max) oC(min) 25oC(avg)
For Combustion Sources:
Volume terms expressed as : wet. dry. ________%O2
(iii) Briefly describe the treatment/abatement and give a reference for details elsewhere
in this application. A clearly labelled process flow diagram for each abatement system should be included in Attachment No 12A.
(iv) Period or periods during which emissions are made, or are to be made, including
daily or seasonal variations (start-up /shutdown to be included):
Periods of Emission (avg) 60 min/hr 24 hr/day 365 day/yr
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TABLE E.1(iii): MAIN EMISSIONS TO ATMOSPHERE -Chemical characteristics of the emission (1 table per emission point)
Attach D.1.A: Table E.1 Page 52 of 104
Emission Point Reference Number: CB1 - 01 Thermal Oxidiser
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
TA Luft
Class I Thermal 0 20 - - 0.6 - - 5,256
Class II
Class III
HCL
Oxidation followed by packed bed scrubbing
5.7
23.1
10
100
100
20
0.171
0.693
0.3
3.0
3.0
0.6
1,436
5,821
2,628
25,280
25,280
5,256
(See Note 2)
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be the same as given in Table 12A(ii) unless clearly stated otherwise. 2. Where organic substances of more than one Class are present, in addition to the above limit, the sum of Classes I & II shall not exceed the Class III limit and the sum of Class I, II, and III shall not exceed the Class III limit.
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TABLE E.1(iii): MAIN EMISSIONS TO ATMOSPHERE -Chemical characteristics of the emission (1 table per emission point)
Attach D.1.A: Table E.1 Page 53 of 104
Emission Point Reference Number: CB1 – 02 Carbon Absorber
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
TA Luft:
Class I 6 20 0.67 2.24 5,286 19,622
Class II Absorber 5.3 100 0.59 11.2 5,168 98,112
Class III
HCL
75.4
14.5
100
20
8.44
1.67
11.2
2.24
73,934
1,402
98,112
19,622
(See Note 2)
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be the same as given in Table 12A(ii) unless clearly stated otherwise. 2. Where organic substances of more than one Class are present, in addition to the above limit, the sum of Classes I & II shall not exceed the Class III limit and the sum of Class I, II, and III shall not exceed the Class III limit.
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EPA Export 25-07-2013:20:19:17
TABLE E.1(iii): MAIN EMISSIONS TO ATMOSPHERE -Chemical characteristics of the emission (1 table per emission point)
Attach D.1.A: Table E.1 Page 54 of 104
Emission Point Reference Number: CB1-03 Scrubber
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
TA Luft:
Class I
Class II
Scrubber
20
100
0.2
1.0
1,752
8,760
Class III 100 1.0 8,760
Ammonia 50 0.5 4,380
HCL 20 0.2 1,752
(See Note 2)
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be the same as given in Table 12A(ii) unless clearly stated otherwise. 2. Where organic substances of more than one Class are present, in addition to the above limit, the sum of Classes I & II shall not exceed the Class III limit and the sum of Class I, II, and III shall not exceed the Class III limit.
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TABLE E.1(iii): MAIN EMISSIONS TO ATMOSPHERE -Chemical characteristics of the emission (1 table per emission point)
Attach D.1.A: Table E.1 Page 55 of 104
Emission Point Reference Number: DR1 - 03 Scrubber
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
TA Luft:
Class I - - 20 - - 0.6 - - 5,256
Class II Scrubber 2 100 0.06 3.0 525.6 26,280
Class III 14.2 100 0.426 3.0 3732 26,280
Particulates 0.40 1 0.012 0.03 105 263
(See Note 2)
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be the same as given in Table 12A(ii) unless clearly stated otherwise. 2. Where organic substances of more than one Class are present, in addition to the above limit, the sum of Classes I & II shall not exceed the Class III limit and the sum of Class I, II, and III shall not exceed the Class III limit.
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TABLE E.1(iii): MAIN EMISSIONS TO ATMOSPHERE -Chemical characteristics of the emission (1 table per emission point)
Attach D.1.A: Table E.1 Page 56 of 104
Emission Point Reference Number: DR1 - 04 Scrubber
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
TA Luft:
Class I 1.8 20 0.108 1.2 946 10,512
Class II Scrubber - - 100 6.0 52,560
Class III - - 100 6.0 52,560
Particulates 0.2 1 0.012 0.06 105 526
(See Note 2)
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be the same as given in Table 12A(ii) unless clearly stated otherwise. 2. Where organic substances of more than one Class are present, in addition to the above limit, the sum of Classes I & II shall not exceed the Class III limit and the sum of Class I, II, and III shall not exceed the Class III limit.
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TABLE E.1(iii): MAIN EMISSIONS TO ATMOSPHERE -Chemical characteristics of the emission (1 table per emission point)
Attach D.1.A: Table E.1 Page 57 of 104
Emission Point Reference Number: CB2 - 01 Thermal Oxidiser
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
TA Luft:
Class I
Class II
Class III
Thermal Oxidation Followed by packed bed scrubbing
20
100
100
0.6
3.0
3.0
5,256
26,280
26,280
HCL 20 0.6 5,256
(See Note 2)
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be the same as given in Table 12A(ii) unless clearly stated otherwise. 2. Where organic substances of more than one Class are present, in addition to the above limit, the sum of Classes I & II shall not exceed the Class III limit and the sum of Class I, II, and III shall not exceed the Class III limit.
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TABLE E.1(iii): MAIN EMISSIONS TO ATMOSPHERE -Chemical characteristics of the emission (1 table per emission point)
Attach D.1.A: Table E.1 Page 58 of 104
Emission Point Reference Number: CB2 -18 Scrubber
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
TA Luft:
Class I
Class II
Scrubber
20
100
0.2
1.0
1,752
8,760
Class III 100 1.0 8,760
Ammonia 50 0.5 4,380
HCL 20 0.2 1,752
(See Note 2)
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be the same as given in Table 12A(ii) unless clearly stated otherwise. 2. Where organic substances of more than one Class are present, in addition to the above limit, the sum of Classes I & II shall not exceed the Class III limit and the sum of Class I, II, and III shall not exceed the Class III limit.
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TABLE E.1: OTHER EMISSIONS TO ATMOSPHERE - Chemical characteristics of the emission (1 table per emission point)
Attach D.1.A: Table E.1 Page 59 of 104
Emission Point Reference Number: TAB - 01 HEPA Filter from Dust Collector from Tablet Coating
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
Dust Fan pulls air through a HEPA Filter. Collection efficiency: 99.97% at 3 micron particle size
<0.028 <0.09 <0.002 <0.004 <17.5 <34
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be the same as given in Table 12A(ii) unless clearly stated otherwise. 2. Where organic substances of more than one Class are present, in addition to the above limit, the sum of Classes I & II shall not exceed the Class III limit and the sum of Class I, II, and III shall not exceed the Class III limit.
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TABLE E.1: OTHER EMISSIONS TO ATMOSPHERE - Chemical characteristics of the emission (1 table per emission point)
Attach D.1.A: Table E.1 Page 60 of 104
Emission Point Reference Number: TAB - 02 HEPA Filter from Dust Collector from Tablet Coating
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
Dust Fan pulls air through a HEPA Filter. Collection efficiency: 99.97% at 3 micron particle size
<0.028 <0.09 <0.002 <0.004 <17.5 <34
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be the same as given in Table 12A(ii) unless clearly stated otherwise. 2. Where organic substances of more than one Class are present, in addition to the above limit, the sum of Classes I & II shall not exceed the Class III limit and the sum of Class I, II, and III shall not exceed the Class III limit.
