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LIST OF ENCLOSURES
S. No Content Annexure
1 CFE Copy Enclosure -I
2 CFO Copy Enclosure -II
3 Land Documents Enclosure-III
COPY OF CFE
COPY OF CFO
LAND DOCUMENT
LIST OF ANNEXURES
S. No Content Annexure
1 List of Products Annexure-I
2 Manufaturing Process Description Annexure-II
3 Water Consumption Details Annexure-III
4 Hazardous waste
Annexure-IV 5 Industrial Process waste
6 Sewage sludge
7 Hazardous & Solid waste
8 Stack Emission Details Annexure-V 9 Process Emission Details Annexure-VI
10 List of Raw Materials Annexure- VII
11 List of By - Products Annexure-VIII
12 Waste water Details Annexure-IX
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Annexure - I
LIST OF PROPOSED PRODUCTS
S. No Name of the Product CAS Number
Therapeutic Category
Quantity In Kg/Month
1 Benzyl Magnesium chloride 6921-34-2 Organic Reagent 10000.00 2 Butyl Magnesium Chloride 693-04-9 Organic Reagent 15000.00 3 Domperidone 57808-66-9 Antiemetic. 5000.00 4 Escitalopram oxalate 219861-08-2 Antidepressant. 3000.00
5 Esomeprazole Magnesium trihydrate 217087-10-0 Antiulcer Agent 5000.00
6 Ethyl magnesium Chloride 925-90-6 Organic Reagent 15000.00
7 Linezolid 165800-03-3 Antibiotic 2000.00 8 Loperamide hydrochloride 34552-83-5 Ant diarrheal 2000.00 9 Magnesium tert.Butoxide 32149-57-8. Organic Reagent 15000.00
10 Metformin hydrochloride 1115-70-4 Hypoglycemic 50000.00
11 Methyl magnesium chloride 676-58-4
Organic Reagent 20000.00
12 N,N-Dimethyl propyl magnesium chloride - Drug Intermediate 20000.00
13 Omeprazole 73590-58-6 Proton pump inhibitor. 20000.00
14 Pantoprazole sodium 138786-67-1 Gastric Acid Secretion Inhibitor
15000.00
15 Phenyl magnesium chloride 100-59-4
Organic Reagents 15000.00
16 Quetiapine Fumarate 111974-72-2 Antipsychotic, 5000.00
17 Rabeprazole Sodium 117976-90-6 Gastric Acid Secretion Inhibitor
5000.00
18 Sodium Methoxide 124-41-4 Antineoplastic 50000.00 19 Sodium tert butoxide 865-48-5 Organic Reagent 20000.00 20 Telmisartan 144701-48-4 Anti hypertensive 3000.00
Total 295000.00
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Annexure - II
MANUFACTURING PROCESS
1. BENZYL MAGNESIUM CHLORIDE
Process Description:
Stage-1
Magnesium metal is charged into a clean and dry reactor under nitrogen purging.
Charge DEE & THF and start stirring. Raise the reactor temperature up to required
temperature. Start and continue the addition of benzyl chloride up to completion of the
reaction. Distill off DEE and maintain for few hours and then cool to room temperature.
Check the sample and unload the material into the containers under nitrogen
atmosphere.Check the Product and unload the material into the containers under
Nitrogen atmosphere.
BENZYL MAGNESIUM CHLORIDE
Route of synthesis:
Stage-1:
Mg
Magnesium
24.31
+
Benzyl chloride
Cl
C7H7Cl
126.58
MgCl
Benzylmagnesium chloride
C7H7ClMg
150.89
THF
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BENZYL MAGNESIUM CHLORIDE
Flow Chart:
MagnesiumBenzyl chlorideDiethyl etherTetrahydrofuran
Diethyl ether RecTHF Rec
Stage-1
BENZYL MAGNESIUM CHLORIDE
BENZYL MAGNESIUM CHLORIDE
Material Balance:
Material Balance of Benzyl Magnesium Chloride Stage-1
Batch Size: 1000.0Kgs Name of the input Quantity
in Kg Name of the out put Quantity
in Kg
Magnesium 160.00 Benzyl magnesium chloride in THF Solution
2056.00
Benzyl chloride 840.00 Diethyl ether Recovery 732.00 Diethyl ether 770.00 Diethyl ether Loss 38.00 Tetrahydrofuran 1100.00 Tetrahydrofuran Loss 44.00 Total 2870.00 Total 2870.00
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2. BUTYL MAGNESIUM CHLORIDE
Process Description
Stage-1
Magnesium metal is charged into a clean and dry reactor under nitrogen purging.
Charge THF and start stirring. Raise the reactor temperature up to required
temperature. Start and continue the addition of butyl chloride up to completion of the
reaction. Maintain for few hours and cool to room temperature. Check the Products and
unload the material into the containers under Nitrogen atmosphere.
BUTYL MAGNESIUM CHLORIDE
Route of Synthesis
Stage-1
Mg
Magnesium
24.31
+
Butyl chloride
Nitrogen
Butyl Magnesium ChlorideTHF
CH3ClMg
ClCH3
116.87
C4H9MgClC4H9Cl
92.57
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BUTYL MAGNESIUM CHLORIDE
Flow Chart
Stage-1 THF RecMagnesium MetalButyl ChlorideTHF
BUTYL MAGNESIUM CHLORIDE
BUTYL MAGNESIUM CHLORIDE
Material Balance:
Material Balance of Butyl Magnesium Chloride Stage-1
Batch Size: 1000.0 Kgs Name of the input Quantity
in Kg Name of the out put Quantity
in Kg
Magnesium Metal 210.00 Butyl Magnesium Chloride in THF Solution
1768.00
Butyl Chloride 790.00 THF Loss 40.00 THF 805.00 Total 1808.00 Total 1808.00
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3. DOMPERIDONE
Process Description: Stage-1
N-carbethoxy-4-piperidone is reacted with Hydrogen and Ammonia in the presence of
Raney nickel as catalyst and Methanol as solvent media to give stage-1 as product.
Stage-2
Stage-1 reacts with 2, 5-Dichloro nitrobenzene & Sodium Carbonate in presence of
Methanol as a solvent media to give Stage-2 as product.
Stage-3
Stage-2 reacts with Hydrogen in presence of Raney Nickel as catalyst and Toluene
as solvent media to give Stage-3 as product.
Stage-4
Stage-3 reacts with Urea in the presence of Sodium Hydroxide as a solvent media to
give Stage-4 as product.
Stage-5
Stage-4 undergoes hydrolysis with Sodium Hydroxide to give Stage-5 as product.
Stage-6
Stage-5 reacts with 1-(3-chloropropyl)-1, 3-dihydro-2H-benzimedazole-2-one and
Sodium Carbonate in the presence of Methyl Isobutyl Ketone as solvent media to give
Domperidone as product.
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DOMPERIDONE
Route of synthesis:
Stage-1
N-Carbethoxy-4-piperidone
N
O
O O CH3
C8H13NO3
171.19
+ H2
Hydrogen
2.00
+ NH3
Ammonia
17.03
+ H2O
4-Amino-piperidine-1-carboxylic acid ethyl ester
N
NH2
O O CH3
18.00
C8H16N2O2
172.22
Raney Nickel
Stage-2
4-Amino-piperidine-1-carboxylic acid ethyl ester
N
NH2
O O CH3
C8H16N2O2
172.22
+
2,5-Dichloro Nitrobenzene
Cl
Cl
NO2
C6H3Cl2NO2
192.00
+ 1/2 Na2CO3
Sodium carbonate
1/2X105.98=52.99
N
HN
O O CH3
NO2
Cl
4-(4-Chloro-2-nitro-phenylamino)-piperidine-1-carboxylic acid ethyl ester
+
C14H18ClN3O4
327.76
NaCl
Sodium chloride
58.44
+ 1/2 H2O1/2 CO2
Carbon dioxide1/2X44=22.00
+
1/2X18=9.00
Methanol
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Stage-3
N
HN
O O CH3
NO2
Cl
4-(4-Chloro-2-nitro-phenylamino)-piperidine-1-carboxylic acid ethyl ester
C14H18ClN3O4
327.76
+ 3 H2
3X2=6.00
Hydrogen
N
HN
O O CH3
NH2
Cl
4-(2-Amino-4-chloro-phenylamino)-piperidine-1-carboxylic acid ethyl ester
C14H20ClN3O2
297.78
+ 2H2O
2X18=36.00
Raney Nickel
Toluene
Stage-4
N
HN
O O CH3
NH2
Cl
4-(2-Amino-4-chloro-phenylamino)-piperidine-1-carboxylic acid ethyl ester
C14H20ClN3O2
297.78
+
Urea
H2N
O
NH2
CH4N2O
60.05
N
O O CH3
N
HNCl
O
4-(5-Chloro-2-oxo-2,3-dihydro-enzoimidazol-1-yl)-piperidine-1-
carboxylic acid ethyl ester
C15H18ClN3O3
323.77
+ 2NH3
2X17.03=34.06
Ammonia
NaOH
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Stage-5
N
O O CH3
N
HNCl
O
C15H18ClN3O3
323.77
+
Sodium hydroxide
NaOH
40.00
4-(5-Chloro-2-oxo-2,3-dihydro-benzoimidazol-1-yl)-piperidine-1-carboxylic acid ethyl ester
NH
N
HNCl
O
5-Chloro-1-piperidin-4-yl-1,3-dihydro-benzoimidazol-2-one
+ C2H5ONa
Sodium ethoxide
68.05
+ CO2
Carbon dioxide
44.00
C12H14ClN3O
251.71
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Stage-6
NH
N
HNCl
O
5-Chloro-1-piperidin-4-yl-1,3-dihydro-benzoimidazol-2-one
C12H14ClN3O
251.71
+
1-(3-chloropropyl)-1,3-dihydro -2H-(Benzimidazole-2-one)
N
HN
O
Cl
C10H11ClN2O
210.66
+ 1/2Na2CO3
Sodium carbonate
NH
N
ON
NH
N
O Cl
425.91
Domperidone
C22H24ClN5O2
+ NaCl
Sodium chloride
58.44
+ 1/2 H2O +1/2 CO2
Carbon dioxideWater
1/2X44=22.001/2X18=9.00
1/2X105.98=52.99
MIBK
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DOMPERIDONE
Flow Chart:
Stage-170.0 Kg
ProductMethanol Rec
Effluent water
Stage-295.0 Kg
ProductMethanol Rec
Effluent water
Stage-375.0 Kg
ProductToluene Rec
Effluent water
Stage-12,5-Dichloro NitrobenzeneSodium CarbonateMethanol
Stage-467.0 Kg
ProductAmmonia
Effluent water
Stage-545.0 Kg
ProductCarbon Dioxide
Effluent water
Stage-650.0 Kg
Product
Sodium chlorideCO2
Effluent water
DOMPERIDONE
N-Carbethoxy-4-piperidoneAmmonia gasMethanolRaney NickelHydrogen
Stage-2HydrogenRaney NickelToluene
Stage-3UreaSodium Hydroxide (48%)
Stage-4Sodium Hydroxide
Stage-51-(3-Chloropropyl)-1,3-dihydro2H-benzimedazole-2-oneSodium CarbonateMethyl Isobutyl Ketone
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DOMPERIDONE
Material Balance:
Material Balance of Domperidone Stage-1
Batch Size:50Kg Name of the input Quantity
in Kg Name of the out put Quantity
in Kg N-Carbethoxy-4-piperidone 80.00 Stage-1 70.00 Ammonia gas 28.00 Methanol Recovery 283.00 Methanol 300.00 Methanol Loss 15.00 Raney Nickel 20.00 Spent Raney Nickel 20.00 Hydrogen 5.00 Generated water 8.40 Process Emission 24.00 (Ammonia-20,Hydrogen-4) Organic Residue 12.60 (Organic Impurities-10.6,Methanol-
2)
Total 433.00 Total 433.00
Material Balance of Domperidone Stage-2
Batch Size:50Kg Name of the input Quantity
in Kg Name of the out put Quantity
in Kg Stage-1 70.00 Stage-2 95.00 2,5-Dichloro Nitrobenzene 78.00 Methanol Recovery 470.00 Sodium Carbonate 30.00 Methanol Loss 25.00 Methanol 500.00 Effluent Water 538.85 Water 500.00 (Water-500,generated water-
3.65,Sodium chloride-23.7,Sodium carbonate-8.5,Methanol-3)
Process Emission 8.93 (Carbon dioxide) Organic Residue 40.22 (Organic Impurities-38.22,
Methanol-2)
Total 1178.00 Total 1178.00
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Material Balance of Domperidone Stage-3
Batch Size:50Kg Name of the input Quantity
in Kg Name of the out put Quantity
in Kg Stage-2 95.00 Stage-3 75.00 Hydrogen 5.00 Toluene Recovery 330.00 Raney Nickel 10.00 Toluene Loss 17.00 Toluene 350.00 Raney Nickel Reuse 10.00 Water 400.00 Effluent Water 411.43 (Water-400,generated water-10.43,
Toluene-1)
Process Emission 3.27 (Hydrogen) Organic Residue 13.30 (Organic Impurities-11.3,Toluene-2) Total 860.00 Total 860.00
Material Balance of Domperidone Stage-4
Batch Size:50Kg Name of the input Quantity
in Kg Name of the out put Quantity
in Kg Stage-3 75.00 Stage-4 67.00 Urea 20.00 Effluent Water 664.90 Sodium Hydroxide (48%) 60.00 (Water-600,Urea-4.9,Sodium
hydroxide-28.8,water from sodium hydroxide-31.2)
Water 600.00 Process Emission 8.57 (Ammonia) Organic Residue 14.53 Total 755.00 Total 755.00
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Material Balance of Domperidone Stage-5
Batch Size:50Kg Name of the input Quantity
in Kg Name of the out put Quantity
in Kg Stage-4 67.00 Stage-5 45.00 Sodium Hydroxide 15.00 Effluent Water 420.70 Water 400.00 (Water-400,Sodium hydroxide-6.7,
Sodium ethoxide-14)
Process Emission 9.10 (Carbon dioxide) Organic Residue 7.20 Total 482.00 Total 482.00
Material Balance of Domperidone Stage-6
Batch Size:50Kg Name of the input Quantity
in Kg Name of the out put Quantity
in Kg Stage-5 45.00 Domperidone 50.00 1-(3-Chloropropyl)-1,3-dihydro-2H-benzimedazole-2-one
40.00 Methyl Isobutyl Ketone Recovery 1135.00
Sodium Carbonate 20.00 Methyl Isobutyl Ketone Loss 60.00 Methyl Isobutyl Ketone 1200.00 Effluent Water 424.50 Water 400.00 (Water-400,generated water-
1.6,Sodium chloride-10.4,Sodium carbonate-10.5,MIBK-2)
Process Emission 3.93 (Carbon Dioxide) Organic Residue 31.57 (Organic Impurities-28.57,MIBK-3) Total 1705.00 Total 1705.00
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4. ESCITALOPRAM OXALATE
Process Description:
Stage-1
5-Bromo phthalide reacts with P-Fluoro Magnesium chloride in the presence of Toluene as a solvent media to give stage-1 as product.
