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M/s.CRYSTALCROPPROTECTIONPVT.LTD.
Plotno:G-54,MIDCButibori,Nagpur,
Maharashtra,Pincode– 441122
PreparedBy:
VirendraChaudhary
V.P.Technical
CrystalCropProtectionPvt.Ltd.
Nathupur,Distt:Sonepat(Haryana)
Manufacturing activities in proposed
project including various process description,
reaction scheme and material balance
1. Epoxiconazole
Manufacturing process:
Step -1
Fluorobenzene is reacted with chloro acetyl chloride in presence of aluminum chloride and ethylene
dichloride to get 4-fluoro phenacyl chloride.
Step -2
4-Fluoro phenacyl chloride reacted with 1,2,4-triazole in presence of potassium hydroxide and DMF to
give 2-(1H-1,2,4-triazole-1-yl)-4-fluoro acetophenone.
Step -3
2-(1H-1,2,4-Triazole-1-yl)-4-fluoro acetophenone reacted with 2-chloro benzyl chloride and dimethyl
sulphide in presence of potassium hydroxide and solvent DMF to give the final product
EPOXICONAZOLE.
Reaction scheme:
Material balance Epoxyconazole
2. Hexaconazole
Manufacturing Process:
Preparation of Trimethyl sulfonium sulfate
Dimethyl sulfate is charged in dimethyl sulfide at 33 °C to form trimethyl sulfonium sulfate.
2,4 Dichloro valerophenone is reacted with trimethyl sulfonium sulfate in presence of potassium hydroxide
to form Oxirane. Solvent dimethyl sulfide is recovered by distillation and product (oxirane) is separated
from potassium hydrogen sulfate. Water is added to dissolve salt and back extracted with methylene
dichloride and then, aqueous layer is transferred to ETP. 1,2,4 1H-triazole and potassium hydroxide is
charged in DMF and previously prepared oxirane is added at elevated temperature to form hexaconazole.
After completion of reaction, organic phase is separated by filtration. Carbonate sludge is washed with
DMF and collected with organic filtrate. Sludge is transferred to solid waste DMF is distilled out from
reaction mass first at atmospheric distillation and then by vacuum distillation.
Hexaconazole is isolated from molten mass with help of water. Slurry is
filtered, centrifuged and dried.
Reaction scheme:
MATERIAL BALANCE-Hexaconazole Batch size (Final output): 1000 Kg
S.No Name of material Input Qty.
(Kg)
Product
Out put
Qty. (Kg)
Recovery Losses Total
Liquid Others
1 Dimethyl sulfate 482
1000
DMF loss
11488
2 Sodium sulfide 26 DMF Waste water 12
3 DCVP 760 1198.0 9278
4 Pot. Hydroxide 310
5 1,2,4-Triazole 245
6 Pot. carbonate 45
7 DMF 1210
8 Water 8410
1000.0 1198.0 9278.0 12.0
Total 11488 11488
3. Propiconazole
Manufacturing process:
1,2,4-1H-Triazole and potassium hydroxide is charged in DMSO to form potassium salt of 1,2 4- 1H-
triazole. 2-Bromo-methyl-2-[(2,4 dichlorophenyl)-4-propyl]-1,3-dioxolan (bromoketal) is gradually added
to DMSO containing potassium salt of triazole. Temperature is raised and maintained for few hours to
complete the reaction. After completion of reaction solvent is removed by distillation. Residue is washed
with water and then crude propiconazole is distilled to get technical grade propiconazole. Residue is
transferred to ETP
Reaction scheme:
MATERIAL BALANCE-Propiconazole Batch size (Final output): 1000 Kg
S.
No
Name of material Input
Qty. (Kg)
Product
Out put
Qty.
(Kg)
Recovery Losses Total
Liquid Others
1 DMSO 1800
1000
DMSO loss
5512
2 Pot. Hydroxide 237 Bromoketal Waste water 20
3 1,2,4-Triazole 265 1210 1480 Residue
4 Bromoketal 1210 DMSO 22
5 Water 2000 1780
1000.0 2990.0 1480.0 42.0
Total 5512 5512
4. Tricyclazole
Manufacturing process:
2-Hydrazino-4-methyl benzothiazol is charged in formic acid at 90-100 °C for 4hours. Temperature is
raised to complete the reaction. After completion of reaction formic acid is distilled out along with some
water. After most of formic acid is distilled out water is charged in to the reactor and residual acid is
neutralized with caustic soda lye slurry is filtered out, centrifuged and dried. Filtrate is sent to ETP.
Reaction scheme:
MATERIAL BALANCE-Tricyclazole Batch size (Final output): 1000 Kg
Name of material Input
Qty. (Kg)
Product
Out put
Qty.
(Kg)
Recovery Losses Total
Liquid Others
HMBT 960
1000
5930
Formic acid 530 Formic acid Waste water
Caustic lye 40 290 4640 Drying loss
Water 4400 40
1000.0 290.0 4600.0 40.0
Total 5930 5930
5. Clodinofob-propargyl
Manufacturing process:
The R-(+)-2-(4-hydroxy-phenoxy)-propionic acid is dissolved in dimethyl formamide and then charge
potassium carbonate and 2,3-difluoro-5-chloro pyridine (DFCP). The mass is heated and stirred for several
hours to complete the reaction. To the resulting intermediate R-(+)-2-[4-(5-chloro-3-fluoro-pyridin-2-
yloxy)-phenoxy]-propionic acid potassium salt propargyl chloride in toluene is charged in the reaction
mass. Temperature is raised to complete the reaction. Reaction mass is filtered to remove inorganic salt.
DMF and toluene is distilled off from organic mass to get crude Clodinafop Propargyl. Further purification
is done to get technical grade Clodinafop Propargyl. Solvent is recovered from mother liquor.
Reaction scheme:
MATERIAL BALANCE-Clodinofob-propargyl Batch size (Final output): 1000 Kg
S.No Name of material Input Qty.
(Kg)
Product
Out put
Qty. (Kg)
Recovery Losses Total
Liquid Others
1 DMF 1889
1000
DMF loss Salt Waste
5481
2 DHPPA 603 DMF 78 1050
3 K2CO3 850 1811 Methanol
Loss
Solvent
Residue
4 DFCP 531 Methanol 48 204
5 Propargyl chloride 289 1100 Aq. Effluent
6 HCl 10 190
7 Methanol 1148
8 Water 161
1000.0 2911 316 1254
Total 5481 5481
6. Penoxsulam
Manufacturing process:
To the mixture of trizolopyrimidine amine, DMSO and pyridine was added substituted benzene sulphonyl
chloride and reaction mixture was stirred for 8h. After completion of reaction DMSO is distilled out
completely. To the crude mixture water was added, stirred and filterted. Filtrate was dried completely to
afford desired product as penoxsulam.
Reaction scheme:
MATERIAL BALANCE-Penoxsulam Batch size (Final output): 1000 Kg
S.
No
Name of material Input
Qty. (Kg)
Product
Out put
Qty.
