Page 1
Annexures
1 List of Products & By-Products Annexure-I
2 Manufacturing Process Description Annexure-II
3 Water Requirement Details Annexure-III
4 Waste Water Details Annexure-IV
5 Hazardous waste / Solid Waste Details Annexure-V
6 Stack Emission Details Annexure-VI
7 Process Emission Details Annexure-VII
8 List of Raw Materials Annexure-VIII
9 Consolidated Statement- Pollution Details Annexure-IX
10 Site Plan Attached
Page 2
Annexure- I
LIST OF PRODUCTS
S. No Product Name Production capacity
MT/Month
1 Albendazole 10.00
2 Biopenem 5.00
3 Carvedilol 5.00
4 Ciprofloxacin 10.00
5 Closantel Sodium 10.00
6 Dorapenem 5.00
7 Enrofloxacin 10.00
8 Gabapentin 5.00
9 Glucosamine HCl 5.00
10 Imipenem 5.00
11 Lamivudine 10.00
12 Lansoprazole 5.00
13 Meropenem 5.00
14 Nevirapine 10.00
15 Niclosamide 10.00
16 Omeprazole 5.00
17 Rafoxanide 10.00
18 Terbinafine HCl 5.00
19 Triclabendazole 10.00
20 Zudovudine 10.00
Total (Worst combination of any 10products at any given point of time)
100.00
Page 3
LIST OF BY-PRODUCTS
S. No
Name of the Product
Name of the By-Product
Quantity In Kg/Day
1 Biapenem 1-Methyl-4-nitro benzene 66.67
2 Ciprofloxacin Piperazine HCl 114.65
Ammonium acetate 71.33
3 Dorepenem Para Nitro Toluene 56.00
4 Enrofloxacin n-Ethyl piperazine 139.76
5 Glucosamine Poly glucosamine compound 81.33
6
Lamivudine
Trimethyl Silanol 142.00
Trimethyl Chloro Silane 175.80
L-Menthol 236.59
7 Meropenem TEA HCl 63.33
8 Zidovudine TEA HCl 348.00
Trityl alcohol 326.97
Page 4
Annexure- II
ALBENDAZOLE
Process Description
Stage-1
Ortho Nitro phenyl amine reacts with Ammonium thiocyanate in presence of Methanol to
give Stage-1 product.
Stage-2
Stage-1 product reacts with n-Propyl bromide to give Stage-2 product.
Stage-3
Stage-2 product reacts with Sodium Hydrosulphide in presence of Methanol to give
Stage-3 product.
Stage-4
Cyanamide reacts with Methylchloroformate to give Methyl-N-cyano carbamate.this
further reacts with Stage-3 product in presence of Acetone to give Albendazole.
Page 5
ALBENDAZOLE
Route of Synthesis:
Stage-1
NO2
NH2
2-Nitro-phenylamine
C6H6N2O2
138.12
+
Ammonium thiocyanate
2 NH4SCN
2X76.12=152.24
+ Cl2
70.19
Methanol
NO2
NH2
NCS
2-Nitro-4-thiocyanato-phenylamine
C7H5N3O2S
195.20
+ HSCN
59.09
+ 2 NH4Cl
Ammonium chloride
106.98
Page 6
Stage-2
NO2
NH2
NCS
2-Nitro-4-thiocyanato-phenylamine
C7H5N3O2S
195.20
+
n-Propyl bromide
CH3
Br
C3H7Br
122.99
NO2
NH2
SH3C
2-Nitro-4-propylsulfanyl-phenylamine
C9H12N2O2S
212.27
+
+ NaOH
Sodium Hydroxide
40.00
+ H2O
18.00
NaBr
Sodium Bromide
102.89
+ CO2
44.00
+ NH3
Ammonia gas
17.03
Page 7
Stage-3
NO2
NH2
SH3C
2-Nitro-4-propylsulfanyl-phenylamine
C9H12N2O2S
212.27
+ 2NaSH
Sodium Hydrosulphide
2X56.06=112.12
+ H2O
18.00
NH2
NH2
SH3C
4-Propylsulfanyl-benzene-1,2-diamine
C9H14N2S
182.29
+ Na2S2O3
158.11
+ H2
Sodium dithionate 2.00
Page 8
Stage-4
Step-A
NC NH2
Ctanamide
42.04
+
Methylchloroformate
O
OClCH3
C2H3ClO2
94.50
+ NaOH
Sodium hydroxide
40.00
CNNH
O
O
CH3
Methyl-N-cyano carbamide
C3H4N2O2
100.08
+NaCl
Sodium chloride
58.44
+ H2O
18.00
Acetone
Page 9
Step-B
CNNH
O
O
CH3
Methyl-N-cyano carbamide
C3H4N2O2
100.08
NH2
NH2
S
CH3
4-Propylsulfanyl-benzene-1,2-diamine
+
C9H14N2S
182.29
S
CH3
N
HN
NHCOOCH3
Albendazole
C12H15N3O2S
265.33
+NH3
Ammonia gas
17.03
Page 10
ALBENDAZOLE
Flow Chart
Stage-1
Stage-2
Stage-3
Stage-4
ALBENDAZOLE
Ortho Nitro phenyl amine Ammonium thiocyanate Methanol
Methanol Rec
Stage-1 n-Propyl bromideSodium Hydroxide
Sodium BromideEffluent water
Stage-2Sodium HydrosulphideMethanol
Methanol Rec
Stage-3Methyl chloroformateMethyl-N-cyano carbamateAcetone
Acetone Rec
Page 11
ALBENDAZOLE
Material Balance
Material Balance of Albendazole
Stage-1 Batch Size: 500.00Kgs
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
O-Nitro aniline 270.00 Stage-1 375.00
Ammonium thio cyanate 298.00 Methanol Recovery 475.00
Chlorine gas 138.00 Methanol Loss 10.00
Methanol 500.00 Effluent water 1834.63
Water 1500.00 (Water-1500,Ammonium chloride-209.12,Thiocyanic acid-115.51,Methanol-10)
Organic Residue 11.37
Process residue – 6.37
Distillation residue – 5 (Methanol -5)
Total 2706.00 Total 2706.00
Material Balance of Albendazole
Stage-2 Batch Size: 500.00Kgs
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-1 375.00 Stage-2 405.00
n-Propyl bromide 237.00 n-Propanol Recovery 475.00
Sodium hydroxide solution (50%) 77.00 n-Propanol Loss 15.00
n-Propanol 500.00 Effluent water 1672.66
Water 1500.00 (Water-1465, Sodium bromide-197.66,n-Propanol-10)
0
Process Emissions 117.23
(Carbon dioxide-84.52, Ammonia-32.71)
0
Organic Residue 4.11
Process residue – 4.11
Total 2689.00 Total 2689.00
Page 12
Material Balance of Albendazole
Stage-3 Batch Size: 500.00Kgs
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-2 405.00 Stage-3 345.00
Methanol 600.00 Methanol Recovery 570.00
Sodium hydrosulphide 214.00 Methanol Loss 12.00
Water 1500.00 Effluent water 1776.66
(Water-1465,Sodium dithionate-301.66,Methanol-10)
Process Emissions 3.81
(Hydrogen-3.81)
Organic residue 11.53
Process residue –3.53
Distillation residue – 8 (Methanol -8)
Total 2719.00 Total 2719.00
Material Balance of Albendazole
Stage-4 Batch Size: 500.00Kgs
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-3 345.00 Albendazole 500.00
Methyl chloroformate 182.00 Acetone Recovery 760.00
Cyanamide 81.00 Acetone Loss 16.00
Sodium hydroxide solution (50%) 77.00 Methanol Recovery 570.00
EDTA 1.00 Methanol Loss 12.00
Acetone 800.00 Effluent water 2136.55
Methanol 600.00 (Water-2000,Generated water-34.65,Sodium chloride-112.55, Methanol-10, Acetone- 14)
Water 2000.00 Process Emissions 32.23
(Ammonia-32.23)
Organic Residue 59.22
Process residue-41.22 Distillation residue - 18 (Methanol-8, Acetone - 10)
Total 4086.00 Total 4086.00
Page 13
BIAPENEM
Process Description
Stage-1:
Stage-A:
3-(Diphenoxy-phosphorylox)-6-(1-hydroxy-ethyl)-4-methyl-7-oxo-1-azbicyclo[3.2.0]hept-
2-ene-2-carboxylic acid 4-nitro-benzyl ester reacts with 6-Mercapto-6,7-dihydro-5H-
pyrazolo[1,2] [1,2,4] triazol-4-ylium in presence of Sodium hydroxide and Acetonitrile to
give Stage-A Product.
Stage-B:
Stage-A Product undergoes Hydrogenation with Hydrogen gas in presence of Pd/c and
Acetonitrile, THF, n-Heptane, Ethyl Acetate to give Biapenem.
Page 14
BIAPENEM
Route of Synthesis:
Stage-1
Step-A
NO
OO
NO2
H3C
OH
P OPh
OPh
OCH3
O
HH
+N
N+
NHS
6-Mercapto-6,7-dihydro-5H-pyrazolo[1,2-a][1,2,4]
triazol-4-yliumC5H8N3S
142.2
+ NaOH
40.0
HO P OPh
OPh
O
+
Phosphoric acid diphenyl ester
C12H11O4P
250.19
+ HCl
+ NaCl
58.44
36.5
+ H2O
18.02
N
OO
NO2
H3C
OH CH3
O
HH
N
N+
NS
6-[6-(1-Hydroxy-ethyl)-4-methyl-2-(4-nitro-benzyloxycarbonyl)-7-oxo-1-aza-bicyclo[3.2.0]hept-2-en-3-ylsulfanyl]-6,7-dihydro-5H-pyrazolo
[1,2-a][1,2,4]triazol-4-ylium
C22H24N5O6S
486.52
3-(Diphenoxy-phosphoryloxy)-6-(1-hydroxy-ethyl)-4-methyl-7-oxo-1-aza-bicyclo[3.2.0]hept-2-ene-2-
carboxylic acid 4-nitro-benzyl esterC29H27N2O10P
594.51
Page 15
Step-B
N
OOH
CH3
NO2
H3C
OH CH3
O
HH
N
N+
NS
C15H19N4O4S
351.4
+
1-Methyl-4-nitro-benzene
C7H7NO2
137.14
Biapenem
N
OO
NO2
H3C
OH CH3
O
HH
N
N+
NS
+ H2
2.00
Pd/C
6-[6-(1-Hydroxy-ethyl)-4-methyl-2-(4-nitro-benzyloxycarbonyl)-7-oxo-1-aza-bicyclo[3.2.0]hept-2-en-3-ylsulfanyl]-6,7-dihydro-5H-pyrazolo
[1,2-a][1,2,4]triazol-4-ylium
C22H24N5O6S
486.52
Page 16
BIAPENEM
Flow Chart:
Methyl Vinyl PhosphatePyrazole triazolium chlorideAcetonitrileTHF Palladium Carbonn-HeptaneHydrogen gasHydrochloric AcidNaOHEthyl Acetate
Acetonitrile RecoveryTHF Recoveryn-Heptane RecoveryEthyl Acetate Recovery
Stage-1
Biapenem
Page 17
BIAPENEM
Material Balance:
Material balance of Biapenem Stage-1
Batch Size:250Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
3-(Diphenoxy-phosphorylox)-6-(1-hydroxy-ethyl)-4-methyl-7-oxo-1-aza-bicyclo[3.2.0]hept-2-ene-2-carboxylic acid 4-nitro-benzyl ester
450.00 Biapenem Sodium 250.00
6-Mercapto-6,7-dihydro-5H-pyrazolo[1,2] [1,2,4] triazol-4-ylium
107.00 Acetonitrile Recovery 275.00
Acetonitrile 300.00 Acetonitrile Loss 25.00
THF 600.00 THF Recovery 570.00
Hydrogen 2.00 THF Loss 12.00
Palladium Carbon 10.00 n-Heptane Recovery 380.00
n-Heptane 400.00 n-Heptane Loss 8.00
Hydrochloric Acid 28.00 Ethyl Acetate Recovery 475.00
Sodium hydroxide 30.00 Ethyl Acetate Loss 10.00
Ethyl Acetate 500.00 Effluent Water 1272.60
DM Water 1000.00 (Water-1000,gen.Water-13.60,Diphenyl phosphoric acid sodium-189,Sodium chloride-44,Ethyl acetate-8,THF-10, n-Heptane-8)
0
Palladium Carbon Reuse 10.00
Byproduct (1-Methyl-4-nitro-benzene)
100.00
Organic Residue 39.40
(Process Residue-20.40 Distillation Residue-19.00 (Ethyl acetate-7,THF-8, n-Heptane-4)
Total 3427.00 Total 3427.00
Page 18
CARVEDILOL
Process Description:
Stage-1
9H-carbazol -4-ol reacts with (chloromethyl) oxirane in presence of Tetrahydrofuran to
give Stage-1 product
Stage-2
Stage-1 compound undergoes condensation with 2-(2-methoxyphenoxy) ethylamine in
presence of Ethyl acetate to give Carvedilol product.
Page 19
CARVEDILOL
Route of synthesis:
Stage-1
NH
OH
9H-Carbazol-4-ol
C12H9NO
183.21
+
(Chloromethyl)oxirane
OCl
C3H5ClO
92.52
THFNH
O O
4-Oxiranylmethoxy-9H-carbazole
C15H13NO2
239.27
HCl
36.46
+
Page 20
Stage-2
NH
O O
4-Oxiranylmethoxy-9H-carbazole
C15H13NO2
239.27
+
2-(2-methoxyphenoxy)ethylamine
NH2
OO
C9H13NO2
167.21
Ethyl acetate
NH
O NH
OH
O
H3CO
Carvedilol
C24H26N2O4
406.47
Page 21
CARVEDILOL
Flow Chart:
4(Oxiranyl methoxy)-9H-Carbazole(2-methoxyphenoxy)ethylamineEthyl acetateMethanol
Stage-2Ethyl acetate RecMethanol Rec
CARVEDILOL
Stage-19H-Carbazol-4-ol(Chloromethyl) oxiraneTetrahydrofuran
Tetrahydrofuran Rec
Page 22
CARVEDILOL
Material Balance:
Material balance of Carvedilol Stage-1
Batch Size:250.0 0Kg Name of the input Quantity
in Kg Name of the out put Quantity
In Kg 9H-Carbazol-4-ol 121.00 Stage-1 152.00 (Chloromethyl) oxirane 60.50 Tetrahydrofuran Recovery 428.00 Tetrahydrofuran 450.00 Tetrahydrofuran loss 10.00 Toluene 500.00 Toluene Recovery 475.00 Sodium sulfate 125.00 Toluene Loss 15.00
Water 100.00 Inorganic waste 125.00 (Sodium sulfate) 0 Effluent water 111.00
(Water-100,THF-6,Toluene-5) 0 Process Emission 23.88 (Hydrogen chloride – 23.88) 0 Organic residue 16.62 Process residue-5.62
Distillation residue-11 (THF-6,Toluene-5)
Total 1356.50 Total 1356.50
Material balance of Carvedilol Stage-2
Batch Size:250.0 0Kg Name of the input Quantity
in Kg Name of the out put Quantity
In Kg Stage-1 152.00 Carvedilol 250.00 (2-methoxyphenoxy)ethylamine 106.06 Ethyl acetate Recovery 475.00 Ethyl acetate 500.00 Ethyl acetate Loss 10.00 Sodium chloride(washing) 50.00 Effluent water 560.00 Activated carbon 20.00 (Water-500,
Sodium chloride-50, Ethyl acetate-10)
0
Sodium sulfate 125.00 Spent Carbon 20.00 Water 500.00 Inorganic waste 0 (Sodium sulfate) 125.00
Organic residue 13.06
Process residue-8.06 Distillation Residue-5 (Ethyl acetate-5)
Total 1453.06 Total 1453.06
Page 23
CIPROFLOXACIN HYDROCHLORIDE
Process Description
Stage-1
2, 4-Dichloro 5-Fluoro Acetophenone reacts with Dimethyl carbonate, Sodium Hydride
Dimethyl Formamide and Cyclo propyl Amine in presence of Toluene to give Stage-1
product.
Stage-2
Stage-1 reacts with Sodium Hydroxide and Hydrochloric acid in presence of Toluene to
give Stage-2 product
Stage-3
Stage-2 reacts with Piperazine in presence of n-Butanol to give Stage-3 product.
Stage-4
Stage-3 reacts with Acetic acid and Ammonium Hydroxide to give Stage-4 product.
Stage-5
Stage-4 reacts with Hydrochloric acid in presence of Methanol to give Ciprofloxacin
Hydrochloride product.