Stage-2
Stage-1 reacts with HBr in the presence of Toluene as a solvent media to give stage-2 as product.
Stage-3
Stage-2 reacts with MPR as a resoluting agent in the presence of Toluene as a solvent media to give stage-3 as product.
Stage-4
Stage-3 undergoes resolution in the presence of Toluene as a solvent media to give stage-4 as product.
Stage-5
Stage-4 undergoes cyclisation in the presence of Toluene as a solvent media to give stage-5 as product.
Stage-6
Stage-5 reacts with Oxalic acid in the presence of Toluene as a solvent media to give stage-6 as product.
Stage-7
Stage-6 reacts with cuprous cyanide in the presence of Toluene as a solvent media to give stage-7 as product.
Stage-8
Stage-7 reacts with Oxalic acid in the presence of Toluene as a solvent media to give Escitalopram Oxalate as product.
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ESCITALOPRAM OXALATE
Route of synthesis:
Stage-1: Br
O
O
5-Bromo pthalide
C8H5BrO2
213.02
+
P-Fluoromagnesium bromide
F
MgBr
199.30
Dimethyl amino magnesium chloride
NH3C
H3CMgCl+
145.91
OH
OHN
CH3
CH3
F
396.29
+ Mg(Br)OH +
121.21
Mg(Cl)OH
76.76
C6H4BrFMg C5H12ClMgN
+ 3H2O
3X18=54.00
Toluene
4-Dimethylamino-1-(4-fluoro-phenyl)-1-(2-hydroxymethyl-
phenyl)-butan-1-olC19H23BrFNO2
Magnesium hydroxy bromide
Magnesium hydroxy chloride
Br
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Stage-2:
OH
OHN
CH3
CH3
F
396.29
4-Dimethylamino-1-(4-fluoro-phenyl)-1-(2-hydroxymethyl-
phenyl)-butan-1-olC19H23BrFNO2
Br
+ HBr
80.91
Hydrobromic acid
OH
OHN
CH3
CH3
F
Br
HBr
4-Dimethylamino-1-(4-fluoro-phenyl)-1-(2-hydroxymethyl-
phenyl)-butan-1-ol
C19H23BrFNO2.HBr
477.20
Toluene
Stage-3:
OHOH
NCH3
CH3
F
Br
HBr
4-Dimethylamino-1-(4-fluoro-phenyl)-1-(2-hydroxymethyl-
phenyl)-butan-1-ol Hydrobromide
C19H23BrFNO2.HBr
477.20
+O
OO OH
O
OO OH
CH3
H3C
MPR
C20H18O8
386.35
Toluene
OHOH
NCH3
CH3
F
Br
O
OO OH
O
OO OH
CH3
H3C
C19H23BrFNO2.C20H18O8
782.64
+ HBr
80.91
Hydrobromic acid1-(4-Bromo-2-hydroxymethyl-phenyl)-4-dimethylamino
-1-(4-fluoro-phenyl)-butan-1-ol with (+)/(-) MPR Salt
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Stage-4:
OHOH
NCH3
CH3
F
Br
O
OO OH
O
OO OH
CH3
H3C
C19H23BrFNO2.C20H18O8
782.64
1-(4-Bromo-2-hydroxymethyl-phenyl)-4-dimethylamino-1-(4-fluoro-phenyl)-butan-1-ol with (+)/(-) MPR Salt
Toluene
OH
OHNCH3
CH3
F
Br
1-(4-Bromo-2-hydroxymethyl-phenyl)-4-dimethylamino-1-(4-fluoro-phenyl)-butan-1-ol
C19H23BrFNO2
396.29
O
OO OH
O
OO OH
CH3
H3C
C20H18O8
386.35
MPR
+
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Stage-5:
OHOH
NCH3
CH3
F
Br
1-(4-Bromo-2-hydroxymethyl-phenyl)-4-dimethylamino-1-(4-fluoro-phenyl)-butan-1-ol
C19H23BrFNO2
396.29
NCH3
CH3
F
BrO
{3-[5-Bromo-1-(4-fluoro-phenyl)-1,3-dihydro-isobenzofuran-1-yl]-propyl}-dimethyl-amine
C19H21BrFNO
378.27
+ H2O
18.00
Toluene
Stage-6:
NCH3
CH3
F
BrO
{3-[5-Bromo-1-(4-fluoro-phenyl)-1,3-dihydro-isobenzofuran-1-yl]-propyl}-dimethyl-amine
C19H21BrFNO
378.27
+
Oxalic acid
O OH
OHO
C2H2O4
90.03
NCH3
CH3
F
BrO
O OH
OHO
{3-[5-Bromo-1-(4-fluoro-phenyl)-1,3-dihydro-isobenzofuran-1-yl]-propyl}-dimethyl-amine salt of Oxalic acid
C19H21BrFNO.C2H2O4
474.36
Toluene
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Stage-7:
NCH3
CH3
F
BrO
O OH
OHO
{3-[5-Bromo-1-(4-fluoro-phenyl)-1,3-dihydro-isobenzofuran-1-yl]-propyl}-dimethyl-amine salt of Oxalic acid
C19H21BrFNO.C2H2O4
468.31
+ CuCN
89.56
Cuprous cyanide
NCH3
CH3
F
NCO
{3-[5-Cyano-1-(4-fluoro-phenyl)-1,3-dihydro-isobenzofuran-1-yl]-propyl}-dimethyl-amine
C20H21FN2O
324.39
+ CuBr +
Oxalic acid
O OH
OHO
Cuprous bromide
143.45 90.03
Toluene
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Stage-8:
NCH3
CH3
F
NCO
{3-[5-Cyano-1-(4-fluoro-phenyl)-1,3-dihydro-isobenzofuran-1-yl]-propyl}-dimethyl-amine
C20H21FN2O
324.39
+
Oxalic acid
O OH
OHO
90.03
C2H2O4
Toluene
NCH3
CH3
F
NCO
O OH
OHO
{3-[5-Cyano-1-(4-fluoro-phenyl)-1,3-dihydro-isobenzofuran-1-yl]-propyl}-dimethyl-amine salt of Oxalic acid
C20H21FN2O.C2H2O4
414.42
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Stage-9
NCH3
CH3
F
NCO
O OH
OHO
C20H21FN2O.C2H2O4
414.42
Esitolopram oxalate
IPA
NCH3
CH3
F
NCO
O OH
OHO
C20H21FN2O.C2H2O4
414.42
Esitolopram oxalate
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ESCITALOPRAM OXALATE
Flow Chart:
Stage-1
Stage-2
Stage-3
Stage-4
Stage-5
BromophthalideFluorobromobenzeneDimethyl amino propylmagnesium chlorideMagnesium turnings
Effluent water
Stage-1Hydrobromic acidActivated carbonToluene
Toluene RecEffluent water
Stage-2MPRActivated carbonIPAToluene
IPA RecToluene RecEffluent water
Stage-3Sodium hydroxideSodium sulfateToluene
Toluene RecEffluent water
Stage-4Methane sulfonyl chlorideTriethylamineSodium sulfateToluene
Acetone RecEffluent water
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Stage-6
Stage-7
Stage-8
Stage-9
Stage-5Oxalic acidAcetone
Acetone Rec
Stage-6Sodium hydroxideCopper cyanideEthylene di amineDMFToluene
DMF RecToluene Rec
Stage-7Oxalic acidTolueneIPA
IPA RecToluene RecEffluent water
Stage-8IPAActivated carbon
IPA Rec
ESCITALOPRAM OXALATE
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ESCITALOPRAM OXALATE
Material Balance:
Material Balance of Escitalopram oxalate Stage-1
Batch Size: 100 Kgs Name of the input Quantity
in Kg Name of the out put Quantity
in Kg Bromo phthalide 110.00 Stage-1 200.00 Fluoro bromo benzene 103.00 Toluene Recovery 474.00 Dimethyl amino propyl magnesium chloride
76.00 Toluene Loss 25.00
Magnesium turnings 28.00 THF Recovery 949.00 Acetic acid 87.00 THF Loss 50.00 Iodine 3.00 Effluent water 883.80 Ammonia Liq 90.00 (Water-572.2, Magnesium hydroxyl
bromide-62.6,Magnesium hydroxyl chloride-40,Magnesium turnings-28,Acetic acid-87, Ammonia-9,Water from ammonia-81,Iodine-3, THF-1)
Activated carbon 4.00 Spent carbon 4.00 Toluene 500.00 Organic Residue 15.20 Tetrahydrofuran 1000.00 (Organic Impurites-14.2,Toluene-
1)
Water 600.00 Total 2601.00 Total 2601.00
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Material Balance of Escitalopram oxalate Stage-2
Batch Size: 100 Kgs Name of the input Quantity
in Kg Name of the out put Quantity
in Kg Stage-1 200.00 Stage-2 225.00 Hydro bromic acid 41.00 Toluene Recovery 333.00 Activated carbon 5.00 Toluene Loss 17.00 Toluene 350.00 Effluent water 601.00 Water 600.00 (Water-600,Toluene-1) 0 Spent carbon 5.00 Organic Residue 15.00 Total 1196.00 Total 1196.00
Material Balance of Escitalopram oxalate Stage-3
Batch Size: 100 Kgs Name of the input Quantity
in Kg Name of the out put Quantity
in Kg Stage-2 225.00 Stage-3 350.00 MPR 173.00 Toluene Recovery 1424.00 Caustic flakes 38.30 Toluene Loss 75.00 Sodium sulfate 62.00 IPA Recovery 949.00 Activated carbon 7.30 IPA Loss 50.00 IPA 1000.00 Effluent water 677.34 Toluene 1500.00 (Water-600,Generated water-
8.47,Sodium bromide-48.4,Sodium hydroxide-19.47,Toluene-1)
Water 600.00 Inorganic sold waste 62.00 (Sodium sulfate) Organic solid waste 10.96 (Organic Impurities-9.96,IPA-1) Spent carbon 7.30 Total 3605.60 Total 3605.60
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Material Balance of Escitalopram oxalate Stage-4
Batch Size: 100 Kgs Name of the input Quantity
in Kg Name of the out put Quantity
in Kg Stage-3 350.00 Stage-4 165.00 Sodium hydroxide 10.00 Toluene Recovery 6173.00 Sodium sulfate 100.00 Toluene Loss 325.00 Toluene 6500.00 Effluent water 411.00 Water 400.00 (Water-400,Sodium hydroxide-
10,Toluene-1)
Inorganic solid waste 100.00 (Sodium sulfate) MPR Reagent Reuse 173.00 Organic Solid waste 13.00 (Organic Impurities-12,Toluene-1) Total 7360.00 Total 7360.00
Material Balance of Escitalopram oxalate Stage-5
Batch Size: 100 Kgs Name of the input Quantity
in Kg Name of the out put Quantity
in Kg Stage-4 165.00 Stage-5 150.00 Methane sulfonyl chloride 50.00 Toluene Recovery 6173.00 Triethylamine 15.00 Toluene Loss 325.00 Sodium chloride 20.00 Effluent water 493.50 Sodium sulfate 100.00 (Water-400,Generated water-7.5,
Methane sulfonyl chloride-50, Sodium chloride-20,Triethyl amine-15,Toluene-1)
Toluene 6500.00 Inorganic solid waste 100.00 Water 400.00 (Sodium sulfate) Organic Residue 8.50 (Organic Impurities-7.5,Toluene-1) Total 7250.00 Total 7250.00
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Material Balance of Escitalopram oxalate Stage-6
Batch Size: 100 Kgs Name of the input Quantity
in Kg Name of the out put Quantity
in Kg Stage-5 150.00 Stage-6 180.00 Oxalic acid 40.00 Acetone Recovery 1095.00 Acetone 1152.00 Acetone Loss 56.00 Organic Residue 11.00 (Organic Impurities-10,Acetone-1) Total 1342.00 Total 1342.00
Material Balance of Escitalopram oxalate Stage-7
Batch Size: 100 Kgs Name of the input Quantity
in Kg Name of the out put Quantity
in Kg Stage-6 180.00 Stage-7 120.00 Copper cyanide 45.00 Toluene Recovery 2660.00 Copper iodide 57.00 Toluene Loss 139.00 Ethylene di amine 267.00 DMF Recovery 2173.00 DMF 2288.00 DMF Loss 114.00 Toluene 2800.00 Ethylene di amine Recovery 254.00 Water 300.00 Ethylene di amine Loss 13.00 Effluent water 458.00 (Water-300,Cuprous bromide-
56,Oxalic acid-44,Copper iodide-57,DMF-1)
Organic Residue 6.00 (Organic Impurities-5,Toluene-1) Total 5937.00 Total 5937.00
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Material Balance of Escitalopram oxalate Stage-8
Batch Size: 100 Kgs Name of the input Quantity
in Kg Name of the out put Quantity
in Kg Stage-7 120.00 Stage-8 129.00 Oxalic acid 34.00 Toluene Recovery 2659.00 Ammonia Liquid 114.00 Toluene Loss 140.00 Acetic acid 34.00 Isopropyl ether Recovery 228.00 Activated carbon 50.00 Isopropyl ether Loss 12.00 Hyflow 10.00 Acetone Recovery 542.00 Toluene 2800.00 Acetone Loss 28.00 Isopropyl ether 240.00 Effluent water 550.00 Acetone 572.00 (Water-400,Acetic acid-34,
Ammonia-11.4,Water from ammonia-102.6, Toluene-1, Acetone-1)
Water 400.00 Spent carbon &Hyflow 60.00 Organic Residue 26.00 (Organic Impurities-25,Acetone-1) Total 4374.00 Total 4374.00
Material Balance of Escitalopram oxalate Stage-9
Batch Size: 100 Kgs Name of the input Quantity
in Kg Name of the out put Quantity
in Kg Stage-8 129.00 Escitalopram oxalate 100.00 IPA 3200.00 IPA Recovery 3039.00 Activated carbon 14.00 IPA Loss 160.00 Spent carbon 14.00 Organic Residue 30.00 (Organic Impurities-29,IPA-1) Total 3343.00 Total 3343.00
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5. ESOMEPRAZOLE MAGNESIUM TRIHYDRATE
Process
Description:
Stage-1
5-Methoxy-2-[(4-Methoxy-3,5-Dimethyl-2-pyridinyl) Methyl Thio]-1H-
Benzimidazole reacts with Cumin hydroperoxide and Potassium hydroxide in the
presence of Toluene as a solvent media to give stage-1 as product. Stage-2
Stage-1 undergoes hydrolysis with Magnesium sulfate in the presence of Toluene
as a solvent media to give Esomepraszole Magnesium Trihydrate as product.