(Kg)
Recovery Losses Total
Liquid Others
1 Trizolopyrimidine
amine
404
1000
DMSO loss
4260
2 Sulphonyl chloride 672 DMSO Waste water 90
3 Pyridine 164 1930 1160 Drying loss
4 DMSO 2020 80
5 Water 1000
1000 1930 1160 170
Total 4260 4260
7. Propaquizafop
Manufacturing process:
Thionyl chloride was added to the stirred solution of (R)-2-(4-((6-chloroquinoxalin-2-
yl)oxy)phenoxy)propanoic acid in toluene and stirred for few hours. After completion of reaction toluene
was distilled out. Into this DMF and propan-2-one O-(2-hydroxyethyl) oxime was charged, pyridine was
added slowly into this reaction and stirred for 6h. After completion of reaction DMF was distilled
completely and crude mixture was treated with water. White solid was filtered and dried to get desired
product.
Reaction scheme:
MATERIAL BALANCE-Propaquizafop Batch size (Final output): 1000 Kg
S.
No
Name of material Input
Qty. (Kg)
Product
Out put
Qty.
(Kg)
Recovery Losses Total
Liquid Others
1 Carboxylic acid 777
1000
Toluene loss
10482
2 Alcohol 265 Toluene Waste water 148
3 Thionyl chloride 269 2960 2300 DMF loss
4 Pyridine 178 DMF 195
5 DMF 3885 3690 Drying loss
6 Toluene 3108 189
7 Water 2000
1000 6650.0 2300 532
Total 10482 10482
8. Quizalofop ethyl
Manufacturing process:
Charge 2,6-dichloro quinaoxaline and potassium carbonate in dimethyl formamide and charge
ethyl(hydroxy phenoxy) propionate. Temperature was raise to complete the reaction. After completion of
reaction, inorganic salt was filtered off. Adjust pH 4.0 with the help of hydrochloric acid to precipitate
inorganic salt from filtrate. Clarify to remove salt. Distill solvent from organic phase. Crystallize crude
using Methanol and water, filter, centrifuge and dry the product.
Reaction Scheme:
MATERIAL BALANCE-Quizalofop ethyl Batch size (Final output): 1000 Kg
S.
No
Name of material Input
Qty. (Kg)
Product
Out put
Qty.
(Kg)
Recovery Losses Total
Liquid Others
1 DMF 1694
1000
DMF loss
4665
2 Dichloro quinoxaline 585 DMF Water (reuse) 24
3 K2CO3 500 1670 1255 Drying loss
4 Ethyl-2-(4-
hydroxyphenoxy)propi
onate
618 151
5 HCl 9 Inorganic
salt
6 Methanol 1047 565
7 Water 212
1000 1670.0 1255.0 740.0
Total 4665 4665
9. Flubendiamide
Manufacturing process:
Iodo benzoic acid and TEA was dissolved in MDC. Into this thionyl chloride was added and stirred the
mixture for few hour. After completion of reaction MDC and thionyl chloride was distilled completely.
Crude mixture was again dissolved in MDC and flubendamine was added and stirred for 4h. After
completion of reaction MDC was distilled out. Crude mixture was dissolved in THF and mCPBA was
added portion wise and stirred for 2h. After completion of reaction THF is distilled out. Crude reaction
mixture was dissolved in 10% NaHCO3 solution white ppt was filterted off. Residue was washed with
water and dried completely to get desired product as white powder.
Reaction scheme:
MATERIAL BALANCE-Flubendiamide Batch size (Final output): 1000 Kg
S.
No
Name of material Input
Qty. (Kg)
Product
Out put
Qty.(Kg)
Recovery Losses Total
Liquid Others
1 Acid 618
1000
THF MDC loss
9754
2 Amine 410 3175 122
3 Thionyl chloride 187 MDC Waste water THF loss
4 TEA 159 2350 2800 165
5 MDC 2472 Drying loss
6 mCPBA 568 142
7 THF 3340
8 10% NaHCO3 2000
1000 5525 2800 429
Total 9754 9754
10. Thiamethoxam
Manufacturing process:
The Intermediate 3-methyl-4-nitroimino-1,2,3,6-tetrahydro-1,3,5-oxadiazine (MMTO) is taken in
acetonitrile and is reacted with 3-chloro-5-chloro methylthiazole (CCMT) in presence of K2CO3 under
reflux. After completing the reaction, the mass is cooled and the product is crystallized, filtered. The
mother liquor is collected and is sent for solvent recovery. The solid product is washed with water and
dried to get the desired product.
Reaction scheme:
MATERIAL BALANCE-Thiamethoxam Batch size (Final output): 1000 Kg
S.
No
Name of material Input
Qty. (Kg)
Product
Out put
Qty.(Kg)
Recovery Losses Total
Liquid Others
1 CCMT 840
1090
Reaction mass DMF loss
11950
2 MNIO 800 3325 760
3 K2CO3 760 Crude
thiamethoxam
Aq.
effluent
4 DMF 2925 1750 3650
5 Reaction mass 3325 Methanol
6 Water 1775 1375
7 Crude thiamethoxam 1750
8 80% MeOH 1775
1090 6450 3650 760
Total 11950 11950
11.Tebuconazole
ProcessDescription:
Step-1
1-(4-Chlorophenyl)-4,4-Dimethyl-3-Pentanone is reacted with Sodium methoxide inDimethyl
Sulfideandtolueneat40–45°Ctemperatureandcookedtillthereactioniscomplete.DMSis
distilledoutand2-[2-(4-Chlorophenyl)ethyl]-2-(1,1–Dimethylethyl)Oxiraneiscollected
asanintermediate.
Step-2
TheOxiraneintermediateisreactedwith1,2,4-TriazoleinpresenceofDMFat135–140°Ctogetthecrudeproduct.
Step-3
DMF is distilled out under vacuum and the reaction mass is taken in water, centrifuged,washedwithwateranddriedtogettechnicalgradeTebuconazole.TheaqueousMLissenttoETP.
ProcessReaction:
MaterialBalance:
MaterialBalanceforTebuconazole
S.No. RawMaterials Input/MTofProduct(KG)
1 1-(4-Chlorophenyl)4-4-Dimethyl-3-Pentanoate 675
2 Sodiummethoxide 162
3 DimethylSulfide 186
4 Toluene 1400
5 1,2,4-Triazole 206
6 DMF 1100
7 Water 1700
Total 5429
S.No.
Output/MTofProduct(KG)
Remarks
Product
Liquid
Effluent
Air
Emission/loss
Recovery
Solid
Waste
1 Tebuconazole - - 1000 - Product
2 Toluene - 40 1360 - Recycle
3 DMF - 30 1070 - Recycle
4 Effluent 1929 - - - ToETP
Total
1929 70 3430 0
5429
12.Azoxystrobin
ProcessDescription:
MMCPOA(Methyl-3-methoxy-2-2-6-chloropyrimidine-4-4-iyl-oxyphenyl-acrylate)andanhydrous
PotassiumcarbonatearechargedinDMF.
Charge2cyanoPhenoltotheabovereactionmass,addcatalyticamountofCuprousChlorideand
heatthereactionmassto100°Cforfewhours.
Filter the reactionmass to remove inorganics and distil out DMF from reactionmass. Add
hexane andwashthereactionmasswithdilutecaustictoremoveunreactedcyanophenolfromthe
reactionmass.