Page 24
CIPROFLOXACIN HYDROCHLORIDE
Route of Synthesis:
Stage-1:
Step-A
Cl
Cl
F
O CH3
2,4Dichloro 5-Fluoro Acetophenone
C8H5Cl2FO
207.03
Dimethyl Carbonate
O
OO
CH3
H3C+
C3H6O3
90.08
+ NaH
Sodium Hydride
24.00
+
Acetic acid
H3C OH
O
C2H4O2
60.05
Toluene
Cl
Cl
F
OCOOCH3
3-(2,4-Dichloro-5-fluoro-phenyl)-3-oxo-propionic acid methyl ester
C10H7Cl2FO3
265.07
+ CH3OH
Methanol
32.04
+
Sodium Acetate
CH3COONa
82.03
+ H2
Hydrogen gas
2.00
Page 25
Step-B
NaH
Sodium Hydride
24.00
Toluene
Cl
Cl
F
OCOOCH3
3-(2,4-Dichloro-5-fluoro-phenyl)-3-oxo-propionic acid methyl ester
C10H7Cl2FO3
265.07
+
Dimethyl Formamide
O N
CH3
CH3
73.09
+
Dimethyl Sulfate
S
O
O
OO
CH3
H3C+
126.13
Cl
Cl
F
OCOOCH3
HC
NH3C CH3
Dimethyl Amine Acrylate
C13H12Cl2FNO3
320.14
Sodium Methyl Sulfate
+ NaCH3SO4
134.09
+ CH3OH
Methanol
32.04
+ H2
Hydroges gas
2.00
Page 26
Step-C
Cl
Cl
F
OCOOCH3
HC
NH3C CH3
Dimethyl Amine Acrylate
C13H12Cl2FNO3
320.14
NH2
Cyclopropylamine
C3H7N
57.09
Cl
Cl
F
OCOOCH3
HC
HN
Toluene
3-Cyclopropylamino-2-(2,4-dichloro-5-fluoro-benzoyl)-acrylic acid methyl ester
C14H12Cl2FNO3
332.15
Dimethyl Amine
HN
CH3H3C+
C2H7N
45.08
Page 27
Stage-2:
Step-A
Cl
Cl
F
OCOOCH3
HC
HN
3-Cyclopropylamino-2-(2,4-dichloro-5-fluoro-benzoyl)-acrylic acid
methyl esterC14H12Cl2FNO3
332.15
+ NaOH
Sodium Hydroxide
40.00
Toluene
N
O
COOCH3
+ NaCl
Sodium Chloride
58.44
Cl
F
7-Chloro-1-cyclopropyl-6-fluoro-4-oxo-1,4-dihydro-quinoline-3-carboxylic acid
methyl esterC14H11ClFNO3
295.69
+ H2O
18.00
Page 28
Step-B
NaOH
Sodium Hydroxide
40.00
N
O
COOCH3
Cl
F
C14H11ClFNO3
295.69
+
N
O
COONa
Cl
F
Methyl ester of Fluoroquinolonic Acid
Sodium salt of Fluoroquinolonic Acid
C13H8ClFNNaO3
303.65
Water
+ CH3OH
32.04
Step-C
N
O
COONa
Cl
F
Sodium salt of Fluoroquinolonic Acid
C13H8ClFNNaO3
303.65
+ HCl
Hydrochloric acid
36.5
N
O
COOH
Cl
F
Q-Acid
C13H9ClFNO3
281.67
+ NaCl
Sodium Chloride
58.44
Page 29
Stage-3:
N
O
COOH
Cl
F
Q-Acid
C13H9ClFNO3
281.67
Piperazine
NH
HN+
N
O
COOH
N
F
HN
n-Butanol
C4H10N2
2X86.14=172.28
Ciprobase (Tech)
C17H18FN3O3
331.34
+
2
NH
HN
HCl
Piperazine Hydrochloride
C4H11ClN2
122.64
Page 30
Stage-4:
N
O
COOH
N
F
HN
Ciprobase (Tech)
C17H18FN3O3
331.34
+ CH3COOH
Acetic acid
60.05
+ NH4OH
Ammonium Hydroxide
35.05
N
O
COOH
N
F
HN
Ciprobase (Pure)
C17H18FN3O3
331.34
+ CH3COONH4
Ammonium Acetate
77.08
+ H2O
18.00
Page 31
Stage-5:
N
O
COOH
N
F
HN
Ciprobase (Pure)
C17H18FN3O3
331.34
+ HCl
Hydrochloric acid
36.5
N
O
COOH
N
F
HN
HCl
(Ciprofloxacin Hydrochloride)
C17H19ClFN3O3
367.80
1-Cyclopropyl-6-fluoro-4-oxo-7-piperazin-1-yl-1,4-dihydro-quinoline-3-carboxylic acid; HCl
Page 32
CIPROFLOXACIN HYDROCHLORIDE
Flow Chart:
Stage-1
Stage-2
Stage-3
Stage-4
Stage-5
AcetophenoneDimethyl carbonateDMFToluene
Toluene RecDMF Rec
Stage-1TolueneC.S.FlakesHydrochloric acid(36%)
Toluene Rec
Stage-2Piperazinen-Butanol n-Butanol Rec
Stage-3Acetic acidAmmonia solution(20%)
Acetic acid Rec
Stage-4Hydrochloric acid(36%)Methanol Methanol Rec
CIPROFLOXACIN HYDROCHLORIDE
Page 33
CIPROFLOXACIN HYDROCHLORIDE
Material Balance:
Material Balance of Ciprofloxacin HCl
Stage-1 Batch Size: 500.0Kgs
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Acetophenone 300.00 Stage-1 472.00
Dimethyl carbonate 131.00 Toluene Recovery 760.00
Sodium hydride 70.00 Toluene Loss 39.00
DMF 105.00 Effluent water 1968.37
Toluene 800.00 (Water-1500,Sodium acetate-118.86,Sodium Methyl sulphate-192.22, Methanol-92.94, Dimethyl amine-64.35)
DMSO 181.00 Process Emission 2.86
Acetic Acid 87.00 (Hydrogen – 2.86)
Cyclopropyl amine 82.00 Organic Residue 13.77
Water 1500.00 Process residue-12.77, Distillation residue-1 (Toluene-1)
Total 3256.00 Total 3256.00
Page 34
Material Balance of Ciprofloxacin HCl
Stage-2 Batch Size: 500.0Kgs
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-1 472.00 Q-Acid 395.00
Toluene 500.00 Toluene Recovery 475.00
C.S.Flakes 125.00 Toluene Loss 23.00
Hydrochloric acid 52.00 Effluent water 2237.86
Water 2000.00 (Water-2000,Generated water-25.57,Sodium chloride-166, Methanol-45.29,Toluene-1)
Organic Residue 18.14
Process residue-17.14, Distillation residue-1 (Toluene-1)
Total 3149.00 Total 3149.00
Material Balance of Ciprofloxacin Hydrochloride
Stage-3 Batch Size: 500.0Kgs
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-2 395.00 Stage-3 460.00
Piperazine 242.00 n-Butanol Recovery 270.00
n-Butanol 300.00 n-Butanol Loss 28.00
Water 2000.00 Effluent water 2001.00
(Water-2000,n-Butanol-1)
By-Product 171.98
(Piperazine HCl-171.98)
Organic Residue 6.02
Process residue-5.02,
Distillation residue-1 n-Butanol-1)
Total 2937.00 Total 2937.00
Page 35
Material Balance of Ciprofloxacin Hydrochloride
Stage-4 Batch Size: 500.0 Kgs
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-3 460.00 Stage-4 455.00
Acetic acid 84.00 Effluent water 1524.36
Ammonia Hydroxide 49.00 (Water-1500,Generated water-24.98)
Activated carbon 3.00 Spent carbon 3.00
Water 1500.00 By-Product 107.00
(Ammonium acetate-107)
Organic Residue 6.64
Process residue-6.64
Total 2096.00 Total 2096.00
Material Balance of Ciprofloxacin Hydrochloride
Stage-5 Batch Size: 500.0Kgs
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-4 455.00 Ciprofloxacin Hydrochloride (Pure)
500.00
Hydrochloric acid (36%) 51.00 Methanol Recovery 949.00
Methanol 1000.00 Methanol Loss 48.00
Water 2000.00 Effluent water 2002.00
(Water-2000, Methanol-2)
Organic Residue 7.00
Process residue-6, Distillation residue-1 (Methanol-1)
Total 3506.00 Total 3506.00
Page 36
CLOSANTEL SODIUM
Process Description:
Stage-1:
4-Chloro -1-methy -2-nitro –benzene undergoes condensation with Para chloro benzyl cyanide in presence of Sodium sulfide, Sodium bicarbonate, Toluene and water to give Stage -1 product. Stage – 2 Stage -1 product undergoes condensation with 2-Hydroxy 3, 5-diido benzoic acid in
presence of PCl3 and Toluene to give Closental Sodium
Page 37
CLOSANTEL SODIUM
Route of Synthesis:
Stage-1
Cl
CH2-CN
Para Chloro Benzyl Cyanide
C8H6ClN
151.59
+ Na2S
78.04
+ NaHCO3
84.01
+
H2N
H3C
Cl
Cl
N
(4-Amino-2-chloro-5-methyl-phenyl)-(4-chloro-phenyl)-acetonitrile
(Closantel Amine Intermediate)
C15H12Cl2N2
291.18
+ NaHSO4
120.06
+ Na2CO3
105.99
Toluene
2 H2O
36.02
+ 2H2
4.03
H3C
NO2
Cl
4-Chloro-1-methyl-2-nitro-benzene
C7H6ClNO2
171.58
+
Page 38
Stage-2
H2N
H3C
Cl
Cl
N
(4-Amino-2-chloro-5-methyl-phenyl)-(4-chloro-phenyl)-acetonitrile
(Amino compound)
C15H12Cl2N2
291.18
+
I
OH
COOH
I
2-Hydroxy-3,5-diiodo-benzoic acid
C7H4I2O3
389.91
+ PCl3
137.33
Toluene
HN
H3C
Cl
Cl
N
ONa
I
I
O
C22H13Cl2I2N2O2Na
Closantel Sodium Sodium phosphite
P
ONa
ONa
NaO+
147.94
+
+
4 NaOH
4X40=160.0
685.06
3X36.5=109.5
3 HCl + 2 H2O
2X18.02=36.04
Page 39
CLOSANTEL SODIUM
Flow Chart
Stage-1
4-Chloro -1-methy -2-nitro -benzenePara Chloro Benzyl CyanideMethanolSodium sulfideSodium bicarbonatePotassium hydroxideToluene
Stage-2
Stage-12-hydroxy -3,5-diiodo-benzoic acidPhosphorus trichlorideSodium HydroxideToluene Methanol
Methanol RecToluene RecEffluent water
Methanol RecToluene RecEffluent water
CLOSANTEL SODIUM
Page 40
CLOSANTEL SODIUM
Material Balance
Material balance of Closantel Sodium Stage-1
Batch Size:500Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
4-Chloro -1-methy -2-nitro -benzene 134.00 Stage-1 220.00
Para Chloro Benzyl Cyanide 118.00 Methanol Recovery 475.00
Methanol 500.00 Methanol loss 10.00
Sodium sulfide 60.80 Toluene Recovery 475.00
Sodium bicarbonate 65.50 Toluene loss 10.00
Toluene 500.00 Effluent water 2158.06
Water 2000.00 (Water-1971.95, Sodium bisulfate-93.53,Sodium carbonate-82.58, Methanol-5,Toluene-5)
Process Emission 4.15
(Hydrogen – 4.15)
Organic Residue 26.09
Process residue-6.09, Distillation Residue-20 (Methanol-10,Toluene-10)
Total 3378.30 Total 3378.30
Page 41
Material balance of Closantel Sodium Stage-2
Batch Size:500Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-1 220.00 Closantel Sodium 500.00
2-hydroxy -3,5-diiodo-benzoic acid 294.00 Methanol Recovery 475.00
Phosphorus trichloride 104.00 Methanol loss 10.00
Sodium Hydroxide 120.50 Toluene Recovery 760.00
Toluene 800.00 Toluene loss 16.00
Methanol 500.00 Effluent water 3159.44
Activated carbon 5.00 (Water-3000, Generated water-27.11,Sodium phosphite-111.33, Methanol-5, Toluene-16)
Hyflow 3.00 Process Emission 84.13
Water 3000.00 (Hydrogen chloride – 84.13)
Spent carbon & Hyflow 8.00
Organic Residue 33.93
Process residue-15.93, Distillation Residue-18 (Methanol-10,Toluene-8)
Total 5046.50 Total 5046.50
Page 42
DOREPENEM
Process Description:
Stage-1:
Methyl Vinyl Phosphate reacts with Mercapto pyrrolidine side chain, Sodium hydroxide
in presence of N-Ethyl diisopropyl amine as a Solvent of DMF. After PH adjustment with
Hydrochloric Acid get Stage-1.
Stage-2:
Protected Dorepenem Reacts with Hydrogen gas in presence of Palladium carbon as a
Catalyst.After Filtration get Dorepenem Product and get 4-Nitro benzyl alcohol By
product.
Page 43
DOREPENEM
Route of Synthesis:
Stage-1
O
O
N
NO2
O
H3C
OHH H CH3
O P
O
OPh
OPh
C29H27N2O10P
594.51
+
ON
HN
SH
O
NO2
C13H18N4O6S2
390.44
O
O
N
NO2
O
H3C
OH
H HCH3
S NH
HN
C22H29N5O8S2
555.62
HO P
O
OPh
OPh
Phosphoric acid diphenyl ester
+
C12H11O4P
250.19
+
+ NaCl58.44
+
S OO
NH2
(2S,3S)-1-p-nitrobenzyloxycarbonyl -2-sulfamylaminomethyl-4-
mercaptopyrrolidone
S OO
NH2
6-(1-Hydroxy-ethyl)-4-methyl-3-(5-methylaminomethyl-pyrrolidin-3-ylsulfanyl)
-7-oxo-1-aza-bicyclo[3.2.0]hept-2-ene-2-carboxylic acid 4-nitro-benzyl ester;
N- Ethyldiisopropylamine
N
+
C8H19N
129.24
+ NaOH
40.00
+ 2 HCl
72.92
N
. HCl
N- Ethyldiisopropylamine Hydrochloride
C8H20ClN
165.70
O
O
NO2
H
C8H7NO4
181.15
Formic acid 4-nitro-benzyl ester
3-(Diphenoxy-phosphoryloxy)-6-(1-hydroxy-ethyl)-4-methyl-7-oxo-1-aza-
bicyclo[3.2.0]hept-2-ene-2-carboxylic acid 4-nitro-benzyl ester
0.5 O2
16.00
+
Page 44
Stage-2
O
O
N
NO2
O
H3C
OHH H CH3
S NH
HN
C22H29N5O8S2
555.62
S OO
NH2
6-(1-Hydroxy-ethyl)-4-methyl-3-(5-methylaminomethyl-pyrrolidin-3-ylsulfanyl)
-7-oxo-1-aza-bicyclo[3.2.0]hept-2-ene-2-carboxylic acid 4-nitro-benzyl ester;
Pd/C, THF,Acetonitrile
CH3
NO2
OH
O
NO
H3C
OHH H CH3
S NH
HN
S OO
NH2
Dorepenem
C15H24N4O6S2
420.50
+ H2
2.00
+
Para nitro toluene
C7H7NO2
137.14
Page 45
DOREPENEM
Flow Chart:
Stage-1
Methyl vinyl phosphate
Mercapto pyrrolidine
N-Ethyl diisopropyl amine
Reactor
Sodium hydroxide
Acetonitrile
DMF
Water
Hydrochloric AcidWorkup
Rec. Acetonitrile
Rec.DMF
Stage-1
Page 46
Stage-2
Stage-1
Acetonitrile
Tetrahydrofuran
Reactor
Palladium carbon
Water
Sodium hydroxide
FiltrationHCl Rec.Actonitrile/THF
Rec. Pd/c
Dorepenem
DOREPENEM
Material Balance:
Material balance of Dorepenem Stage-1
Batch Size:250Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
3-(Diphenoxy-phosphoryloxy)-6-(1-hydroxy-ethyl)-4-methyl-7-oxo-1-aza-bicyclo[3.2.0]hept-2-ene-2-carboxylic acid 4-nitro-benzyl ester
365.00 Stage-1 340.00
(2S,3S)-1-p-nitrobenzyloxycarbonyl-2-sulfamylaminomethyl-4-mercaptopyrrolidone
246.00 Acetonitrile Recovery 285.00
Acetonitrile 300.00 Acetonitrile Loss 6.00
N-Ethyl Diispropyl Amine 82.00 DMF Recovery 285.00
DMF 300.00 DMF Loss 6.00
Sodium Hydroxide 46.00 Effluent Water 919.00
Hydrochloric acid 42.00 (Water-500, DMF-4, Sodium Chloride-36, n-DIPEA HCl-104,Acetonitrile-4,
Page 47
Diphenyl phosphoric acid-157,Formic acid 4-nitro-benzylester-114)
Water 500.00 Process emission 10.00
(Oxygen)
Organic Residue 30.00
Process Residue-20, Distillation Residue-10 (DMF-5,Acetonitrile-5)
Total 1881.00 Total 1881.00
Material balance of Dorepenem Stage-2
Batch Size:250Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-1 340.00 Dorepenem 250.00
Palladium Carbon 20.00 Acetonitrile Recovery 289.00
Hydrogen 2.00 Acetonitrile Loss 6.00
Acetonitrile 300.00 THF Recovery 289.00
Tetrahydrofuran 300.00 THF Loss 6.00
Acivated carbon 10.00 Effluent water 500.00
Water 500.00 (Water-500) 0
Palladium Carbon Recovery 20.00
Spent carbon 10.00
By- Product 84.00
(Para Nitro toluene-84) 0
Organic Residue 18.00
Process Residue-8, Distillation Residue-10 (THF-5, Acetonitrile-5)
Total 1472.00 Total 1472.00
Page 48
ENROFLOXACIN
Process Description:
Stage-1
7-Chloro-1-cyclopropyl-6-fluoro-4-oxo-1, 4-dihydro-quinoline-3-carboxylic acid (Q.Acid)
reacts with n-Ethyl Piperazine in presence of n-Butanol to give Enrofloxacin .
Page 49
ENROFLOXACIN
Route of Synthesis:
Stage-1:
7-Chloro-1-cyclopropyl-6-fluoro-4-oxo-1,4-dihydro-quinoline-3-carboxylic acid
N
O
OH
O
F
Cl
+2
N-Ethyl piperazine
N NH
n-Burtanol
Enrofloaxcin
N
O
HO
O
F
N
N+
N-Ethyl piperazine
N NH HCl
C13H9ClFNO3
C6H14N2
C6H15ClN2
359.40 150.69
281.67
228.4
C19H22FN3O3
.