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ESOMEPRAZOLE MAGNESIUM TRIHYDRATE
Route of synthesis:
Stage-1:
OCH3
H3C CH3
N OCH3
CH3 OH
H3C O
Toluene
N C S +
H2 N
H
+ KOH
5-Methoxy-2-[(4-methoxy-3, 5-dimethyl-pyridin
-2-ylmethyl Thio]-1H -Benzoimidazole
C17H19N3O2S
329.41
OCH3
H3C CH3
Cumin hydroperoxide
C9H12O2
152.19
H3C
Potassium hydroxide
56.10
CH3
OH
O N
N C S H2
N
K+
OCH3
H2O +
Esomeprazole potassium salt.Monohydrate Cumin hydroxide
C17H20KN3O4S C9H12O 136.19
401.52
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Stage-2:
OCH3
H3C CH3
O
2
N OCH3
N C S H2
N
K+
H2O + MgSO4 + H2O
Esomeprazole potassium salt.Monohydrate
C17H20KN3O4S
2X401.52=803.04
Magnesium sulfate
120.36
18.00
OCH3
H3C CH3
O
N OCH3
Mg 3H2O + K2SO4
N C S H2
N 2
Esomeprazole Magnesium Tri Hydrate
C17H18N3O3S.Mg3H2O
767.15
Potassium sulfate
174.25
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ESOMEPRAZOLE MAGNESIUM TRIHYDRATE Flow Chart:
Omeprazole sulfide Cumin hydroperoxide Potassium hydroxide Methanol
Stage-1
Methanol Rec
Stage-1 Magnesium sulfate Water
Stage-2
Effluent Water
ESOMEPRAZOLE MAGNESIUM
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ESOMEPRAZOLE MAGNESIUM TRIHYDRATE
Material Balance:
Material Balance of Esomeprazole Magnesium trihydrate Stage-1
Batch Size: 100 Kgs Name of the input Quantity in
Kg Name of the out put Quantity in
Kg Name of the input Quantity
in Kg Name of the out put Quantity
In Kg Omeprazole sulfide 88.00 Stage-1 107.00 Cumin hydro peroxide 41.00 Toluene Recovery 305.00 Potassium hydroxide 15.20 Toluene loss 15.00 DET 11.30 Methanol Recovery 95.00 Titanium isopropoxide 2.50 Methanol Loss 5.00 NEDIPA 4.50 NEDIPA Loss 4.50 Toluene 320.00 Organic Residue 51.00 Methanol 100.00 (DET-11.3,Titanium
isopropoxide-2.5,Cumin hydroxide-37.2,)
Total 582.50 Total 582.50
Material Balance of Esomeprazole Magnesium trihydrate Stage-2
Batch Size: 100 Kgs Name of the input Quantity in
Kg Name of the out put Quantity in
Kg Name of the input Quantity in
Kg Name of the out put Quantity
In Kg Stage-1 107.00 Esomeprazole Magnesium
trihydrate 100.00
Magnesium sulfate 16.00 Effluent water 980.80 Water 960.00 (Water-957.6,Potassium
sulfate-23.2)
Organic Residue 2.20 Total 1083.00 Total 1083.00
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6. ETHYL MAGNESIUM CHLORIDE
Process Description:
Stage-1
Magnesium metal is charged into a clean and dry reactor under Nitrogen purging,
Charge THF and start stirring. Raise the reactor temperature up to required
temperature. Start and continue the addition of ethyl chloride up to completion of
the reaction. Maintain few hours and cool to room temperature. Check sample and
unload the material into containers under Nitrogen atmosphere.
ETHYL MAGNESIUM CHLORIDE
Route of Synthesis:
Stage-1:
Mg +
Magnesium
24.31 C2H5MgCl
Ethyl Magnesium Chloride
88.82
THFH3C Cl
64.51
Ethyl Chloride
H3C MgCl
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ETHYL MAGNESIUM CHLORIDE
Flowchart:
Stage-1
ETHYL MAGNESIUM CHLORIDE
Ethyl ChlorideMg turningsTHF
THF Recovery
ETHYL MAGNESIUM CHLORIDE
Material Balance:
Material Balance of Ethyl Magnesium Chloride Stage-1
Batch Size: 1000.0 Kgs Name of the input Quantity
in Kg Name of the out put Quantity
in Kg
Ethyl Chloride 724.00 Ethyl Magnesium Chloride in THF Solution
2425.00
Mg turnings 276.00 THF Loss 75.00 THF 1500.00 Total 2500.00 Total 2500.00
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7. LINEZOLID
Process Description:
Stage-1:
N-[3-pthalimido-2R-Hydroxy propyl]-3-(fluoro-4-morpholinyl) aniline is treated with
carbonyl diimidazole, Hydrazine hydrate and acetic anhydride in the presence of
MDC and Methanol to give Linezolid as product.
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LINEZOLID Route of Synthesis: Stage-1
O N
F
NH
N
OH
O
O
2-[3-(3-Fluoro-4-morpholin-4-yl-phenylamino)-2-hydroxy-propyl]-isoindole-1,3-dione
C21H22FN3O4
399.42
+
Carbonyl diimidazole
O
N
HNNH
N
C7H6N4O
162.15
+
Hydrazine hydrate
H2NNH2H
OH
H6N2O
50.06
+
Acetic anhydride
OO
O
C4H6O3
102.09
MDC
O N
F
NO
O
HN CH3
O
Linezolid
C16H20FN3O4
337.35
+
Imidazole
N
HN
2
C3H4N2
2X68.08=136.16
+ CH3COOH
60.0
+
Phthalazine -1,4-diol
N
N
OH
OH
C8H6N2O2
162.15
+ H2O
18.0
LINEZOLID
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Flow Chart:
N-[3-Phthalimido-2R-hydroxypropyl-3-fluoro-4-morpholinyl anilineCarbonyl diimidazoleHydrazine HydrateMethanol
Stage-1 Methanol Rec
LINEZOLID
LINEZOLID
Material Balance:
Material balance of Linezolid Stage-1
Batch Size:90.0 Kg Name of the input Quantity
in Kg Name of the out put Quantity
In Kg N-[3-Phthalimido-2R-hydroxypropyl-3-fluoro-4-morpholinyl aniline
110.00 Linezolid 90.00
Carbonyl di imidazole 43.25 Methanol Recovery 710.00 Hydrazine Hydrate 13.35 Methanol Loss 37.00 Acetic anhydride 27.23 MDC Recovery 2548.00 Methanol 753.00 MDC Loss 134.00 MDC 2682.00 Ethyl acetate Recovery 765.00 Activated carbon 10.80 Ethyl acetate Loss 40.00 Ethyl acetate 805.00 Acetone Recovery 1471.00 Acetone 1548.00 Acetone Loss 77.00 Water 1422.00 Effluent water 1523.38 (Water-1422,Generated water-
4.8,Acetic acid-16,Phthalazine-1,4-diol-43.25,Methanol-1,Imidazole-36.33)
Spent carbon 10.80 Organic Residue 8.45 (Organic Impurities-
3.45,Methanol-5)
Total 7414.63 Total 7414.63
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8. LOPERAMIDE HYDROCHLORIDE
Process Description:
Stage-1:
N-(3,3-diphenyldihydrofuran-2(3H)-ylidene)-N-methylmethanaminium bromide is
reacted with 4-(Chloro phenyl) - Piperidine –4-ol in presence of Potassium
carbonate(K2CO3), Potassium iodide(KI), Potassium hydroxide (KOH) acetone,
Toluene ,HCl & Water to get Stage-1 compound.
Stage-2
Stage I is reacted with Methanolic HCl and then it is purified in presence of Acetone,
Methanol & Activated carbon to get Loperamide HCl (Pharama)
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LOPERAMIDE HYDROCHLORIDE
Route of Synthesis
Stage-1:
N-(3,3-diphenyldihydrofuran-2(3H)-ylidene)-N-methylm
ethanaminium bromide
N+
O
Br-
4-(Chloro phenyl) - Piperidine -4-ol
HN
OH Cl
4-[4-(4-chlorophenyl)-4-hydroxypiperidin-1-yl]-N,N-dimethyl-2,2-
diphenylbutanamide
++ 1/2 K2CO3
PotassiumCarboante
ON
N
OH
Cl
C18H20BrNO
346.26
C11H14ClNO
211.69
1/2X138.21=69.1
C29H33ClN2O2477.04
+ KBr + 1/2 CO2 + 1/2H2O
119.0 1/2X44=22.0 1/2X18=9.0
Acetone / KI
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Stage-2:
4-[4-(4-chlorophenyl)-4-hydroxypiperidin-1-yl]- N,N-dimethyl-2,2-diphenylbutanamide
O
NN
OHCl
C29H33ClN2O2
477.04
O
NN
OHCl
4-[4-(4-chlorophenyl)-4-hydroxypiperidin-1-yl]-N,N-dimethyl-2,2-
diphenylbutanamide Hydrochloride
C29H34Cl2N2O2
513.50
+ HCl
Hydrochloric Acid
36.46
Methanol
Carbon
HCl
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LOPERAMIDE HYDROCHLORIDE
Flow Chart
Stage-1
Stage-2
N-[(2Z)-3-(diphenylmethyl)dihydrafuran-2(3H)-ylidene]methanamine4-(Chloro phenyl)-Piperidine-4-ol Potassium carbonateAcetone
Acetone RecEffluent water
Stage-1MethanolAcetoneMethanolic HClActivated Carbon
Methanol RecAcetone RecSpent carbon
LOPERAMIDE HYDROCHLORIDE
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LOPERAMIDE HYDROCHLORIDE
Material Balance
Material Balance of Loperamide Hydrochloride Stage-1
BatchSize:180 Kg Name of the input Quantity
in Kg Name of the out put Quantity
in Kg N-[(2Z)-3-(diphenylmethyl)dihydrafuran-2(3H)-ylidene]methanamine
122.00 Stage-1 168.00
4-(Chloro phenyl)-Piperidine-4-ol 75.00 Acetone Recovery 563.00 Potassium carbonate 25.00 Acetone Loss 30.00 Potassium Iodide 1.00 Effluent Water 3051.11 Acetone 600.00 (Water-3000,generated water-
3.19,Potassium bromide-41.92, Acetone-5 , Potassium Iodide-1
Water 3000.00 Process Emission 7.96 (Carbon dioxide) Organic Residue 2.93 (Organic Impurities-0.93,
Acetone-2)
Total 3823.00 Total 3823.00
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Material Balance of Loperamide Hydrochloride Stage-2
BatchSize:180Kg Name of the input Quantity
in Kg Name of the out put Quantity
in Kg Stage-1 168.00 Loperamide Hydrochloride 180.00 Methanol 600.00 Methanol Recovery 677.50 Acetone 300.00 Methanol Loss 30.00 Methanolic HCl (10%) 125.00 Acetone Recovery 280.00 Activated Carbon 20.00 Acetone Loss 20.00 Spent Carbon 20.00 Organic Residue 5.50 (Organic Impurities-0.5,
Methanol-5)
Total 1213.00 Total 1213.00
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9. MAGNESIUM TERTIARY BUTOXIDE
Process Description
Stage-1
2 moles of Methyl Magnesium Chloride in THF are reacted under certain conditions
to form Di methyl Magnesium and Magnesium Chloride.
Stage-2
Di methyl Magnesium in THF is reacted with Tertiary Butanol to get Magnesium
Tertiary Butoxide. The Magnesium Tertiary Butoxide solution in THF is taken into a
dryer and THF is recovered and used in next batches. The dried product is packed in
polythene bags and kept in MS drums.
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MAGNESIUM TERTIARY BUTOXIDE
Route of Synthesis
Stage-1
2 CH3MgCl
Methl magnesium chloride
2X74.79=149.58
THF(CH3)2Mg
Di MethylMagnesium
54.37
+ MgCl2
Magnesium Chloride
95.21
Stage-2
THF(CH3)2Mg
Dimethyl Magnesium
54.37
+
Tert Butanol
CH3
H3C
CH3
OH2
2X74.12=148.24
C4H9OH
Magnesium Tertiary Butoxide
(C4H9O)2Mg
C8H18MgO2
170.53
+ 2 CH4
Methane gas
2X16.04=32.08
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MAGNESIUM TERTIARY BUTOXIDE
Flow Chart
Stage-1
Stage-2
Methyl magnesium ChlorideTHF
THF RecMgCl2(Byproduct)
Stage-1Tert-Butanol
Methane gasTert-Butanol Rec
MAGNESIUM TERTIARY BUTOXIDE
MAGNESIUM TERTIARY BUTOXIDE
Material Balance:
Material Balance of Magnesium Tertiary Butoxide Stage-1
Batch Size:200.0Kgs Name of the input Quantity
in Kg Name of the out put Quantity
in Kg Methyl Magnsium Chloride 214.00 Stage-1+ THF 1400.00 THF 1400.00 THF Loss 70.00 By-product 144.00 (Magnesium chloride-144) Total 1614.00 Total 1614.00
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Material Balance of Magnesium Tertiary Butoxide Stage-2
Batch Size: 200.0Kgs Name of the input Quantity
in Kg Name of the out put Quantity
in Kg
Stage-1 + THF 1369.30 Magnesium Tertiary Butoxide in THF Solution
1528.00
Tert-Butanol 200.00 Process Emission 41.30 (Methane gas-41.30) Total 1569.30 Total 1569.30
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10. METFORMIN HYDROCHLORIDE
Process Description
Dimethylamine hydrochloride reacts with Dicyanodiamide in the presence of Xylene
and Water Solvent media to produce aqueous layer containing Metformin
Hydrochloride which is purified with Activated carbon in the presence of Methanol
Solvent media to produce Metformin Hydrochloride.
METFORMIN HYDROCHLORIDE
Route of Synthesis:
Stage-1:
HN
CH3H3C
C2H8NCl
81.58
+ H2N NH
CN
NH
N-Cyanoguanidine
C2H4N4
84.08
Dimethyl amine Hydrochloride
HCl
NH3C
CH3
HN NH2
NH NH
HCl
Metformin Hydrochloride
C4H12N5Cl
165.66
Xylene
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METFORMIN HYDROCHLORIDE
Flow Chart:
Stage - 1
Dimethylamine HclN-Cyano guanidineXyleneMethanol
Xylene RecoveryMethanol Recovery
Metformin Hydrochloride
METFORMIN HYDROCHLORIDE
Material Balance:
Material Balance of Metformin Hydrochloride Stage-1
Batch Size: 250Kg Name of the input Quantity
in Kg Name of the out put Quantity
in Kg Dimethyl amine Hcl 126.00 Metformin Hydrochloride 250.00 N-Cyano guanidine 130.00 Xylene Recovery 285.00 Xylene 300.00 Xylene Loss 15.00 Activated carbon 2.00 Methanol Recovery 90.00 Hyflo 1.00 Methanol Loss 5.00 Methanol 100.00 Effluent water 324.00 Water 320.00 (Water-320,Methanol-1,Dimethyl
Amine Hydrochloride-3)
Spent carbon + Hyflo 2.00 Organic Residue 8.00 (Organic Impurities-4,Methanol-4) Total 979.00 Total 979.00
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11. METHYL MAGNESIUM CHLORIDE
Process Description
Stage-1
Magnesium metal is charged into a clean and dry reactor under nitrogen purging.