Crystallize the crude with methanol, centrifuge and dry to get technical grade Azoxystrobin as
whitecrystallinesolid.
ReactionScheme
MaterialBalanceforAzoxystrobinS.No. RawMaterials Input/MTofProduct(KG)
1 MMCPOA 880
2 K2CO3 379
3 DMF 2500
4 2CYANOPHENOL 327
5 CuCl2 11
6 CAUSTICSODA 23
7 WATER 500
8 HEXANE 2500
9 METHANOL 2200
Total 9320
Output/MTofProduct(KG)
S.No.
Product
Liquid
Effluent
AirEmission
/Loss
Recovery
Solid
Waste
Remarks
1 Azoxystrobin - - 1000 - Product
2 DMF - 100 2400 - Recycle
3 AqueousLayer 1000 - - - ToETP
4 METHANOL - 130 2070 - Recycle
5 Hexane - 100 2400 - Recycle
6 InorganicSalts - - - 120 ToIncineration
Total
1000 330 7870 120
9320
13.Pyraclostrobin
ProcessDescription
Step–1
1,4DichloroBenzenereactswith3-ChloroPyrazole inpresenceofcatalyst&solventXylene toform
Intermediate(A)as3-Chloro4-ChloroPhenylPyrazole.
Step-2
2-ChloroBenzylAlcoholreactswithN-MethoxyCarbamatetoformthesecondIntermediate(B),N-
methoxy,N-(2-OxymethylPhenol)Carbamate.
Step-3
Intermediates(A)&(B)thenundergoesCondensationreactioninpresenceofCatalyst&SolventXylene
to give the final product Pyraclostrobin Technical after Filtration, Washing & Drying.Xylene is
recoveredfromtheMLandrecycled.
ReactionScheme
MaterialBalance
14.Picoxystrobin
ProcessDescription
ReactionScheme
MaterialBalance
15.Fluoxastrobin
ProcessDescription:
Step-1
2-HydroxyPhenacylBromide is reactedwithMethoxyAmine inpresenceof catalystaswell asSolvent-
Toluenetoform2-[(1E)-2-Bromo–N-MethoxyEthanimidoyl]Phenolat60–65°C.
Distilouttolueneaftercompletionofreaction.
Step-2
2- [(1E) -2- Bromo–N-MethoxyEthanimidoyl] Phenol reactedwith potassiumTertiary Butoxide
and Tertiary Butyl Nitrate in presence of Butyl Alcohol to form N- Hydroxy –N- Methoxy -1-
Benzofuran-2,3-Diamineat75–80°C.
Step-3
N-Hydroxy–N-Methoxy-1-Benzofuran-2,3-DiamineisreactedwithEthyleneOxideinpresence
ofPotassiumHydroxideat20–25°Ctogive2-[{(3E)-3-Methoxyiaino-1-Benzofuran-2-(3H)–
ylidene}amino}oxy]Ethanol.
Step-4
2- [{(3E) -3-Methoxyamino-1- Benzofuran-2-(3H) –ylidene} amino} oxy] Ethanol undergoes
CyclizationinpresenceofPotassiumHydroxidetoform2-[{(E)5,6–Dihydro1,4,2Dioxazin-3-yl
(methoxyimino)methyl)Phenolat55–60°C.Distiloffn-Butanol.
Step-5
2-[{(E)5,6–Dihydro1,4,2Dioxazin-3-yl(methoxyimino)methyl)Phenolisreactedat80–85°C,
with4,6–Dichloro-5-FluoroPyrimidineinpresenceofPotassiumHydroxideaswellasSolvent–
DimethylFormamidetoform(E)-1-[2-{6-Chloro-5-FluoroPyrimidine-4-yl)oxy}Phenyl]-1-(5,6
Dihydro-1,4,2-Dioxazin-3-yl)–N–Methoxymethanimine.
Step-6
(E)-1-[2-{6-Chloro-5-FluoroPyrimidine-4-yl)oxy}Phenyl]-1-(5,6Dihydro-1,4,2-Dioxazin-3-yl)
–N –Methoxymethanimine is reacted at 60 – 65°C, with O–Chloro Phenol in presence of
PotassiumHydroxideandSolvent–DMFto formfinalproductasFluoxastrobin.DistiloutDMF,
charge water, centrifuge and dry to get Fluoxastrobin technical.
ReactionScheme
Material Balance for Fluoxastrobin
S. No.
Raw Materials
Input/MTof
Product(KG)1 HydroxyPhenylBromide 450
2 MethoxyAmine 100
3 Catalyst 50
4 Toluene 1450
5 PotassiumTertButoxide 233
6 TertButylNitrate 215
7 ButylAlcohol 1600
8 EthyleneOxide 92
9 PotassiumHydroxide 350
10 TrifluoroPyrimidine 345
11 DMF 1200
12 O-Chloro-Phenol 266
13 WaterforWashing 1700
Total 8051
S. No.
Output/MT of Product (KG)
Remarks
Product
Liquid
Air
Emission
Recovery
Solid
1 Fluoxastrobin - - 1000 - Product
2
Aqueous
Layer
2613
-
-
-
ToETP
3 Toluene - 150 1300 - Recycle
4 HBr - 170 - ToScrubber
5 Butanol - 150 1450 - Recycle
6
Residue
-
-
-
18
To
Incineration7 DMF - 120 1080 Recycle
Total
2613 590 4830 18
8051
16.Imidacloprid
ProcessDescription:
2–Chloro,5–ChloromethylPyridine(CCMP)isreactedwithN–NitroIminoImidazolidine
(N-NII)inpresenceofSodiumHydroxideandDimethylFormamideassolventat55–60°C.
After completion of the reaction the slurry is filtered to remove the salts of Sodium
Chloride(NaCl)etc.
The solvent is then removed by distillation from the reaction mass under vacuum, the
residual mass is diluted with water and the resultant slurry is filtered to remove
Imidacloprid.Thewetcakeiswashedwithwater.AqueouslayerissenttoETP.
Methanol is used to crystallize the product to get Imidacloprid Technical.
Reaction Scheme
MaterialBalance:
MaterialBalanceforImidacloprid
S.No.
RawMaterials
Input/MTofProduct
(MT)1 CCMP 873
2 N-NitroIminoidmmidazolidine(N-NII) 825
3 DMF 2134
4 K2CO3 684
5 Water 1000
6 Methanol 400
Total 5916
S.No.
Output/MTofProduct
Remarks
Product
Liquid
Effluent
Air
Emission/
loss
Recovery
Solid
Waste
1 Imidacloprid - - 1000 - Product
2 AqueousLayer 2260 - - - ToETP
3 DMF - 87 2048 - Recycle
4 Methanol - 40 360 - Recycle
6
Residue
-
-
-
121
To
Incineration
Total
2260 127 3408 121
5916
17.Acetamiprid
ProcessDescription:
N-CyanomethylAcetamidate(NCMA)isreactedwith2-Chloro5-(methylaminomethyl)
Pyridine(CMAMP)inMethanolassolventmediaatasub-atmospherictemperature(10–
15°C).Afterthereactioniscompletedtheproductisfilteredanddriedtoobtaintechnical
gradeproduct.ThemotherliquorisdistilledtorecoverMethanolsolventwhichisthen
recycled.