Page 50
ENROFLOXACIN
Flow Chart:
Stage-1
Quinoline-3- Carboxylic acidn-Ethyl PiperazineSodium HydroxideHydrochloric Acid n-Butanol
N-Butanol Rec
ENROFLOXACIN
Page 51
ENROFLOXACIN
Material Balance:
Material Balance of Enrofloxacin Stage-1
Batch Size:500Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Quinoline-3- Carboxylic acid 405.00 Enrofloxacin 500.00
n-Ethyl Piperazine 328.00 n-Butanol Recovery 950.00
Sodium Hydroxide 11.65 n-Butanol Loss 50.00
Hydrochloric Acid 10.62 Effluent water 5034.49
n-Butanol 1000.00 (Water-5000, Sodium acetate-23.87, Hydrochloric acid-10.62)
Acetic acid 17.46 By-product 209.64
Activated Carbon 12.00 (n-Ethyl Piperazine-209.64)
Water 5000.00 Spent carbon 12.00
Organic Residue 28.60
Process residue - 28.60
Total 6784.73 Total 6784.73
Page 52
GABAPENTIN
Process Description:
Stage-1
(1-caramoylmethyl-cyclohexyl)-acetic acid reacts with sodium hypochlorite in presence
of MDC to give Stage-1 product.
Stage-2
Stage-1 compound reacts with Hydrochloric acid in presence of water to give Stage-2
product.
Stage-3
Stage-2 compound reacts with sodium hydroxide in presence of Activated carbon and
water to give Gabapentin.
Page 53
GABAPENTIN
Route of Synthesis:
Stage-1
+ NaOCl
Sodium hypochlorite
74.44
HN
O
MDC
C9H15NO
153.22
+ NaCl
58.44
+ CO2
44.01
+ H2O
18.02
C10H17NO3
199.25
O
OH
O
NH2
(1-Carbamoylmethyl-cyclohexyl)-acetic acid
2-Aza-spiro[4.5]decan-3-one
Page 54
Stage-2
HN
O
C9H15NO
153.22
+ HCl
Hydrochloric acid36.46
O
HO
NH2
H
Cl
C9H18ClNO2
207.70
+ H2O
18.022-Aza-spiro[4.5]decan-3-one (1-Aminomethyl-cyclohexyl)-acetic acid; hydrochloride
Stage-3
O
HO
NH2
H
Cl
C9H18ClNO2
207.70
+ NaOH
Sodium Hydroxide
40.0
Water
O
HO
NH2
GabapentinC9H17NO2
171.24
+ NaCl + H2O
58.44 18.02(1-Aminomethyl-cyclohexyl)-acetic
acid; hydrochloride
Page 55
GABAPENTIN
Flow Chart:
Stage-1Hydrochloric acid
Stage-2Sodium HydroxideActivated Carbon
GABAPENTIN
Effluent water
Effluent water
MDC RecEffluent waterStage-1
Stage-2
Stage-3
(1-Carbamoylmethyl-cyclohexyl)-acetic acidSodium HypochloriteMethylene Dichloride
Page 56
GABAPENTIN
Material Balance:
Material Balance of Gabapentin Stage-1
Batch Size: 250.00Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
(1-Carbamoylmethyl-cyclohexyl)-acetic acid
318.00 Stage-1 237.00
Sodium Hypochlorite 118.00 MDC Recovery 475.00
Methylene Dichloride 500.00 MDC Loss 15.00
Water 500.00 Effluent Water 621.00
(Water-500, generated water-28. Sodium Chloride-93)
0
Process Emission 70.00
(Carbon Dioxide) 0
Organic residue 18.00
Process residue-8 Distillation residue - 10 (MDC-10)
0
Total 1436.00 Total 1436.00
Material Balance of Gabapentin Stage-2
Batch Size:250.00Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-1 237.00 Stage-2 312.00
Hydrochloric acid 57.00 Effluent Water 472.10
Water 500.00 (Water-472.10)
Organic residue 9.90
Process residue-9.90
Total 794.00 Total 794.00
Page 57
Material Balance of Gabapentin Stage-3
Batch Size:250.00Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-2 312.00 Gabapentin 250.00
Sodium Hydroxide 61.00 Effluent Water 715.02
Activated Carbon 8.00 (Water-600,Generated water-27.12,Sodiumchloride-87.90)
Water 600.00 Spent Carbon 8.00
Organic Residue 7.98
Process residue-7.98
Total 981.00 Total 981.00
Page 58
GLUCOSAMINE HYDROCHLORIDE
Process Description
Stage-1
Chitin undergoes deacetylation with Hydrochloric acid in presence of Methanol to give
Glucosamine Hydrochloride.
Page 59
GLUCOSAMINE HYDROCHLORIDE
Route of Synthesis
Chitin (Pure)
C26H45N3O16
OO
H O
NHCOCH3H
CH2OH
H
O
OO
H
NHCOCH3H
CH2OH
H
H NHCOCH3
CH2OH
H
O
n
HOHOH HH
HHOH
655.65
O
HO
OH
OH
OH
NH2
HCl
+ HCl
Hydrochloric acid
36.5
Methanol
Glucosamine Hydrochloride
C6H14ClNO5
215.63
OO
H O
NHCOCH3H
CH2OH
H
O
H NHCOCH3
CH2OH
H
O HOHOH HH
+ 2 H2O
2X18=36.0
Byproduct
+
C18H32N2O11
452.45
+ CH3COOH
Acetic acid
C2H4O2
60.05
n
Page 60
GLUCOSAMINE HYDROCHLORIDE
Reaction Scheme
Stage-1
Stage-1 Product
MAINTENANCE
DECANTING -ACID
ML’S ML’S EFFLUENT
WASHINGS
Glucosamine
Hydrochloride
Water
RECYCLING TANK
Chitin
HCl
Page 61
GLUCOSAMINE HYDROCHLORIDE
Material Balance
Material Balance of Glucosamine Hydrochloride
Stage-1
Batch Size:250.0Kg’s
Name of the input Quantity
in Kg
Name of the out put Quantity
In Kg
Chitin 375.00 Glucosamine Hydrochloride 250.00
Hydrochloric acid 20.00 Methanol Recovery 760.00
Methanol 800.00 Methanol Loss 16.00
Water 1200.00 Effluent water 1225.50
(Water-1179.5,Acetic acid-
34,Methanol-12)
0
By-Product 122.00
(poly glucosamine
compound)
0
Organic Residue 21.50
Process residue-9.5,
Distillation residue-12
(Methanol-12)
Total 2395.00 Total 2395.00
Page 62
IMIPENEM
Process Description:
Stage-1:
Bi cyclic ketone Acetophenone reacts with amino ethane thiol in presence of Di
isopropyl amine, Acetonitrile and MDC, After PH adjustment with Hydrochloric Acid get
Stage-1.
Stage-2:
Stage -1 reacts with Formamidine in presence of Para toluene sulfonyl chloride .After
filtration get Stage-2
Stage-3:
Stage-2 reacts with Hydrogenation, Palladium carbon as a catalyst, Ethyl acetate using
as a solvent. After Filtration get Imipenem Product
Page 63
IMIPENEM
Route of synthesis:
Stage-1
NO
H3C
H H
O
NO2
O
OH
O
+
+
6-(1-Hydroxy-ethyl)-3,7-dioxo-1-aza-bicyclo[3.2.0]heptane-2-carboxylic acid
4-nitro-benzyl esterC16H16N2O7
348.31
2-Amino-ethanethiol
NH2HS
C2H7NS
77.15
Diisopropyl-amine
NO
H3C
H H
O
NO2
O
OH
SNH2
3-(2-Amino-ethylsulfanyl)-6-(1-hydroxy-ethyl)-7-oxo-1-aza-bicyclo[3.2.0]hept-2-ene-2-carboxylic acid
4-nitro-benzyl ester
C18H21N3O6S
407.44
H2O
18.02
Page 65
NO
H3C
H H
O
NO2
O
OH
SNH2
3-(2-Amino-ethylsulfanyl)-6-(1-hydroxy-ethyl)-7-oxo-1-aza-bicyclo[3.2.0]hept-2-ene-2-carboxylic acid
4-nitro-benzyl esterC18H21N3O6S
407.44
C2H5NO
59.07
NO
H3C
H H
O
NO2
O
OH
SNH
NH
SO2Cl
H3C
C7H7ClO2S
190.65
+
+
+
NaOH
+
Formimidic acid methyl ester
O NHH3C
Para Toluene Sulfonyl chloride
40.00
3-(2-Formimidoylamino-ethylsulfanyl)-6-(1-hydroxy-ethyl)-7-oxo-1-aza-bicyclo
[3.2.0]hept-2-ene-2-carboxylic acid 4-nitro-benzyl ester
C19H22N4O6S
434.47
Para Toluene Sulfonic acid
SO
OOH
C7H8O3S
172.20
+ NaCl
58.44
+ CH3OH
32.04
Acetonitrile
Stage-3
Page 66
NO
H3C
H H
O
NO2
O
OH
SNH
NH
+
3-(2-Formimidoylamino-ethylsulfanyl)-6-(1-hydroxy-ethyl)-7-oxo-1-aza-bicyclo
[3.2.0]hept-2-ene-2-carboxylic acid 4-nitro-benzyl ester
C19H22N4O6S
434.47
H2
2.02
Pd/C, Ethyl acetate
NO
H3C
H H
OHO
OH
SNH
NH
IMIPENEM
C12H17N3O4S
299.35
CH3
NO2
Para Nitro Toluene
C7H7NO2
137.14
+
IMIPENEM
Page 67
Flow Chart:
Stage-1
Bi cyclic ketone Acetophenone
Amino ethane thiol
Di isopropyl Amine
Acetone
MDC
Reactor
Hydrochloric Acid
Water
Rec.MDC/AcetoneWorkup
Di isopropyl amine HCl
Stage-1
Stage-2
Page 68
Stage-1
Formamidine
PTSC
Acetonitrile
EthylacetateReactor
Hydrochloric acid
Activated Carbon
Sodium hydroxide Water
FiltrationRec.Acetonitrile/Ethylacetate
Spent Carbon
Stage-2
Stage-3
Stage-2
Palladium CarbonMethanol
Ethyl Acetate
Reactor
Hexane
WaterFiltration
Rec.Ethyl acetate/Methanol
Rec.Palladium carbon
Imipenem
IMIPENEM
Page 69
Material Balance:
Material balance of Imipenem Stage-1
Batch Size:250Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
6-(1-Hydroxy-ethyl)-3,7-dioxo-1-aza-bicyclo[3.2.0]heptanes-2-carboxylic acid 4-nitro-benzyl ester
318.00 Stage-1 361.00
2-Amine -ethanethiol 70.00 Acetonitrile Recovery 570.00
Di-Isopropyl Amine 500.00 Acetonitrile Loss 24.00
Acetonitrile 600.00 MDC Recovery 285.00
MDC 300.00 MDC Loss 12.00
DM Water 1000.00 Di-Isopropyl Amine Recovery 475.00
Di-Isopropyl Amine loss 20.00
Effluent Water 1016.00
(Water-1000, Generated Water-16)
Organic Residue 25.00
Process residue-11 Distillation residue-14 ( Acetonitrile-6, MDC-3, Di-Isopropyl Amine-5)
Total 2788.00 Total 2788.00
Material Balance of Imipenem
Stage-2
Batch Size:250Kg
Name of the input Quantity
in Kg
Name of the out put Quantity
in Kg
Stage-1 361.00 Stage-2 374.00
Formimidic acid methyl ester 52.00 Acetonitrile Recovery 333.00
Para toluene sulfonyl chloride 170.00 Acetonitrile Loss 14.00
Sodium Hydroxide 35.00 Ethyl Acetate Recovery 665.00
Acetonitrile 350.00 Ethyl Acetate Loss 28.00
Ethyl Acetate 700.00 Effluent Water 1031.00
Activated Carbon 5.00 (Water-800,Sodium Chloride-51,
Methanol-28,Para Toluene
sulfonic acid-152)
Water 800.00 Spent Carbon 5.00
Organic Residue 23.00
Page 70
Process residue-13
Distillation Residue-10
(Acetonitrile-3, Ethyl acetate-7,
Total 2473.00 Total 2473.00
Material Balance of Imipenem
Stage-3
Batch Size:250Kg
Name of the input Quantity
in Kg
Name of the out put Quantity
in Kg
Stage-2 374.00 Imipenem 250.00
Palladium Carbon 5.00 Ethyl Acetate Recovery 760.00
Ethyl Acetate 800.00 Ethyl Acetate Loss 32.00
Hydrogen 2.00 Methanol Recovery 380.00
Methanol 400.00 Methanol Loss 8.00
n- Hexane 400.00 n-Hexane Recovery 390.00
Activated carbon 20.00 n-Hexane Loss 8.00
Water 750.00 Effluent Water 876.00
(Water-750, Methanol-8, Para
Nitro Toluene – 118)
Spent carbon 20.00
Spent Palladium Carbon 5.00
Organic Residue 22.00
Process residue-8
Distillation residue-14
(Ethyl acetate-8, Methanol-4, n-
Hexane-2)
Total 2751.00 Total 2751.00
Page 71
LAMIVUDINE
Process Description
Stage – 1
Step-A
L (-) Menthol is reacts with glyoxylic acid in presence of sulphuric acid and
cyclohexane to give Step-A Product.
Step-B
Step-A Product reacts with Sodium bisulphite in presence of water to give Step-B
Product.
Step-C
Step-B Product reacts with Formaldehyde in presence of water and Toluene to give
Stage-1 Product.
Stage – 2
.Stage-1 Product reacts with 1, 4, Dithiane-2, 5-diol in presence of Acetic acid and
Toluene to give Stage-2 Product.
Stage – 3
Step-A
Stage-2 Product reacts with Thionyl chloride in presence of MDC to give Step-A
Product.
Step-B
Cytosine reacts with Hexamethyl disilazane in presence of Methane sulfonic acid to
give Step-B Product.
Step-C
Step-A Product reacts with Step-B in presence of TEA to give Step-C Product.
Step-D
Step-C Product undergoes hydrolysis with water in presence of n-Hexane to give
Step-D Product.
Step-E
Page 72
Step-D Product undergoes Purification in Ethyl acetate to give Cyclohexyl ester
Tech Product.
Stage-4
Step-A
Stage-3 Product reacts with Sodium borohydride in presence of Toluene and IPA to
give Step-A Product.
Step-B
Step-A Product undergoes purification in Methanol and IPA to give Lamivudine.