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TABLE E.1: OTHER EMISSIONS TO ATMOSPHERE - Chemical characteristics of the emission (1 table per emission point)
Attach D.1.A: Table E.1 Page 61 of 104
Emission Point Reference Number: TAB - 03 HEPA Filter from Sampling Room
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
Dust Fan pulls air through a HEPA Filter. Collection efficiency: 99.97% at 3 micron particle size
<0.0002 <0.09 <1X10-6 <0.0004 <9X10-3 <3.4
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be the same as given in Table 12A(ii) unless clearly stated otherwise. 2. Where organic substances of more than one Class are present, in addition to the above limit, the sum of Classes I & II shall not exceed the Class III limit and the sum of Class I, II, and III shall not exceed the Class III limit.
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TABLE E.1: OTHER EMISSIONS TO ATMOSPHERE - Chemical characteristics of the emission (1 table per emission point)
Attach D.1.A: Table E.1 Page 62 of 104
Emission Point Reference Number: TAB - 04 HEPA Filter from Solution Preparation Room
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
Dust Fan pulls air through a HEPA Filter. Collection efficiency: 99.97% at 3 micron particle size
<1.6X10-3 <0.09 <1X10-5 <0.001 <0.15 <14
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be the same as given in Table 12A(ii) unless clearly stated otherwise. 2. Where organic substances of more than one Class are present, in addition to the above limit, the sum of Classes I & II shall not exceed the Class III limit and the sum of Class I, II, and III shall not exceed the Class III limit.
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TABLE E.1: OTHER EMISSIONS TO ATMOSPHERE - Chemical characteristics of the emission (1 table per emission point)
Attach D.1.A: Table E.1 Page 63 of 104
Emission Point Reference Number: TAB – 05 Dust Collector from Weighing Booths
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
Dust Fan pulls air through a HEPA Filter. Collection efficiency: 99.97% at 3 micron particle size
<3.4X10-3 <0.09 <2.2X10-4 <0.007 <2 <61
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be the same as given in Table 12A(ii) unless clearly stated otherwise. 2. Where organic substances of more than one Class are present, in addition to the above limit, the sum of Classes I & II shall not exceed the Class III limit and the sum of Class I, II, and III shall not exceed the Class III limit.
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TABLE E.1: OTHER EMISSIONS TO ATMOSPHERE - Chemical characteristics of the emission (1 table per emission point)
Attach D.1.A: Table E.1 Page 64 of 104
Emission Point Reference Number: TAB - 06 HEPA Filter from Weighing Booth
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
Dust Fan pulls air through a HEPA Filter. Collection efficiency: 99.97% at 3 micron particle size
<2.4X10-3 <0.09 <8X10-5 <0.003 <0.77 <29
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be the same as given in Table 12A(ii) unless clearly stated otherwise. 2. Where organic substances of more than one Class are present, in addition to the above limit, the sum of Classes I & II shall not exceed the Class III limit and the sum of Class I, II, and III shall not exceed the Class III limit.
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TABLE E.1: OTHER EMISSIONS TO ATMOSPHERE - Chemical characteristics of the emission (1 table per emission point)
Attach D.1.A: Table E.1 Page 65 of 104
Emission Point Reference Number: TAB - 10 HEPA Filter from Tablet Coater Vent
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
Dust Fan pulls air through a HEPA Filter. Collection efficiency: 99.97% at 3 micron particle size
<0.008 <0.09 <5X10-4 <0.006 <4.38 <52
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be the same as given in Table 12A(ii) unless clearly stated otherwise. 2. Where organic substances of more than one Class are present, in addition to the above limit, the sum of Classes I & II shall not exceed the Class III limit and the sum of Class I, II, and III shall not exceed the Class III limit.
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TABLE E.1: OTHER EMISSIONS TO ATMOSPHERE - Chemical characteristics of the emission (1 table per emission point)
Attach D.1.A: Table E.1 Page 66 of 104
Emission Point Reference Number: TAB - 11 HEPA Filter from Tablet Coater Vent
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
Dust Fan pulls air through a HEPA Filter. Collection efficiency: 99.97% at 3 micron particle size
<0.008 <0.09 <5X10-4 <0.006 <4.38 <52
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be the same as given in Table 12A(ii) unless clearly stated otherwise. 2. Where organic substances of more than one Class are present, in addition to the above limit, the sum of Classes I & II shall not exceed the Class III limit and the sum of Class I, II, and III shall not exceed the Class III limit.
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TABLE E.1: OTHER EMISSIONS TO ATMOSPHERE - Chemical characteristics of the emission (1 table per emission point)
Attach D.1.A: Table E.1 Page 67 of 104
Emission Point Reference Number: TAB - 12 HEPA Filter form Tablet Coater Vent
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
Dust Fan pulls air through a HEPA Filter. Collection efficiency: 99.97% at 3 micron particle size
<0.008 <0.09 <5X10-4 <0.006 <4.38 <52
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be the same as given in Table 12A(ii) unless clearly stated otherwise. 2. Where organic substances of more than one Class are present, in addition to the above limit, the sum of Classes I & II shall not exceed the Class III limit and the sum of Class I, II, and III shall not exceed the Class III limit.
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TABLE E.1: OTHER EMISSIONS TO ATMOSPHERE - Chemical characteristics of the emission (1 table per emission point)
Attach D.1.A: Table E.1 Page 68 of 104
Emission Point Reference Number: TAB - 13 HEPA Filter from Tablet Coater Vent
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
Dust Fan pulls air through a HEPA Filter. Collection efficiency: 99.97% at 3 micron particle size
<0.008 <0.09 <5X10-4 <0.006 <4.38 <52
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be the same as given in Table 12A(ii) unless clearly stated otherwise. 2. Where organic substances of more than one Class are present, in addition to the above limit, the sum of Classes I & II shall not exceed the Class III limit and the sum of Class I, II, and III shall not exceed the Class III limit.
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TABLE E.1: OTHER EMISSIONS TO ATMOSPHERE - Chemical characteristics of the emission (1 table per emission point)
Attach D.1.A: Table E.1 Page 69 of 104
Emission Point Reference Number: TAB - 14 HEPA Filter from Tablet Coater Vent
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
Dust Fan pulls air through a HEPA Filter. Collection efficiency: 99.97% at 3 micron particle size
<0.008 <0.09 <5X10-4 <0.006 <4.38 <52
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be the same as given in Table 12A(ii) unless clearly stated otherwise. 2. Where organic substances of more than one Class are present, in addition to the above limit, the sum of Classes I & II shall not exceed the Class III limit and the sum of Class I, II, and III shall not exceed the Class III limit.
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TABLE E.1: OTHER EMISSIONS TO ATMOSPHERE - Chemical characteristics of the emission (1 table per emission point)
Attach D.1.A: Table E.1 Page 70 of 104
Emission Point Reference Number: TAB - 15 HEPA Filter from Fluid Bed Dryer
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
Dust Fan pulls air through a HEPA Filter. Collection efficiency: 99.97% at 3 micron particle size
<0.012 <0.09 <8X10-4 <0.006 <7 <51
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be the same as given in Table 12A(ii) unless clearly stated otherwise. 2. Where organic substances of more than one Class are present, in addition to the above limit, the sum of Classes I & II shall not exceed the Class III limit and the sum of Class I, II, and III shall not exceed the Class III limit.