ReactionScheme
MaterialBalance
MaterialBalanceforAcetamiprid
S.No.
RawMaterials
Input/MTofProduct
(KG)
1 NCMA 520
2 CMAMP 700
3 Methanol 1950
Total 3170
S.No.
Output/MTofProduct(KG)
Remarks
Product
Liquid
Effluent
Air
Emission/
Recovery
Solid
Waste1 Acetamiprid - - 1000 - Product
2
Methanol
-
50
2043
-
Recycle
(Also
includes
byproduct
methanol
3
Residue
-
-
-
77
To
Incineratio
n
Total
- 50 3043 77
3170
18.PyrazosulfuronEthyl
ProcessDescription:
Ethyl-1-methyl-5-Sulfenamide-isocyanate-1H-pyrazole-4-carboxylateisreactedwith2-amino-
4,6- dimethoxy pyrimidine in presence of toluene in a reactor under stirring. Mass is
cooked for 2hoursat85-90°C.
Then, cool themass and centrifuge it. Dry the cake to get technical grade Pyrazosulfuron
Ethylproduct.RecoverthetoluenefromtheMLbydistillation.
ReactionScheme
MaterialBalance
MaterialBalanceforPyrazosulfuronEthyl
S.No. RawMaterials Input/MTofProduct(KG)
1 Pyrazole 668
2 Pyrimidine 435
3 Toluene 1300
Total 2403
S.No.
Output/MTofProduct(KG)
Remarks
Product
Liquid
Effluent
Air
Emission
Recovery
Solid
Waste1 Pyrazosulfuron - - 1000 - Product
2 Toluene - 60 1240 - Recycle
3 Residue - - - 80 ForIncineration
4 DryingLoss
-23 - - Toatmosphere
Total
0 83 2240 80
2403
19.Cymoxanil
ProcessDescription:
Step-1:
1-cyanoacetyl-3-ethyl urea and sodium nitrite solution (40%) are added sequentially into
thereactorcontainingwater.Thereactionisallowedtotakeplaceatcontrolledtemperature
of40–
45°Candthereactionmassisheldatthistemperaturetillcompletionofthe
reaction.Thereactionmassisthencooledtoroomtemperature.
Step-2:
Afterthereactionmassof1ststepiscooledtoroomtemperaturedimethylsulfateisadded
toit.
Thereactionmassisheldat50–55°Ctillcompletionofthereaction.
The reactionmass is then cooled to room temperature and centrifuged. The cake
obtained iswashedwithwateranddriedtogiveCymoxaniltechnical.
ReactionScheme:
MaterialBalance:
MaterialBalanceforCymoxanil
S.No. RawMaterials Input/MTofProduct(KG)
7 1CyanoAcetyl3Ethylurea 834
8 Water 1900
9 SodiumNitrite 353
10 DMSO4 626
Total 3713
S.No.
Output/MTofProduct(KG)
Remarks
Product
Liquid
Effluent
Air
Emission
Recovery
Solid
Waste1 Cymoxanil - - 1000 - Product
2 AqueousLayer 2713 - - - ToETP
Total
2713 - 1000 -
3713
20.Flonicamid
ReactionScheme:
MaterialBalance:
21.Chlorantraniliprole
ReactionScheme:
MassBalance:
22.Spirotetramat
ProcessDescription
ReactionScheme:
MassBalance:
23.Metamifop
ProcessDescription:
ReactionScheme:
MassBalance:
24. Pyridaben
Manufacturing process:
To the stirred solution of 2-(tert-butyl)-4,5-dichloropyridazin-3(2H)-one in MeOH was added
sodium methoxide and tert-butylphenylmethyl mercaptan and again stir for 2h at 15 °C.
Methanol was recovered and added water white solid was obtain which was further crystalize in
aq. Methanol.
Reaction scheme:
MATERIAL BALANCE- Pyridaben Batch size (Final output): 1000 Kg
S.
No
Name of material Input
Qty. (Kg)
Product
Out put
Qty. (Kg)
Recovery Losses Total
Liquid Others
1 2-(tert-butyl)-4,5-
dichloropyridazin-3(2H)one
605
1000
MeOH
loss
5450
2 tert-butylphenylmethyl
mercaptan
495 Methanol Aq.
Waste
75
3 NaOMe 150 1425 2900 Drying
loss
4 MeOH 1500 50
5 Water 2000
6 Aq. MeOH 700
1000.0 1425.0 2900.0 125.0 5450
Total 5450
25. Oxadiazon
Manufacturing process:
Reaction was carried out in toluene in presence of NaOMe. Reaction was carried at 100 °C for
6h and then reaction mixture was cooled to room temperature and toluene was recovered. Crude
product was crystallize in MeOH:H2O and then filtered off. White solid was dried completely to
get oxadiazon as desired product.
Reaction scheme:
MATERIAL BALANCE- Oxidiazon Batch size (Final output): 1000 Kg
S.No Name of material Input
Qty.
(Kg)
Product
Qty. (Kg)
Recovery Losses Total
Liquid Others
1 Hydrazine carboxylate 1092.8
1000
Toluene
loss
5249
2 Sodium methoxide 156.4 Toluene Aqueous waste 150
3 Toluene 3000 2850 1149
4 MeOH 800
5 Water 200 Drying
loss
100
1000.0 2850.0 3053.0 250.0
Total 5249 5249
26. Clothianidin
Manufacturing process:
Aqueous MeNH2 in MeOH was added in the nitramide intermediate and heated at 55 °C for 4h.
Reaction mixture was cooled to 10 °C to crystallize the product and then filtered. Solid was dried
to get clothianidin technical.
Reaction Scheme:
MATERIAL BALANCE- Clothianidin Batch size (Final output): 1000 Kg
S.No Name of material Input
Qty.
(Kg)
Product
Qty. (Kg)
Recovery Losses Total
Liquid Others
1 Nitramide 1220
1000
2480
2 Aq. MeNH2 260 800 Aqueous waste
3 MeOH 1000 600
Drying
loss
80
1000.0 800 600 80.0
Total 2480 2480
27. Metiram
Manufacturing process
1st Step: Ethylene diamine and water are charged under stirring condition and added aqueous
ammonia solution and temperature is raised to about 45-50 °C. Now CS2 is added under reflux. So
that pH of the mass is maintained around 10. The mass is kept under these conditions for 6 to 8 h till
the reaction is complete. Reaction mass of the above reaction was charge within 1 and half hour. Then
reaction mass was allowed to settle. The slurry is get filtered under vacuum to get wet cake of
Metiram intermediate.
2nd
Step: Intermediate react with zinc sulphate and hydrogen peroxide under stirring condition. After
30 minutes’ interval, left over mass of is added and maintain for 1 h. At the temperature of 10-20 °C,
slurry is dried using spray drier to get Metiram as desired product.