Charge THF and start stirring. Raise the reactor temperature up to required
temperature. Start and continue the addition of methyl chloride up to completion of
the reaction. Maintain for few hours and cool to room temperature. Check Product
and unload the material into the containers under nitrogen atmosphere.
METHYL MAGNESIUM CHLORIDE
Route of Synthesis
Stage-1
Mg
Magnesium
24.31
+ CH3Cl
Methyl chloride
Nitrogen
50.49
CH3MgCl
Methyl Magnesium Chloride
74.79
THF
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METHYL MAGNESIUM CHLORIDE
Flow Chart
Stage-1 THF RecMagnesium MetalMethyl ChlorideTHF
METHYL MAGNESIUM CHLORIDE
METHYL MAGNESIUM CHLORIDE
Material Balance:
Material Balance of Methyl Magnesium Chloride Stage-1
Batch Size: 3000.0Kgs Name of the input Quantity
in Kg Name of the out put Quantity
in Kg
Magnesium Metal 974.00 Methyl Magnesium Chloride in THF Solution
4156.50
Methyl Chloride 2026.00 THF Loss 113.50 THF 1270.00 Total 4270.00 Total 4270.00
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12. N, N-DIMETHYL PROPYL MAGNESIUM CHLORIDE
Process Description Stage-1 N, N-Dimethyl proyl amino chloride reacts with magnesium in presence of THF and
Toluene by addition of Catalytic amount of Iodine and EDB.
N, N-DIMETHYL PROPYL MAGNESIUM CHLORIDE
Route of Synthesis
Stage-1
Cl NCH3
CH3
(3-Chloro-propyl)-dimethyl-amine
C5H12ClN
+ Mg
24.31
121.61
I2 / EDB
THF/Toluene
ClMg NCH3
CH3
N,N-Dimethyl propylmagnesium chloride
C5H12ClMgN
145.91
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N, N-DIMETHYL PROPYL MAGNESIUM CHLORIDE
Flow Chart
Stage-1
N, N-DIMETHYL PROPYL MAGNESIUM CHLORIDE
(3-Chloro-propyl)-dimethyl-amineMagnesium turningsEDBIodineTHFToluene
THF RecToluene Rec
N, N-DIMETHYL PROPYL MAGNESIUM CHLORIDE
Material Balance:
Material Balance of N,N-Dimethyl propyl Magnesium chloride Stage-1
Batch Size:500Kg Name of the input Quantity
in Kg Name of the out put Quantity
in Kg (3-Chloro-propyl)-dimethyl-amine
417.00 N,N-Dimethyl propyl Magnesium chloride
500.00
Magnesium turnings 84.00 THF Recovery 950.00 EDB 1.00 THF Loss 50.00 Iodine 0.20 Toluene Recovery 950.00 THF 1000.00 Toluene Loss 50.00 Toluene 1000.00 Organic Residue 2.20 Total 2502.20 Total 2502.20
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13. OMEPRAZOLE
Process Description
Stage-1
3, 5-Lutidine undergoes oxidation with Hydrogen peroxide initially in Acetic acid.
Then the reaction mass will be subjected to Nitration with Nitric acid and Sulphuric
acid mixture. Below is the equation.
Stage-2
Above stage compound on reaction with Sodium methoxide, Sodium Hydroxide and
Dimethyl sulphate in Methanol and water produces stage-2 product. Reaction takes
place as per the equation
Stage-3
A Stage-2 product on reaction with Thionyl chloride, APS and sodium hydroxide
produces stage-3 compound. Toluene is the solvent used in the process. Below is
the equation.
Stage-4
Stage-3 product on condensation with 5-Methoxy -2-Mercapto benzimidazole in
presence of C.S. Lye Produces stage-4.Toluene is the solvent medium
Stage-5
Above stage-4 compound on reaction with Hydrogen Peroxide produces stage-5
pharma. Methanol and Acetone are used in the process.
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OMEPRAZOLE
Route of Synthesis:
Stage-1
N
3,5-LutidineC7H9N
107.15
+ H2O2
Hydrogen peroxide
34.01
+ HNO3
Nitric acid63.01
N
NO2
3,5-Dimethyl-4-nitro-pyridine N-Oxide
O
C7H8N2O3
168.15
Acetic acid+ 2H2O
2X18=36.0
.Stage-2
N
NO2
3,5-Dimethyl-4-nitro-pyridine N-Oxide
O
C7H8N2O3
168.15
+ CH3ONa
Sodium methoxide
54.02
+ 2NaOH
Sodium hydroxide
2X40=80.0
+ (CH3)2SO4
Dimethyl sulfate
126.13
Methanol
N
COOH
3,5-Dimethyl-isonicotinic acid N-Oxide
O
+ NaNO2
69.0
+ H2O
18.0
+ Na2SO4
142.04
+ CH3OH
32.0
C8H9NO3
167.16
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Stage-3
N
COOH
3,5-Dimethyl-isonicotinic acid N-Oxide
O
C8H9NO3
167.16
+ SOCl2
Thionyl chloride
118.97
+ NH4OH
Ammonium hydroxide
35.05
Toluene N
ClO
3,5-Dimethyl-isonicotinoyl chloride N-Oxide
O
C8H8ClNO2
185.61
+ NH4Cl + H2O + SO2
53.49 18.0 64.06
Stage-4
N
ClO
3,5-Dimethyl-isonicotinoyl chloride N-Oxide
O
C8H8ClNO2
185.61
2-Mercapto-5-methoxy benzimidazole
N
HN
O
HS+
C8H8N2OS
180.23
+ NH4OH
Ammonium Hydroxide
35.05
Toluene
N
NH
O
S
N
CH3
H3C OCH3
5-Methoxy-2-(4-methoxy-3,5-dimethyl-pyridin-2-ylmethylsulfanyl)-
1H-benzoimidazoleC17H19N3O2S
329.42
+ NH4Cl + H2O
18.053.49
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Stage-5
N
NH
O
S
N
CH3
H3C OCH3
5-Methoxy-2-(4-methoxy-3,5-dimethyl-pyridin-2-ylmethylsulfanyl)-1H-benzoimidazole
C17H19N3O2S
329.42
+ H2O2
Hydrogen peroxide
34.01
Methanol
HN
N
S
O
N
O
O
Omeprazole
C17H19N3O3S
345.42
+ H2O
18.0
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OMEPRAZOLE
Flow Chart:
Stage-147.3 Kg
Product
Effluent water
Stage-242.5 Kg
ProductMethanol Rec
Effluent water
Stage-352.40 Kg
ProductToluene Rec
Effluent water
Stage-1Sodium methoxideSodium hydroxideDimethyl sulphateMethanol
Stage-494.0 Kg
ProductToluene Rec
Effluent water
Stage-5100.0 Kg
ProductMethanol RecAcetone Rec
3,5-LutidineHydrogen PeroxideAcetic acid
Stage-2Thionyl ChlorideSodium hydroxideToluene
Stage-32-Mercapto-5-methoxy BenzimidazoleCS LyeToluene
Stage-4Hydrogen peroxideMethanolAcetone
Effluent water
OMEPRAZOLE
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OMEPRAZOLE
Material Balance:
Material balance of Omeprazole Stage-1
Batch Size:100Kg Name of the input Quantity
in Kg Name of the out put Quantity
in Kg 3,5-Lutidine 33.00 Stage-1 51.00 Hydrogen Peroxide 11.00 Effluent Water 411.14 Acetic acid 25.00 (Water-400,gen.water-
11.14) 0
Nitric acid 19.50 Acetic acid recovery 25.00 Water 400.00 Organic Residue 1.36 Total 488.50 Total 488.50
Material balance of Omeprazole Stage-2
Batch Size:100Kg Name of the input Quantity
in Kg Name of the out put Quantity
in Kg Stage-1 51.00 Stage-2 50.00 Sodium methoxide 16.40 Methanol Recovery 475.00 Sodium hydroxide 24.30 Methanol Loss 25.00 Dimethyl sulphate 38.30 Effluent Water 615.17 Methanol 500.00 (Water-600,gen.water-5.45,
Methanol-9.72) 0
Water 600.00 By-Product 64.06 (Sodium Sulphate-43.13,
Sodium nitrate-20.93) 0
Organic Residue 0.77 Total 1230.00 Total 1230.00
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Material balance of Omeprazole Stage-3
Batch Size:100Kg Name of the input Quantity
in Kg Name of the out put Quantity
in Kg Stage-2 50.00 Stage-3 55.00 Thionyl Chloride 36.00 Toluene Recovery 465.00 Ammonium hydroxide 11.00 Toluene Loss 25.00 Toluene 500.00 Effluent water 415.38 Water 400.00 (Water-400,gen.water-5.38
Toluene-10)
By-Product 16.80 (Ammonium chloride) Process Emission 19.38 (Sulphur dioxide) Organic Residue 0.44 Total 997.00 Total 997.00
Material balance of Omeprazole Stage-4
Batch Size:100 Kg Name of the input Quantity
in Kg Name of the out put Quantity
in Kg Stage-3 55.00 Stage-5 96.00 2-Mercapto-5-methoxy Benzimidazole
53.50 Toluene Recovery 470.00
Ammonium hydroxide 11.00 Toluene Loss 25.00 Toluene 500.00 Effluent Water 355.33 Water 350.00 (Water-350,Generated water-
5.33)
By-Product 16.80 (Ammonium chloride-16.8) Organic Residue 6.37 Total 969.50 Total 969.50
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Material balance of Omeprazole Stage-5:Pharma
Batch Size:100 Kg Name of the input Quantity
in Kg Name of the out put Quantity
in Kg Stage-4 96.00 Omeprazole 100.00 Hydrogen peroxide 12.00 Methanol Recovery 237.50 Methanol 250.00 Methanol Loss 12.50 Acetone 250.00 Acetone Recovery 237.50 Acetone Loss 12.50 Effluent water 5.25 (Generated Water) Organic Residue 2.75 Total 608.00 Total 608.00
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14. PANTOPRAZOLE SODIUM
Process Description
Stage-1 Maltol and Dimethyl sulphate condense in Acetone solvent medium. Excess Dimethyl sulphate is removed by treating the reaction mass with Potassium Carbonate. Reaction takes place as per the below equation.
Stage-2 Stage-1 compound on treating with Liquor Ammonia solution stage-2 compound is formed. Reaction proceeds as per the below equation
Stage-3 Stage-2 compound on reaction with Phosphorous oxy chloride produces stage-3 compound. Further reaction is stopped by treating the reaction mass with water. Final product is extracted with MDC and after distilling out MDC compound is obtained. Below is the reaction scheme.
Stage-4 Stage-3 compound when reacts with Hydrogen peroxide in presence of Acetic acid, stage-4 compound is obtained. Methanol is the solvent employed.
Stage-5 Stage-4 compound on reaction with Methanol in sodium methoxide presence produces stage-5 compound. Execs Methanol is used. Below is the reaction
Stage-6 Above stage compound on reaction with Acetic anhydride produces an intermediate.MDC used as solvent. Product is precipitated with C.S. Flakes. Below is the reaction scheme.
Stage-7 Stage-6 compound when reacts with Sodium hydroxide MDC is used as solvent.
Stage-8 Stage-7 compound when reacts with Thionyl chloride an intermediate is formed.MDC is used as solvent. Product is crystallized in Methanol. Finally product is purified with Acetone.
Stage-9 When 2-Chloromethyl-3, 4-dimethoxy-pyridine Hydrochloride reacts with 5-diFluoro methoxy-2-mercapto-benzimidazole, in presence of Sodium hydroxide, product is formed. Methylene dichloride is the solvent.
Stage-10 Stage-9 is treated with Sodium hypochlorite in presence of Sodium hydroxide, to produce the Pantoprazole sodium .This is purified in Acetone. Methylene dichloride is used as solvent.