LAMIVUDINE
Page 73
Route of synthesis:
Stage-1
Step-A
CH3
H3C CH3
OH
Glyoxalic acid
O
O
OH
CH3
H3C CH3
O C
O
CH
OH
OH
+H2SO4
L-Menthol
C10H20O
156.27
C2H2O3
74.04
L-Menthyl glyoxilate
C12H22O4
230.31
Step-B
CH3
H3C CH3
O C
O
CH
OH
OH
L-Menthyl glyoxilate
C12H22O4
230.31
+ NaHSO3
Sodium bisulphite
104.06
Water
CH3
H3C CH3
O C
O
CH
SO3Na
OH
Sodiumbisulphite aduct
C12H21NaO6S
316.35
+ H2O
18.0
Step-C
Page 74
CH3
H3C CH3
O C
O
CH
SO3Na
OH
Sodiumbisulphite aduct
C12H21NaO6S
316.35
+ HCHO
Formaldehyde
30.03
+ H2O
18.0
CH3
H3C CH3
O C
O
CH
OH
OH
L-Menthyl glyoxilate
C12H22O4
230.3
+
Formaldehyde bisulphite
-OS O
HNa+
O
16.0
O2
CH3O3SNa
118.09
Stage-2
CH3
H3C CH3
O C
O
CH
OH
OH
L-Menthyl glyoxilate
C12H22O4
2X230.3=460.6
S
SHO
OH
CH3
H3C CH3
O C
O
S
OOH
2
+
1,4-Dithiane-2,5-diol
C4H8O2S2
152.24
Acetic acid
Toluene
2
5-Hydroxy-1,3-oxathiolane-2-arboxylic acid(1R,2S,5R)menthyl ester
C14H24O4S
2X288.4=576.8
+ 2H2O
36.0
Stage-3
Page 75
(Step-A)
CH3
H3C CH3
O C
O
S
OOH
5-Hydroxy-1,3-oxathiolane-2-carboxylic acid(1R,2S,5R)menthyl ester
C14H24O4S
288.4
+ SOCl2
Thionyl cloride
118.97
CH3
H3C CH3
O C
O
S
OCl
5-Chloro-[1,3]oxathiolane-2-carboxylic acid-2-isopropyl-5-
methyl-cyclohexyl ester
C14H23ClO3S
306.85
+ HCl + SO2
36.5 64.06
Step-B
N
NH
NH2
O
Cytosine
C4H5N3O
111.10
+
Hexamethyl disilazane
Si
N HSi
H3C
CH3
CH3
H3CCH3
CH3
C6H19NSi2
161.39
CH3SO3H N
N
NH
O
Si(CH3)3
Si(CH3)3
Bis trimethylsilyl cytosine
C10H21N3OSi2
255.46
+ NH3
Ammonia
17.03
Step-C
Page 76
N
N
NH
O
Si(CH3)3
Si(CH3)3
Bis trimethylsilyl cytosine
C10H21N3OSi2
255.46
CH3
H3C CH3
O C
O
S
OCl
5-Chloro-[1,3]oxathiolane-2-carboxylic acid2-isopropyl-5-methyl-cyclohexyl ester
C14H23ClO3S
306.85
+
CH3
H3C CH3
O CO
S
O
N
N
NH
O
Si(CH3)3
Silyl cyclohexyl ester
C21H35N3O4SSi
453.67
+(CH3)3SiCl
Trimethyl chlorosilane
108.64
Step-D
CH3
H3C CH3
O C
O
S
O
N
N
NH
O
Si(CH3)3
Silyl cyclohexyl ester
C21H35N3O4SSi
453.67
+ H2O
18.0
CH3
H3C CH3
O C
O
S
O
N
N
NH2
O
C18H27N3O4S
381.49
+(CH3)3SiOH
Trimethyl silanol
90.60
(2R-Cis)-5-(4-amino-1,2-dihydro-2-oxo-1-pyrimidinyl1,3-oxathiolane-2-carboxylic acid(2S,5R)-Methylester
(CYCLOHEXYL ESTER TECH)
Step-E
Page 77
CH3
H3C CH3
O C
O
S
O
N
N
NH2
O
C18H27N3O4S
381.49
(2R-Cis)-5-(4-amino-1,2-dihydro-2-oxo-1-pyrimidinyl1,3-oxathiolane-2-carboxylic acid(2S,5R)-Methylester
(CYCLOHEXYL ESTER TECH)
CH3
H3C CH3
O C
O
S
O
N
N
NH2
O
C18H27N3O4S
381.49
(2R-Cis)-5-(4-amino-1,2-dihydro-2-oxo-1-pyrimidinyl1,3-oxathiolane-2-carboxylic acid(2S,5R)-Methylester
(CYCLOHEXYL ESTER TECH)
Ethylacetate
Stage-4
Page 78
CH3
H3C CH3
O C
O
S
O
N
N
NH2
O
C18H27N3O4S
381.49
CH3
H3C CH3
OH
S
O
N
N
NH2
O
HO
+
Lamivudine (Crude)
+
229.26
L-Menthol
C10H20O
156.27
K2HPO4
+ NaBH4
37.83
+
C8H11N3O3S
HCl
Hydrochloric acidSodium boro hydride(2R-Cis)-5-(4-amino-1,2-dihydro-2-oxo-1-pyrimidinyl-1,3-oxathiolane-2-
carboxylic acid(2S,5R)-Methylester
Toluene
36.5
NaCl
Sodium chloride
58.44
+ 3 H2O
+ H3BO3
Boric acid
61.83
3X18.02=54.06
+ 2 H2
4.03
Stage-5
Page 79
S
O
N
N
NH2
O
HO
Lamivudine (Crude)
229.26
C8H11N3O3S
Methanol,IPA
S
O
N
N
NH2
O
HO
Lamivudine Pure)
229.26
C8H11N3O3S
LAMIVUDINE
Page 80
Flow-chart:
L(-) MentholGlyoxylic Acid (50%)Sulphuric AcidSodium Carbonate Sodium BisulphiteFormaldehyde Cyclohexane
Stage - 1Acetic acid2,5-Dithiane-1,4-diolHyflow Triethylaminen-Hexane Toluene
Toluene + Acetic Acid Recoveryn-Hexane Recovery
Stage- 2Thionyl chlorideHexamethyldisilazane cytosineToluenen-HexaneEthyl AcetateMethylene dichloride
MDC Recoveryn-Hexane RecoveryEthyl acetate RecoveryToluene Recovery
Stage-1
Stage-2
Stage-3
Cyclohexane RecoveryEffluent water
Stage -3Dipotassium hydrogen ortho phosphateSodium BorohydrideActivated CarbonConc. HClTolueneMethanolIso propyl alcohol
Toluene RecoveryIsopropyl alcohol RecoveryMethanol Recovery
Stage-4
Lamivudine
LAMIVUDINE
Page 81
Material Balance:
Material balance of Lamivudine Stage-1 Batch size : 500kg
Name of the input Quantity In kg
Name of the out put Quantity In kg
L(-) Menthol 443.00 Stage-1 595.00
Glyoxylic Acid (50%) 420.00 Cyclohexane Recovery 598.00
Sulphuric Acid 3.00 Cyclohexane Loss 12.00
Sodium Carbonate 15.00 Effluent water 1039.51
Sodium Bisulphite 286.00 (Water-752.05, Generated water-49.45, Sodium carbonate-15, Cyclo hexane-10, Sulfuric acid-3, Water from Glyoxylic acid-210)
Formaldehyde 80.00 Process emission 42.62
Cyclohexane 630.00 (Oxygen)
Water 800.00 Organic residue 389.87
Process Residue-379.87 (Formaldehyde bi sulphate-314.64) Distillation residue-10 (Cyclo hexane-10)
Total 2677.00 Total 2677.00
Material balance of Lamivudine
Page 82
Stage-2 Batch size : 500kg
Name of the input Quantity In kg
Name of the out put Quantity In kg
Stage - 1 595.00 Stage- 2 722.00
Acetic acid 18.00 Toluene + Acetic Acid Recovery 683.00
2,5-Dithiane-1,4-diol 196.50
Toluene Loss 14.00
Hyflow 5.00 n-Hexane Recovery 218.00
Triethylamine 3.00 n-Hexane Loss 4.00
n-Hexane 230.00 Generated Water 46.50
Toluene 700.00 Spent Hyflow 5.00
Organic residue 55.00
Process residue-26 (Triethylamine-3) Distillation Residue-29 (n- Hexane-8, Toluene-21)
Total 1747.50 Total 1747.50
Material balance of Lamivudine Stage-3 Batch size : 500kg
Name of the input Quantity In kg
Name of the out put Quantity In kg
Stage- 2 722.00 Stage-3 867.00
Thionyl chloride 298.00 MDC Recovery 950.00
Methane Sulphonic Acid 2.00 MDC loss 30.00
Hexamethyldisilazane 404.00 Triethylamine Recovery 209.00
cytosine 279.00 Triethylamine Loss 4.00
Toluene 388.00 n-Hexane Recovery 190.00
Triethylamine 220.00 n-Hexane Loss 4.00
n-Hexane 200.00 Ethyl acetate Recovery 142.00
Ethyl Acetate 150.00 Ethyl acetate Loss 3.00
Methylene dichloride 1000.00 Toluene Recovery 368.00
Water 1000.00 Toluene Loss 7.00
By Products 476.70
(trimethyl silanol-213,
Tri methyl chloro silane-263.7)
Effluent water 972.69
(water -957.69 , Methane sulfonic acid-2, TEA-3, n-Hexane-3, Toluene-5,Ethyl acetate-2)
Process emission 294.47
Page 83
(Hydrogen chloride-91.36, Sulphur dioxide-160.5, Ammonia-42.61)
Organic Residue 145.14
Process Residue-107.14 Distillation Residue-38 ( MDC-20, Ethyl acetate-3, n-Hexane-3, Toluene-8, Triethylamine-4)
Total 4663.00 Total 4663.00
Material balance of Lamivudine Stage-4 Batch size : 500kg
Stage -3 867.00 Stage-4 505.00
Sodium Borohydride 86.00 Toluene Recovery 190.00
Activated Carbon 8.00 Toluene Loss 4.00
Conc. HCl 83.00 Isopropyl alcohol Recovery 570.00
Toluene 200.0 Isopropyl alcohol Loss 12.00
Methanol 800.00 Methanol Recovery 760.00
Iso propyl alcohol 600.00 Methanol Loss 16.00
Water 1500.0 By-product 354.88
(L-Menthol – 354.88)
Spent Carbon 8.00
Effluent water 1674.15
(Water-1377, Boric acid-140.43, Sodium chloride-132.72, Toluene-3,IPA-9, Methanol-12)
Process emission 9.15
(Hydrogen)
Organic residue 40.82
Process Residue-16.82, Distillation Residue-24 (IPA-9, Toluene-3, Methanol-12)
Total 4144.00 Total 4144.00
Page 84
Material balance of Lamivudine Stage-5 Batch size : 500kg
Stage -4 505.00 Lamivudine 500.00
Methanol 400.00 Methanol Recovery 380.00
IPA 50.00 Methanol Loss 16.00
IPA Recovery 48.00
IPA Loss 2.00
Organic residue 9.00
Process residue -5.00 Distillation residue- 4 (Methanol-4)
Total 955.00 Total 955.00
Page 85
LANSOPRAZOLE
Process Description
Stage-1
2, 3-Lutidine reacts with Hydrogen Peroxide and Nitric Acid in Presence of Acetic acid
to give stage-1 product.
Stage-2
Stage-1 Product reacts with 2, 2, 2- trifluoroehtanol and Acetic Anhydride in presence of
Potassium Carbonate to give stage-2 product.
Stage-3
Stage-2 product undergoes chlorination with Thionyl Chloride inpresence of Toluene to
give stage-3 product.
Stage-4
Stage-3 product undergoes condensation with 2-Mercapto benzimidazole in presence of
Sodium Hydroxide to give stage-4 product.
Stage-5
Stage-4 product undergoes oxidation with Hydrogen peroxide in presence of IPA to give
Lansoprazole.
Page 86
LANSOPRAZOLE
Route of Synthesis:
Stage-1
N
CH3
CH3
2,3-Lutidine
107.15
+ H2O2
34.00
+ HNO3
63.00
N
NO2
CH3
CH3
O + 2
4-Nitro-2,3-Dimethyl pyridine-N-Oxide
168.15
H2O
C7H9N
C7H8N2O3
36.04
Page 87
Stage-2
N
NO2
CH3
CH3
O
+
4-Nitro-2,3-Dimethyl pyridine-N-Oxide
168.00
CF3CH2OH + K2CO3 + (CH3CO)2O + NaoH + HCl
Trifluoro ethanol
Potassium carbonate
Acetic anhydride
Sodium hydroxide
Hydrogen chloride
100 138 102 40 36.5
N
OCH2CF3
CH3
CH2OH
. HCl
2-Hydroxy methyl-3-methyl pyridine hydrochloride
257.5
+ KHCO3
Potassium bicarbonate
100
+ KNO2
Potassium nitrite
85
+ CH3COONa
Sodium acetate
82
+ CH3COOH
Acetic acid
60
C7H8N2O3
C9H11ClF3NO2
Stage-3
N
OCH2CF3
CH3
CH2OH
. HCl
2-Hydroxy methyl-3-methyl pyridine hydrochloride
257.5
+ SOCl2
Thionyl chloride
119
N
OCH2CF3
CH3
CH2Cl
. HCl
2-Chloromethyl-3-methyl pyridine hydrochloride
276
+ SO2
64
+ HCl
36.5
C9H11ClF3NO2
C9H10Cl2F3NO
Page 88
Stage-4
N
OCH2CF3
CH3
CH2Cl
. HCl
2-Chloromethyl-3-methyl pyridine hydrochloride
276
+N
HN
HS + 2 NaoH
2-Mercapto benzimidazole
Sodium hydroxide
2x40=80.0
150
N
OCH2CF3
CH3
CH2 S
N
HN
2[4-(2,2,2-Tri fluoro ethoxy)-3-methylpyridinyl]methyl thio]-1H-Benzimidazole
+ 2 NaCl
Sodium chloride
2x58.5=117.0
+ 2H2O
Water
36.0
C9H10Cl2F3NO C7H6N2S
C16H14F3N3OS
353.0
Page 89
Stage-5
N
OCH2CF3
CH3
CH2 S
N
HN
2[4-(2,2,2-Tri fluoro ethoxy)-3-methylpyridinyl]methyl thio]-1H-Benzimidazole
353
+ H2O2
Hydrogen peroxide
34
N
OCH2CF3
CH3
CH2 S
N
HN
O
Lansoprazole
369
+ H2O
Water
18
C16H14F3N3OS
C16H14F3N3O2S
Page 90
LANSOPRAZOLE
Flow Chart:
Stage - 1
Stage - 2
2,3-LutidineAcetic AcidHydrogen Peroxide Sulfuric AcidNitric Acid
Generated water
Stage-1Sodium HydroxidePotassium CarbonateTri Fluoro EthanolToluene
Potassium nitritePotassium bicarbonateSodium acetateToluene Recovery
Stage-2Methylene DichlorideTolueneThionyl Chloride
Sulphur dioxiodeHydrogen chlorideToluene Recovery
Stage - 3
Stage-3Sodium Hydroxide2-Mercapto Benzimidazole
Generated waterSodium chloride
Stage - 4
Stage - 5
Stage-4Isopropyl AlcoholHydrogen Peroxide ChloroformAcetoneAcetic Acid
Generated waterIsopropyl alcohol RecoveryAcetone Recovery
Lansoprazole
Page 91
LANSOPRAZOLE
MATERIAL BALANCE:
Material Balance of Lansoprazole
Stage-1
Batch Size:250Kg
Name of the input Quantity
in Kg
Name of the out put Quantity
in Kg
2,3-Lutidine 84.00 Stage-1 128.00
Hydrogen Peroxide (50%) 30.00 Spent Sulfuric Acid 50.00
Sulfuric Acid 50.00 Effluent water 534.00
Nitric Acid 49.00 (Water-500, gen.water-28,water from
hydrogen peroxide-6)
0
Water 500.00 Organic Residue 1.00
Total 713.00 Total 713.00
Material Balance of Lansoprazole
Stage-2
Batch Size:250Kg
Name of the input Quantity
in Kg
Name of the out put Quantity
in Kg
Stage-1 128.00 Stage-2 190.00
Sodium Hydroxide 30.00 MIBK Recovery 124.00
Potassium Carbonate 105.00 MIBK Loss 3.00
Tri Fluoro Ethanol 76.00 Toluene Recovery 214.00
MIBK 130.00 Toluene Loss 5.00
Acetic Anhydride 77.00 Effluent Water 610.00
TEBAC 1.00 (Water-500, Sodium Acetate-62,
Acetic Acid-45,Toluene-3)
Toluene 225.00 Inorganic solid waste 140.00
Hydrogen Chloride Gas 27.00 (Potassium Nitrite-64, Potassium
Bicarbonate-76)
Activated Carbon 3.00 Spent Carbon 3.00
Water 500.00 Organic Residue 13.00
Process Residue-7
Distillation Residue-6
(MIBK-3,Toluene-3)
Total 1302.00 Total 1302.00
Page 92
Material Balance of Lansoprazole
Stage-3
Batch Size:250Kg
Name of the input Quantity
in Kg
Name of the out put Quantity
in Kg
Stage-2 190.00 Stage-3 198.00
Methylene Dichloride 200.00 Toluene Recovery 238.00
Toluene 250.00 Toluene Loss 5.00
Thionyl Chloride 88.00 Methylene Dichloride Recovery 190.00
Methylene Dichloride Loss 4.00
Process Emissions 74.00
(Sulfur Dioxide-47,Hydrogen
Chloride-27)
Organic Residue 19.00
Process residue-6
Distillation Residue-13
(Toluene-7, MDC-6)
Total 728.00 Total 728.00
Material Balance of Lansoprazole
Stage-4
Batch Size:250Kg
Name of the input Quantity
in Kg
Name of the out put Quantity
in Kg
Stage-3 198.00 Stage-4 246.00
Sodium Hydroxide 57.00 Effluent Water 649.00
2-Mercapto Benzimidazole 107.00 (Water-540, gen.Water-25,Sodium
Chloride-84)
Water 540.00 Organic Residue 7.00
Process Residue-7
Total 902.00 Total 902.00
Page 93
Material Balance of Lansoprazole
Stage-5
Batch Size:250Kg
Name of the input Quantity
in Kg
Name of the out put Quantity
in Kg
Stage-4 246.00 Lansoprazole Pharma 250.00
Isopropyl Alcohol 250.00 Isopropyl Alcohol Recovery 238.00
Hydrogen Peroxide (50%) 30.00 Isopropyl Alcohol Loss 5.00
Catalyst 1.00 Chloroform Recovery 384.00
Chloroform 400.00 Chloroform Loss 12.00
Acetone 150.00 Acetone Recovery 143.00
Water 400.00 Acetone Loss 3.00
Effluent Water 428.00
(Water-400, gen.Water-12,Water
from Hydrogen Peroxide-10,
Acetone-2,IPA-4)
Catalyst Reuse 1.00
Organic Residue 13.00
Process residue-4
Distillation residue-9
(IPA-3, Chloroform-4,Acetone-2)
Total 1477.00 Total 1477.00
Page 94
MEROPENEM
Process Description:
Stage-1:
Methyl Vinyl Phosphate reacts with Mercapto side chain and Sodium hydroxide as a
solvent of Acetonitrile and MDC.After PH Adjustment with Hydrochloric acid get Stage-
1.
Stage-2:
Stage-1reacted with Hydrogen gas Palladium carbon As a Catalyst .Ethyl acetate as a
solvent using this reaction. After Filtration get Meropenem tech and finally get 4-nitro
toluene by product.