Chemical reaction
Step-1
H2O
C2H8N2 + 2CS2 + 2 NH4OH C4H14 N4S4 + 2H2O
60 2*76 2*35 246 2*18
Step- 2
4C4H14 N4S4 + 3ZnSO4 + 4H2O + H2O2
4*246 3* 161.5 4*18 34
(C16H33N11S16Zn3)n + 5NH4OH + 3H2SO4 + H2O
1088 5*35 3*98 18
Mass balance
Material Balance-Metiram Batch size (Final output):1000 Kg
S. No. Name of material Input
Qty(Kg)
Product
output
Qty.(Kg)
Recovery
(Kg)
Losses (Kg) Total
liquid other
1. Ethylene di amine 275.73 CS2 Waste
water
Filtration
loss
5567.52
2. Water 200
3. Aq. ammonia 25% 1608.4 72 4145.52 350
4. Carbon disulfide 768.36 1000
5. Zinc sulphate 2371.29
6. Hydrogen
peroxide 50%
343.74
Total 5567.52 5567.52
28. Mandipropamid
Manufacturing process
Step-1: 4-Chloromandilic acid, is taken in toluene and is reacted with Thionyl chloride, evolved gases
are removed by nitrogen purging.
Step-2: The acid chloride is coupled with 3,4-Dichloro-5-fluoro-1,1-Biphenyl]-2-amine at room
temperature and the product is filtered, washed and dried to get the intermediate.
Step-3: The Intermediate substitution with 2-propinyl methanesulfonate at room temperature Filter
and the product is filtered, washed and dried to get the desired product.
Chemical reaction:
Cl
OH
O
OH+ S O
Cl
Cl Cl
OH
O
Cl
+ SO
O+ H Cl
OH
O
Cl
Cl
+
OH
O CH3
NH2
OH
O
NHCl
O CH3
OH
+ H Cl
OH
O
NHCl
O CH3
OH
+ CH3 S
O
O
O CH
O
O
NHCl
OCH3
O
CH
CH
+CH3 S
O
O
OH
Chloro mandilic acid186.59
Thionyl chloride119
DMF
Acid chloride205
Sulfer dioxide64
Hydrochloric acid36.5
Acid chloride 205
Hydroxy methoxy phenethylamine167.2
Intermediate335.7
Hydrochloric acid36.5
Itermediate335.7
2-propinyl methanesulfonate134
Mandipropamid411.8
Methane sulfonic acid96
Mass balance
Material Balance-Mandipropamid Batch size (Final output):1000 Kg
S. No. Name of material Input
Qty (Kg)
Product
output
Qty.(Kg)
Recovery
(Kg)
Losses (Kg) Total
Liquid Others
1. 4-chloromandilic
acid
607.7 Toluene Thionyl
chloride
SO2
4261.96
1620 32.57 208.5
2. Thionyl chloride 407.3
3. DMF 6.07 DMF Toluene HCL
4. toluene 1800 1000
5. 3-methoxy
phenethylamine
544.78 5kg 180 215.92
Methane
sulfonic
acid
Organic
waste
6. 2-propinyl
methanesulfonate
896.11 416.82
583.15
Total 4261.96 4261.96
29. Bixafen
Manufacturing process
Step-1: 3-(Difluoromethyl)-1-methyl-1-H-pyrazol-4-carboxylic acid, is taken in toluene and is
reacted with Thionyl chloride, evolved gases are removed by nitrogen purging.
Step-2: The acid chloride is coupled with 3,4-Dichloro-5-fluoro-1,1-Biphenyl]-2-amine at room
temperature and the product is filtered, washed and dried to get the desired product.
Chemical reaction
N
N
CH3
F F
O
OH
+ S
Cl
Cl
ON
N
CH3
F F
O
Cl
+ S
O
O+ H Cl
N
N
CH3
F F
O
Cl
+ NH2
F
Cl
Cl
NN
CH3
F
F O
NH
F
Cl
Cl
+ H Cl
Carboxylic acid176.2
thionyl chloride119
Acid chloride194.5
sulfer dioxide64
Hydrochloric acid36.5
Di chloro fluoro biphenyl amine256.1
Bixafen 414
Acid chloride194.5
Hydrochloric acid36.5
Mass Balance
Material Balance-Bixafen Batch size (Final output):1000 Kg
S. No. Name of material Input
Qty(Kg)
Product
output
Qty.(Kg)
Recovery
(Kg)
Losses (Kg) Total
Liquid Others
1. Carboxylic acid 500.7 Toluene Thionyl
chloride
SO2
3503.03
1350 16.84 181.86
2. Thionyl chloride 355
3. DMF 5 Toluene HCL
4. toluene 1500 1000
5. Dichlorofluoro
biphenyl amine
742.33 150 207.4
Organic
waste
Aqueous
waste
6. Potassium
carbonate
400 195.72 401.21
Total 3503.03 3503.03
30. Fluxapyroxad
Manufacturing process
Step-1: 3-(Difluoromethyl)-1-methyl-1-H-pyrazol-4-carboxylic acid, is taken in toluene and is
reacted with Thionyl chloride, evolved gases are removed by nitrogen purging.
Step-2: The acid chloride is coupled with 3,4,5-trifluoro-2-aminobiphenyl at room temperature and
the product is filtered, washed and dried to get the desired product.
Chemical Reaction
NN
F
F
CH3
O
OH
+ S O
Cl
Cl
NN
F
F
CH3
O
Cl
+ S
O
O
+ H Cl
Carboxylic acid176.2
Thionyl chloride119
Acid chloride194.5
Sulfer dioxide64
Hydrochloride36.5
NN
F
F
CH3
O
Cl
+
F
FF
NH2 N
N
FF
CH3
O
NH
F
F
F
+
3,4,5-Trifluoro-2-aminobiphenyl223.19
Fluxapyroxad381.3
H Cl
Hydrochloride36.5
Acid chloride194.5
DMF
K2CO3
Material Balance-Fluxapyroxad Batch size (Final output):1000 Kg
S. No. Name of material Input
Qty(Kg)
Product
output
Qty.(Kg)
Recovery
(Kg)
Losses (Kg) Total
Liquid Others
1. Carboxylic acid 554.74 Toluene Thionyl
chloride
SO2
3745.92
1498 19.02 201.42
2. Thionyl chloride 393.54
3. DMF 5.54 Toluene HCL
4. toluene 1664 1000
5. 3,4,5-trifloro-2-
aminobiphenyl
702.40 166 227.53
Organic
waste
Aqueous
waste
6. Potassium
carbonate
425.7 190.25 443.7
Total !"#$.!" 3745.92
31. Sulfoxaflor
Manufacturing process
Sulfilimine dissolve in ethylene dichloride and added sodium permanganate at 0-5 °C digest
for 4-5 h. After 5 h added sodium bisulphite dissolve in water at room temperature maintain for
5-6 h and the product is filtered, washed and dried to get the desired product.