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TABLE E.1: OTHER EMISSIONS TO ATMOSPHERE - Chemical characteristics of the emission (1 table per emission point)
Attach D.1.A: Table E.1 Page 71 of 104
Emission Point Reference Number: TAB - 16 HEPA Filter from Fluid Bed Dryer
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
Dust Fan pulls air through a HEPA Filter. Collection efficiency: 99.97% at 3 micron particle size
<0.012 <0.09 <8X10-4 <0.006 <7 <51
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be the same as given in Table 12A(ii) unless clearly stated otherwise. 2. Where organic substances of more than one Class are present, in addition to the above limit, the sum of Classes I & II shall not exceed the Class III limit and the sum of Class I, II, and III shall not exceed the Class III limit.
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TABLE E.1: OTHER EMISSIONS TO ATMOSPHERE - Chemical characteristics of the emission (1 table per emission point)
Attach D.1.A: Table E.1 Page 72 of 104
Emission Point Reference Number: TAB - 17 HEPA Filter from Fluid Bed Dryer
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
Dust Fan pulls air through a HEPA Filter. Collection efficiency: 99.97% at 3 micron particle size
<0.012 <0.09 <8X10-4 <0.006 <7 <51
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be the same as given in Table 12A(ii) unless clearly stated otherwise. 2. Where organic substances of more than one Class are present, in addition to the above limit, the sum of Classes I & II shall not exceed the Class III limit and the sum of Class I, II, and III shall not exceed the Class III limit.
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EPA Export 25-07-2013:20:19:18
TABLE E.1: OTHER EMISSIONS TO ATMOSPHERE - Chemical characteristics of the emission (1 table per emission point)
Attach D.1.A: Table E.1 Page 73 of 104
Emission Point Reference Number: TAB - 18 HEPA Filter from Fluid Bed Dryer
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
Dust Fan pulls air through a HEPA Filter. Collection efficiency: 99.97% at 3 micron particle size
0.012 <0.09 <8X10-4 <0.006 <7 <51
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be the same as given in Table 12A(ii) unless clearly stated otherwise. 2. Where organic substances of more than one Class are present, in addition to the above limit, the sum of Classes I & II shall not exceed the Class III limit and the sum of Class I, II, and III shall not exceed the Class III limit.
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TABLE E.1: OTHER EMISSIONS TO ATMOSPHERE - Chemical characteristics of the emission (1 table per emission point)
Attach D.1.A: Table E.1 Page 74 of 104
Emission Point Reference Number: TAB – 19 HEPA Filter from Dust Collector from Tablet Coating
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
Dust Fan pulls air through a HEPA Filter. Collection efficiency: 99.97% at 3 micron particle size
<0.028 <0.09 <0.002 <0.004 <17 <34
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be the same as given in Table 12A(ii) unless clearly stated otherwise. 2. Where organic substances of more than one Class are present, in addition to the above limit, the sum of Classes I & II shall not exceed the Class III limit and the sum of Class I, II, and III shall not exceed the Class III limit.
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TABLE E.1: OTHER EMISSIONS TO ATMOSPHERE - Chemical characteristics of the emission (1 table per emission point)
Attach D.1.A: Table E.1 Page 75 of 104
Emission Point Reference Number: TAB - 20 HEPA Filter from Tablet Coater
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
Dust Fan pulls air through a HEPA Filter. Collection efficiency: 99.97% at 3 micron particle size
<0.008 <0.09 <5X10-4 <0.006 <4.38 <52
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be the same as given in Table 12A(ii) unless clearly stated otherwise. 2. Where organic substances of more than one Class are present, in addition to the above limit, the sum of Classes I & II shall not exceed the Class III limit and the sum of Class I, II, and III shall not exceed the Class III limit.
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EPA Export 25-07-2013:20:19:18
TABLE E.1: OTHER EMISSIONS TO ATMOSPHERE - Chemical characteristics of the emission (1 table per emission point)
Attach D.1.A: Table E.1 Page 76 of 104
Emission Point Reference Number: TAB - 21 HEPA Filter from Fluid Bed Dryer
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
Dust Fan pulls air through a HEPA Filter. Collection efficiency: 99.97% at 3 micron particle size
<0.012 <0.09 <8X10-4 <0.006 <7 <51
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be the same as given in Table 12A(ii) unless clearly stated otherwise. 2. Where organic substances of more than one Class are present, in addition to the above limit, the sum of Classes I & II shall not exceed the Class III limit and the sum of Class I, II, and III shall not exceed the Class III limit.
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EPA Export 25-07-2013:20:19:18
TABLE E.1: OTHER EMISSIONS TO ATMOSPHERE - Chemical characteristics of the emission (1 table per emission point)
Attach D.1.A: Table E.1 Page 77 of 104
Emission Point Reference Number: TAB - 22 HEPA Filter from Dust Collector (proposed)
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
Dust Fan pulls air through a HEPA Filter. Collection efficiency: 99.97% at 3 micron particle size
<1.6X10-3 <0.09 <1X10-5 <0.001 <0.09 <14
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be the same as given in Table 12A(ii) unless clearly stated otherwise. 2. Where organic substances of more than one Class are present, in addition to the above limit, the sum of Classes I & II shall not exceed the Class III limit and the sum of Class I, II, and III shall not exceed the Class III limit.
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.
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EPA Export 25-07-2013:20:19:18
TABLE E.1: OTHER EMISSIONS TO ATMOSPHERE - Chemical characteristics of the emission (1 table per emission point)
Attach D.1.A: Table E.1 Page 78 of 104
Emission Point Reference Number: TAB - 23 HEPA Filter from Dust Collector (proposed)
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
Dust Fan pulls air through a HEPA Filter. Collection efficiency: 99.97% at 3 micron particle size
<3.4X10-3 <0.09 <2.2X10-4 <0.007 <1.7 <61
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be the same as given in Table 12A(ii) unless clearly stated otherwise. 2. Where organic substances of more than one Class are present, in addition to the above limit, the sum of Classes I & II shall not exceed the Class III limit and the sum of Class I, II, and III shall not exceed the Class III limit.
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.
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EPA Export 25-07-2013:20:19:18
TABLE E.1: OTHER EMISSIONS TO ATMOSPHERE - Chemical characteristics of the emission (1 table per emission point)
Attach D.1.A: Table E.1 Page 79 of 104
Emission Point Reference Number: TAB - 24 HEPA Filter from Dust Collector (proposed)
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
Dust Fan pulls air through a HEPA Filter. Collection efficiency: 99.97% at 3 micron particle size
2.4X10-3 <0.09 <7.6X10-5 <0.003 <0.61 <26
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be the same as given in Table 12A(ii) unless clearly stated otherwise. 2. Where organic substances of more than one Class are present, in addition to the above limit, the sum of Classes I & II shall not exceed the Class III limit and the sum of Class I, II, and III shall not exceed the Class III limit.
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.
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EPA Export 25-07-2013:20:19:18
TABLE E.1: OTHER EMISSIONS TO ATMOSPHERE - Chemical characteristics of the emission (1 table per emission point)
Attach D.1.A: Table E.1 Page 80 of 104
Emission Point Reference Number: TAB - 25 HEPA Filter from Tablet Coater Vent (proposed)
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
Dust Fan pulls air through a HEPA Filter. Collection efficiency: 99.97% at 3 micron particle size
<0.008 <0.09 <5X10-4 <0.006 <4.38 <52
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be the same as given in Table 12A(ii) unless clearly stated otherwise. 2. Where organic substances of more than one Class are present, in addition to the above limit, the sum of Classes I & II shall not exceed the Class III limit and the sum of Class I, II, and III shall not exceed the Class III limit.