Page 95
MEROPENEM
Route of Synthesis:
Stage-1
O
O
N
NO2
O
H3C
OHH H CH3
O PO
OPhOPh
3-(Diphenoxy-phosphoryloxy)-6-(1-hydroxy-ethyl)-4-methyl-7-oxo-1-aza-bicyclo[3.2.0]hept-2-ene-2-
carboxylic acid 4-nitro-benzyl esterC29H27N2O10P
594.51
+
ON
OMe2N
SH
O
NO2
2-Dimethylcarbamoyl-4-mercapto-pyrrolidine-1-carboxylic acid
4-nitro-benzyl ester
C15H19N3O5S
353.39
+
Triethylamine
N
C6H15N
101.19
NaOH
40.00
+ 2 HCl
72.92
O
O
N
NO2
O
H3C
OHH H CH3
S
+
O
N
OMe2N
O NO2
3-[5-Dimethylcarbamoyl-1-(4-nitro-benzyloxycarbonyl)-pyrrolidin-
3-ylsulfanyl]-6-(1-hydroxy-ethyl)-4-methyl-7-oxo-1-aza-bicyclo[3.2.0]
hept-2-ene-2-carboxylic acid 4-nitro-benzyl ester
C32H35N5O11S
697.71
HO P
O
OPh
OPh
Phosphoric acid diphenyl ester
+
C12H11O4P
250.19
+ (C6H14)NH HCl
137.65
+ NaCl
58.44
+ H2O
18.02Triethyl amine Hydrochloride
Page 96
Stage-2
O
O
N
NO2
O
H3C
OHH H CH3
S
O
N
O
Me2N
O NO2
3-[5-Dimethylcarbamoyl-1-(4-nitro-benzyloxycarbonyl)-pyrrolidin-3-yl
sulfonyl]-6-(1-hydroxy-ethyl)-4-methyl-7-oxo-1-aza-bicyclo[3.2.0]
hept-2-ene-2-carboxylic acid 4-nitro-benzyl ester
C32H35N5O11S
697.71
Ethyl acetate,Pd/C
OH
O
NO
H3C
OHH H CH3
S NH
O
Me2N CH3
NO2
O
O NO2H
1-Methyl-4-nitro-benzene
Meropenem
C17H25N3O5S
383.46
+
C8H7NO4
181.15
+
C7H7NO2
137.14
Formic acid 4-nitro-benzyl ester
+ 2 H2
4.03
MEROPENEM
Page 97
Flow Chart:
Stage-1
Methyl vinyl phosphate
Mercapto side chain
Triethyl amine Sodium hydroxide
Acetonitrile
MDCReactor
Water
Hydrochloric Acid Rec. MDC
Rec. Acetonitrile
Stage-1
Workup
Stage-2
Page 98
Stage-1Ethyl Acetate
Isopropyl Alcohol
Reactor
n-Hexane
Hexane
Water
Palladium carbon
FiltrationRec.Ethyl Acetate
Rec.Palladium carbon
Meropenem
Rec.Isopropyl Alcohol
4-Nitro toluene
MEROPENEM
Page 99
Material Balance:
Material balance of Meropenem Stage-1
Batch Size:250Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
3-(Diphenoxy-phosphoryloxy)-6- (1-hydroxy-ethyl)-4-methyl-7-oxo- 1-aza-bicyclo[3.2.0]hept-2-ene-2- carboxylic acid 4-nitro-benzyl ester
430.00 Stage-1 469.00
2-Dimethylcarbamoyl-4-mercapto- pyrrolidine-1-carboxylic acid 4-nitro-benzyl ester
245.00 Acetonitrile Recovery 570.00
Acetonitrile 600.00 Acetonitrile Loss 30.00
Triethylamine 70.00 MDC Recovery 570.00
MDC 600.00 MDC Loss 30.00
Sodium Hydroxide 50.00 Byproduct (TEA HCl- 95) 95.00
Water 800.00 Effluent water 1025.00
(Water-800, gen.water-12,Sodium chloride-40, Diphenyl phosphoric acid-173)
0
Organic Residue 6.00
Process residue-6
Total 2795.00 Total 2795.00
Material balance of Meropenem
Stage-2
Batch Size:250Kg
Name of the input Quantity
in Kg
Name of the out put Quantity
in Kg
Stage-1 469.00 Meropenem 250.00
10% Palladium Carbon 5.00 Ethyl Acetate Recovery 970.00
Hydrogen 3.000 Ethyl Acetate Loss 30.00
Ethyl Acetate 1000.00 Isopropyl Alcohol Recovery 670.00
Isopropyl Alcohol 700.00 Isopropyl Alcohol Loss 25.00
Hexane 350.00 n-Hexane Recovery 335.00
Water 950.00 n-Hexane Loss 15.00
Effluent Water 955.00
(Water-950,Isopropyl Alcohol-5)
Page 100
10% Palladium Carbon Reuse 5.00
Organic Residue 222.00
Process Residue-7.99
Distillation Residue-214.10
(Formic acid 4-Nitro-benzyl
ester-122,1-Methyl-4-Nitro-
benzene-92)
Total 3477.00 Total 3477.00
NEVIRAPINE
Page 101
Description:
Stage – 1
Nevirapine amide reacts with calcium oxide and cyclopropylamine in presence of o-
xylene to give stage-1 product.
Stage – 2
Stage-1 product undergoes reduction with Sodium hydride in presence of Diglyme,
Acetic Acid and O–xylene to give Nevirapine Crude.
Stage – 3
Nevirapine crude undergoes purification in methanol and Carbon to give Nevirapine.
NEVIRAPINE
Page 102
Route of synthesis:
Stage -1:
N Cl HN
HN
N
OCH3
N Cl Cl
HN
N
OCH3
C12H9Cl2N3O
282.12
+
Cyclo propyl amine
H2N O-Xylene
Nevirapine Penultimate
C3H7N
57.09
C15H15ClN4O
302.75
+ HCl
36.5
CaO
2-Chloro-N-(2-chloro-4-methyl-pyridin-3-yl)-
nicotinamide
Stage – 2:
N ClHN
HN
N
OCH3
Nevirapine Penultimate
C15H15ClN4O
302.75
+ NaH
Sodium hydride
24.00
N
HN
N
OCH3
N
Nevirapine (Crude)
C15H14N4O
266.30
O-Xylene
Acetic acid
+ NaCl + H2
58.44 2.00
Stage – 3:
Page 103
N
HN
N
OCH3
N
Nevirapine (Crude)
C15H14N4O
266.29
Methanol
CarbonN
HN
N
OCH3
N
Nevirapine (Pure)
C15H14N4O
266.29
Page 104
NEVIRAPINE
Flow chart:
Stage-1
Stage-2
Stage-3
2-Chloro-N-(2-Chloro-4-Methyl-3-Pyridinyl)-3-Pyridine CarboxamideCalcium oxideOrtho xyleneCyclopropylamine
Stage-1Ortho xyleneSodium hydroxideDiglymeCyclohexane
Ortho xylene Rec
Ortho xylene RecDiglyme Rec
Stage-2Methanol Methanol Rec
NEVIRAPINE
NEVIRAPINE
Page 105
Material Balance:
Material Balance of Nevirapine Stage-1
Batch Size: 500Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
2-Chloro-N-(2-Chloro-4-Methyl-3-Pyridinyl)-3-Pyridine Carboxamide
570.00 Stage-1 593.00
Calcium oxide 25.50 Ortho-Xylene Recovery 1140.00
Ortho-Xylene 1200.00 Ortho-Xylene Loss 24.00
Cyclo propyl amine 115.50 Effluent Water 4025.50
DM Water 4000.00 (Water-4000, Calcium oxide-25.5)
0
Process emission 73.71
(Hydrogen chloride-73.71) 0
Organic Residue 54.79
Process Residue-18.79 Distillation Residue-36 (Xylene-36)
Total 5911.00 Total 5911.00
Material Balance of Nevirapine Stage-2
Batch Size: 500Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-1 593.00 Stage-2 505.00
Ortho-Xylene 800.00 Ortho-Xylene Recovery 760.00
Sodium Hydride 47.00 Ortho-Xylene Loss 16.00
Hyflow 5.00 Cyclohexane Recovery 380.00
Activated Carbon 15.00 Cyclohexane Loss 8.00
Cyclohexane 400.00 Effluent Water 3630.25
Acetic acid 10.00 (Water-3500,Acetic Acid-10, Sodium Chloride-114.25, Cyclohexane-6)
DM Water 3500.00 Spent Carbon & Hyflow 20.00
Process Emission 3.91
(Hydrogen – 3.91)
Organic residue 46.84
Process Residue-16.84, Distillation Residue-30 (Xylene-24,Cyclo hexane-6)
Total 5370.00 Total 5370.00
Page 106
Material Balance of Nevirapine
Stage-3 Batch Size: 500Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-2 505.00 Nevirapine 500.00
Methanol 900.00 Methanol Recovery 855.00
Activated Carbon 20.00 Methanol Loss 18.00
Hyflow 8.00 Spent Carbon & Hyflow 28.00
Organic Residue 32.00
Process Residue-5, Distillation Residue-27 (Methanol-27)
Total 1433.00 Total 1433.00
NICLOSAMIDE
Process Description:
Page 107
Stage-1:
5 Chloro salicylic acid undergoes chlorination with Thionyl chloride in presence of Mono
chloro benzene to give Stage -1 product
Stage-2:
Stage -1 product undergoes condensation with 2-Chloro 4-nitro aniline in presence of
Mono chloro benzene to give Niclosamide
NICLOSAMIDE
Page 108
Route of Synthesis:
Stage-1
Cl
OH
COOH
5-Chloro Salicylic Acid
C7H5ClO3
172.57
+ SOCl2
118.97
Cl
OH
COCl
5-Chloro-2-hydroxy-benzoyl chloride
C7H4Cl2O2
191.01
+ SO2
64.06
+ HCl
36.46
MCB
Stage-2
Cl
OH
COCl
5-Chloro-2-hydroxy-benzoyl chloride
C7H4Cl2O2
191.01
+
H2N
Cl
NO2
2-Chloro-4-nitro-phenylamine
C6H5ClN2O2
172.57
MCB
Cl
OH
HN
Cl
NO2
O
Niclosamide
C13H8Cl2N2O4
327.12
+ HCl
36.46
NICLOSAMIDE
Flow Chart
Page 109
Stage-1
Stage-2
NICLOSAMIDE
5-Chloro Salicylic AcidThionyl chlorideMono Chloro Benzene
Mono Chloro Benzene RecEffluent water
Stage-12-Chloro 4-Nitro anilineMono Chloro Benzene
Mono Chloro Benzene RecEffluent water
NICLOSAMIDE
Material Balance:
Page 110
Material balance of Niclosamide Stage-1
Batch Size:500Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
5-Chloro Salicylic Acid 282.00 Stage-1 302.00
Thionyl chloride 194.00 Mono Chloro Benzene Recovery
475.00
Mono Chloro Benzene 500.00 Mono Chloro Benzene loss 10.00
Water 2000.00 Effluent water 2000.00
(Water-2000)
Process emission 163.85
(Sulfur dioxide-104.42, Hydrogen chloride-59.43)
Organic residue 25.15
Process Residue-10.15, Distillation Residue-15 (Mono chloro benzene-15)
Total 2976.00 Total 2976.00
Material balance of Niclosamide Stage-2
Batch Size:500Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-1 302.00 Niclosamide 500.00
2-Chloro 4-Nitro aniline 272.00 Mono Chloro Benzene Recovery
570.00
Mono Chloro Benzene 600.00 Mono Chloro Benzene loss 12.00
water 3000.00 Effluent water 3000.00
(Water-3000)
Process emission 57.45
(Hydrogen chloride-57.45)
Organic residue 34.55
Process Residue-16.55 Distillation Residue-18 (Mono Chloro benzene-18)
Total 4174.00 4174.00
OMEPRAZOLE
Process Description
Page 111
Stage-1
3, 5-Lutidine undergoes oxidation with Hydrogen peroxide and then Nitration with Nitric
acid in presence of Acetic acid to give stage-1 product.
Stage-2
Stage-1 product reacts with Sodium methoxide and Dimethyl sulphate in presence of
sodium hydroxide and Methanol to give satge-2 product.
Stage-3
Stage-2 product undergoes chlorination with Thionyl chloride in presence of Sodium
hydroxide and Toluene to give stage-3 product.
Stage-4
Stage-3 product undergoes condensation with 2-Mercapto-5-methoxy benzimidazole in
presence of sodium hydroxide and Toluene to give stage-5 product.
Stage-5
Stage-4 product undergoes reduction with hydrogen peroxide in presence of Methanol
to give Omeprazole.
OMEPRAZOLE
Route of Synthesis:
Page 112
Stage-1
N
3,5-Lutidine
C7H9N
107.15
+ H2O2
Hydrogen peroxide
34.01
+ HNO3
Nitric acid
63.01
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
O
+ NaNO2
69.0
+ Na2SO4
142.04
+ CH3OH
32.0
C9H13NO2
167.21
OH
(4-methoxy-3,5-dimethylpyridin-2-yl)methanol
+ H2O
18.0
Page 113
Stage-3
+ SOCl2
Thionyl chloride
118.97
+ NaOH
Sodium hydroxide
40.0
Toluene
C9H12ClNO
185.65
H2O + SO2
18.0 64.06
N
O
C9H13NO2
167.21
OH
(4-methoxy-3,5-dimethylpyridin-2-
yl)methanol
N
O
Cl
2-(chloromethyl)-4-methoxy-3,5-dimethylpyridine
+NaCl
58.4
Stage-4
2-Mercapto-5-methoxy benzimidazole
N
HN
O
HS+
C8H8N2OS
180.23
+ NaOH
Sodium Hydroxide
40.0
Toluene
N
NH
O
S
N
CH3
H3C OCH3
5-Methoxy-2-(4-methoxy-3,5-dimethyl-pyridin-2-ylmethylsulfanyl)-1H-benzoimidazole
C17H19N3O2S
329.42
+ NaCl
58.5
+ H2O
18.0
C9H12ClNO
185.65
N
O
Cl
2-(chloromethyl)-4-methoxy-3,5-dimethylpyridine
Page 114
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
Page 115
OMEPRAZOLE
Flow Chart:
Stage-1
3,5-LutidineHydrogen peroxideNitric acidAcetic acid
Acetic acid Rec
Stage-2
Stage-1MethanolSodium hydroxideDimethyl sulfateToluene
Sodium NitriteToluene Rec
Stage-3Stage-3Thionyl chlorideToluene
Sulphur dioxideHydrogen chlorideToluene Rec
Stage-4
Stage-42-Mercapto-5-methoxybenzimidazoleSodium hydroxideToluene
Toluene RecSodium chloride
Stage-5Stage-5Hydrogen peroxideMethanolAcetone
Methanol RecAcetone Rec
OMEPRAZOLE
Page 116
OMEPRAZOLE
Material Balance:
Material balance of Omeprazole Stage-1
Batch Size:250Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
3,5-Lutidine 89.00 Stage-1 136.00
Hydrogen Peroxide 28.00 Effluent Water 280.00
Nitric acid 52.00 (Water-200, gen.water-30, Acetic acid-25, sulphuric acid-25)
Sulphuric acid 25.00 Organic Residue 3.00
Acetic acid 25.00 Process residue-3
Water 200.00
Total 419.00 Total 419.00
Material balance of Omeprazole Stage-2
Batch Size:250Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-1 136.00 Stage-2 132.00
Sodium methoxide 44.00 Methanol Recovery 475.00
Sodium hydroxide 65.00 Methanol Loss 10.00
Dimethyl sulphate 102.00 Effluent Water 846.00
Methanol 500.00 (Water-750, gen.water-14, Methanol-26, Sodium nitrate-56)
Water 750.00 Inorganic Solid Waste 115.00
(Sodium Sulphate-115.00)
Organic Residue 19.00
Process residue-4 Distillation Residue-15 (Methanol-15)
Total 1597.00 Total 1597.00
Page 117
Material balance of Omeprazole Stage-3
Batch Size:250Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-2 132.00 Stage-3 142.00
Thionyl Chloride 93.00 Toluene Recovery 475.00
Sodium hydroxide 31.00 Toluene Loss 10.00
Toluene 500.00 Effluent water 564.00
Water 500.00 (Water-500, gen.water-14, Sodium chloride-45, Toluene-5)
0
Process Emission 50.00
(Sulphur dioxide - 50) 0
Organic residue- 15.00
Process residue-5 Distillation Residue-10 (Toluene-10)
Total 1256.00 Total 1256.00
Material balance of Omeprazole Stage-4
Batch Size:250 Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-3 142.00 Stage-4 245.00
2-Mercapto-5-methoxy Benzimidazole
138.00 Toluene Recovery 475.00
Sodium chloride 30.00 Toluene Loss 10.00
Toluene 500.00 Effluent Water 464.00
Water 400.00 (Water-400, Generated water-14 Sodium Chloride - 45, Toluene-5)
Organic Residue 16.00
Process residue-6 Distillation residue-10 (toluene-10)
Total 1210.00 Total 1210.00
Page 118
Material balance of Omeprazole Stage-5:Pharma
Batch Size:250 Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-4 245.00 Omeprazole 250.00
Hydrogen peroxide 25.00 Methanol Recovery 238.00
Methanol 250.00 Methanol Loss 5.00
Acetone 250.00 Acetone Recovery 238.00
Acetone Loss 5.00
Generated Water 13.00
Organic residue 21.00
Process residue-7 Distillation residue-14 (methanol-7, Acetone-7)
Total 770.00 Total 770.00
Page 119
RAFOXANIDE
Process Description:
Stage-1:
Iodine is reacts with Chlorine in presence of dilute HCl to give Iodine mono chloride
[Step - A] and further it is reacts with Salicylic acid to stage-1 product.
Stage-2:
3, 4 Dichloro nitro benzene undergoes condensation with Para Chloro Phenol in
presence of Potassium Hydroxide to give Stage-2 product.
Stage-3:
Stage-2 product undergoes reduction with Iron dust in presence of HCl to give Stage -3
product
Stage-4:
Stage-3 product undergoes condensation with stage-1 product in presence of Toluene
and Potassium trichloride to give stage-4product.
Stage-5:
Stage-4 product undergoes purification in presence of acetone to give Refoxanide.