Chemical Reaction
N
S
CH3
N
CH3
F
F
F
N
+O Mn
5-
O
O
O Na
N
S
CH3
N
CH3
F
FF
N
O
sulfilimine261.27
sodium permagnate142
Na2S2O7
Sulfoxaflor277.27
Mass Balance
Material Balance- Sulfoxaflor Batch size (Final output):1000 Kg
S. No. Name of material Input
Qty(Kg)
Product
output
Qty.(Kg)
Recovery
(Kg)
Losses (Kg) Total
Liquid Other
1. Sulfilimine 1070 EDC EDC Vapour
loss
Aqueous
waste
14200.6
6
4922
428 7850.66
2. Sodium
permanganate
581.97
3. Ethylene dichloride 5350
4. Sodium bisulphite 778.69 1000
5. Water 6420
Total !"#$$.!! 14200.6
6
32. Benzovindiflupyr
Manufacturing Process
Step-1: 3-(Difluoromethyl)-1-methyl-1-H-pyrazol-4-carboxylic acid, is taken in ethylene dichloride
and is reacted with Thionyl chloride, evolved gases are removed by nitrogen purging.
Step-2: The acid chloride is coupled with 1, 2,3, 4-tetrahydro-1,4-methanonaphthalen-5-amine
at room temperature and the product is filtered, washed and dried to get the desired product.
Chemical reaction:
N
N
CH3
O
OH
F
F
+ S
O
Cl Cl
NN
CH3
O
Cl
F
F
+
Step-1
Step-2
NN
CH3
O
Cl
F
F
+
NH2
Cl
Cl
NN
NH
O
CH3
F
F Cl
Cl
3-(difluoromethyl)-1-methyl-1H-pyrazole-4-carboxylic acid
Mass: 176.12
sulfurous dichloride
Mass: 118.97
DMF
3-(difluoromethyl)-1-methyl-1H-pyrazole-4-carbonyl chloride
Mass: 194.56
Mass: 36.46
3-(difluoromethyl)-1-methyl-1H-pyrazole-4-carbonyl chloride
Mass: 194.56
9-(dichloromethylidene)-1,2,3,4-tetrahydro-1,4-methanonaphthalen-5-amine
Mass: 240.13Mass: 398.23
N-[9-(dichloromethylidene)-1,2,3,4-tetrahydro-1,4-methanonaphthalen-5-yl]-3-(difluoromethyl)-1-methyl-1H-pyrazole-4-carboxamide
+ ClH
Mass: 36.46
ClH + S
O
OSulferdioxide64
Mass Balance
MATERIAL BALANCE- Benzovindiflupyr Batch size (Final output): 1000 Kg
S.
No.
Name of
Material
Input
Qty.
(Kg)
Products
out put
Qty. (Kg)
Recovery
(Kg)
Losses (Kg) Total
Liquid Others
4709.58
1. EDC 1672
1000
EDC EDC
vapour
loss
HCL
2. Carboxylic acid 557.33 1505
115.5
3. DMF 5.57
4. Triethylamine 320.28 167 SO2
5. SOCl2 395.40
6. DCMTMPA 759.00 202.5
7. Water 1000
Aqueous
waste
1719.58
Total 4709.58 4709.58
33. FLUOPRAM TECHNICAL
Manufacturing Process
Step-1: 2-(Trifluoromethyl) benzoic acid (TFBC), is taken in ethylene dichloride and is reacted with
Thionyl chloride, evolved gases are removed by nitrogen purging.
Step-2: 3-chloro-5-(trifluoromethyl)-2-ethylacetamide-pyridinyl with water under stirrer heat reaction
mass at 40-45°C. Started addition of hydrochloric acid in two hours.
Reaction mass heat up to reflux for 3-4 hours. Cool to 30°C, added two times EDC in mass under
stirrer for one hour, reaction mass taken for layer separation, organic layer concentrate under vacuum
distillation. Obtained crude material taken for next step.
Step-3: The acid chloride is coupled with Intermediate at room temperature and the product is
filtered, washed and dried to get the desired product.
Chemical reaction:
FF
F
O
OH
+
F F
F
O
ClS
OO+S
O
ClCl
Step-1
Step-2
F
FF O
Cl
+
N
F
F
FCl
NH
OCH3
ON
F
FF Cl
NH
F
FF
ClHOH2 N
F
F
F
Cl
NH2
+CH3
O
OH
+ N
F
F
F
Cl
NH2
+ ClH
Step-3
+ ClH
chloro tri fluro methyl 2-pyridine ethanamine266.64
Acetic acid60.05
Cat
NaOH
Trifluoromethyl banzoic acid190.11
Thionyl chloride119 Acid chloride
208.56
sulpher dioxide64
Hydrochloric acid36.5
Acid chloride208.56
Water18 Intermediate
224.61
intermediate224.61
Fluopyram396.71
Hydrochloric acid36.5
Mass Balance
MATERIAL BALANCE- Fluopyram Batch size (Final output): 1000 Kg
S.
No
Name of
Material
Input
Qty.
(Kg)
Product
s out put
Qty.
(Kg)
Recovery
Kg
Losses (Kg) Total
Liquid Others
1 EDC
1690
1000
EDC
EDC
vapour
loss
HCL
6147.16
2 DFMPCA 563.64 1555 135 108.21
3 DMF 5.63 Acetic acid SO2
4 SOCl2 370.31 191.04 189.74
5. Chloro
trifluoromethyl
pyridine
ethaneamine
849
Aqueous
waste
6 Hydrochloric
acid 387
2968.17
7 Water 2163
8 Sodium
hydroxide 118.58
Total 6147.16 6147.16
34. Dinetofuron technical
Manufacturing Process
3-Aminomethyl tetrahydrofuron with water under stirrer added sodium hydroxide, sodium chloride
and diethylnitrosourea reaction at 0-5 °C. Maintain for 10 h and the product is filtered, washed and
dried to get the desired product.
Chemical Reaction:
O
NH2
+
CH3
N
O
CH3
NH
N O
O
O
N
NH
CH3
NH
N
O
O
+ CH3 OH
3-Amino methyl tetrahydrofuron101.15
Dimethylnitroso urea133.11
NaOH
NaCL
Dinetofuron202.21
Methanol32
Mass balance
Material Balance- Dinetofuron Batch size (Final output): 1000 Kg
S.
No
Name of
Material
Input
Qty.
(Kg)
Product
s out
put Qty.
(Kg)
Recovery
Losses Total
Liquid Others
3463.6
1. 3-Amino methyl
tetrahydrofuron 610.02
1000
Methanol Aqueous
waste
2. Dimethylnitroso
urea 842.87
192.62 2270.94
3. Sodium
hydroxide 237.67
4. Sodium chloride 553
5. Water 1220
Total 3463.56 3463.56
35. Bentazone Technical
Manufacturing Process
2-Amino benzoic acid is charged in to ethylene dichloride and reacted with isopropyl amine
and chlorosulphonic acid at room temperature for 6 h. Washed with water and concentrate
EDC under vacuum and filtered dried to get the desired product.
Chemical Reaction:
NH2 O
OCH3 +
NH2
CH3CH3
+ Cl S
O
O
OH
O
NCH3
NH
S O
O
+ H Cl + CH3 OH + OH2
2-Amino banzoic acid methyl ester151.16
Isopropylamine59.11
chlorosulphonic acid116.5
Bentazone240.27
36.5
3218
Mass Balance
Material Balance- Bantazone Batch size (Final output): 1000 Kg
S.
No
Name of
Material
Input
Qty.