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.
Conse
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EPA Export 25-07-2013:20:19:18
TABLE E.1: OTHER EMISSIONS TO ATMOSPHERE - Chemical characteristics of the emission (1 table per emission point)
Attach D.1.A: Table E.1 Page 81 of 104
Emission Point Reference Number: TAB - 26 HEPA Filter from Tablet Coater Vent (proposed)
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
Dust Fan pulls air through a HEPA Filter. Collection efficiency: 99.97% at 3 micron particle size
<0.008 <0.09 <5X10-4 <0.006 <4.38 <52
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be the same as given in Table 12A(ii) unless clearly stated otherwise. 2. Where organic substances of more than one Class are present, in addition to the above limit, the sum of Classes I & II shall not exceed the Class III limit and the sum of Class I, II, and III shall not exceed the Class III limit.
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.
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EPA Export 25-07-2013:20:19:18
TABLE E.1: OTHER EMISSIONS TO ATMOSPHERE - Chemical characteristics of the emission (1 table per emission point)
Attach D.1.A: Table E.1 Page 82 of 104
Emission Point Reference Number: TAB - 27 HEPA Filter from Fluid Bed Dryer (proposed)
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
Dust Fan pulls air through a HEPA Filter. Collection efficiency: 99.97% at 3 micron particle size
<0.012 <0.09 <8X10-4 <0.006 <7 <51
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be the same as given in Table 12A(ii) unless clearly stated otherwise. 2. Where organic substances of more than one Class are present, in addition to the above limit, the sum of Classes I & II shall not exceed the Class III limit and the sum of Class I, II, and III shall not exceed the Class III limit.
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.
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EPA Export 25-07-2013:20:19:18
TABLE E.1: OTHER EMISSIONS TO ATMOSPHERE - Chemical characteristics of the emission (1 table per emission point)
Attach D.1.A: Table E.1 Page 83 of 104
Emission Point Reference Number: TAB - 28 HEPA Filter from Dust Collector (proposed)
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
Dust Fan pulls air through a HEPA Filter. Collection efficiency: 99.97% at 3 micron particle size
<0.028 <0.09 <0.002 <0.004 <17 <34
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be the same as given in Table 12A(ii) unless clearly stated otherwise. 2. Where organic substances of more than one Class are present, in addition to the above limit, the sum of Classes I & II shall not exceed the Class III limit and the sum of Class I, II, and III shall not exceed the Class III limit.
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.
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EPA Export 25-07-2013:20:19:18
TABLE E.1: OTHER EMISSIONS TO ATMOSPHERE - Chemical characteristics of the emission (1 table per emission point)
Attach D.1.A: Table E.1 Page 84 of 104
Emission Point Reference Number: TAB - 29 HEPA Filter from Fluid Bed Dryer (proposed)
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
Dust Fan pulls air through a HEPA Filter. Collection efficiency: 99.97% at 3 micron particle size
<0.012 <0.09 <8X10-45 <0.006 <7 <51
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be the same as given in Table 12A(ii) unless clearly stated otherwise. 2. Where organic substances of more than one Class are present, in addition to the above limit, the sum of Classes I & II shall not exceed the Class III limit and the sum of Class I, II, and III shall not exceed the Class III limit.
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.
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EPA Export 25-07-2013:20:19:18
TABLE E.1: OTHER EMISSIONS TO ATMOSPHERE - Chemical characteristics of the emission (1 table per emission point)
Attach D.1.A: Table E.1 Page 85 of 104
Emission Point Reference Number: TAB - 30 HEPA Filter from Tablet Coater Vent (proposed)
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
Dust Fan pulls air through a HEPA Filter. Collection efficiency: 99.97% at 3 micron particle size
<0.008 <0.09 <5X10-4 <0.006 <438 <52
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be the same as given in Table 12A(ii) unless clearly stated otherwise. 2. Where organic substances of more than one Class are present, in addition to the above limit, the sum of Classes I & II shall not exceed the Class III limit and the sum of Class I, II, and III shall not exceed the Class III limit.
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.
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EPA Export 25-07-2013:20:19:18
TABLE E.1: OTHER EMISSIONS TO ATMOSPHERE - Chemical characteristics of the emission (1 table per emission point)
Attach D.1.A: Table E.1 Page 86 of 104
Emission Point Reference Number: TAB - 31 HEPA Filter from Fluid Bed Dryer (proposed)
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
Dust Fan pulls air through a HEPA Filter. Collection efficiency: 99.97% at 3 micron particle size
<0.012 <0.09 <8X10-4 <0.006 <7 <51
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be the same as given in Table 12A(ii) unless clearly stated otherwise. 2. Where organic substances of more than one Class are present, in addition to the above limit, the sum of Classes I & II shall not exceed the Class III limit and the sum of Class I, II, and III shall not exceed the Class III limit.
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.
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EPA Export 25-07-2013:20:19:18
TABLE E.1: OTHER EMISSIONS TO ATMOSPHERE - Chemical characteristics of the emission (1 table per emission point)
Attach D.1.A: Table E.1 Page 87 of 104
TABLE 12A(iii): MAIN EMISSIONS TO ATMOSPHERE - Chemical characteristics of the emission Emission Point Reference Number: TAB - 32 HEPA Filter from Dust Collector (proposed)
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
Dust Fan pulls air through a HEPA Filter. Collection efficiency: 99.97% at 3 micron particle size
<0.028 <0.09 <0.002 <0.004 <17 <34
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be the same as given in Table 12A(ii) unless clearly stated otherwise. 2. Where organic substances of more than one Class are present, in addition to the above limit, the sum of Classes I & II shall not exceed the Class III limit and the sum of Class I, II, and III shall not exceed the Class III limit.
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.
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EPA Export 25-07-2013:20:19:18
TABLE E.1: OTHER EMISSIONS TO ATMOSPHERE - Chemical characteristics of the emission (1 table per emission point)
Attach D.1.A: Table E.1 Page 88 of 104
Emission Point Reference Number: TAB - 33 HEPA Filter from Tablet Coater (proposed)
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
Dust Fan pulls air through a HEPA Filter. Collection efficiency: 99.97% at 3 micron particle size
<0.008 <0.09 <5X10-4 <0.006 <4.38 <52
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be the same as given in Table 12A(ii) unless clearly stated otherwise. 2. Where organic substances of more than one Class are present, in addition to the above limit, the sum of Classes I & II shall not exceed the Class III limit and the sum of Class I, II, and III shall not exceed the Class III limit.
For
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.
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EPA Export 25-07-2013:20:19:18
TABLE E.1: OTHER EMISSIONS TO ATMOSPHERE - Chemical characteristics of the emission (1 table per emission point)
Attach D.1.A: Table E.1 Page 89 of 104
Emission Point Reference Number: TAB - 34 HEPA Filter from Fluid Bed Dryer (proposed)
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
Dust Fan pulls air through a HEPA Filter. Collection efficiency: 99.97% at 3 micron particle size
<0.012 <0.09 <8X10-4 <0.006 <7 <51
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be the same as given in Table 12A(ii) unless clearly stated otherwise. 2. Where organic substances of more than one Class are present, in addition to the above limit, the sum of Classes I & II shall not exceed the Class III limit and the sum of Class I, II, and III shall not exceed the Class III limit.
For
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.