Page 120
RAFOXANIDE
Route of Synthesis:
Stage-1:
Step-A
I2
253.81
+ Cl2
70.91
324.72
Iodine monochloride
I Cl2
Step-B
OH
COOH
Salicylic acid
C7H6O3
138.12 324.72
Iodine monochloride
I Cl2+
OH
COOHI
I
3,5 Di Iodo Salicylic acid(DISA)
C7H4I2O3
389.91
+ 2 HCl
72.92
Page 121
Stage-2
C6H3Cl2NO2
192.00
+O2N
Cl
Cl
1,2-Dichloro-4-nitro-benzene
HO
Cl
4-Chloro-phenol
C6H5ClO
128.56
+ KOH
56.11
O2N
O
Cl Cl
2-Chloro-1-(4-chloro-phenoxy)-4-nitro-benzene
C12H7Cl2NO3
284.09
+ KCl
74.55
+ H2O
18.02
Page 122
Stage-3
O2N
O
Cl Cl
2-Chloro-1-(4-chloro-phenoxy)-4-nitro-benzene
C12H7Cl2NO3
284.09
+ Fe
55.84
HCl
H2N
O
Cl Cl
3-Chloro-4-(4-chloro-phenoxy)-phenylamine
254.11
C12H9Cl2NO
+ +
H2O
FeO
71.84
+
O2
32.00
18.02
Page 123
Stage-4
H2N
O
Cl Cl
3-Chloro-4-(4-chloro-phenoxy)-phenylamine
254.11
C12H9Cl2NO
OH
COOHI
I
2-Hydroxy-3,5-diiodo-benzoic acid
C7H4I2O3
389.91
(Stage-1)
+
(Stage-3)
PCl3+
137.33
OH
CI
I
NH
O
Cl Cl
O
N-[3-Chloro-4-(4-chloro-phenoxy)-phenyl]-2-hydroxy-3,5-diiodo-benzamide
626.01
C19H11Cl2I2NO3
+ H3PO3
82.00
+
2 H2O+
36.03
3 HCl
109.38
Page 124
Stage-5
OH
CI
I
NH
O
Cl Cl
O
N-[3-Chloro-4-(4-chloro-phenoxy)-phenyl]-2-hydroxy-3,5-diiodo-benzamide
626.01
C19H11Cl2I2NO3
OH
CI
I
NH
O
Cl Cl
O
Refoxanide
626.01
C19H11Cl2I2NO3
Acetone,Acetic acid
Page 125
RAFOXANIDE
Flow Chart
Stage-1
Stage-2
Stage-3
Stage-4
Stage-5
RAFOXANIDE
Iodine Chlorine gasSalicylic acidMDC
1,2 -Di chloro -4-nitro-benzene4-chloro -phenolPotassium hydroxide Methanol MDC
Stage-2Iron powder Hydrochloric acidToluene
Stage-1Stage-3Phosphorus trichlorideToluene
Stage-4Acetone Acetic acid
MDC RecEffluent water
Methanol RecMDC RecEffluent water
Toluene RecEffluent water
Toluene RecEffluent water
Acetone RecEffluent water
Page 126
RAFOXANIDE
Material Balance:
Material balance of Rafoxanide Stage-1
Batch Size:500Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Iodine 210.00 Stage-1 325.00
Chlorine gas 60.00 MDC Recovery 475.00
Salicylic acid 119.00 MDC loss 10.00
MDC 500.00 Effluent water 1000.00
Water 1000.00 (Water-1000)
Process emission 62.66
(Hydrogen chloride – 62.66)
Organic residue 16.34
Process Residue-1.34, Distillation Residue-15 (MDC -15)
Total 1889.00 Total 1889.00
Material balance of Rafoxanide Stage-2
Batch Size:500Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
1,2 –Di chloro -4-nitro-benzene 171.00 Stage-2 245.00
4-chloro -phenol 115.00 Methanol recovery 475.00
Potassium hydroxide 50.00 Methanol loss 10.00
Methanol 500.00 MDC Recovery 475.00
MDC 500.00 MDC loss 10.00
Water 1500.00 Effluent water 1591.30
(water-1500, Methanol -9, Potassium chloride-66.28, Generated water-16.02)
Organic residue 29.70
Process Residue -8.7, Distillation Residue-21 (Methanol-6, MDC-15)
Total 2836.00 Total 2836.00
Page 127
Material balance of Rafoxanide Stage-3
Batch Size:500Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-2 245.00 Stage-3 212.00
Iron powder 48.00 Toluene recovery 760.00
Hydrochloric acid 10.00 Toluene loss 16.00
Toluene 800.00 Effluent water 1494.51
Water 1500.00 (water- 1484.51, Toluene-10)
Spent Iron(II) oxide 61.78
Process emission 27.52
(Oxygen)
Organic residue 31.19
Process Residue -17.19, Distillation Residue-14 (Toluene-14)
Total 2603.00 Total 2603.00
Material balance of Rafoxanide Stage-4
Batch Size:500Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-1 325.00 Stage-4 505.00
Stage-3 212.00 Toluene Recovery 665.00
Phosphorus trichloride 115.00 Toluene loss 14.00
Toluene 700.00 Effluent water 1548.22
Water 1500.00 (Water-1470.03, Toluene-10, Phosphorous acid-68.19)
0
Process emission 90.99
(Hydrogen chloride) 0
Organic residue 28.79
Process residue-17.79, Distillation Residue-11 (Toluene -11)
Total 2852.00 Total 2852.00
Page 128
Material balance of Rafoxanide Stage-5
Batch Size:500Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-4 505.00 Rafoxanide 500.00
Acetone 500.00 Acetone Recovery 475.00
Acetic acid 20.00 Acetone loss 10.00
Activated carbon 5.00 Effluent water 1027.00
Hyflow 3.00 (Water-1000, Acetic acid-20, Acetone-7)
Water 1000.00 Spent Carbon & Hyflow 8.00
Organic Residue 13
Process Residue-5 Distillation Residue-8 (Acetone-8)
Total 2033.00 Total 2033.00
Page 129
TERBINAFINE HYDROCHLORIDE
Process Description
Stage-1
1-Chloromethyl-naphthalene reacts with Methyl amine in presence of to give Stage-1
product.
Stage-2
Stage-1 product reacts with 1-chloro-6, 6-Dimethyl Hept-2-ene-4-Yne in presence of
Toluene to give Stage-2 product.
Stage-3
Stage-2 product reacts with Hydrochloric acid in presence of Isopropyl alcohol to give
Terbinafine Hydrochloride.
Page 130
TERBINAFINE HYDROCHLORIDE
Route of Synthesis
Stage-1
Cl
1-Chloromethyl-naphthalene
C11H9Cl
176.64
+
Methyl amine
H2N CH3
31.06
Toluene
NH3C CH3
Dimethyl-naphthalen-1-yl-amine
C12H13N
171.24
+ HCl
Hydrochloric acid
36.5
Stage-2
Toluene
NH3C CH3
Dimethyl-naphthalen-1-yl-amine
C12H13N
171.24
1-Chloro-6,6-Dimethyl Hept-2-ene-4-yne
H3C
H3CCH3
Cl
C9H13Cl
156.65
+
N
CH3H3C
CH3
CH3
Terbinafine
C21H25N
291.43
+ KCl
+ 1/2K2CO3
Potassium carbonate
69.10
74.55
+ 1/2CO2
22.0
+ 1/2H2O
9.0
Page 131
Stage-3
N
CH3H3C
CH3
CH3
Terbinafine
C21H25N
291.43
+ HCl
Hydrochloric acid
36.5
IPA
N
CH3H3C
CH3
CH3
H
Cl
Terbinafine Hydrochloride
C21H26ClN
327.89
Page 132
TERBINAFINE HYDROCHLORIDE
Flow Chart
Stage-1
Stage-2
Stage-3
TERBINAFINE HYDROCHLORIDE
1-Chloromethyl-naphthalene Methyl amine Toluene
Toluene Rec
Toluene Rec
Stage-11-chloro-6, 6-Dimethyl Hept-2-ene-4-YneToluene
Stage-2Hydrochloric acidIsopropyl alcohol
Isopropyl alcohol Rec
Page 133
TERBINAFINE HYDROCHLORIDE
Material Balance:
Material Balance of Terbinafine Hydrochloride
Stage-1
Batch Size: 250.0Kgs
Name of the input Quantity
in Kg
Name of the out put Quantity
in Kg
Napthyl methyl chloride 140.00 Stage-1 135.00
Mono methyl amine 25.00 Toluene Recovery 284.00
Toluene 300.00 Toluene Loss 15.00
MDC 500.00 MDC Recovery 475.00
Water 450.00 MDC Loss 25.00
Effluent water 451.00
(Water-450, Toluene-1)
Process emission 28.92
(Hydrogen chloride – 28.92)
Organic Residue 1.08
Process residue-1.08
Total 1415.00 Total 1415.00
Material Balance of Terbinafine Hydrochloride
Stage-2
Batch Size: 250.0Kgs
Name of the input Quantity
in Kg
Name of the out put Quantity
in Kg
Stage-1 135.00 Stage-2 225.00
Chloro methyl heptane 124.00 Toluene Recovery 284.00
Toluene 300.00 Toluene Loss 15.00
Potassium carbonate 55.00 Effluent water 866.86
Water 800.00 (Water-800,Potassium chloride-58.77,
Generated water-7.09,Toluene-1)
Process Emission 17.34
(Carbon dioxide – 17.34)
Organic Residue 5.80
Process residue-5.80
Total 1414.00 Total 1414.00
Page 134
Material Balance of Terbinafine Hydrochloride
Stage-3
Batch Size: 250 Kgs
Name of the input Quantity
in Kg
Name of the out put Quantity
in Kg
Stage-2 225.00 Terbinafine Hydrochloride 250.00
IPA 600.00 IPA Recovery 570.00
Hydrochloric acid 30.00 IPA Loss 30.00
Organic Residue 5.00
Process residue-5.0
Total 855.00 Total 855.00
Page 135
TRICLABENDAZOLE
Process Description:
Stage-1:
3, 4, Dichloro aniline undergoes Acetylation with Acetic anhydride in presence of acetic
acid to give Acetamide further it is reacts with Nitric acid and potassium hydroxide to
give stage-1 product
Stage-2:
Stage-1 product reacts with 2, 3, Dichloro Phenol in presence of DMSO to give Stage-2
product
Stage-3:
Stage-2 product undergoes reduction with Hydrogen in presence of Methanol and
Raney nickel to give Stage-3 product
Stage-4:
Stage-3 product reacts with carbon disulfide and sodium hydroxide in presence of
Methanol to give Stage- 4 product
Stage-5:
Stage-4 product reacts with Dimethyl sulphate in presence of methanol and Sodium
hydroxide to give Triclabendazole.
Page 136
TRICLABENDAZOLE
Route of Synthesis
Stage-1
Step-A
Cl
Cl
NH2
3,4-Dichloro-phenylamine
C6H5Cl2N
162.02
+ (CH3CO)2O
Acetic anhydride
102.09
Cl
Cl
NHCOCH3
N-(3,4-Dichloro-phenyl)-acetamide
C8H7Cl2NO
204.05
+ CH3COOH
60.05
Acetic acid
Step-B
Cl
Cl
NHCOCH3
N-(3,4-Dichloro-phenyl)-acetamide
C8H7Cl2NO
204.05
+ HNO3
Nitric acid
Cl
Cl
NHCOCH3
NO2
N-(4,5-Dichloro-2-nitro-phenyl)-acetamide
C8H6Cl2N2O3
249.05
+ H2O
18.02
63.01
Page 137
Step-C
Cl
Cl
NHCOCH3
NO2
N-(4,5-Dichloro-2-nitro-phenyl)-acetamide
C8H6Cl2N2O3
249.05
+ KOH
Cl
Cl
NH2
NO2
+ CH3COOK
98.14
Potassium acetate4,5-Dichloro-2-nitro-phenylamine
C6H4Cl2N2O2
207.01
56.11
Stage-2
Cl
Cl
NH2
NO2
4,5-Dichloro-2-nitro-phenylamine
C6H4Cl2N2O2
207.01
+
Cl
Cl
OH
2,3-Dichloro-phenol
C6H4Cl2O
163
NH2
NO2
O
Cl
Cl
Cl
4-Chloro-5-(2,3-dichloro-phenoxy)-2-nitro-phenylamine
C12H7Cl3N2O3
333.55
+ HCl
36.5
Page 138
Stage-3
NH2
NO2
O
Cl
Cl
Cl
4-Chloro-5-(2,3-dichloro-phenoxy)-2-nitro-phenylamine
C12H7Cl3N2O3
333.55
+ H2
2.00
Raney Nickel
NH2
NH2
O
Cl
Cl
Cl
4-Chloro-5-(2,3-dichloro-phenoxy)-benzene-
1,2-diamineC12H9Cl3N2O
303.57
+ O2
32.0
Page 139
Stage-4
NH2
NH2
O
Cl
Cl
Cl
4-Chloro-5-(2,3-dichloro-phenoxy)-benzene-
1,2-diamine
C12H9Cl3N2O
303.57
+ CS2
76.14
Carbon disulfide
O
Cl
Cl
Cl
N
HN
C13H7Cl3N2OS345.63
SH
5-Chloro-6-(2,3-dichloro-phenoxy)-1H-benzoimidazole-2-thiol
2 NaOH+
79.99
Na2S+
78.04
2 H2O+
36.03
Page 140
Stage-5
O
Cl
Cl
Cl
N
HN
C13H7Cl3N2OS345.63
SH
5-Chloro-6-(2,3-dichloro-phenoxy)-1H-benzoimidazole-2-thiol
Di methyl sulphate
S
O
O
O
H3COOCH3
+
O
Cl
Cl
Cl
N
HN
S
Triclabendazole
C14H9Cl3N2OS
359.66
142.13
C2H6O5S
+ 2 NaOH
80.00
Na2S+
78.04
CH3OH+
32.04
+ 3 O2
96.00
H2+
2.02
Page 141
TRICLABENDAZOLE
Flow Chart
Stage-1
Stage-2
Stage-3
Stage-4
Stage-5
TRICLABENDAZOLE
3,4-Di chloro-phenyl amineAcetic anhydrideNitric acidPotassium hydroxide
Stage-12,3-Di chloro -phenolToluene Methanol
Stage-2Hydrogen Raney nickel Methanol
Stage-3Carbon di sulfideSodium hydroxideMethanol Ethyl acetate
Stage-4Di methyl sulphateSodium hydroxideMethanol
Effluent water
Toluene RecMethanol RecEffluent water
Methanol Rec
Methanol RecEthyl acetateEffluent water
Methanol RecEffluent water
Page 142
TRICLABENDAZOLE
Material Balance:
Material balance of Triclabendazole
Stage-1 Batch Size:500Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
3,4-Di chloro-phenyl amine 283.00 Stage-1 328.00
Acetic anhydride 179.00 Effluent water 1795.33
Nitric acid 107.00 (Water-1500, Acetic acid-104.67, Potassium acetate-160.31, generated water-30.35)
Potassium hydroxide 92.00 Organic residue 37.67
Water 1500.00 Process Residue-37.67
Total 2161.00 Total 2161.00
Material balance of Triclabendazole
Stage-2 Batch Size:500Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-1 328.00 Stage-2 511.00
2,3-Di chloro -phenol 258.00 Methanol recovery 665.00
Toluene 500.00 Methanol loss 14.00
Methanol 700.00 Toluene recovery 475.00
Water 1500.00 Toluene loss 10.00
Effluent water 1516
(Water-1500, Toluene -7, Methanol-9)
Process emission 57.64
(Hydrogen chloride – 57.64)
Organic residue 37.36
Process Residue-17.36 Distillation bottom Residue-20 (Methanol-12, Toluene-8,)
Total 3286.00 Total 3286.00
Page 143
Material balance of Triclabendazole
Stage-3 Batch Size:500Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-2 511.00 Stage-3 450.00
Hydrogen 3.05 Methanol Recovery 760.00
Raney nickel 10.00 Methanol Loss 16.00
Methanol 800.00 Effluent water 1512.00
Water 1500.00 (Water-1500,Methanol-12)
Spent Raney nickel 10.00
Process emission 48.90
(Oxygen – 48.90)
Organic Residue 27.15
Process Residue-15.15, Distillation Residue-12 (Methanol-12)
Total 2824.05 Total 2824.05
Material balance of Triclabendazole
Stage-4 Batch Size:500Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-3 450.00 Stage-4 496.00
Carbon di sulfide 113.00 Methanol Recovery 760.00
Sodium hydroxide 120.00 Methanol Loss 16.00
Methanol 800.00 Ethyl acetate recovery 475.00
Ethyl acetate 500.00 Ethyl acetate loss 10.00
Water 1500.00 Effluent water 1680.75
(Water-1500,Methanol-12, Di sodium sulfide-115.45, generated water-53.30)
Organic Residue 45.25
Process Residue-18.25, Distillation residue-27 ( Methanol-12, Ethyl acetate-15)
Total 3483.00 Total 3483.00
Page 144
Material balance of Triclabendazole
Stage-5 Batch Size:500Kg
Name of the input Quantity in Kg
Name of the out put Quantity in Kg
Stage-4 496.00 Triclabendazole 500.00
Di methyl sulphate 204.00 Methanol Recovery 760.00
Sodium hydroxide 115.00 Methanol Loss 16.00
Methanol 800.00 Effluent water 1657.80
Water 1500.00 (Water-1500,Methanol-45.95, Di sodium sulfide-111.85)
Process emission 140.47
(Oxygen-137.58, Hydrogen-2.89)
Organic Residue 40.73
Process residue-28.73, Distillation Residue-12 (Methanol-12)
Total 3115.00 Total 3115.00
Page 145
ZIDOVUDINE
Process Description
Stage-1
Step-A
Thymidine reacts with Trityl chloride in presence of TEA and 1, 4-Dioxane to give
Step-A Product
Step-B
Step-A compound reacts with Methane sulfonyl chloride in presence of TEA and
Toluene to give Step-B Product.
Step-C
Step-B Product reacts with TEA in presence of Methanol to give stage-1 Product.
Stage-2
Stage-1 Product reacts with sodium azide in presence of DMSO and Ammonium
chloride to give Stage-2 Product.
Stage-3
Stage-2 Product reacts with p-Toluene sulphonic acid and Sodium hydroxide in
presence of Toluene to give Zidovudine.