(Kg)
Products
out put
Qty. (Kg)
Recovery
Kg
Losses (Kg) Total
Liquid Others
5396.42
1. Amino benzoic
acid 741
1000
EDC Aqueou
s waste HCL
2. Isopropyl amine 304.22
2045.16
1837.6 178.92
3. Chlorosulphonic
acid
628.20 EDC Methan
ol
4. EDC 2223
177.84 156.9
5. Water 1500
Total 5396.42 5396.42
36. Saflufenacil
Manufacturing process
2-chloro-5-[2,6-dioxo-4-(trifluoromethyl)-3,6-dihydropyrimidin-1(2H)-yl]-4-fluoro-N[methyl(propan-
2-yl) sulfamoyl]benzamide in to toluene and added catalyst under stirring and added dimethyl
sulphate at room temperature for 3 h and digest 40-45 °C. The desired product is filtered, washed and
dried to get the desired product.
Chemical Reaction
NNH
F
F
FO
OF Cl
NH
O
S
O
ON
CH3
CH3CH3
+
O
S
OO
O
CH3CH3
NN
F
F
FO
OF Cl
NH
O
S
O
ON
CH3
CH3CH3
CH3+
CH3 O
SO
O
OH
2-chloro-5-[2,6-dioxo-4-(trifluoromethyl)-3,6-dihydropyrimidin-1(2H)-yl]-4-fluoro-N-[methyl(pr
opan-2-yl)sulfamoyl]benzamide486.82
Dimethyl sulphate126
Saflufenacil501.85
Methyl hydrogen sulfate112
Mass Balance Material Balance- Saflufenacil Batch size (Final output): 1000 Kg
S.
No
Name of
Material
Input Qty.
(Kg)
Products
out put
Qty. (Kg)
Recovery
(Kg)
Losses (Kg) Total
Liquid Others 5793.66
1. Starting
Material 1143.2
1000
Toluene
Toluene
Vapour
loss
Aqueous
waste
2. Toluene 3429.6 3120.93
308.66 1100.67
3. Dimethyl
sulphate 353
Methyl
hydrogen
Sulphate
4. Catalyst
22.86
5. 10% NaOH
Solution 845 263.4
Total 5793.66 5793.66
37. Clomazone
Manufacturing process:
Charged in reactor ethylene dichloride and 1-chloro-2-(chloromethyl)benzene under stirrer with
triethylamine, isoxazolidinone. Reaction mass maintained at 0 °C for 24 h to give final products of
Clomazone. Acidic water and solvent was recovered to get desired Clomazone technical.
Chemical reaction:
NH
O
CH3
CH3
O
+
Cl
ClN
O
CH3
CH3
OCl
+ ClH
Step-1
Mass: 115.13
4,4-dimethyl-1,2-oxazolidin-3-one
Mass: 161.02
1-chloro-2-(chloromethyl)benzene
Mass: 239.69
2-[(2-chlorophenyl)methyl]-4,4-dimethyl-1,2-oxazolidin-3-one
Mass: 36.46
Mass Balance
MATERIAL BALANCE-Clomazone Batch size (Final output): 1000 Kg
S. No Name of Material Input
Qty. (Kg)
Products
output Qty.
(Kg)
Recovery Losses
Total Liquid Others
1 EDC 3750.87
1000
EDC Water mL EDC
6791.62
2 Isoxazolidinone 600.41 3375.78 1266.52 375.09
3 Dichloromethylben
zene 856.25 TEA HCL
4 Triethylamine 554.09 554.09 190.14
5 Hydrochloric acid 30.00 HCL
6 Water 1000 30.00
Total 6791.62 6791.62
38. Tembortione
Manufacturing process
Charged in reactor acetonitrile and Benzoic acid Cyclohexen ester under stirrer with triethylamine
Cynoacetone. Reaction mass maintained at 30 °C for 24 h to give final products of Tembortione.
Recovered solvent, given acidic water wash to get crystallized Tembortione technical.
Chemical reaction:
O
O
O
Cl S
O
O
CH3
O
F
FF
O
Cl
S OO
CH3
O
F
F
F
O
O
Mass: 440.81
3-oxocyclohex-1-en-1-yl 2-chloro-4-(methanesulfonyl)-3-[(2,2,2-trifluoroethoxy)methyl]benzoate
2-{2-chloro-4-(methanesulfonyl)-3-[(2,2,2-trifluoroethoxy)methyl]benzoyl}cyclohexane-1,3-dione
Mass: 440.81
catalyst
Mass Balance
MATERIAL BALANCE- Tembortione Batch size (Final output): 1000 Kg
S.
No Name of Material
Input
Qty. (Kg)
Products
output
Qty. (Kg)
Recovery
Kg
Losses (Kg) Total
Liquid Others
1 ACN 4623.53
1000
ACN Aqueous
waste ACN
7441.16
2 Benzoic
acidcyclohexen 1176.47
3 Cynoacetone 58.82 4161.17 1641.16
462.35 4 Triethylamine 58.82
Organic
waste 5 Hydrochloric acid 23.52
6 Water 1500 176.48
Total 7441.16 7441.16
39. Sulfentrazone technical
Manufacturing process:
2-(5-amino-2,4-dichlorophenyl)-4-(difluoromethyl)-5-methyl-2,4-dihydro-3H-1,2,4-triazol-3-one in
toluene under stirrer with Methane sulfonyl chloride. Reaction mass maintained at 120 °C for 12 h to
give final products of Sulfentrazone. Recovered half volume of toluene and cool to room temperature
filtered and dried to get final desired compound.
Chemical reaction:
++ ClH
Step-1
Methanesulfonyl chloride114.55
36.46
Cl
Cl
NH2
N
N
N
F
F
CH3
OCH3
S
O
O
Cl
Cl
Cl
NH
N
N
N
F
F
CH3
O
S
O
CH3O
Sulfentrazone387.19
ADMDT309.10
Mass Balance
MATERIAL BALANCE- Sulfentrazone Batch size (Final output): 1000 Kg
S.
No Name of Material
Input
Qty. (Kg)
Products
output
Qty. (Kg)
Recovery Losses
Total Liquid Others
1 Toluene 3990.28
1000
Toluene Toluene Organic
waste
5293.87
2 ADMDT
939.19
3591.25
399.02 205.81
3 Methane sulfonyl
chloride 355.02
Triphen
ylphosp
hine
HCL
4 Triphenylphosphine 9.38
9.38
88.41
Total 5293.87 5293.87
27. Metiram
Manufacturing process
1st Step: Ethylene diamine and water are charged under stirring condition and added aqueous
ammonia solution and temperature is raised to about 45-50 °C. Now CS2 is added under reflux. So
that pH of the mass is maintained around 10. The mass is kept under these conditions for 6 to 8 h till
the reaction is complete. Reaction mass of the above reaction was charge within 1 and half hour. Then
reaction mass was allowed to settle. The slurry is get filtered under vacuum to get wet cake of
Metiram intermediate.
2nd
Step: Intermediate react with zinc sulphate and hydrogen peroxide under stirring condition. After
30 minutes’ interval, left over mass of is added and maintain for 1 h. At the temperature of 10-20 °C,
slurry is dried using spray drier to get Metiram as desired product.