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EPA Export 25-07-2013:20:19:18
TABLE E.1: OTHER EMISSIONS TO ATMOSPHERE - Chemical characteristics of the emission (1 table per emission point)
Attach D.1.A: Table E.1 Page 90 of 104
Emission Point Reference Number: TAB - 35 HEPA Filter from Fluid Bed Dryer (proposed)
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
Dust Fan pulls air through a HEPA Filter. Collection efficiency: 99.97% at 3 micron particle size
<0.012 <0.09 <8X10-4 <0.006 <7 <51
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be the same as given in Table 12A(ii) unless clearly stated otherwise. 2. Where organic substances of more than one Class are present, in addition to the above limit, the sum of Classes I & II shall not exceed the Class III limit and the sum of Class I, II, and III shall not exceed the Class III limit.
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.
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EPA Export 25-07-2013:20:19:19
TABLE E.1: OTHER EMISSIONS TO ATMOSPHERE - Chemical characteristics of the emission (1 table per emission point)
Attach D.1.A: Table E.1 Page 91 of 104
Emission Point Reference Number: TAB - 36 HEPA Filter from Tablet Coater Vent (proposed)
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
Dust Fan pulls air through a HEPA Filter. Collection efficiency: 99.97% at 3 micron particle size
<0.008 0.09 <5X10-4 <0.006 <4.38 <52
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be the same as given in Table 12A(ii) unless clearly stated otherwise. 2. Where organic substances of more than one Class are present, in addition to the above limit, the sum of Classes I & II shall not exceed the Class III limit and the sum of Class I, II, and III shall not exceed the Class III limit.
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.
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EPA Export 25-07-2013:20:19:19
TABLE E.1: OTHER EMISSIONS TO ATMOSPHERE - Chemical characteristics of the emission (1 table per emission point)
Attach D.1.A: Table E.1 Page 92 of 104
Emission Point Reference Number: TAB - 37 HEPA Filter from Dust Collector (proposed)
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
Dust Fan pulls air through a HEPA Filter. Collection efficiency: 99.97% at 3 micron particle size
<0.028 <0.09 <0.002 <0.004 <17 <34
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be the same as given in Table 12A(ii) unless clearly stated otherwise. 2. Where organic substances of more than one Class are present, in addition to the above limit, the sum of Classes I & II shall not exceed the Class III limit and the sum of Class I, II, and III shall not exceed the Class III limit.
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.
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EPA Export 25-07-2013:20:19:19
TABLE E.1: OTHER EMISSIONS TO ATMOSPHERE - Chemical characteristics of the emission (1 table per emission point)
Attach D.1.A: Table E.1 Page 93 of 104
Emission Point Reference Number: TAB - 38 HEPA Filter from Tablet Coater (proposed)
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
Dust Fan pulls air through a HEPA Filter. Collection efficiency: 99.97% at 3 micron particle size
<0.008 <0.09 <5X10-4 <0.006 <4.38 <52
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be the same as given in Table 12A(ii) unless clearly stated otherwise. 2. Where organic substances of more than one Class are present, in addition to the above limit, the sum of Classes I & II shall not exceed the Class III limit and the sum of Class I, II, and III shall not exceed the Class III limit.
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.
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EPA Export 25-07-2013:20:19:19
TABLE E.1: OTHER EMISSIONS TO ATMOSPHERE - Chemical characteristics of the emission (1 table per emission point)
Attach D.1.A: Table E.1 Page 94 of 104
Emission Point Reference Number: TAB - 39 HEPA Filter from Dust Collector (proposed)
Parameter Prior to treatment(1) Brief As discharged(1)
mg/Nm3 kg/h description mg/Nm3 kg/h. kg/year
Avg Max Avg Max of treatment Avg Max Avg Max Avg Max
Dust Fan pulls air through a HEPA Filter. Collection efficiency: 99.97% at 3 micron particle size
0.0002 <0.09 <1X10-6 <0.0004 <9X10-3 <3.4
1. Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be the same as given in Table 12A(ii) unless clearly stated otherwise. 2. Where organic substances of more than one Class are present, in addition to the above limit, the sum of Classes I & II shall not exceed the Class III limit and the sum of Class I, II, and III shall not exceed the Class III limit.
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EPA Export 25-07-2013:20:19:19
TABLE E.1(iv): EMISSIONS TO ATMOSPHERE - Minor atmospheric emissions Note: Air handling units, HVAC vents and other minor emissions which have no significant impact on emissions to atmosphere at outlined in SI 394 have not been included.
Attach D.1.A: Table E.1 Page 95 of 104
Emission point Description Emission details1 Abatement system
employed
Reference Numbers material mg/Nm3(2) kg/h. kg/year
Minor Emissions from CB1 Vent No. 20 Vent No. 22 Vent No. 24 Vent No. 28 Vent No. 30 Vent No. 39 Vent No. 40 Vent No. 42
Charge Booth 01-22-1500 Charge Booth 01-92-1715 Charge Booth 01-04-1600 Charge Booth 01-103-1600 Charge Booth 01-16-1500 Hydrogenation Vent Tk 01-103-1000 Hydrogenation Vent Tk 01-105-1000 Hydrogenation Vent Re 01-33-1000
Trace organic solvents/ pharmaceutical dusts Trace organic solvents/ pharmaceutical dusts Hydrochloric Acid Trace organic solvents/ pharmaceutical dusts Trace organic solvents/ pharmaceutical dusts H2/ trace organic solvents H2/ trace organic solvents H2/ trace organic solvents
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible Negligible Negligible Negligible Negligible Negligible Negligible Negligible
Negligible Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
HEPA Filter HEPA Filter HEPA Filter HEPA Filter HEPA Filter Flame Arrestor Flame Arrestor Flame Arrestor
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EPA Export 25-07-2013:20:19:19
TABLE E.1(iv): EMISSIONS TO ATMOSPHERE - Minor atmospheric emissions Note: Air handling units, HVAC vents and other minor emissions which have no significant impact on emissions to atmosphere at outlined in SI 394 have not been included.
Attach D.1.A: Table E.1 Page 96 of 104
Emission point
Reference Numbers
Description Emission details1 Abatement system employed
material mg/Nm3(2) kg/h. kg/year Vent No. 45 Vent No. 47 Vent No. 48 Vent No. 66 Vent No. 74 Vent No. 76 Vent No. 77 Vent No. 78 Vent No. 81
Hydrogenation Vent Re 01-36-1000 Hydrogenation Vent Re 01-38-1000 Hydrogenation Vent Re 301-37-1000 Hydrogenation Vent Tk 01-36-2500 Charge Booth 01-103-1500 Charge Booth 01-92-1915 Hydrogenation Vent Re 01-31-1000 Hydrogenation Vent Tk 01-92-1800 Charge booth 01-07-1600
H2/ trace organic solvents H2/ trace organic solvents H2/ trace organic solvents H2/ trace organic solvents Trace organic solvents/ pharmaceutical dusts Trace organic solvents/ pharmaceutical dusts H2/ trace organic solvents H2/ trace organic solvents Trace organic solvents/ pharmaceutical dusts
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible Negligible Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Flame Arrestor Flame Arrestor Flame Arrestor Flame Arrestor HEPA Filter HEPA Filter Flame Arrestor Flame Arrestor HEPA Filter
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EPA Export 25-07-2013:20:19:19
TABLE E.1(iv): EMISSIONS TO ATMOSPHERE - Minor atmospheric emissions Note: Air handling units, HVAC vents and other minor emissions which have no significant impact on emissions to atmosphere at outlined in SI 394 have not been included.