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PANTOPRAZOLE SODIUM
Route of Synthesis:
Stage-1:
O
O
OH
CH3
Maltol
C6H6O3
2X126.11=252.22
Dimethyl sulphate
(CH3)2SO4
126.13
K2CO3
138.21
Acetone
O
O
OCH3
CH3
C7H8O3
2x140.14=280.28
K2SO4
174.26
CO2
44.0
+ + +
+ + H2O
18.0
2 2
3-Methoxy-2-methyl-pyran-4-one
Stage-2:
O
O
OCH3
CH3
C7H8O3
140.14
(NH4)2CO3
Ammonium carbonate
96.0
NH
O
OCH3
CH3
C7H9NO2139.15
+ + NH4OH + CO2 + H2O
35.0 44.0 18.03-Methoxy-2-methyl-pyran-4-one 3-Methoxy-2-methyl-
1H-pyridin-4-one
Stage-3:
NH
O
OCH3
CH3
C7H9NO2
3X139.15=417.45
+ POCl3
Phosphorous oxychloride
153.33
MDC
N
Cl
OCH3
CH3
C7H8ClNO
3X157.60=472.8
+ H3PO4
Phosphoric Acid
98.0
3 3
3-Methoxy-2-methyl-1H-pyridin-4-one
4-Chloro-3-methoxy-2-methyl-pyridine
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Stage-4:
N
Cl
OCH3
CH3
C7H8ClNO
157.60
+ H2O2
Hydrogen peroxide
34.01
MeOH
Acetic acidN
Cl
OCH3
CH3
O
3-methoxy-2-methyl-4-chloro pyridine-N-oxide
C7H8ClNO
173.60
+ H2O
18.04-Chloro-3-methoxy-2-methyl-pyridine
Stage-5:
N
Cl
OCH3
CH3
O
C7H8ClNO
173.60
+ CH3ONaMeOH
54.02
N
OCH3
OCH3
CH3
O
C8H11NO3169.18
+ NaCl
58.53,4-Dimethoxy-2-methyl
pyridine-N-oxide3,4-Dimethoxy-2-methyl
pyridine-N-oxide
Stage-6:
N
OCH3
OCH3
CH3
O
C8H11NO3
169.18
+ (CH3CO)2O
Acetic anhydride
102.09
MDC
N
OCH3
OCH3
CH2OCOCH3
C10H13NO4
211.21
+ CH3COOH
Acetic acid
60.0Acetic acid 3,4-dimethoxy-
pyridin-2-ylmethyl ester3,4-Dimethoxy-2-methyl pyridine-N-oxide
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Stage-7
N
OCH3
OCH3
CH2OCOCH3
C10H13NO4
211.21
+ NaOHMDC
N
OCH3
OCH3
CH2OH
C8H11NO3
169.18
+ CH3COONa
Sodium acetate
82.0340.0Acetic acid 3,4-dimethoxy-
pyridin-2-ylmethyl ester
(3,4-Dimethoxy-pyridin-2-yl)-methanol
Stage-8:
N
OCH3
OCH3
CH2OH
C8H11NO3
169.18
+ SOCl2
Thionyl chloride
118.97
MDC,MeOH
N
OCH3
OCH3
CH2Cl
HCl
224.12
+ SO2
Sulphur dioxide
64.02-Chloromethyl-3,4-dimethoxy-
pyridine Hydrochloride
C8H11Cl2NO2
(3,4-Dimethoxy-pyridin-2-yl)-methanol
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Stage-9:
N
OCH3
OCH3
CH2ClHCl
C8H10ClNO2.HCl
224.12
+
NHN
OF
F
SH
5-Difluoromethoxy-2-mercaptobenzimidazole
C8H6F2N2OS
216.21
+ MDC
N
OCH3
OCH3
CH2 SN
HN
OF
F
C16H15F2N3O3S
367.37
+ 2 NH4Cl + 2 H2O
Ammonium chloride
106.98
2x18.0=365-Difluoromethoxy-2-(3,4-dimethoxy-pyridin-2-ylmethylsulfanyl)-
1H-benzoimidazole
2-Chloromethyl-3,4-dimethoxy-pyridine Hydrochloride
Ammonium hydroxide
2 NH4OH
2X35.04=70.08
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Stage-10:
N
OCH3
OCH3
CH2 SN
HN
OF
F
C16H15F2N3O3S
367.37
+ NaOCl + NaOHMDC
Acetone
N
OCH3
OCH3
CH2 SN
N
OF
F
O
+ NaCl +Na
H2O
Pantoprazole sodium
C16H14F2N3NaO4S
405.35
Sodium chloride
58.5
18.0
Sodium hypochlorite
74.44
Sodium hydroxide
40.0
5-Difluoromethoxy-2-(3,4-dimethoxy-pyridin-2-ylmethylsulfanyl)-
1H-benzoimidazole
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PANTOPRAZOLE SODIUM
Flow Chart:
Stage-1
Stage-2
Stage-3
Stage-4
Stage-5
Stage-6
MaltolDimethyl sulphatePotassium carbonate
Potassium sulfate
Stage-1Ammonium CarbonateToluene
Toluene Rec
Stage-2Phosphorous oxy chlorideMDC
MDC Rec
Stage-3Hydrogen peroxide Acetic acidMethanol
Methanol Rec
Stage-4MethanolSodium methoxide
Methanol Rec
Stage-5Acetic AnhydrideChloroform
Chloroform rec
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Stage-7Thionyl chloridechloroform Stage-8 Chloroform Rec
Stage-85-diFluoromethoxy-2-mercapto-benzimidazole
Sodium chlorideStage-9
Stage-9Sodium hypochloriteSodium Hydroxide
Sodium chlorideStage-10
PANTOPRAZOLE SODIUM
Stage-6Sodium hydroxideMDC
Stage-7 MDC Rec
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PANTOPRAZOLE SODIUM
Material Balance:
Material Balance of Pantoprazole Sodium Stage-1
Batch Size: 200 Kg Name of the input Quantity
in Kg Name of the output Quantity
in Kg Maltol 66.00 Stage-1 73.00 Dimethyl sulphate 33.00 Acetone Recovery 378.00 Potassium carbonate 36.00 Acetone Loss 20.00 Acetone 400.00 Generated water 4.70 Process Emission 11.46 (Carbon dioxide) By-Product 45.60 (Potassium Sulphate) Organic Residue 2.24 (Organic Impurities-0.24,
Acetone-2)
Total 535.00 Total 535.00
Material Balance of Pantoprazole Sodium Stage-2
Batch Size: 200Kg Name of the input Quantity
in Kg Name of the output Quantity
in Kg Stage-1 73.00 Stage-2 72.00 Ammonium Carbonate 50.00 Toluene Recovery 280.00 Toluene 300.00 Toluene Loss 15.00 Water 600.00 Effluent Water 629.57 (Water-600,Ammonium
hydroxide-18.2 ,Generated water-9.37,Toluene-2)
0
Organic Residue 3.53 (Organic Impurities-0.53,
Toluene-3) 0
Process Emission 22.90 (Carbon dioxide) Total 1023.00 Total 1023.00
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Material Balance of Pantoprazole Sodium Stage-3
Batch Size: 200Kg Name of the input Quantity
in Kg Name of the output Quantity
in Kg Stage-2 72.00 Stage-3 79.00 Phosphorous oxy chloride 26.00 MDC Recovery 285.00 Ammonia 9.00 MDC Loss 15.00 Methylenedichloride 300.00 Effluent Water 600.00 Water 600.00 (Water-600) 0 By-Product 26.30 (Ammonium phosphate) 0 Organic Residue 1.70 Total 1007.00 Total 1007.00
Material Balance of Pantoprazole Sodium Stage-4
Batch Size: 200Kg Name of the input Quantity
in Kg Name of the output Quantity
in Kg Stage-3 79.00 Stage-4 87.00 Hydrogen peroxide 17.00 MDC Recovery 668.00 Acetic acid 30.00 MDC Loss 30.00 Methanol 250.00 Methanol Recovery 233.00 Sodium Hydroxide 20.00 Methanol Loss 12.50 MDC 700.00 Effluent Water 419.50 Water 400.00 (Water-400, Generated
water-17, Methanol-2.5)
By-Product 41.00 (Sodium acetate) Organic Solid Waste 5.00 (Organic Impurities-
1,MDC-2,Methanol-2)
Total 1496.00 Total 1496.00
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Material Balance of Pantoprazole Sodium Stage-5
Batch Size: 200 Kg Name of the input Quantity
in Kg Name of the output Quantity
in Kg Stage-4 87.00 Stage-5 85.00 Methanol 500.00 Methanol Recovery 465.00 Sodium methoxide 27.00 Methanol Loss 20.00 Acetic Acid 10.00 Effluent Water 642.20 Water 600.00 (Water-600, Sodium
Chloride-29.2,Methanol-3,Acetic acid-10)
0
Organic Residue 11.80 Total 1224.00 Total 1224.00
Material Balance of Pantoprazole Sodium Stage-6
Batch Size: 200Kg Name of the input Quantity
in Kg Name of the output Quantity
in Kg Stage-5 85.00 Stage-6 106.00 Acetic Anhydride 172.00 Chloroform Recovery 190.00 Chloroform 200.00 Chloroform Loss 10.00 Water 400.00 Acetic acid Recovery 101.00 Effluent Water 400.00 (Water-400) 0 Organic Residue 50.00 Total 857.00 Total 857.00
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Material Balance of Pantoprazole Sodium Stage-7
Batch Size: 200Kg Name of the input Quantity
in Kg Name of the output Quantity
in Kg Stage-6 106.00 Stage-7 85.00 MDC 200.00 MDC Recovery 190.00 Sodium hydroxide 20.00 MDC Loss 10.00 Water 200.00 Effluent Water 200.00 (Water-200) By-Product 41.00 (Sodium acetate) Total 526.00 Total 526.00
Material Balance of Pantoprazole Sodium Stage-8
Batch Size: 200Kg Name of the input Quantity
in Kg Name of the output Quantity
in Kg Stage-7 85.00 Stage-8 (Chloro
compound) 112.00
Thionyl chloride 60.00 Chloroform Recovery 810.00 Chloroform 850.00 Chloroform Loss 40.00 Methanol 125.00 Methanol Recovery 99.00 Acetone 200.00 Methanol Loss 25.00 Acetone Recovery 189.00 Acetone Loss 10.00 Process Emission 32.00 (Sulphur Dioxide) Organic Residue 3.00 (Organic Impurities-1,
Methanol-1,Acetone-1)
Total 1320.00 Total 1320.00
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Material Balance of Pantoprazole Sodium Stage-9
Batch Size: 200Kg Name of the input Quantity
in Kg Name of the output Quantity
in Kg Stage-8 112.00 Stage-9 183.00 5-diFluoromethoxy-2-mercapto- benzimidazole
108.00 Toluene Recovery 472.00
Ammonium hydroxide 35.50 Toluene Loss 25.00 Toluene 500.00 Effluent Water 619.50 Water 600.00 (Water-600, gen.Water-
18, Toluene-1.5) 0
B-Product 54.19 (Ammonium chloride) 0 Organic Residue 1.81 (Organic Impurities-0.31,
Toluene-1.5)
Total 1355.50 Total 1355.50
Material Balance of Pantoprazole Sodium Stage-10:Pharma Batch Size: 200Kg
Name of the input Quantity in Kg
Name of the output Quantity in Kg
Stage-8 183.00 Pantoprazole Sodium 200.00 Sodium hypochlorite 37.00 MDC Recovery 950.00 Sodium Hydroxide flakes 20.00 MDC Loss 50.00 Ammonium Chloride 25.00 Acetone Recovery 378.00 Methylene dichloride 1000.00 Acetone Loss 20.00 Activated Carbon 10.00 Effluent Water 465.00 Acetone 400.00 (Water-400,gen.water-9,
Sodium chloride-29, Aluminum chloride-25, Acetone-2)
0
Water 400.00 Spent carbon 10.00 Organic Residue 2.00 Total 2075.00 Total 2075.00
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15. PHENYL MAGNESIUM CHLORIDE
Process Description
Stage-1
Magnesium metal is charged into a clean and dry reactor under nitrogen purging.
Charge THF and start stirring. Raise the reactor temperature up to required
temperature. Start and continue the addition of Chlorobenzene up to completion of
the reaction. Maintain for few hours and cool to room temperature. Check Product
and unload the material into the containers under nitrogen atmosphere.
PHENYL MAGNESIUM CHLORIDE
Route of Synthesis:
Stage-1:
Mg +
Magnesium
24.31
Chlorobenzene
Cl
C6H5Cl
112.56
MgCl
C6H5ClMg
Phenyl Magnesium chloride
136.86
THF
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PHENYL MAGNESIUM CHLORIDE
Flow Chart:
Stage-1
PHENYL MAGNESIUM CHLORIDE
THF RecoveryChlorobenzeneMagnesium turningsTHF
PHENYL MAGNESIUM CHLORIDE
Material Balance:
Material Balance of phenyl Magnesium Chloride Stage-1
Batch Size: 1000.0 Kgs Name of the input Quantity
in Kg Name of the out put Quantity
in Kg
Chlorobenzene 820.00 Phenyl Magnesium Chloride in THF Solution
1750.00
Magnesium turnings 180.00 THF Loss 50.00 THF 800.00 Total 1800.00 Total 1800.00
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16. QUETIAPINE FUMARATE
Process Description:
Stage-1
2-Aminbiphenylsulphate when reacts with Phenyl chloro fumarate, the compound is
formed. Toluene is the solvent .Toluene layer is washed with water to remove acidic
salts that form during the reaction.
Stage-2
Stage-1 compound is hydrolyzed in presence of Phosphoric acid to obtain the stage-
2 compound. Acetone wash is given to remove water traces.
Stage-3
Stage-2 compound made to react with Piperazine in Toluene medium to produce the
stage -3 compound.
Stage-4
Stage-3 is converted to pharma by treating with Chloro ethoxy ethanol and Fumaric
acid in Toluene medium. Toluene layer is washed with water to remove water
soluble impurities. Finally the pharma is re-crystallized in Methanol.
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QUETIAPINE FUMARATE
Route of synthesis:
Stage-1:
O
NH2
S OOO
2-Aminodiphenyl sulphate
C12H11NO4S
265.29
+
-O O
Cl
O-O
Phenyl chloro fumarate
C10H5ClO4
224.60
Toluene
S
NH O
O
Phenyl-2-(phenyl carbamate
C19H15NO2S
321.39
+
Hydroperoxy-hydroxy-acetyl chloride
+ CO2
Carbondioxide
44.01C2HClO4
124.48
O
HO OOH
Cl
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Stage-2:
S
NH O
O
Phenyl-2-(phenyl carbamate
C19H15NO2S
321.39
S
HN
OH
Dibenzo,1,4-thiozepin,1-H-one
C13H11NOS
229.30
+Phosphoric acid
Hydrogen
H2
2.00
+
Phenol
OH
94.11
C6H6O
Stage-3:
S
HN
OH
Dibenzo,1,4-thiozepin 1-H-one
C13H11NOS
229.30
+ HN NH
Piperazine
C4H10N2
86.14
Toluene
S
HN
N
+ H2O
18.00
NH
11-Piperazin-1-yl-5a,9a,10,11-tetrahydro-dibenzo[b,f]
[1,4]thiazepineC17H19N3S
297.42
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Stage-4:
Step-A
S
HN
N
NH
11-Piperazin-1-yl-5a,9a,10,11-tetrahydro-dibenzo[b,f]
[1,4]thiazepineC17H19N3S
297.42
+ HOO
Cl
2-(2-Chloro-ethoxy)-ethanol
C4H9ClO2
124.57
Toluene
S
HN
N
NO
Cl
11-{4-[2-(2-Chloro-ethoxy)-ethyl]-piperazin-1-yl}-10,11-dihydro-dibenzo[b,f]
[1,4]thiazepineC21H26ClN3OS
403.97
+ H2O
18.00
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Step-B
S
HN
N
NO
Cl
11-{4-[2-(2-Chloro-ethoxy)-ethyl]-piperazin-1-yl}-10,11-dihydro-dibenzo[b,f]
[1,4]thiazepineC21H26ClN3OS
403.97
+
Fumaric acid
O OH
OHO
C4H4O4
116.07
S
HN
N
NO
OHO Cl
OHO
+
QuetiapineC21H27N3O2S
385.52
Chloro fumaric acid
Toluene
C4H3ClO3
134.52
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Step-C
+
Fumaric acid
O OH
OHO
C4H4O4
116.07
S
HN
N
NO
OH
Quetiapine
2X385.52=770.00
2
S
HN
N
NO
OH
2
O OH
OHO
Quetiapine fumarate
C42H50N6O4S2
C46H54N6O8S2
886.07
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QUETIAPINE FUMARATE
Flow Chart:
2-AminbiphenylsulphatePhenyl chloro fumarateToluene
Toluene RecStage-1
Stage-2Stage-1phosphoric acidAcetone
Acetone Rec
Stage-3Stage-2PiperazineToluene
Toluene Rec
Stage-4Stage-3Chloro ethoxy ethanolFumaric acidMethanol.