Page 146
ZIDOVUDINE
Route of Synthesis:
Stage-1:
Step-A
OHO
HO
N
HN
O
O
CH3
+ (C6H5)3CCl
Triethyl amine
+ C6H15N1,4-Dioxane
C O O
HO
N
HN
O
O
CH3
+
Thymidine
C10H14N2O5
242.23
Trityl chloride
278.78 101.19
Trityl thymidine
C29H28N2O5
484.54
C6H15N.HCl
Triethyl amine hydrochloride
137.69
Page 147
Step-B
C O O
HO
N
HN
O
O
CH3
Trityl thymidine
C29H28N2O5
484.54
+ CH3SO2Cl + C6H15N
114.55 101.19
Toluene
C O O
O
N
HN
O
O
CH3
+
SO2CH3
C6H15N.HCl
Methanesulfonic acid 5-(5-methyl-2,4-dioxo-3,4-dihydro-2H-pyrimidin-1-yl)-2-trityloxymethyl-
tetrahydro-furan-3-yl ester137.69
C30H30N2O7S
562.63
Page 148
Step-C
C O O
O
N
HN
O
O
CH3
SO2CH3
Methanesulfonic acid 5-(5-methyl-2,4-dioxo-3,4-dihydro-2H-pyrimidin-1-yl)-2-
trityloxymethyl-tetrahydro-furan-3-yl esterC30H30N2O7S
562.63
C O ON
N
O
CH3
O
Methanol
5-O-Trityl-2,3-anhydro thymidin
C29H26N2O4
466.53
+ C6H15N
101.19
+
C7H16O3S
Triethyl methane sulfonate
SO O
O
180.27
+ NH3
17.0
Page 149
Stage-2:
C O ON
N
O
CH3
O
5-O-Trityl-2,3-anhydro thymidin
C29H26N2O4
466.53
+ NaN3 + NH4Cl
C O ON
HN
O
CH3
+
O
N3
NaCl + NH3
5-O-Trityl-Zidovudine
C29H27N5O4
509.56
58.5
Sodium azide
65.01
53.49
17.0
Page 150
Stage-3:
C O ON
HN
O
CH3
O
N3
5-O-Trityl-Zidovudine
C29H27N5O4
509.56
+H2O Toluene
HOO
N
HN
O
CH3
O
N3
+ C OH +
Zidovudine
C10H13N5O4
267.24
Trityl alcohol
CH3
S OO
OH
p-Toulenesulfonic Acid Mono hydrate
C7H10SO4
190.22
C19H16O
260.33
+ 2 NaOH
80.0
Na2SO4
142.04
+
CH3
Toluene
92.14
H2O+
18.0
Page 151
ZIDOVUDINE
Flow Chart:
?-Thymidine1,4-DioxaneTri ethyl amineTrityl chlorideTolueneMethane sulfonyl chlorideMethanol
Stage-1Sodium azideAmmonium chlorideDMSO
DMSO RecoveryEffluent water
Toluene RecoveryEthyl Acetate RecoveryMethanol Recovery
Stage-1
Stage-2
Stage-3
Stage-2TolueneMethanolPTSA MonohydrateEthyl acetateActivated CarbonHyflowSodium hydroxide
1,4-Dioxane Recovery + TEAToluene RecoveryMethanol Recovery+TEA
Zidovudine
Page 152
ZIDOVUDINE
Material Balance:
Material balance of Zidovudine Stage-1
Batch Size:500.0 Kg
Name of the input Quantity in Kg
Name of the out put Quantity In Kg
β-Thymidine 495.00 Stage-1 880.00
1,4-Dioxane 800.00 1,4-Dioxane + TEA Recovery 779.00
Tri ethyl amine 575.00 1,4-Dioxane + TEA Loss 17.00
Trityl chloride 530.00 Toluene Recovery 285.00
Toluene 300.00 Toluene Loss 6.00
Methane sulfonyl chloride 220.00 Methanol +TEA Recovery 969.00
Methanol 1000.00 Methanol + TEA Loss 21.00
Water 1000.00 Effluent water 1366
(Water-1000, Triethylmethane sulfonate-341,Toluene-5,Methanol-20)
By-Product 522.00
(Triethyl Amine Hydrochloride- 522.00)
Process Emission 32.00
(Ammonia -32)
Organic residue 43.00
Process residue-5.00 Distillation residue-38 (Toluene-4,Methanol-10, 1,4-Dioxane-24)
Total 4920.00 Total 4920.00
Page 153
Material balance of Zidovudine Stage-2
Batch Size:500.0 Kg
Name of the input Quantity in Kg
Name of the out put Quantity In Kg
Stage-1 880.00 Stage-2 960.00
Sodium azide 125.00 DMSO Recovery 570.00
Ammonium chloride 105.00 DMSO Loss 12.00
DMSO 600.00 Effluent water 2120.00
Water 2000.00 (Water-2000,Sodium Chloride-110.0,DMSO-10)
Process Emission 32.00
(Ammonia)
Organic Residue 16.00
Process residue-8, Distillation residue-8.00 ( DMSO-8)
Total 3710.00 Total 3710.00
Page 154
Material balance of Zidovudine Stage-3
Batch Size:500.0 Kg
Name of the input Quantity in Kg
Name of the out put Quantity In Kg
Stage-2 960.00 Zidovudine 500.00
Toluene 800.00 Toluene Recovery 760.00
Methanol 800.00 Toluene Loss 16.00
PTSA Monohydrate 393.00 Ethyl Acetate Recovery 760.00
Ethyl acetate 600.00 Ethyl Acetate Loss 16.00
Activated Carbon 5.00 Methanol Recovery 570.00
Hyflow 5.00 Methanol Loss 12.00
Sodium hydroxide 151.00 Effluent water 3513.51
Water 3000.00 (Water-3000,Generated water-33.91,Sodium sulphate-267.60,Toluene-185, Methanol-14,Ethyl acetate-13)
Spent Carbon & Hyflow 10.00
By-Product 490.45
(Trityl alcohol – 490.45)
Organic Residue 66.04
Process residue-33.04, Distillation residue- 33 (Toluene-12,Methanol-10, Ethyl acetate-11)
Total 6714.00 Total 6714.00
Page 155
Annexure- III
Water Requirement
S. No Purpose Water Input In KLD
1 Process 44
2 Washings 5
3 Boiler make up 42
4 Cooling towers make up 53
5 Scrubbing system 4
6 Domestic 4
7 Gardening 5
Total 157
Page 156
Annexure- IV
Waste Water Details
Unit HTDS KLD
LTDS KLD
Effluent Generation
in KLD
Treatment Method
Process 32.18 17.64 49.82 HTDS Effluent sent to stripper
followed by MEE system.
LTDS effluents treated in ETP along with MEE condensate. Treated effluent is sent to RO, RO permeate water is recycled and RO rejects taken for evaporation in MEE followed by ATFD to collect evaporation salts for disposal to TSDF.
Washings 5.00 0.00 5.00
Boiler Blow down 0.00 6.00 6.00
Cooling towers Blow down 0.00 6.00 6.00
Scrubbing system 4.00 0.00 4.00
Domestic 0.00 3.60 3.60
Total 41.18 33.24 74.42
Page 157
Annexure- V
Details of Hazardous/Solid Waste Generation & Disposal
S. No Name of the Solid/ Hazardous Waste
Quantity Disposal Method
1 Organic waste (Process Residue)
657.39 Kgs/Day Sent to Cement Industries
2 Spent Carbon 90 Kgs/Day Sent to Cement Industries
3 Solvent Distillation Residue 404 Kgs/Day Sent to Cement Industries
4 Inorganic Waste 350 Kgs/Day Sent to TSDF
5 MEE Salts 3160.93 Kgs/Day Sent to TSDF
6 Organic Evaporative Liquid (from MEE Stripper)
824 Kgs/Day Sent to Cement Industry
7 ETP Sludge 300 Kgs/Day Sent to TSDF
8 Used Oils 500 Ltrs/Annum SPCB Authorized Agencies for Reprocessing/Recycling
9 Containers liners 300 No’s / Month After Detoxification sent to
outside agencies
10 Used Lead Acid Batteries 4 No’s/ Annum Send back to suppliers for buyback of New Batteries
11 Ash from boiler 9800 Kgs/Day Sent to Brick Manufacturers
Page 158
Annexure- VI
Stack Emission Details for Boiler
Particulars Units 2.0 TPH Coal fired
Boiler 5.0 TPH Coal fired
Boiler
Type of Fuel -- Indian Coal Indian Coal
Coal Consumption TPD 8.00 20.00
Ash Content % 35 35
Sulphur Content % 0.8 0.8
Nitrogen Content % 1.07 1.15
No. of Stacks No 1 1
Height of stack M 30 30
Diameter of Stack M 0.60 0.60
Temperature of Flue Gas oC 95 110
Velocity of Flue Gas m/s 6.5 8.0
Particulate Matter at outlet of Bag filter (Based on 115 mg/Nm3 at outlet)
gm/sec 0.26
0.33
Sulphur dioxide emission 110 mg/Nm3
gm/sec 0.25 0.32
Oxides of Nitrogen emission 120 mg/Nm3
gm/sec 0.27 0.35
Pollution control equipment - Cyclone separator
followed by suitable pack of Bag filters
Cyclone separator followed by suitable pack of Bag filters
Table: Stack Emission Details for DG Sets
Capacity
In KVA
Emission
of SPM in
mg/Nm3
Emission
Of SO2 in
mg/Nm3
Emission
of NOx In
mg/Nm3
Stack
dia.
In m
Flue Gas
Temp. in OC
Stack
Height
in (m)
Flue gas
Velocity
In m/sec.
250 KVA 50.0 20.0 40.0 0.30 290 10 12.76
380 KVA 74.0 150.0 185.0 0.30 220 10 21.0
Page 159
Annexure-VII
PROCESS EMISSION DETAILS
S.No. Name of the Gas Quantity Treatment Method
1 Carbon dioxide 117.34 Kgs/Day Dispersed into the atmosphere
2 Sulphur dioxide 241.28 Kgs/Day Scrubbed by using C.S.Lye Solution
3 Hydrogen 15.08 Kgs/Day Diffused by using Nitrogen through Flame arrestor
4 Ammonia 114.37 Kgs/Day Scrubbed by using chilled water media
5 Hydrogen chloride 439.45 Kgs/Day Scrubbed by using chilled water media
6 Oxygen 177.75 Kgs/Day Dispersed into the atmosphere
Page 160
Annexure- VIII
LIST OF RAW MATERIALS
ALBENDAZOLE
S .No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
1 O-Nitro aniline 270.00 180.00
2 Acetone 800.00 533.33
3 Ammonium thio cyanate 298.00 198.67
4 Chlorine gas 138.00 92.00
5 Cyanamide 81.00 54.00
6 EDTA 1.00 0.67
7 Methanol 1700.00 1133.33
8 Methyl chloroformate 182.00 121.33
9 n-Propanol 500.00 333.33
10 n-Propyl bromide 237.00 158.00
11 Sodium hydrosulphide 214.00 142.67
12 Sodium hydroxide solution (50%) 77.00 51.33
13 Sodium hydroxide solution (50%) 77.00 51.33
BIAPENEM
S .No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
1 3-(Diphenoxy-phosphorylox)-6-(1-hydroxy-ethyl)-4-methyl-7-oxo-1-aza-bicyclo[3.2.0]hept-2-ene-2-carboxylic acid 4-nitro-benzyl ester
450.00
300.00
2 6-Mercapto-6,7-dihydro-5H-pyrazolo[1,2] [1,2,4] triazol-4-ylium
107.00 71.33
3 Acetonitrile 300.00 200.00
4 Ethyl Acetate 500.00 333.33
5 Hydrochloric Acid 28.00 18.67
6 Hydrogen 2.00 1.33
7 n-Heptane 400.00 266.67
8 Palladium Carbon 10.00 6.67
9 Sodium hydroxide 30.00 20.00
10 THF 600.00 400.00
Page 161
CARVEDILOL
S .No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
1 9H-Carbazol-4-ol 121.00 80.67
2 (2-methoxyphenoxy)ethylamine
106.06 70.71
3 (Chloromethyl) oxirane 60.50 40.33
4 Activated carbon 20.00 13.33
5 Ethyl acetate 500.00 333.33
6 Sodium chloride(washing) 50.00 33.33
7 Sodium sulfate 150.00 100.00
8 Tetrahydrofuran 450.00 300.00
9 Toluene 500.00 333.33
CIPROFLOXACIN HYDROCHLORIDE
S .No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
1 Acetophenone 300.00 200.00
2 Acetic Acid 171.00 114.00
3 Activated carbon 3.00 2.00
4 Ammonia Hydroxide 49.00 32.67
5 C.S.Flakes 125.00 83.33
6 Cyclopropyl amine 82.00 54.67
7 Dimethyl carbonate 131.00 87.33
8 DMF 105.00 70.00
9 DMSO 181.00 120.67
10 Hydrochloric acid 52.00 34.67
11 Hydrochloric acid (36%) 51.00 34.00
12 Methanol 1000.00 666.67
13 n-Butanol 300.00 200.00
14 Piperazine 242.00 161.33
15 Sodium hydride 70.00 46.67
16 Toluene 1600.00 1066.67
Page 162
CLOSANTEL SODIUM
S .No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
1 4-Chloro -1-methy -2-nitro -benzene 134.00 89.33
3 Methanol 500.00 333.33
2 Para Chloro Benzyl Cyanide 118.00 78.67
4 Sodium sulfide 60.80 40.53
5 Sodium bicarbonate 65.50 43.67
6 2-hydroxy -3,5-diiodo-benzoic acid 294.00 196.00
7 Activated carbon 5.00 3.33
8 Hyflow 3.00 2.00
9 Methanol
500.00 333.33
10 Phosphorus trichloride 104.00 69.33
11 Sodium Hydroxide 120.50 80.33
12 Toluene 1300.00 866.67
DOREPENEM
S .No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
1 3-(Diphenoxy-phosphoryloxy)-6-(1-hydroxy-ethyl)-4-methyl-7-oxo-1-aza-bicyclo[3.2.0]hept-2-ene-2-carboxylic acid 4-nitro-benzyl ester
365.00
243.33
2 (2S,3S)-1-p-nitrobenzyloxycarbonyl-2-sulfamylaminomethyl-4-mercaptopyrrolidone
246.00
164.00
3 Acetonitrile 600.00 400.00
4 Acivated carbon 10.00 6.67
5 DMF 300.00 200.00
6 Hydrochloric acid 42.00 28.00
7 Hydrogen 2.00 1.33
8 N-Ethyl Diispropyl Amine 82.00 54.67
9 Palladium Carbon 20.00 13.33
10 Sodium Hydroxide 46.00 30.67
11 Tetrahydrofuran 300.00 200.00
Page 163
ENROFLOXACIN
S .No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
1 Quinoline-3- Carboxylic acid
405.00 270.00
2 Acetic acid 17.46 11.64
3 Activated Carbon 12.00 8.00
4 Hydrochloric Acid 10.62 7.08
5 n-Butanol 1000.00 666.67
6 n-Ethyl Piperazine 328.00 218.67
7 Sodium Hydroxide 11.65 7.77
GABAPENTIN
S .No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
1 (1-Carbamoylmethyl-cyclohexyl)-acetic acid
318.00
212.00
2 Activated Carbon 8.00 5.33
3 Hydrochloric acid 57.00 38.00
4 Methylene Dichloride 500.00 333.33
5 Sodium Hypochlorite 118.00 78.67
GLUCOSAMINE HYDROCHLORIDE
S .No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
1 Chitin 375.00 250.00
2 Hydrochloric acid 20.00 13.33
3 Methanol 800.00 533.33
Page 164
IMIPENEM
S .No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
1 6-(1-Hydroxy-ethyl)-3,7-dioxo-1-aza-bicyclo[3.2.0]heptanes-2-carboxylic acid 4-nitro-benzyl ester 318.00 212.00
2 2-Amine -ethanethiol 70.00 46.67
3 Acetonitrile 950.00 633.33
4 Activated Carbon 25.00 16.67
5 Di-Isopropyl Amine 500.00 333.33
6 Ethyl Acetate 1500.00 1000.00
7 Formimidic acid methyl ester 52.00 34.67
8 Hydrogen 2.00 1.33
9 MDC 300.00 200.00
10 Methanol 400.00 266.67
11 n- Hexane 400.00 266.67
12 Palladium Carbon 5.00 3.33
13 Para toluene sulfonyl chloride 170.00 113.33
14 Sodium Hydroxide 35.00 23.33
LAMIVUDINE
S .No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
1 L(-) Menthol 280.00 186.67
2 2,5-Dithiane-1,4-diol 136.00 90.67
3 Acetic acid 18.00 12.00
4 Activated Carbon 8.00 5.33
5 Conc. HCl 83.00 55.33
6 Cyclohexane 630.00 420.00
7 cytosine 279.00 186.00
8 Ethyl Acetate 150.00 100.00
9 Formaldehyde 55.00 36.67
10 Glyoxylic Acid (50%) 266.00 177.33
11 Hexamethyldisilazane 404.00 269.33
12 Hyflow 5.00 3.33
13 IPA 50.00 33.33
14 Iso propyl alcohol 600.00 400.00
15 Methane Sulphonic Acid 2.00 1.33
16 Methanol 1200.00 800.00
17 Methylene dichloride 1000.00 666.67
18 n-Hexane 430.00 286.67
Page 165
19 Sodium Bisulphite 186.00 124.00
20 Sodium Borohydride 86.00 57.33
21 Sodium Carbonate 15.00 10.00
22 Sulphuric Acid 3.00 2.00
23 Thionyl chloride 298.00 198.67
24 Toluene 1288.00 858.67
25 Triethylamine 223.00 148.67
LANSOPRAZOLE
S .No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
1 2,3-Lutidine 84.00 56.00
2 2-Mercapto Benzimidazole 107.00 71.33
3 Acetic Anhydride 77.00 51.33
4 Acetone 150.00 100.00
5 Activated Carbon 3.00 2.00
6 Catalyst 1.00 0.67
7 Chloroform 400.00 266.67
8 Hydrogen Chloride Gas 27.00 18.00
9 Hydrogen Peroxide (50%) 30.00 20.00
10 Hydrogen Peroxide (50%) 30.00 20.00
11 Isopropyl Alcohol 250.00 166.67
12 Methylene Dichloride 200.00 133.33
13 MIBK 130.00 86.67
14 Nitric Acid 49.00 32.67
15 Potassium Carbonate 105.00 70.00
16 Sodium Hydroxide 87.00 58.00
17 Sulfuric Acid 50.00 33.33
18 TEBAC 1.00 0.67
19 Thionyl Chloride 88.00 58.67
20 Toluene 475.00 316.67
21 Tri Fluoro Ethanol 76.00 50.67
Page 166
MEROPENEM
S .No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
1 3-(Diphenoxy-phosphoryloxy)-6- (1-hydroxy-ethyl)-4-methyl-7-oxo- 1-aza-bicyclo[3.2.0]hept-2-ene-2- carboxylic acid 4-nitro-benzyl ester 430.00 286.67
2 10% Palladium Carbon 5.00 3.33
3 2-Dimethylcarbamoyl-4-mercapto- pyrrolidine-1-carboxylic acid 4-nitro-benzyl ester 245.00 163.33
4 Acetonitrile 600.00 400.00
5 Ethyl Acetate 1000.00 666.67
6 Hexane 350.00 233.33
7 Hydrogen 3.000 2.00
8 Isopropyl Alcohol 700.00 466.67
9 MDC 600.00 400.00
10 Sodium Hydroxide 50.00 33.33
11 Triethylamine 70.00 46.67
NEVIRAPINE
S .No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
1 2-Chloro-N-(2-Chloro-4-Methyl-3-Pyridinyl)-3-Pyridine Carboxamide
570.00 380.00
2 Acetic acid 10.00 6.67
3 Activated Carbon 35.00 23.33
4 Calcium oxide 25.50 17.00
5 Cyclo propyl amine 115.50 77.00
6 Cyclohexane 400.00 266.67
7 DM Water 1000.00 666.67
8 DM Water 1200.00 800.00
9 Hyflow 13.00 8.67
10 Methanol 900.00 600.00
11 Ortho-Xylene 2000.00 1333.33
12 Sodium Hydride 47.00 31.33
Page 167
NICLOSAMIDE
S .No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
1 5-Chloro Salicylic Acid 282.00 188.00
2 2-Chloro 4-Nitro aniline 272.00 181.33
3 Mono Chloro Benzene 1100.00 733.33
4 Thionyl chloride 194.00 129.33
OMEPRAZOLE
S .No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
1 3,5-Lutidine 89.00 59.33
2 2-Mercapto-5-methoxy Benzimidazole 138.00 92.00
3 Acetic acid 25.00 16.67
4 Acetone 250.00 166.67
5 Dimethyl sulphate 102.00 68.00
6 Hydrogen Peroxide 53.00 35.33
7 Methanol 750.00 500.00
8 Nitric acid 52.00 34.67
9 Sodium chloride 30.00 20.00
10 Sodium hydroxide 96.00 64.00
11 Sodium methoxide 44.00 29.33
12 Sulphuric acid 25.00 16.67
13 Thionyl Chloride 93.00 62.00
14 Toluene 1000.00 666.67
Page 168
RAFOXANIDE
S .No.
Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
1 Iodine 210.00 140.00
2 1,2 –Di chloro -4-nitro-benzene 171.00 114.00
3 4-chloro -phenol 115.00 76.67
4 Acetic acid 20.00 13.33
5 Acetone 500.00 333.33
6 Activated carbon 5.00 3.33
7 Chlorine gas 60.00 40.00
8 Hydrochloric acid 10.00 6.67
9 Hyflow 3.00 2.00
10 Iron powder
48.00 32.00
11 MDC 1000.00 666.67
12 Methanol 500.00 333.33
13 Phosphorus trichloride 115.00 76.67
14 Potassium hydroxide 50.00 33.33
15 Salicylic acid 119.00 79.33
16 Toluene 1500.00 1000.00
TERBINAFINE HYDROCHLORIDE
S .No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
1 Napthyl methyl chloride 140.00 93.33
2 Chloro methyl heptane 124.00 82.67
3 Hydrochloric acid 30.00 20.00
4 IPA 600.00 400.00
5 MDC 500.00 333.33
6 Mono methyl amine 25.00 16.67
7 Potassium carbonate 55.00 36.67
8 Toluene 300.00 200.00
Page 169
TRICLABENDAZOLE
S .No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
1 3,4-Di chloro-phenyl amine 283.00 188.67
2 2,3-Di chloro -phenol 258.00 172.00
3 Acetic anhydride 179.00 119.33
4 Carbon di sulfide 113.00 75.33
5 Di methyl sulphate 204.00 136.00
6 Ethyl acetate 500.00 333.33
7 Hydrogen 3.05 2.03
8 Methanol 3100.00 2066.67
9 Nitric acid 107.00 71.33
10 Potassium hydroxide 92.00 61.33
11 Raney nickel 10.00 6.67
12 Sodium hydroxide 235.00 156.67
13 Toluene 500.00 333.33
ZIDOVUDINE
S .No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
1 β-Thymidine 495.00 330.00
2 1,4-Dioxane 800.00 533.33
3 Activated Carbon 5.00 3.33
4 Ammonium chloride 105.00 70.00
5 DMSO 600.00 400.00
6 Ethyl acetate 600.00 400.00
7 Hyflow 5.00 3.33
8 Methane sulfonyl chloride 220.00 146.67
9 PTSA Monohydrate 393.00 262.00
10 Sodium azide 125.00 83.33
11 Sodium hydroxide 151.00 100.67
12 Toluene 1100.00 733.33
13 Tri ethyl amine 575.00 383.33
14 Trityl chloride 530.00 353.33
Page 170
11. LOSARTAN POTASSIUM
S.No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
source
1. 2-Cyano-4-Methyl biphenyl (OTBN)
236.00 157.33
indigenous
2. Activated Carbon 15.00 10.00 indigenous
3. Butyl chloro formyl imidazole (BCFI)
206.00 137.33
indigenous
4. Ethyl Acetate 200.00 133.33 indigenous
5. Hydrochloric acid 83.00 55.33 indigenous
6. MDC 500.00 333.33 indigenous
7. Methanol 1700.00 1133.33 indigenous
8. Methylenedichloride 400.00 266.67 indigenous
9. N-Bromosuccinimide (NBS) 195.00 130.00 indigenous
10. Potassium hydroxide 61.00 40.67 indigenous
11. Sodium Azide 73.00 48.67 indigenous
12. Sodium hydroxide 44.00 29.33 indigenous
13. Sodium meta bisulphate 10.00 6.67 indigenous
14. Sodium nitrite 78.00 52.00 indigenous
15. TBAB 5.00 3.33 indigenous
16. TEA 30.00 20.00 indigenous
17. TEA HCl 25.00 16.67 indigenous
18. Toluene 400.00 266.67 indigenous
19. Trityl chloride 276.00 184.00 indigenous
12. NEVIRAPINE
S.No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
source
1. 2-Chloro-N-(2-Chloro-4-Methyl-3-Pyridinyl)-3-Pyridine Carboxamide
541.00 360.67 indigenous
2. Acetic acid 10.00 6.67 indigenous
3. Activated Carbon 35.00 23.33 indigenous
4. Calcium oxide 25.50 17.00 indigenous
5. Cyclo propyl amine 109.50 73.00 indigenous
6. Cyclohexane 400.00 266.67 indigenous
7. Hyflow 13.00 8.67 indigenous
8. Methanol 900.00 600.00 indigenous
9. Ortho-Xylene 2000.00 1333.33 indigenous
10. Sodium Hydride 46.00 30.67 indigenous
Page 171
13. OMEPRAZOLE
S.No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
source
1. 3,5-Lutidine 157.00 104.67 indigenous
2. 2-Mercapto-5-methoxy Benzimidazole
260.00 173.33
indigenous
3. Acetic acid 25.00 16.67 indigenous
4. Acetone 250.00 166.67 indigenous
5. Dimethyl sulphate 183.80 122.53 indigenous
6. Hydrogen Peroxide 98.60 65.73 indigenous
7. Methanol 750.00 500.00 indigenous
8. Nitric acid 92.35 61.57 indigenous
9. Sodium chloride 58.00 38.67 indigenous
10. Sodium hydroxide 174.80 116.53 indigenous
11. Sodium methoxide 78.70 52.47 indigenous
12. Sulphuric acid 25.00 16.67 indigenous
13. Thionyl Chloride 172.90 115.27 indigenous
14. Toluene 1000.00 666.67 indigenous
14. PANTOPRAZOLE SODIUM
S.No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
source
1. Maltol 66.00 44.00 indigenous
2. 5-diFluoromethoxy-2-mercapto- benzimidazole
108.00
72.00
indigenous
3. Acetic Acid 10.00 6.67 indigenous
4. Acetic Anhydride 172.00 114.67 indigenous
5. Acetone 1000.00 666.67 indigenous
6. Activated Carbon 10.00 6.67 indigenous
7. Ammonia 9.00 6.00 indigenous
8. Ammonium Carbonate 50.00 33.33 indigenous
9. Ammonium Chloride 25.00 16.67 indigenous
10. Ammonium hydroxide 35.50 23.67 indigenous
11. Dimethyl sulphate 33.00 22.00 indigenous
12. Hydrogen peroxide 17.00 11.33 indigenous
13. MDC 1950.00 1300.00 indigenous
14. Methanol 875.00 583.33 indigenous
15. Methylene dichloride 1300.00 866.67 indigenous
16. Phosphorous oxy chloride 26.00 17.33 indigenous
Page 172
17. Potassium carbonate 36.00 24.00 indigenous
18. Sodium hydroxide 40.00 26.67 indigenous
19. Sodium hypochlorite 37.00 24.67 indigenous
20. Sodium methoxide 27.00 18.00 indigenous
21. Thionyl chloride 60.00 40.00 indigenous
22. Toluene 800.00 533.33 indigenous
15. PREGABALIN
S.No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
source
1. Isoveraldehyde 112.00 149.33 indigenous
2. (S)-Mandelic acid 100.00 133.33 indigenous
3. Acetic acid 169.00 225.33 indigenous
4. Di isopropyl amine 10.00 13.33 indigenous
5. Diethyl malonate 209.00 278.67 indigenous
6. Ethanol 900.00 1200.00 indigenous
7. Hydrogen gas 5.00 6.67 indigenous
8. IPA 1870.00 2493.33 indigenous
9. Methanol 220.00 293.33 indigenous
10. n-Hexane 180.00 240.00 indigenous
11. Potassium hydroxide 73.00 97.33 indigenous
12. Raney nickel 30.00 40.00 indigenous
13. Sodium cyanide 64.00 85.33 indigenous
14. Tetrahydrofuran 900.00 1200.00 indigenous
15. Toluene 500.00 666.67 indigenous
16. SERTRALINE HYDROCHLORIDE
S.No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
source
1. Racemic Cis and Trans Sertraline
100.00 166.67
indigenous
2. Activated carbon 17.80 29.67 indigenous
3. Caustic Lye 125.00 208.33 indigenous
4. D(-) Mandelic acid 5.00 8.33 indigenous
5. Hydrochloric acid 12.00 20.00 indigenous
6. Hyflow 2.00 3.33 indigenous
7. IPA 4500.00 7500.00 indigenous
8. Methanol 800.00 1333.33 indigenous
9. Methylene chloride 4550.00 7583.33 indigenous
Page 173
17. TRAMADOL HYDROCHLORIDE
S.No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
source
1. Di methyl amine 32.00 53.33 indigenous
2. Bromo Anisole 125.00 208.33 indigenous
3. Cyclohexanone 65.75 109.58 indigenous
4. Glacial Acetic acid 2.00 3.33 indigenous
5. Hydrochloric acid 48.80 81.33 indigenous
6. Isopropyl Alcohol 500.00 833.33 indigenous
7. Magnesium 16.25 27.08 indigenous
8. Methanol 400.00 666.67 indigenous
9. Nitric acid 43.00 71.67 indigenous
10. p-Formaldehyde 20.11 33.52 indigenous
11. Sodium hydroxide 53.80 89.67 indigenous
12. Sulfuric Acid 66.00 110.00 indigenous
13. Tetrahydrofuran 400.00 666.67 indigenous
14. Toluene 1100.00 1833.33 indigenous
18. ZIDOVUDINE
S.No. Raw Material Consumption/ Batch in Kgs
Consumption/ Day in Kgs
source
1. β-Thymidine 363.00 302.50 indigenous
2. 1,4-Dioxane 800.00 666.67 indigenous
3. Activated Carbon 5.00 4.17 indigenous
4. Ammonium chloride 80.00 66.67 indigenous
5. DMSO 1200.00 1000.00 indigenous
6. Ethyl acetate 1300.00 1083.33 indigenous
7. Hyflow 5.00 4.17 indigenous
8. Methane sulfonyl chloride 172.00 143.33 indigenous
9. Methanol 2600.00 2166.67 indigenous
10. PTSA Monohydrate 284.50 237.08 indigenous
11. Sodium azide 97.40 81.17 indigenous
12. Sodium hydroxide 119.50 99.58 indigenous
13. Toluene 3300.00 2750.00 indigenous
14. Tri ethyl amine 496.00 413.33 indigenous
15. Trityl chloride 418.00 348.33 indigenous
Page 174
Annexure-IX
Consolidated Statement- Pollution Details
S.No
Product Name
Productioncapaci
ty kg/ Month
Effluent in kg/day Solid waste Details in Kg/day Distillation
Residue in Kg
/Day
Emissions in Kg/day
Water Input
Water In
Effluent
Inorganics in
water
Organics in
water TDS COD HTDS LTDS Total
Effluent Organi
c
Inorgani
c
Spent carbo
n
Total solid waste
Process
Fugitive
1 Albendazole 10000.00 4333.33
4309.77 492.56 36.00 492.56
66.63
3854.99
983.33 4838.33 36.82 0.00 0.00 36.82 20.67 102.18 43.33
2 Biopenem 5000.00 666.67 675.73 155.33 17.33 155.33 25.9
7 848.40 0.00 848.40 13.60 0.00 0.00 13.60 12.67 0.00 20.00
3 Carvedilol 5000.00
400.00 400.00 33.33 14.00 33.33 53.1
9 373.33 74.00 447.33 9.12 166.
67 13.33 189.12 10.67 17.87 23.33
4 Ciprofloxacin 10000.00 6000.00
6033.42 318.05
137.72 318.05
233.69
2804.15
3685.04 6489.19 31.71 0.00 0.00 31.71 2.67 1.91 92.00
5 Closantel Sodium 10000.00 3333.33
3332.71 191.63 20.67 191.63
53.82
3545.00 0.00 3545.00 14.81 0.00
5.33 20.15 25.33 58.85 30.67
6 Dorapenem 5000.00 666.67 666.67 274.00 5.33 274.00 8.24 612.67
333.33 946.00 18.67
13.33 6.67 38.67 13.33 6.67 16.00
7 Enrofloxacin 10000.00 3333.33
3333.33 22.99 0.00 22.99 0.00
3356.33 0.00 3356.33 19.07 0.00 0.00 19.07 0.00 0.00 33.33
8 Gabapentin 5000.00 1066.67
1084.81 120.60 0.00 120.60 0.00 890.68
314.73 1205.41 17.25 0.00 5.33 22.59 6.67 46.67 10.00
9 Glucosamine HCl 5000.00 800.00 786.33 22.67 8.00 22.67
12.00 817.00 0.00 817.00 6.33 0.00 0.00 6.33 8.00 0.00 10.67
10 Imipenem 5000.00 1700.00 1710.6
7 198.67 5.33 198.67 8.00 1237.3
3 677.3
3 1914.67 21.33 0.00 16.67 38.00 25.33 0.00 97.33
11 Lamivudine 10000.00 5333.33
4893.13 335.43 31.33 335.43
82.36
3942.10
1317.79 5259.89 356.55 0.00 8.67 365.22 70.00 202.41 85.33
12 Lansoprazole 5000.00 1293.33
1347.33 127.33 6.00 127.33
12.46 839.33
641.33 1480.67 22.67
93.33 2.00 118.00 18.67 49.33 24.67
13 Meropenem 5000.00 1166.67
1174.67 142.00 3.33 142.00 8.00 683.33
636.67 1320.00 9.33 0.00 0.00 9.33 0.00 0.00 66.67
14 Nevirapine 10000.00 5000.00
5000.00 99.83 0.00 99.83
13.72
2420.17
2683.67 5103.83 27.09 0.00 13.33 40.42 62.00 51.75 44.00
15 Niclosamide 10000.00 3333.33
3333.33 0.00 0.00 0.00 0.00 0.00
3333.33 3333.33 17.80 0.00 0.00 17.80 22.00 147.53 14.67
16 Omeprazole 5000.00 1233.33
1290.00 114.00 40.67 114.00
64.70
1436.00 8.67 1444.67 16.67
76.67 0.00 93.33 32.67 33.33 26.67
Page 175
17 Rafoxanide 10000.00 4333.33
4303.03 102.98 24.00 102.98
61.00
2767.00
1663.01 4430.01 33.35 0.00 12.00 45.35 46.00 120.78 46.67
18 Terbinafine HCl 5000.00 833.33 838.06 39.18 1.33 39.18 4.17 577.91
300.67 878.57 7.92 0.00 0.00 7.92 0.00 30.84 56.67
19 Triclabendazole 10000.00 5000.00
5022.23 328.19 57.30 328.19
93.56
3389.05
2018.67 5407.72 78.11 0.00 0.00 78.11 47.33 164.67 54.67
20 Zudovudine 10000.00 4000.00
4022.61 479.07
164.67 479.07
457.17
4666.34 0.00 4666.34 30.69 0.00 6.67 37.36 52.67 42.67 58.67
Total (Worst combination of any 10 products at any given point of time)
100000.00
44000.00
43583.55 2914.93
543.69
2914.93
1192.09
32181.13
17640.17 49821.31 657.39
350.00 90.00
1097.39 404.00 986.85
645.33
Page 176
Annexure-X
Site Plan