Attach D.1.A: Table E.1 Page 97 of 104
Emission point
Reference Numbers
Description Emission details1 Abatement system employed
material mg/Nm3(2) kg/h. kg/year Vent No. 82 Vent No. 83 Vent No. 96 Vent No. 612 Vent No. 613
Charge booth 0128-1500 Charge booth 01-08-1500 Charge booth 01-65-1500 Tk 01-102-1000 Tk 01-101-1000
solvents/ pharmaceutical dusts Trace organic solvents/ pharmaceutical dusts Trace organic solvents/ pharmaceutical dusts Trace organic solvents Trace organic solvents
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible Negligible Negligible Negligible Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
HEPA Filter HEPA Filter HEPA Filter Conservation Vent Conservation Vent
1 The maximum emission should be stated for each material emitted, the concentration should be based on the maximum 30 minute mean. 2 Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be clearly stated. Include
reference oxygen conditions for combustion sources. 3 3. For empty tanks the worst case solvent emission is for Methylene dichloride which has a vapour density of 1.2 mg/Nm3 and a mass vent rate of 5.77
kg/day at 15oC.
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EPA Export 25-07-2013:20:19:19
TABLE E.1(iv): EMISSIONS TO ATMOSPHERE - Minor atmospheric emissions Note: Air handling units, HVAC vents and other minor emissions which have no significant impact on emissions to atmosphere at outlined in SI 394 have not been included.
Attach D.1.A: Table E.1 Page 98 of 104
Emission point
Reference Numbers
Description Emission details1 Abatement system employed
material mg/Nm3(2) kg/h. kg/year
Minor Emissions from CB2 Vent No. 203 Vent No. 219
Hydrogenation Vent Re 02-20-1000 Fume extraction system
H2/ trace organic solvents Trace organic solvents/ pharmaceutical dusts
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Flame Arrestor HEPA Filter
Emission point
Reference Numbers
Description Emission details1 Abatement system employed
material mg/Nm3(2) kg/h. kg/year
Minor Emissions from SDD Building Vent No. 1001
Fume and dust extraction system
Pharmaceutical dusts/trace organic solvents
Negligible
Negligible
Negligible
HEPA Filter
1 The maximum emission should be stated for each material emitted, the concentration should be based on the maximum 30 minute mean.
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TABLE E.1(iv): EMISSIONS TO ATMOSPHERE - Minor atmospheric emissions Note: Air handling units, HVAC vents and other minor emissions which have no significant impact on emissions to atmosphere at outlined in SI 394 have not been included.
Attach D.1.A: Table E.1 Page 99 of 104
2 Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be clearly stated. Include reference oxygen conditions for combustion sources.
3. For empty tanks the worst case solvent emission is for Methylene dichloride which has a vapour density of 1.2 Kg/Nm3 and a mass vent rate of 5.77 kg/day at 15oC
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TABLE E.1(iv): EMISSIONS TO ATMOSPHERE - Minor atmospheric emissions Note: Air handling units, HVAC vents and other minor emissions which have no significant impact on emissions to atmosphere at outlined in SI 394 have not been included.
Attach D.1.A: Table E.1 Page 100 of 104
Emission point
Reference Numbers
Description Emission details1 Abatement system employed
material mg/Nm3(2) kg/h. kg/year
Minor Emissions from QA Sampling Area
Vent No. 416 Vent No. 417
Warehouse sampling booth Warehouse sampling booth
Trace organic solvents/ pharmaceutical dusts Trace organic solvents/ pharmaceutical dusts
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
HEPA Filter HEPA FIlter
1 The maximum emission should be stated for each material emitted, the concentration should be based on the maximum 30 minute mean. 2 Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be clearly stated. Include
reference oxygen conditions for combustion sources. 3. For empty tanks the worst case solvent emission is for Methylene dichloride which has a vapour density of 1.2 Kg/Nm3 and a mass vent rate of 5.77 kg/day at 15oC
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TABLE E.1(iv): EMISSIONS TO ATMOSPHERE - Minor atmospheric emissions Note: Air handling units, HVAC vents and other minor emissions which have no significant impact on emissions to atmosphere at outlined in SI 394 have not been included.
Attach D.1.A: Table E.1 Page 101 of 104
Emission point
Reference Numbers
Description Emission details1 Abatement system employed
material mg/Nm3(2) kg/h. kg/year
Minor Emissions from Engineering Building
Vent No. 1101 Vent No. 1102
Diesel generator exhaust Diesel generator exhaust
Combustion gasses Combustion gasses
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
None None
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TABLE E.1(iv): EMISSIONS TO ATMOSPHERE - Minor atmospheric emissions Note: Air handling units, HVAC vents and other minor emissions which have no significant impact on emissions to atmosphere at outlined in SI 394 have not been included.
Attach D.1.A: Table E.1 Page 102 of 104
Emission point
Reference Numbers
Description Emission details1 Abatement system employed
material mg/Nm3(2) kg/h. kg/year
Minor Emissions from Laboratories
Vent No. 3104
Vent No. 3105
Vent No. 3106
Vent No. 3107
Vent No. 3108
Vent No. 3109
Vent No. 3110
Vent No. 3111
Vent No. 3112
Vent No. 3113
Vent No. 3114
Vent No. 3115
Laboratory Fume Hood
Laboratory Fume Hood
Laboratory Fume Hood
Laboratory Fume Hood
Laboratory Fume Hood
Laboratory Fume Hood
Laboratory Fume Hood
Laboratory Fume Hood
Laboratory Fume Hood
Laboratory Fume Hood
Laboratory Fume Hood
Laboratory Fume Hood
Trace organic solvents
Trace organic solvents
Trace organic solvents
Trace organic solvents
Trace organic solvents
Trace organic solvents
Trace organic solvents
Trace organic solvents
Trace organic solvents
Trace organic solvents
Trace organic solvents
Trace organic solvents
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligibl
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
None
None
None
None
None
None
None
None
None
None
None
None
1 The maximum emission should be stated for each material emitted, the concentration should be based on the maximum 30 minute mean. 2 Concentrations should be based on Normal conditions of temperature and pressure, (i.e. 0oC101.3kPa). Wet/dry should be clearly stated. Include
reference oxygen conditions for combustion sources.
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TABLE E.1(iv): EMISSIONS TO ATMOSPHERE - Minor atmospheric emissions Note: Air handling units, HVAC vents and other minor emissions which have no significant impact on emissions to atmosphere at outlined in SI 394 have not been included.