Methanol Rec
QUETIAPINE FUMARATE
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QUETIAPINE FUMARATE
Material Balance:
Material Balance of Quetiapine fumarate Stage-1
Batch Size: 200Kg Name of the input Quantity
in Kg Name of the out put Quantity
in Kg 2-Aminbiphenylsulphate 140.00 Stage-1 165.00 Phenyl chloro fumarate 118.50 Toluene Recovery 378.00 Toluene 400.00 Toluene Loss 20.00 Water 200.00 Effluent Water 266.60 (Water-200,Chloro-oxo
ethane peroxic acid-65.6, Toluene-1)
Process Emission 23.21 (Carbon dioxide) Organic Residue 5.69 (Organic Impurities-4.69,
Toluene-1)
Total 858.50 Total 858.50
Material Balance of Quetiapine fumarate Stage-2
Batch Size: 200Kg Name of the input Quantity
in Kg Name of the out put Quantity
in Kg Stage-1 165.00 Stage-2 115.00 phosphoric acid 46.70 Acetone Recovery 372.00 Acetone 400.00 Acetone Loss 20.00 Hydrogen gas 1.02 Effluent Water 324.80 Water 250.00 (Water-250,Acetic Acid-
20.1,Acetone-8,Phosphoric Acid-46.7)
Phenol Recovery 30.92 Total 862.72 Total 862.72
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Material Balance of Quetiapine fumarate Stage-3
Batch Size: 200Kg Name of the input Quantity
in Kg Name of the out put Quantity
in Kg Stage-2 115.00 Stage-3 140.00 Piperazine 44.00 Toluene Recovery 332.00 Toluene 350.00 Toluene Loss 17.00 Gen. Water 9.02 Organic Residue 10.98 (Organic Impurities-9.98,
Toluene-1)
Total 509.00 Total 509.00
Material Balance of Quetiapine fumarate Stage-4 Pharma
Batch Size: 200Kg Name of the input Quantity
in Kg Name of the out put Quantity
in Kg Stage-3 140.00 Quetiapine fumarate 200.00 Chloro ethoxy ethanol 59.00 Toluene Recovery 380.00 Fumaric acid 85.00 Toluene Loss 20.00 Methanol. 400.00 Methanol Recovery 377.00 Toluene 400.00 Methanol Loss 20.00 Water 800.00 Effluent Water 873.76 (Water-800,gen.water-8.46,
Methanol-2, Chloro fumaric acid-63.3)
Organic Residue 13.24 (Organic Impurities-12.24,
Methanol-1)
Total 1884.00 Total 1884.00
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17. RABEPRAZOLE SODIUM
Process Description
Stage-1
2, 3-Lutidine is reacted with Hydrogen Peroxide in presence of Acetic Acid to give N-Oxide it further reacts with Nitration mixture (Nitric Acid + Sulfuric Acid) to give Stage-1
Stage-2
Stage-1 is reacted with 3-Methoxy-1-Propanol and Sodium Hydroxide to get Stage-2 Compound
Stage-3
Stage-2 Compound is reacted with Acetic Anhydride, Sodium Hydroxide and Hydrochloric Acid to get Stage-3 Compound
Stage-4
Stage-3 Compound is reacted with Thionyl Chloride, 2Mercapto benzimidazole and sodium hydroxide in the presence of MDC as a solvent media to give stage-4 as product.
Stage-5
Stage-4 Compound is reacted with Sodium Hypochlorite to get Rabeprazole Base
Stage-6
Stage-5 reacts with Sodium hydroxide to get Rabeprazole Sodium
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RABEPRAZOLE SODIUM
Route of Synthesis:
Stage-1:
N
CH3
CH3
2,3-Lutidine
C7H9N
107.15
+ H2O2
Hydrogen peroxide
34.01
+ HNO3
Niric acid
63.0
H2SO4
N
CH3
CH3
+
O
NO2
C7H8N2O3
168.15
2H2O
36.04-Nitro-2,3-Dimethyl
pyridine-N-oxide
Stage-2:
N
CH3
CH3O
NO2
C7H8N2O3
168.15
4-Nitro-2,3-Dimethyl pyridine-N-oxide
3-Methoxy-1-Propanol
HO O
4(3-Methoxy propoxy)-2,3-Dimethyl pyridine-N-oxide
N+
O-
H3C
H3C
O O
+ NaOH+
C4H10O2
90.12 C11H17NO3
211.26
+ NaNO2 + H2O
Sodium Nitrite
69.0
18.0
40.0
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Stage-3:
4(3-Methoxy propoxy)-2,3-Dimethyl pyridine-N-oxide
N+
O-
H3C
H3C
O O
C11H17NO3
211.26
+(CH3CO)2O + NaOH
4(3-methoxy propoxy)-2-hydroxy methyl -3-methyl pyridine
hydrochloride
N
O O
HO + CH3COONa + CH3COOH
82.0 60.0
Acetic Anhydride
102.0
40.0
C11H17NO3 HCl
HCl
247.72
+ HCl
36.5
Stage-4:
4(3-methoxy propoxy)-2-hydroxy methyl -3-methyl pyridine
hydrochloride
N
O O
HO
C11H17NO3 HCl
HCl
247.72
+ SOCl2N
O O
Cl
4-(3-methoxy-propoxy)-2-Chloromethyl-3-methyl-
Pyridine
ThionylChloride
118.97 C11H16ClNO2
229.7
+ SO2
+ 2 HCl
64.0
2X36.5=73
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Stage-5:
N
O O
Cl
4-(3-methoxy-propoxy)-2-Chloromethyl-3-methyl-
pyridineC11H16ClNO2
229.7
2-Mercapto benzimidazole
N
HN
HS+ +
35.05
NCH2
O O
N
NH
S
2-[4-(3-Methoxy-propoxy)-3-methyl-pyridin-2-ylmethylsulfanyl]-1H-benzoimidazole
NH4OH
C18H21N3O2S
343.44
+ NH4Cl + H2O
53.49 18.0
C7H6N2S150.25
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Stage-6:
NCH2
O O
N
NH
S
2-[4-(3-Methoxy-propoxy)-3-methyl-pyridin-2-ylmethylsulfanyl]-
1H-benzoimidazoleC18H21N3O2S
343.44
+NaOCl NC
H2
O O
N
NH
S
O
SodiumHypochlorite
2-[4-(3-Methoxy-propoxy)-3-methyl-pyridin-2-ylmethanesulfinyl]-
1H-benzoimidazoleC18H21N3O3S
359.44
+ NaCl
58.5
74.44
Stage-7:
NCH2
O O
N
NH
S
O
2-[4-(3-Methoxy-propoxy)-3-methyl-pyridin-2-ylmethanesulfinyl]-
1H-benzoimidazoleC18H21N3O3S
359.44
+ NaOH NCH
O O
N
NH
S
O
Na
Rabeprazole Sodium40.0
+ H2O
18.0C18H20N3NaO3S
381.42
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RABEPRAZOLE SODIUM Flow Chart:
2,3 LutidineHydrogen peroxideNitric acid
Generated waterStage-1
Stage-13-Methoxy-1-propanolSodium hydroxide
Sodium nitriteStage-2
Stage-23-Methoxy-1-propanolAcetic anhydride
Stage-3 Sodium acetate
Stage-3Thionyl chloride
Sulphur dioxideStage-4
Stage-42-mercaptobenzimidazole
Stage-5 Sodium chloride
Stage-5Sodium hypochlorite
Sodium chlorideStage-6
RABEPRAZOLE SODIUM
Stage-7Stage-6Sodium hydroxide
Generated water
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RABEPRAZOLE SODIUM
Material Balance:
Material balance of Rabeprazole Sodium Stage-1
Batch Size: 100Kg Name of the input Quantity
in Kg Name of the out put Quantity
in Kg 2,3-Lutidine 46.00 Stage-1 65.00 Hydrogen Peroxide (50%) 33.00 Effluent Water 350.80 Nitric acid 38.00 (Water-300 ,Acetic Acid-
6,Hydrogen Peroxide-1.9,Nitric Acid-10.9, gen. water-15.5,Water from Hydrogen peroxide-16.5)
0
Acetic acid 6.00 Organic Residue 7.20 Water 300.00 Total 423.00 Total 423.00
Material balance of Rabeprazole Sodium Stage-2
Batch Size: 100Kg Name of the input Quantity
in Kg Name of the out put Quantity
in Kg Stage-1 65.00 Stage-2 80.00 3-Methoxy-1-Propanol 43.00 Toluene Recovery 235.00 Sodium Hydroxide 15.50 Toluene Loss 12.00 Toluene 250.00 DMSO Recovery 188.00 DMSO 200.00 DMSO Loss 10.00 Generated water 7.00 By-Product 29.70 (Sodium Nitrite-29.7) Organic Solid Waste 11.80
(Organic Impurities-6.8,
Toluene-3,DMSO-2)
Total 573.50 Total 573.50
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Material balance of Rabeprazole Sodium Stage-3
Batch Size: 100Kg Name of the input Quantity
in Kg Name of the out put Quantity
in Kg Stage-2 80.00 Stage-3 90.00 Acetic anhydride 39.00 Toluene Recovery 660.00 Sodium Hydroxide 15.00 Toluene Loss 35.00 Hydrochloric acid 20.00 Effluent Water 302.00 Toluene 700.00 (Water-300, Toluene-2) Water 300.00 Acetic Acid Recovery 25.20 By-Product 34.50 (Sodium Acetate) Organic Residue 7.30 (Organic Impurities-
4.3,Toluene-3)
Total 1154.00 Total 1154.00
Material balance of Rabeprazole Sodium Stage-4
Batch Size: 100Kg Name of the input Quantity
in Kg Name of the out put Quantity
in Kg Stage-3 90.00 Stage-4 80.00 Thionyl Chloride 53.00 MDC Recovery 710.00 MDC 750.00 MDC Loss 37.00 Sodium Sulphate 10.00 Effluent Water 426.50 Water 400.00 (Water-400,Hydrochloric
acid-26.5)
Inorganic Solid Waste 10.00 (Sodium Sulphate) Organic Residue 16.30 (Organic Impurites-13.3,
MDC-3)
Process Emission 23.20 (sulfur dioxide) Total 1303.00 Total 1303.00
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Material balance of Rabeprazole Sodium Stage-5
Batch Size: 100Kg Name of the input Quantity
in Kg Name of the out put Quantity
in Kg Stage-4 80.00 Stage-5 100.00 2-Mercaptobenzimidazole 53.00 Toluene Recovery 375.00 Ammonium hydroxide 12.50 Toluene Loss 20.00 Toluene 400.00 Effluent Water 308.42 Water 300.00 (Water-300, generated
water-6.42,Toluene-2)
By-Product 19.07 (Ammonium chloride) Organic Residue 23.01 (Organic Impurites-
20.01, Toluene-3)
Total 845.50 Total 845.50
Material balance of Rabeprazole Sodium Stage-6
Batch Size: 100Kg Name of the input Quantity
in Kg Name of the out put Quantity
in Kg Stage-5 100.00 Stage-6 100.00 Sodium Hypochlorite (8%) 327.00 MDC Recovery 570.00 MDC 600.00 MDC Loss 30.00 Acetone 150.00 Acetone Recovery 137.00 Sodium hydro sulphate 12.00 Acetone Loss 10.00 MMA in Methanol 10.00 Effluent Water 1344.30 Water 1000.00 (Water-1000,Sodium
Chloride-17,water from sodium hypochlorite-300,Sodium Hypochlorite-5.3,MMA-10, Sodium hydrosulphate-12)
0
Organic Solid Waste 7.70 (Organic Impurities-4.7,
Acetone-3) 0
Total 2199.00 Total 2199.00
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Material balance of Rabeprazole Sodium Stage-7:Pharma
Batch Size: 100Kg Name of the input Quantity
in Kg Name of the out put Quantity
in Kg Stage-6 100.00 Rabeprazole Sodium 100.00 Sodium Hydroxide 13.00 IPA Recovery 280.00 Isopropyl Alcohol 300.00 IPA Loss 15.00 Activated Carbon 10.00 Generated water 5.00 Spent carbon 10.00 Organic Residue 13.00 (Organic Impurities-
8,IPA-5)
Total 423.00 Total 423.00
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18. SODIUM METHOXIDE
Process Description
Stage-1
Sodium hydroxide reacts with Methanol to give sodium methoxide,by eliminating
water.
SODIUM METHOXIDE
Route of Synthesis
Stage-1
NaOH
Sodium hydroxide
40.00
+ CH3OH
Methanol
32.04
CH3ONa
54.02
Sodium methoxide
+ H2O
18.02
SODIUM METHOXIDE
Flow Chart
Stage-1
SODIUM METHOXIDE
Methanol RecSodium hydroxideMethanol
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SODIUM METHOXIDE
Material Balance:
Material Balance of Sodium methoxide Stage-1
Batch Size:2000Kg Name of the input Quantity
in Kg Name of the out put Quantity
in Kg Sodium hydroxide 1482.00 Sodium methoxide in Methanol 2000.00 Methanol 1700.00 Methanol Recovery 475.00 Methanol Loss 38.00 Generated water 668.00 Organic Residue 1.00 Total 3182.00 Total 3182.00
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19. SODIUM TERT BUTOXIDE
Process Description
Stage-1
Sodium is added into excess tert-butanol in a rotary drier cum reactor. Excess Tert-
Butanol is used to ensure the complete reaction of the corresponding metals. Then
the excess Tert-Butanol is recovered by thermic fluid heating through a condensor
and used again in the next batches. A small quantity of hydrogen is let out through a
liquid paraffin trap.
SODIUM TERT BUTOXIDE
Route of Synthesis
Stage-1:
Na
22.99
+
Tert-Butanol
CH3
H3C
CH3
OH
CH3
H3C
CH3
ONa
Sodium metalC4H10O
74.12
Sodium tert-butoxide
96.10
+ 1/2 H2
Hydrogen gas
1/2X2=1.00C4H9ONa
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SODIUM TERT BUTOXIDE
Flow Chart:
Stage-1SodiummetalTert-Butanol
Hydrogen gasTert-Butanol Rec
SODIUM TERT- BUTOXIDE
SODIUM TERT BUTOXIDE
Material Balance:
Material Balance of Sodium tert-Butoxide Stage-1
Batch Size:500.0 Kgs Name of the input Quantity
in Kg Name of the out put Quantity
in Kg Sodium 141.18 Sodium tert-Butoxide 500.00 Tert-Butanol 650.00 t-Butanol Recovery 271.25 t-Butanol Loss 15.48 Process Emission 4.45 (Hydrogen-4.45) Total 791.18 Total 791.18
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20. TELMISARTAN
Process Description Stage-1 Step-A Methyl-4-(butyramido)3-methyl-5-nitrobenzoate undergoes hydrogenation in the presence of Palladium carbon as catalyst by using Methanol as solvent media to give Stage-1A as product. Step-B Stage-1A product reacts with sodium hydroxide and hydrochloric acid to give Stage-1B as product. Stage-2 Stage-1 B product reacts with N-Methylbenzene-1,2-diamine in the presence of Sodium hydroxide and polyphosphoric acid to give Stage -2 as product. Stage-3 Stage-2 product reacts with 1, 3-dibromo-5, 5-dimethylimidazolidine-2,4-dione in the presence of Chloroform as solvent media to give Stage-3 as product. Stage-4 Stage-2 product reacts with Stage-3 and potassium hydroxide in the presence of acetone as solvent media to give Stage-4 as product. Stage-5 Stage-4 product reacts with potassium hydroxide and hydrochloric acid in the presence of MDC as solvent media to give stage-5 as product. Stage-6 Stage-5 product undergoes purification with Methanolic ammonia, acetic acid and activated carbon in the presence of methanol as solvent media to give Telmisartan as product.
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TELMISARTAN
Route of Synthesis:
Stage-1
Step-A
methyl-4-(buytramido)-3-methyl-5-nitrobenzoate
H3CO
O
NO2
NH
O + H2
Hydrogen
C13H16N2O5
280.28
2.0
H3CO
O
NH2
NH
OPd/C
MeOH
Methyl-3-amino-4-(buytramido)-5-methylbenzoate
C13H18N2O3
250.29
+ O2
Oxygen
32.0
Step-B
H3CO
O
NH2
NH
O
Methyl-3-amino-4-(buytramido)-5-methylbenzoate
C13H18N2O3250.29
+ NaOH + HCl
Sodium hydroxide
40.0
Hydrochloric acid
36.5
7-Methyl-2-propyl-3H-benzoimidazole-5-carboxylic acid
NH
N
O
OH
C12H14N2O2
218.25
+ CH3OH
Methanol
32.0
+ NaCl
Sodium chloride
58.5
+ H2O
Water18.0
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Stage-2
7-Methyl-2-propyl-3H-benzoimidazole-5-carboxylic acid
NH
N
O
OH
C12H14N2O2
218.25
N-Methylbenzene-1,2-diamine
NH
NH2
+
C7H10N2
122.17
4-Methyl-6-(1-methyl-1H-benzoimidazol-2-yl)-2-propyl-1H-benzo imidazole
N
NH
N
NNaOH
PPA
C19H20N4
304.39+ 2H2O
36.0
H3PO4 + 3 NaOH Na3PO4 + 3 H2O
Phosphoric Acid Sodium hydroxide Sodium phosphate Water
98.0 3X40=120 163.94 3X18=54
Stage-3
methyl-4-methyl-1,1-biphenyl-2-carboxylate
H3C
COOCH3
C15H14O2
226.27
+
1,3-Dibromo-5,5-dimethylimidazolidine-2,4-dione
NN
O
O
Br
Br
C5H6N2O2
285.92
BrH2C
COOCH3
Chloroform
4-(bromomethyl)biphenyl-2-carboxylic acid methyl ester
C15H13BrO2
305.17
+
1-Bromo-5,5-dimethylimidazolidine-2,4-dione
HNN
O
O
Br
C5H7BrN2O2
207.03
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Stage-4
4-Methyl-6-(1-methyl-1H-benzoimidazol-2-yl)-2-propyl-1H-benzo imidazole
N
NH
N
N
C19H20N4
304.39
BrH2CCOOCH3
4-(bromomethyl)biphenyl-2-carboxylic acid methyl ester
C15H13BrO2
305.17
++ KOH
Potassium hydroxide
56.11
Acetone
methyl-4-[[2n-propyl-4-methyl-6-(1-methylbenzimidazole-2-yl)-benzimidazole-1-yl]-methyl]biphenyl carboxylate
N
N
N
N
COOCH3
C34H32N4O2
528.64
+ KBr
119.0
+ H2O
18.0
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Stage-5
methyl-4-[[2n-propyl-4-methyl-6-(1-methylbenzimidazole-2-yl)-benzimidazole-1-yl]-methyl]biphenyl carboxylate
N
N
N
N
COOCH3
C34H32N4O2
528.64
+ KOH
Potassium hydroxide
56.11
+ HCl
Hydrochloric acid
36.5
N
N
N
N
COOH
MeOH
4-[[2n-Propyl-4-methyl-6-(1-methyl benzimidazole-2-yl)-benzimidazole-1-yl]-methylbiphenyl carboxylic acid
C33H30N4O2
514.62
+ CH3OH + KCl
32.0 74.55
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Stage-6
N
N
N
N
COOH
4-[[2n-Propyl-4-methyl-6-(1-methyl benzimidazole-2-yl)-benzimidazole-1-yl]-methylbiphenyl carboxylic acid
C33H30N4O2
514.62
+ CH3OH NH3
Methanolic ammonia
CH7NO
49.07
+ CH3COOH
Acetic acid
60.0
MeOH
N
N
N
N
COOH
+
Telmisaratn
C33H30N4O2
514.62
+ CH3OH
Ammonium acetate
CH3COONH4
77.08
Methanol
32.0
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TELMISARTAN
Flow chart:
Stage-155.0 Kg
ProductMethanol Rec
Effluent water
Stage-273.0 Kg
Product
Effluent water
Stage-373.50 Kg
Productn-Hexane Rec
Effluent water
Stage-1N-Methylbenzene-1,2-diaminePoly phosphoric acidSodium hydroxide
Stage-4123.0 Kg
ProductAcetone Rec
Effluent water
Stage-5115.0 Kg
ProductCarbon Dioxide
Effluent water
Stage-6100.0 Kg
ProductMethanol Rec
Effluent water
TELMISARTAN
Methyl-4-(butyramido)-3-methyl-5-nitrobenzeneMethanolPalladium carbon(Wet 5% MC)Sodium hydroxideHydrochloric acid
Methyl-4-methyl-1,1-biphenyl-2-carboxylate1,3-dibromo-5,5-dimethyl imidazolidine-2,4-dioneSodium meta bisulphateChloroformn-Hexane
Stage-4Potassium hydroxideMDCMethanolHydrochloric acid (20%)
Stage-2Stage-3Potassium hydroxideAcetone
Stage-5Methanolic ammoniaAcetic acidMethanol
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TELMISARTAN
Material Balance:
Material Balance of Telmisartan Stage-1
Batch Size: 100Kg Name of the input Quantity
in Kg Name of the out put Quantity
in Kg Methyl-4-(butyramido)-3-methyl-5-nitrobenzene
73.00 Stage-1 55.00
Methanol 865.00 Methanol Recovery 822.00 Palladium carbon(Wet 5% MC) 3.00 Methanol Loss 43.00 Sodium hydroxide 10.40 Effluent water 550.20 Hydrochloric acid 31.60 (Water-500,generated water-4.6,
Sodium chloride-15.2,Hydrochloric acid-22.1, Methanol-8.3)
Water 500.00 Palladium Carbon Reuse 3.00 Process Emission 8.33 (Oxygen) Organic Residue 1.47 Total 1483.00 Total 1483.00
Material Balance of Telmisartan Stage-2
Batch Size: 100Kg Name of the input Quantity
in Kg Name of the out put Quantity
in Kg Stage-1 55.00 Stage-2 73.00 N-Methylbenzene-1,2-diamine 32.00 Effluent Water 658.67 Phosphoric acid 90.00 (Water-600,generated water-58.67) Sodium hydroxide 110.20 By-Product 150.56 Water 600.00 (Sodium Phosphate) Organic Residue 4.97 Total 887.20 Total 887.20
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Material Balance of Telmisartan Stage-3
Batch Size: 100Kg Name of the input Quantity
in Kg Name of the out put Quantity
in Kg Methyl-4-methyl-1,1-biphenyl-2-carboxylate
57.00 Stage-3 73.50
1,3-dibromo-5,5-dimethyl imidazolidine-2,4-dione
72.00 Chloroform Recovery 304.00
Azo bis isobutyronitrile 2.90 Chloroform Loss 16.00 Sodium meta bisulphate 4.30 n-Hexane Recovery 95.00 Chloroform 320.00 n-Hexane Loss 5.00 n-Hexane 100.00 Effluent water 407.20 Water 400.00 (Water-400,Sodium meta
bisulphate-4.3,Azobis isobutyronitrile-2.9,)
By-Product 52.13 (1-Bromo-5,5-dimethyl imidazoline-
2,4-dione)
Organic Solid Waste 3.37 Total 956.20 Total 956.20
Material Balance of Telmisartan Stage-4 Batch Size: 100Kg Name of the input Quantity
in Kg Name of the out put Quantity
in Kg Stage-2 73.00 Stage-4 123.00 Stage-3 73.50 Acetone Recovery 427.00 Potassium hydroxide 18.00 Acetone Loss 22.00 Acetone 450.00 Effluent water 939.30 Water 900.00 (Water-900,generated water-4.3,
Potassium hydroxide-4.5,Acetone-2,Potassium bromide-28.5)
Organic Residue 3.20 (Organic Impurities-2.2,Acetone-1) Total 1514.50 Total 1514.50
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Material Balance of Telmisartan Stage-5
Batch Size: 100Kg Name of the input Quantity
in Kg Name of the out put Quantity
in Kg Stage-4 123.00 Stage-5 115.00 Potassium hydroxide 15.00 MDC Recovery 1138.00 MDC 1200.00 MDC Loss 60.00 Methanol 1000.00 Methanol Recovery 948.00 Hydrochloric acid (20%) 50.00 Methanol Loss 50.00 Acetic acid 40.00 Effluent water 706.20 Activated carbon 5.00 (Water-600,Potassium chloride-
17.3,Methanol-7.4,Acetic acid-40, water from HCl-40,Hydrochloric acid-1.5)
Water 600.00 Spent Carbon 5.00 Organic Residue 10.80 (Organic Impurities-6.8, Methanol-
2,MDC-2)
Total 3033.00 Total 3033.00
Material Balance of Telmisartan Stage-6
Batch Size: 100Kg Name of the input Quantity
in Kg Name of the out put Quantity
in Kg Stage-5 115.00 Telmisartan 100.00 Methanolic ammonia 50.00 Methanol Recovery 833.00 Acetic acid 20.00 Methanol Loss 40.00 Methanol 830.00 Effluent water 234.40 Activated carbon 5.00 (Water-230,Acetic acid-2.4,
Methanol-2)
By-Product (Ammonium acetate) 22.70 Water 230.00 Spent Carbon 5.00 Organic Residue 7.90 Total 1243.00 Total 1243.00
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Annexure - III
WATER CONSUMPTION DETAILS
S. No Purpose Water
Requirement In KLD
1 Process 49.82 2 Washings 2.00 3 Boiler Make up 58.50 4 Cooling towers Make up 144.50 5 DM Plant 2.00 6 Scrubbing system 2.00 7 Domestic usage 2.00 8 Gardening 5.00
Total 266.0
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Annexure - IV
HAZARDOUS WASTE DETAILS
S. No Name of the Hazardous Waste
Quantity Kg/Day Disposal Method
1 Organic waste 1254.00 Sent to Cement Industries 2 Spent Carbon 146.00 Sent to Cement Industries 3 Solvent Distillation Residue 176.00 Sent to Cement Industries 4 Inorganic Waste 279.00 Sent to TSDF 5 MEE Salts 5990.0 Sent to TSDF 6 ETP Sludge 50.00 Sent to TSDF 7 Used Oils 800
L/Annum SPCB Authorized Agencies for Reprocessing/Recycling
8 Detoxified Containers 600 No’s /
Month
After Detoxification sent back to suppliers/SPCB Authorized Parties
9 Used Lead Acid Batteries 4 No’s/ Annum
Send back to suppliers for buyback of New Batteries
Solid Waste Details 10 Coal ash from boiler 11750 Sent to Brick Manufacturers
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Annexure - V
STACK EMISSIONS FOR PROPOSED BOILERS
Particulars Units 10.0 TPH Coal fired
Boiler (Proposed)
6.0 TPH Coal fired Boiler (Stand By )
Type of Fuel -- Indian Coal Indian Coal Coal Consumption TPD 25.0 15.0 Ash Content % 47 47 Sulphur Content % 0.8 0.8 Nitrogen Content % 1.07 1.07 No. of Stacks No 1 1 Height of stack M 32 30 Diameter of Stack M 0.80 0.60 Temperature of Flue Gas oC 140 110 Velocity of Flue Gas m/s 8.50 8.50 Particulate Matter at outlet of Bag filter (Based on 115 mg/Nm3 at outlet)
gm/sec 0.74 0.62
Sulphur dioxide emission gm/sec 2.31 1.39 Oxides of Nitrogen emission gm/sec 3.01 1.86
Pollution control equipment
-
Cyclone separator followed by suitable pack of Bag filters
Cyclone separator followed by
suitable pack of Bag filters
6 TPH Coal fired boiler is kept as stand by
STACK EMISSION DETAILS FOR EXISTING & PROPOSED DG SETS
Capacity In KVA
Emission of SPM in mg/Nm3
Emission Of SO2 in mg/Nm3
Emission of NOx In mg/Nm3
Stack dia. In m
Flue Gas Temp. in
OC
Stack Height in m
Flue gas Velocity In m/sec.