Attach D.1.A: Table E.1 Page 103 of 104
Emission point
Reference Numbers
Description Emission details1 Abatement system employed
material mg/Nm3(2) kg/h. kg/year
Minor Emissions from Laboratories
Vent No. 3116
Vent No. 3117
Vent No. 3118
Vent No. 3119
Vent No. 3120
Vent No. 3121
Vent No. 3122
Vent No. 1210
Vent No. 1211
Laboratory Fume Hood
Laboratory Fume Hood
Laboratory Fume Hood
Laboratory Fume Hood
QC/tech sves lab emissions
QC/tech sves lab emissions
QC/tech sves lab emissions
Laboratory Fume Hood
Laboratory Fume Hood
Trace organic solvents
Trace organic solvents
Trace organic solvents
Trace organic solvents
Trace organic solvents
Trace organic solvents
Trace organic solvents
Trace organic solvents
Trace organic solvents
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
Negligible
None
None
None
None
None
None
None
None
None
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TABLE E.1(v): EMISSIONS TO ATMOSPHERE - Potential atmospheric emissions
Attach D.1.A: Table E.1 Page 104 of 104
Emission point Reference Numbers
Description Malfunction which could cause an emission
Emission details (Potential max. emissions)1
material mg/Nm3 kg/hour
Vent No. 16
Vent No. 17
Vent No. 23
Vent No. 44
Vent No. 46
Vent No. 53
Vent No. 61
Vent No. 72
Vent No. 75
Vent No. 303
Vent No. 304
Vent No. 1324
Vent No. 1325
Vent No. 1328
Vent No. 1329
Vent No. 1330
Vent No. 1332
Vent No. 1334
Vent No. 1012
Rupture Disc Reactor RE-01-22-1000
Rupture Disc Reactor RE-01-23-1000
Rupture Disc Reactor RE-01-04-1000
Rupture Disc Plough Filter PF 01-67-1000
Rupture Disc Plough Filter PF 01-66-1000
Rupture Disc Reactor RE-01-47-1000
Rupture Disc Reactor RE-01-40-2000
Rupture Disc Reactor RE-01-05-1000
Rupture Disc Reactor RE-01-92-1900
Rupture Disc Vara unit TK 01-74-2000
Rupture Disc Vara unit TK 01-74-1000
Ammonia pressure relief valve
Ammonia pressure relief valve
Ammonia pressure relief valve
Ammonia pressure relief valve
Ammonia pressure relief valve
Ammonia pressure relief valve
Ammonia pressure relief valve
Relief vent SDD catch tank
Pressure rise under abnormal conditions
Pressure rise under abnormal conditions
Pressure rise under abnormal conditions
Pressure rise under abnormal conditions
Pressure rise under abnormal conditions
Pressure rise under abnormal conditions
Pressure rise under abnormal conditions
Pressure rise under abnormal conditions
Pressure rise under abnormal conditions
Pressure rise under abnormal conditions
Pressure rise under abnormal conditions
Pressure rise under abnormal conditions
Pressure rise under abnormal conditions
Pressure rise under abnormal conditions
Pressure rise under abnormal conditions
Pressure rise under abnormal conditions
Pressure rise under abnormal conditions
Pressure rise under abnormal conditions
Pressure rise under abnormal conditions
Solvent & Product Mixture
Solvent & Product Mixture
Solvent & Product Mixture
Solvent & Product Mixture
Solvent & Product Mixture
Solvent & Product Mixture
Solvent & Product Mixture
Solvent & Product Mixture
Solvent & Product Mixture
Solvent & Product Mixture
Solvent & Product Mixture
Ammonia
Ammonia
Ammonia
Ammonia
Ammonia
Ammonia
Ammonia
Trace organic solvents
N/A
N/A
N/A
N/A
N/A
N/A
N/A
N/A
N/A
N/A
N/A
N/A
N/A
N/A
N/A
N/A
N/A
N/A
N/A
30,000
30.000
30,000
30,000
30,000
30,000
30,000
30,000
30,000
3,000
3,000
1000
1000
1000
1000
1000
1000
1000
5000
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Review of current noise monitoring programme
Attach D.5.A.1: Noise summary report Page 1 of 1
SUMMARY OF NOISE SURVEY RESULTS
The noise survey report for 2006 is detailed in Table 1. The specific noise level, compared with the previous surveys is presented in Table 2. This indicates that there has been no detectable systematic change in plant emissions over this period.
Position D Time Measured Noise Level dB(A) Comments
LAeq LA90 LA10 Specific
14:00 46 43 47 43
14:15 50 44 49 44
14:33 48 46 49 46
14:50 49 47 50 47
15:05 48 46 50 46
15:21 50 46 52 46
15:37 49 45 52 45
15:58 51 46 54 46
Loughbeg 23rd July 2006
Mean Specific Plant Noise 45
Steady plant noise audible. Waves, aircraft, seacraft, some noise from Pfizer audible-trucks, etc.
Table 1. Results of Noise Survey 23rd June 2006 at Pfizer Ireland Pharmaceuticals,
Loughbeg.
Measured Specific Noise Level dB(A) Year 1999 2000 2001 2002 2003 2004 2005 2006
Specific Noise Level on beach 48 45-51 44-48 46 45 46-47 47 45
Table 2. Comparison of measured levels, 1999-2006.
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Review of Groundwater monitoring and extraction programme on the Loughbeg API facility.
Attach D.4.A.1 Page 1 of 2
In June/July 1991 six monitoring wells (MW-1 to MW-6) were installed around the site. In November 1991 a remediation proposal was put to Cork County Council and this was accepted. It involved the installation of six abstraction wells, EW-1 to EW-6. An additional seventh well (EW-7) was also installed in February 1992 with along with two more abstraction wells, EW-8 and EW-9 in 1995. Today there are four wells active, two monitoring wells (MW-2 and MW-5) and two extraction wells (EW-2 and EW-4). The activity was reduced in 1997 due a significant improvement on groundwater data; this was detailed by URS (formerly Dames & Moore) and accepted by the Environmental Protection Agency as detailed in IPC licence P0010-03. Groundwater Results Groundwater results for the site are summarised by sub-dividing them into two groups, as follows:
• Eastern Groundwater Area (MW-2,EW-2 and EW-4) • Western Groundwater Area (MW-5)
Eastern Groundwater Area The results from the biannual testing of EW-2 and MW-2 from 1997 have continued to show the presence of only trace levels of organic solvents. Overall these results reflect a progressive and sustained decrease of contaminants to the trace levels observed today.
Quality of Groundwater Wells (EW2,MW2,MW5) Main Containment Component versus its acceptable Dutch Interventation Level
0
50
100
150
200
250
300
350
2000 2001 2002 2003 2004 2005 2006
Year
Con
c of
Chl
orob
enze
ne (m
g/l) Dutch Intervention Limit for Chlorobenzene
EW2
MW2
MW5
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Review of Groundwater monitoring and extraction programme on the Loughbeg API facility.
Attach D.4.A.1 Page 2 of 2
In the same period, Chlorobenzene concentrations greater than the Dutch Intervention Values has been detected in EW4 during the biannual testing. Chlorobenzene has not been used at the Loughbeg site since 1993, its presence in the groundwater is related to historical sources. This has been detailed in a report issued by URS entitled “Chlorobenzene in EW4-Loughbeg site”. The fluctuation in these concentration levels may be related to the time the samples have been collected. During winter, with a higher water table and increased groundwater flow, the concentration levels are observed to be lower. Water from this well is extracted and treated in the WWTP. Analysis of the discharge from the WWTP shows that the parameters are well below the Dutch Intervention Values. Western Groundwater Area The results to date have shown that the residual levels of organic solvents in the groundwater have become very low, well below the Dutch Intervention Values. This well can be considered uncontaminated with the residual levels posing no risk to the environment. Conclusion: On the basis of above information it is proposed that EW-2, MW-2 and MW-5 be decommissioned. Extraction from EW-4 will continue to the continued presence on contaminants in the area.
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D.6 Environmental Consideration and BAT
Attachment D.6.A Pfizer Loughebg API Page 1 of 3
Year Project Title Result
2001/2002
Introduction of the ATL B
process to CB 2 • a reduction in use of sponge nickel catalyst
from 0.2 kg catalyst to 0.09 kg catalyst per kg
of product,
• a reduction in the number of solvents used,
• a reduction in the volume of aqueous waste
from 38 kg to 26 kg per kg of product,
• a reduction in solvent waste from 61 kg per
batch of product to 39 kg per batch of
product.
• a reduction in ammonia use from 1kg
ammonia to 2.5 kg product to 1 kg ammonia
to 14 kg product. 2002/2003
Improve the yield in ATL-B
from 67.5% to 70% thereby
Reduction in the number of batches and volume of
solvent required.
2002/2003
Reduction in the quantity of
TEB in the TBIN process by
75%
Reduction from 168kg per batch to 42kg per batch.
2002/2003
Improve the yield in TBIN
from 68.5% to 69.5% Reduction in the number of batches and the volume of
solvent required
2002/2003
Reduction in the number of
fibre kegs (from 4500 to 1400
per annum) used in the DKT
process
Replacing with 375 No. reusable (up to four times)
mausers
2002/2003
Installation of a weighbridge
on site Improved recording of waste materials and product
leaving the site.
2002/2003
Increase the ATL- A batch
size by 10%
Increase from a 300kg TBIN charge to a 330kg TBIN
charge.
2003/2004
Develop a new improved
synthetic route to ATL
allowing for a reduction in the
volume of toluene required
per batch
Reduction of toluene from 15540L to 11000L with an
equivalent reduction in waste solvent generated.
2003/2004 Introduction of the ATL- B
process to CB 1 • a reduction in use of sponge nickel catalyst
from 0.2 kg catalyst to 0.09 kg catalyst per kg
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D.6 Environmental Consideration and BAT
Attachment D.6.A Pfizer Loughebg API Page 2 of 3
of product,
• a reduction in the number of solvents used,
• a reduction in the volume of aqueous waste
from 38 kg to 26 kg per kg of product
• a reduction in solvent waste from 61 kg per
batch of product to 39 kg per batch of product.
• a reduction in ammonia use from 1kg
ammonia to 2.5 kg product to 1 kg ammonia
to 14 kg product.
2003/2004 Reduction in MTBE usage in
the ATL- B process Reduction from 6449kg to 5998kg per batch
2003/2004 Increase the TBIN charge in
the ATL B process from
460kg to 485 kg per batch.
Reduction in the THF charge from 1.3L per kg TBIN to
1.2L per kg TBIN, MTBE reduction of 2.4L per kg
TBIN to 2.3L per kg TBIN 2003/2004 Re route the utility effluent
from surface water drainage
system to the wastewater
treatment plant
2003/2004 Reduction in the filter use on
water purification systems
2003/2004 Upgrade the chemical dosing
and control system in the
wastewater treatment plant
allowing for
Increase reliability and reduction in material usage.
2003/2004 Reduction in potential
ammonia losses (100kg
ammonia per year) from the
utilities low temperature
refrigeration systems
Reduction in material usage
2005
Introduction of ATL- C to
CB1 thereby reducing the
quantity of THF used
Reduction of 15%in usage i.e. from 598L to 504L and
reducing the quantity of MTBE used by 15% i.e. from
1100L to 935 L. 2005 Reduction in TEB usage in
the TBIN process by 11% Reductions from 900kg to 800kg per batch.
2005 Reduction in the volume of
dichloromethane by 50L per
batch of QPR
Reduction from 50 L to 0L.
2005 Replacement of wooden Reduction in material usage
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D.6 Environmental Consideration and BAT
Attachment D.6.A Pfizer Loughebg API Page 3 of 3
pallets with plastic pallets in
Production
.
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D.6 Environmental Consideration and BAT
Attachment D.6.B Pfizer Loughebg DP Page 1 of 4
Year Project Title Result
2001/2002
Transport product in re-
usable FIBCs instead of
plastic drums
• Achieved 80/20 distribution of FIBCs to plastic
drums – equating to a saving of 62,400 plastic
drums annually (by using 7,200 FIBCs)
2001/2002
Purchase a dechimber &
establish a resource to
dechimb and recycle fibre
drums
• ~25,000 drums dechimbed & 100% recycled annually
2001/2002 2nd waste compactor
purchased for recyclable
material (cardboard,
fibreboard, plastics)
• Ensured better segregation of waste and a
significant increase in amount of waste
recycled.
2002/2003
Focus on better segregation
and management of waste,
increasing amount of waste
recycled
• Landfill waste reduced by 3.2 tons • Recyclable material increased by 22 tons
(cardboard; fibreboard; plastics)
• Tabletting waste reduced by 4 tons • Tablets produced increased from 4.4 billion
(2002) to 4.8 billion (2003) • Numbers of people working onsite increased
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D.6 Environmental Consideration and BAT
Attachment D.6.B Pfizer Loughebg DP Page 2 of 4
from 139 (2002) to 250 (2003)
2003/2004
Increase use of re-usable
FIBCs for transporting
product instead of plastic
drums
Pallet repair for re-use
scheme
• 65.4 tons of plastic not used
• 465,920 desiccant bags (32614kg) not used
• 1,120 pallets not be used
• 2,000 pallets a year = 6.6 acres forest
growth/10 years
2003/2004
Optimise the Heating,
Ventilation & Air Conditioning
(HVAC) system
• HVAC had been on constant supply -
changed to using it on demand to re-generate
the dessicant wheel. Also non-GMP units
have been set on setback mode. Both have
shown significant savings in energy usage.
2004/2005
Attain 70% improvement in the elegance pass rate during the coating stage of production
• 70% improvement in elegance achieved
2004/2005
Improve plant’s yield • Yield increased from 96.4% to 98.62% across the compression unit.
2004/2005 Reduce and standardize the • Approx. 980 tons of product saved per annum with the completion of this project.
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D.6 Environmental Consideration and BAT
Attachment D.6.B Pfizer Loughebg DP Page 3 of 4
amount of sample tablet
taken from the compression
stage of production
2005
Improve plant’s yield • At year end plant yield was 97.43%.
2005
Recycle Coating Suspension remaining from process thereby reducing waste
• Residual coating suspension from production of a batch is being re-used in making of subsequent batches, without impacting product quality, thereby reducing waste produced at final stage of process.
2005
Improve waste management
in LODP restaurant / kitchen • Food waste reduced by 2.76 tons from 2004
to 2005 • Canteen / kitchen received Gold Award in the
Green Failte Award programme (having
received a Silver Award in 2004)
2005
Optimise lighting system in
plant thereby reducing energy
consumption
• 13 harmonic rejection transformers installed
preventing premature failure of electronic
starters & fluorescent lighting tubes
• Achieved 2.9% reduction in electrical power
consumption of lighting transformers
2005
Optimise lighting system in
plant thereby reducing energy
consumption
• 9,750 lamps in the plant replaced with Aura Long Life lamps. Previous lamps had a life expectancy of 10,000 hours whereas the AURA replacements have a life expectancy of 60,000 hours
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D.6 Environmental Consideration and BAT
Attachment D.6.B Pfizer Loughebg DP Page 4 of 4
2005
Foster positive relations with local community /school – particularly in terms of heightening environmental awareness
• The plant runs fortnightly environmental learning sessions with 3rd, 4th, 5th and 6th class children from the School. These learning sessions are interactive with lots of questions asked and a tour of the plant's recycling and waste handling facilities.
• The plant purchased and donated to the
school recycling bins for the proper segregation of paper, cardboard, plastic, glass and aluminium cans.
• At the school’s request, the plant arranged for a representative from An Taisce to meet with a nominated teacher to explain the Green Flag programme. The school hopes to attain a green flag in late 2006.
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