275 KVA (Existing)
67.0 118.0 140.0 0.25 200 10 18.50
500 KVA (Existing) 80.0 190.0 235.0 0.30 220 12 23.20
275KVA (Proposed)
67.0 118.0 140.0 0.25 200 10 18.50
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Annexure - VI
EXPECTED PROCESS EMISSION DETAILS
S. No Name of the Gas Quantity
In Kg/Day
Treatment Method
Polluting Process Emission Details 1 Ammonia 95.00 Scrubbed by using chilled water media 2 Sulphur dioxide 248.00 Scrubbed by using C. S. Lye solution
Non- Polluting Process Emission Details 1 Carbon dioxide 150.00 Dispersed into atmosphere 2 Oxygen 8.00 Dispersed into atmosphere
3 Hydrogen 30.00 Diffused by using Nitrogen through Flame arrestor
4 Methane 103.00 Dispersed into atmosphere through Nitrogen
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Annexure - VII
LIST OF RAW MATERIALS
1. BENZYL MAGNESIUM CHLORIDE
S. No Raw Material Used /Batch in Kgs
Used/ Day in Kgs Source
1 Magnesium 160.00 53.33 Indigenous 2 Benzyl chloride 840.00 280.00 Indigenous 3 Diethyl ether 770.00 256.67 Indigenous 4 Tetrahydrofuran 1100.00 366.67 Indigenous
2. BUTYL MAGNESIUM CHLORIDE
S. No Raw Material Used /Batch in Kgs
Used/ Day in Kgs Source
1 Magnesium Metal 210.00 105.00 Indigenous 2 Butyl Chloride 790.00 395.00 Indigenous 3 THF 805.00 402.00 Indigenous
3. DOMPERIDONE
S. No Raw Material Used /Batch in Kgs
Used/ Day in Kgs Source
1 N-Carbethoxy-4-piperidone 80.00 266.67 Indigenous
2 1-(3-Chloropropyl)-1,3-dihydro-2H-benzimedazole-2-one
40.00 133.33 Indigenous
3 2,5-Dichloro Nitrobenzene 78.00 260.00 Indigenous 4 Ammonia gas 28.00 93.33 Indigenous 5 Hydrogen 10.00 33.33 Indigenous 6 Methanol 800.00 2666.67 Indigenous 7 Methyl Isobutyl Ketone 1200.00 4000.00 Indigenous 8 Raney Nickel 30.00 100.00 Indigenous 9 Sodium Carbonate 50.00 166.67 Indigenous
10 Sodium Hydroxide 75.00 250.00 Indigenous 11 Toluene 350.00 1166.67 Indigenous 12 Urea 20.00 66.67 Indigenous
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4. ESCITALOPRAM OXALATE
S. No Raw Material Used /Batch in Kgs
Used/ Day in Kgs Source
1 Bromo phthalide 110.00 110.00 Indigenous 2 Acetic acid 121.00 121.00 Indigenous 3 Acetone 1724.00 1724.00 Indigenous 4 Activated carbon 80.30 80.30 Indigenous 5 Ammonia Liq 204.00 204.00 Indigenous 6 Caustic flakes 38.30 38.30 Indigenous 7 Copper cyanide 45.00 45.00 Indigenous 8 Copper iodide 57.00 57.00 Indigenous
9 Dimethyl amino propyl magnesium chloride 76.00 76.00 Indigenous
10 DMF 2288.00 2288.00 Indigenous 11 Ethylene di amine 267.00 267.00 Indigenous 12 Fluoro bromo benzene 103.00 103.00 Indigenous 13 Hydro bromic acid 41.00 41.00 Indigenous 14 Hyflow 10.00 10.00 Indigenous 15 Iodine 3.00 3.00 Indigenous 16 IPA 4200.00 4200.00 Indigenous 17 Isopropyl ether 240.00 240.00 Indigenous 18 Magnesium turnings 28.00 28.00 Indigenous 19 Methane sulfonyl chloride 50.00 50.00 Indigenous 20 MPR 173.00 173.00 Indigenous 21 Oxalic acid 74.00 74.00 Indigenous 22 Sodium chloride 20.00 20.00 Indigenous 23 Sodium hydroxide 10.00 10.00 Indigenous 24 Sodium sulfate 260.00 260.00 Indigenous 25 Tetrahydrofuran 1000.00 1000.00 Indigenous 26 Toluene 20950.00 20950.00 Indigenous 27 Triethylamine 15.00 15.00 Indigenous
5. ESOMEPRAZOLE MAGNESIUM TRIHYDRATE
S. No Raw Material Used /Batch in Kgs
Used/ Day in Kgs Source
1 Omeprazole sulfide 88.00 146.67 Indigenous 2 Cumin hydro peroxide 41.00 68.33 Indigenous 3 Potassium hydroxide 15.20 25.33 Indigenous 4 DET 11.30 18.83 Indigenous 5 Titanium isopropoxide 2.50 4.17 Indigenous 6 NEDIPA 4.50 7.50 Indigenous 8 Toluene 320.00 533.33 Indigenous 9 Methanol 100.00 166.67 Indigenous 10 Magnesium sulfate 16.00 26.67 Indigenous
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6. ETHYL MAGNESIUM CHLORIDE
S. No Raw Material Used /Batch in Kgs
Used/ Day in Kgs Source
1 Ethyl Chloride 724.00 362.00 Indigenous 2 Mg turnings 276.00 138.00 Indigenous 3 THF 1500.00 750.00 Indigenous
7. LINEZOLID
S. No Raw Material Used /Batch in Kgs
Used/ Day in Kgs Source
1 N-[3-Phthalimido-2R-hydroxypropyl-3-fluoro-4-morpholinyl aniline
110.00 81.47 Indigenous
2 Carbonyl di imidazole 43.25 32.03 Indigenous 3 Hydrazine Hydrate 13.35 9.89 Indigenous 4 Acetic anhydride 27.23 20.17 Indigenous 5 Methanol 753.00 557.72 Indigenous 6 MDC 2682.00 1986.47 Indigenous 7 Activated carbon 10.80 8.00 Indigenous 8 Ethyl acetate 805.00 596.24 Indigenous 9 Acetone 1548.00 1146.55 Indigenous
8. LOPERAMIDE HYDROCHLORIDE
S. No Raw Material Used /Batch in Kgs
Used/ Day in Kgs Source
1 N-[(2Z)-3-(diphenylmethyl)dihydrafuran-2(3H)-ylidene]methanamine
122.00 45.18 Indigenous
2 4-(Chloro phenyl)-Piperidine-4-ol 75.00 27.78 Indigenous
3 Potassium carbonate 25.00 9.26 Indigenous 4 Potassium Iodide 1.00 0.37 Indigenous 5 Acetone 600.00 222.20 Indigenous 6 Methanol 600.00 222.20 Indigenous 7 Acetone 300.00 111.10 Indigenous 8 Methanolic HCl (10%) 125.00 46.29 Indigenous 9 Activated Carbon 20.00 7.41 Indigenous
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9. MAGNESIUM TERTIARY BUTOXIDE
S. No Raw Material Used /Batch in Kgs
Used/ Day in Kgs Source
1 Methyl Magnsium Chloride 214.00 535.00 Indigenous 2 THF 2769.30 6923.25 Indigenous 3 Tert-Butanol 200.00 500.00 Indigenous
10. METFORMIN HYDROCHLORIDE
S. No Raw Material Used /Batch in Kgs
Used/ Day in Kgs Source
1 Dimethyl amine Hcl 126.00 840.00 Indigenous 2 N-Cyano guanidine 130.00 866.67 Indigenous 3 Xylene 300.00 2000.00 Indigenous 4 Activated carbon 2.00 13.33 Indigenous 5 Hyflow 1.00 6.67 Indigenous 6 Methanol 100.00 666.67 Indigenous
11. METHYL MAGNESIUM CHLORIDE
S. No Raw Material Used /Batch in Kgs
Used/ Day in Kgs Source
1 Magnesium Metal 974.00 216.55 Indigenous 2 Methyl Chloride 2026.00 450.45 Indigenous 3 THF 1270.00 282.36 Indigenous
12. N, N-DIMETHYL PROPYL MAGNESIUM CHLORIDE
S. No Raw Material Used /Batch in Kgs
Used/ Day in Kgs Source
1 (3-Chloro-propyl)-dimethyl-amine 417.00 556.00 Indigenous
2 Magnesium turnings 84.00 112.00 Indigenous 3 EDB 1.00 1.33 Indigenous 4 Iodine 0.20 0.27 Indigenous 5 THF 1000.00 1333.33 Indigenous 6 Toluene 1000.00 1333.33 Indigenous
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13. OMEPRAZOLE
S. No Raw Material Used /Batch in Kgs
Used/ Day in Kgs Source
1 3,5-Lutidine 33.00 220.00 Indigenous
2 2-Mercapto-5-methoxy Benzimidazole 53.50 356.67 Indigenous
3 Acetic acid 25.00 166.67 Indigenous 4 Acetone 250.00 1666.67 Indigenous 5 Ammonium hydroxide 22.00 146.67 Indigenous 6 Dimethyl sulphate 38.30 255.33 Indigenous 7 Hydrogen Peroxide 23.00 153.33 Indigenous 8 Methanol 750.00 5000.00 Indigenous 9 Nitric acid 19.50 130.00 Indigenous
10 Sodium hydroxide 24.30 162.00 Indigenous 11 Sodium methoxide 16.40 109.33 Indigenous 12 Stage-1 252.00 1680.00 Indigenous 13 Thionyl Chloride 36.00 240.00 Indigenous 14 Toluene 1000.00 6666.67 Indigenous
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14. PANTOPRAZOLE SODIUM
S. No Raw Material Used /Batch in Kgs
Used/ Day in Kgs Source
1 Maltol 66.00 165.00 Indigenous
2 5-diFluoromethoxy-2-mercapto- benzimidazole
108.00 270.00 Indigenous
3 Acetic acid 40.00 100.00 Indigenous 4 Acetic Anhydride 172.00 430.00 Indigenous 5 Acetone 1000.00 2500.00 Indigenous 6 Activated Carbon 10.00 25.00 Indigenous 7 Ammonia 9.00 22.50 Indigenous 8 Ammonium Carbonate 50.00 125.00 Indigenous 9 Ammonium Chloride 25.00 62.50 Indigenous
10 Ammonium hydroxide 35.50 88.75 Indigenous 11 Chloroform 1050.00 2625.00 Indigenous 12 Dimethyl sulphate 33.00 82.50 Indigenous 13 Hydrogen peroxide 17.00 42.50 Indigenous 14 MDC 900.00 2250.00 Indigenous 15 Methanol 875.00 2187.50 Indigenous 16 Methylene dichloride 1300.00 3250.00 Indigenous 17 Phosphorous oxy chloride 26.00 65.00 Indigenous 18 Potassium carbonate 36.00 90.00 Indigenous 19 Sodium Hydroxide 40.00 100.00 Indigenous 20 Sodium Hydroxide flakes 20.00 50.00 Indigenous 21 Sodium hypochlorite 37.00 92.50 Indigenous 22 Sodium methoxide 27.00 67.50 Indigenous 24 Thionyl chloride 60.00 150.00 Indigenous 25 Toluene 800.00 2000.00 Indigenous
15. PHENYL MAGNESIUM CHLORIDE
S. No Raw Material Used /Batch in Kgs
Used/ Day in Kgs Source
1 Magnesium turnings 180.00 90.00 Indigenous 2 Chlorobenzene 820.00 410.00 Indigenous 3 THF 800.00 400.00 Indigenous
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16. QUETIAPINE FUMARATE
S. No Raw Material Used /Batch in Kgs
Used/ Day in Kgs Source
1 2-Aminbiphenylsulphate 140.00 116.67 Indigenous 2 Acetone 400.00 333.33 Indigenous 3 Chloro ethoxy ethanol 59.00 49.17 Indigenous 4 Fumaric acid 85.00 70.83 Indigenous 5 Hydrogen gas 1.02 0.85 Indigenous 6 Methanol. 400.00 333.33 Indigenous 7 Phenyl chloro fumarate 118.50 98.75 Indigenous 8 phosphoric acid 46.70 38.92 Indigenous 9 Piperazine 44.00 36.67 Indigenous
10 Toluene 1150.00 958.33 Indigenous
17. RABEPRAZOLE SODIUM
S. No Raw Material Used /Batch
in Kgs Used/ Day in
Kgs Source
1 2,3-Lutidine 46.00 76.67 Indigenous 2 2-Mercaptobenzimidazole 53.00 88.33 Indigenous 3 3-Methoxy-1-Propanol 43.00 71.67 Indigenous 4 Acetic acid 6.00 10.00 Indigenous 5 Acetic anhydride 39.00 65.00 Indigenous 6 Acetone 150.00 250.00 Indigenous 7 Activated Carbon 10.00 16.67 Indigenous 8 Ammonium hydroxide 12.50 20.83 Indigenous 9 DMSO 200.00 333.33 Indigenous
10 Hydrochloric acid 20.00 33.33 Indigenous 11 Hydrogen Peroxide (50%) 33.00 55.00 Indigenous 12 Isopropyl Alcohol 300.00 500.00 Indigenous 13 MDC 1350.00 2250.00 Indigenous 14 MMA in Methanol 10.00 16.67 Indigenous 15 Nitric acid 38.00 63.33 Indigenous 16 Sodium hydro sulphate 12.00 20.00 Indigenous 17 Sodium Hydroxide 43.50 72.50 Indigenous 18 Sodium Hypochlorite (8%) 327.00 545.00 Indigenous 19 Sodium Sulphate 10.00 16.67 Indigenous 20 Stage-1 515.00 858.33 Indigenous 21 Thionyl Chloride 53.00 88.33 Indigenous 22 Toluene 1350.00 2250.00 Indigenous
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18. SODIUM METHOXIDE
S. No Raw Material Used /Batch in Kgs
Used/ Day in Kgs Source
1 Sodium hydroxide 1482.00 1235.00 Indigenous 2 Methanol 1700.00 1416.67 Indigenous
19. SODIUM TERT BUTOXIDE
S. No Raw Material Used /Batch in Kgs
Used/ Day in Kgs Source
1 Sodium 141.18 188.24 Indigenous 2 Tert-Butanol 650.00 866.67 Indigenous
20. TELMISARTAN
S. No Raw Material Used /Batch in Kgs
Used/ Day in Kgs Source
1 Methyl-4-methyl-1,1-biphenyl-2-carboxylate 57.00 57.00 Indigenous
2 1,3-dibromo-5,5-dimethyl imidazolidine-2,4-dione 72.00 72.00 Indigenous
3 Acetic acid 80.00 80.00 Indigenous 4 Acetone 450.00 450.00 Indigenous 5 Activated carbon 10.00 10.00 Indigenous 6 Azo bis isobutyronitrile 2.90 2.90 Indigenous 7 Chloroform 320.00 320.00 Indigenous 8 Hydrochloric acid 81.00 81.00 Indigenous 9 MDC 1200.00 1200.00 Indigenous
10 Methanol 2695.00 2695.00 Indigenous 11 Methanolic ammonia 50.00 50.00 Indigenous
12 Methyl-4-(butyramido)-3-methyl-5-nitrobenzene 73.00 73.00 Indigenous
13 n-Hexane 100.00 100.00 Indigenous
14 N-Methylbenzene-1,2-diamine 32.00 32.00 Indigenous
15 Palladium carbon(Wet 5% MC) 3.00 3.00 Indigenous
16 Phosphoric acid 90.00 90.00 Indigenous 17 Potassium hydroxide 33.00 33.00 Indigenous 18 Sodium hydroxide 120.60 120.60 Indigenous 19 Sodium meta bisulphate 4.30 4.30 Indigenous
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Annexure - VIII
LIST OF BY -PRODUCTS
S. No Name of the Product Name of the By- Product
Quantity In Kg/Day
1 Ciprofloxacin Hydrochloride Piperazine Hydrochloride 41.00
2 N-Butyl Lithium Lithium Chloride 171.00 3 Ritonovir 4-Nitro phenol 46.00
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Annexure - IX
WASTE WATER DETAILS
S. No Purpose Effluent In KLD
1 Process 52.39 2 Washings 2.00 3 Boiler Blow down 8.50 4 Cooling towers Blow down 26.00 5 DM Plant Regeneration 2.00 6 Scrubbing system 2.00 7 Domestic 2.00 Total 95.00
HTDS & LTDS DETAILS
Unit HTDS KLD
LTDS KLD
Effluent Generation
in KLD
Treatment Method
Process 29.98 22.41 52.39 HTDS Effluent after neutralization, filtration sent to MEE. LTDS effluents along with MEE condensate will be sent to Biological treatment and finally to RO system RO Rejects to MEE system and RO permeate to reuse; MEE residue to ATFD for drying.
Washings 0.00 2.00 2.00 Boiler Blow down 8.50 0.00 8.50 Cooling towers Blow down 26.00 0.00 26.00 DM Plant Regeneration 2.00 0.00 2.00
Scrubbing system 2.00 0.00 2.00
Domestic 0.00 2.00 2.00 Septic tank followed by soak pit
Total 68.48 26.41 95.00