Chemical reaction
Step-1
H2O
C2H8N2 + 2CS2 + 2 NH4OH C4H14 N4S4 + 2H2O
60 2*76 2*35 246 2*18
Step- 2
4C4H14 N4S4 + 3ZnSO4 + 4H2O + H2O2
4*246 3* 161.5 4*18 34
(C16H33N11S16Zn3)n + 5NH4OH + 3H2SO4 + H2O
1088 5*35 3*98 18
Mass balance
Material Balance-Metiram Batch size (Final output):1000 Kg
S. No. Name of material Input
Qty(Kg)
Product
output
Qty.(Kg)
Recovery
(Kg)
Losses (Kg) Total
liquid other
1. Ethylene di amine 275.73 CS2 Waste
water
Filtration
loss
5567.52
2. Water 200
3. Aq. ammonia 25% 1608.4 72 4145.52 350
4. Carbon disulfide 768.36 1000
5. Zinc sulphate 2371.29
6. Hydrogen
peroxide 50%
343.74
Total 5567.52 5567.52
28. Mandipropamid
Manufacturing process
Step-1: 4-Chloromandilic acid, is taken in toluene and is reacted with Thionyl chloride, evolved gases
are removed by nitrogen purging.
Step-2: The acid chloride is coupled with 3,4-Dichloro-5-fluoro-1,1-Biphenyl]-2-amine at room
temperature and the product is filtered, washed and dried to get the intermediate.
Step-3: The Intermediate substitution with 2-propinyl methanesulfonate at room temperature Filter
and the product is filtered, washed and dried to get the desired product.
Chemical reaction:
Cl
OH
O
OH+ S O
Cl
Cl Cl
OH
O
Cl
+ SO
O+ H Cl
OH
O
Cl
Cl
+
OH
O CH3
NH2
OH
O
NHCl
O CH3
OH
+ H Cl
OH
O
NHCl
O CH3
OH
+ CH3 S
O
O
O CH
O
O
NHCl
OCH3
O
CH
CH
+CH3 S
O
O
OH
Chloro mandilic acid186.59
Thionyl chloride119
DMF
Acid chloride205
Sulfer dioxide64
Hydrochloric acid36.5
Acid chloride 205
Hydroxy methoxy phenethylamine167.2
Intermediate335.7
Hydrochloric acid36.5
Itermediate335.7
2-propinyl methanesulfonate134
Mandipropamid411.8
Methane sulfonic acid96
Mass balance
Material Balance-Mandipropamid Batch size (Final output):1000 Kg
S. No. Name of material Input
Qty (Kg)
Product
output
Qty.(Kg)
Recovery
(Kg)
Losses (Kg) Total
Liquid Others
1. 4-chloromandilic
acid
607.7 Toluene Thionyl
chloride
SO2
4261.96
1620 32.57 208.5
2. Thionyl chloride 407.3
3. DMF 6.07 DMF Toluene HCL
4. toluene 1800 1000
5. 3-methoxy
phenethylamine
544.78 5kg 180 215.92
Methane
sulfonic
acid
Organic
waste
6. 2-propinyl
methanesulfonate
896.11 416.82
583.15
Total 4261.96 4261.96
29. Bixafen
Manufacturing process
Step-1: 3-(Difluoromethyl)-1-methyl-1-H-pyrazol-4-carboxylic acid, is taken in toluene and is
reacted with Thionyl chloride, evolved gases are removed by nitrogen purging.
Step-2: The acid chloride is coupled with 3,4-Dichloro-5-fluoro-1,1-Biphenyl]-2-amine at room
temperature and the product is filtered, washed and dried to get the desired product.
Chemical reaction
N
N
CH3
F F
O
OH
+ S
Cl
Cl
ON
N
CH3
F F
O
Cl
+ S
O
O+ H Cl
N
N
CH3
F F
O
Cl
+ NH2
F
Cl
Cl
NN
CH3
F
F O
NH
F
Cl
Cl
+ H Cl
Carboxylic acid176.2
thionyl chloride119
Acid chloride194.5
sulfer dioxide64
Hydrochloric acid36.5
Di chloro fluoro biphenyl amine256.1
Bixafen 414
Acid chloride194.5
Hydrochloric acid36.5
Mass Balance
Material Balance-Bixafen Batch size (Final output):1000 Kg
S. No. Name of material Input
Qty(Kg)
Product
output
Qty.(Kg)
Recovery
(Kg)
Losses (Kg) Total
Liquid Others
1. Carboxylic acid 500.7 Toluene Thionyl
chloride
SO2
3503.03
1350 16.84 181.86
2. Thionyl chloride 355
3. DMF 5 Toluene HCL
4. toluene 1500 1000
5. Dichlorofluoro
biphenyl amine
742.33 150 207.4
Organic
waste
Aqueous
waste
6. Potassium
carbonate
400 195.72 401.21
Total 3503.03 3503.03
30. Fluxapyroxad
Manufacturing process
Step-1: 3-(Difluoromethyl)-1-methyl-1-H-pyrazol-4-carboxylic acid, is taken in toluene and is
reacted with Thionyl chloride, evolved gases are removed by nitrogen purging.
Step-2: The acid chloride is coupled with 3,4,5-trifluoro-2-aminobiphenyl at room temperature and
the product is filtered, washed and dried to get the desired product.
Chemical Reaction
NN
F
F
CH3
O
OH
+ S O
Cl
Cl
NN
F
F
CH3
O
Cl
+ S
O
O
+ H Cl
Carboxylic acid176.2
Thionyl chloride119
Acid chloride194.5
Sulfer dioxide64
Hydrochloride36.5
NN
F
F
CH3
O
Cl
+
F
FF
NH2 N
N
FF
CH3
O
NH
F
F
F
+
3,4,5-Trifluoro-2-aminobiphenyl223.19
Fluxapyroxad381.3
H Cl
Hydrochloride36.5
Acid chloride194.5
DMF
K2CO3
Material Balance-Fluxapyroxad Batch size (Final output):1000 Kg
S. No. Name of material Input
Qty(Kg)
Product
output
Qty.(Kg)
Recovery
(Kg)
Losses (Kg) Total
Liquid Others
1. Carboxylic acid 554.74 Toluene Thionyl
chloride
SO2
3745.92
1498 19.02 201.42
2. Thionyl chloride 393.54
3. DMF 5.54 Toluene HCL
4. toluene 1664 1000
5. 3,4,5-trifloro-2-
aminobiphenyl
702.40 166 227.53
Organic
waste
Aqueous
waste
6. Potassium
carbonate
425.7 190.25 443.7
Total !"#$.!" 3745.92
31. Sulfoxaflor
Manufacturing process
Sulfilimine dissolve in ethylene dichloride and added sodium permanganate at 0-5 °C digest
for 4-5 h. After 5 h added sodium bisulphite dissolve in water at room temperature maintain for
5-6 h and the product is filtered, washed and dried to get the desired product.
Chemical Reaction
N
S
CH3
N
CH3
F
F
F
N
+O Mn
5-
O
O
O Na
N
S
CH3
N
CH3
F
FF
N
O
sulfilimine261.27
sodium permagnate142
Na2S2O7
Sulfoxaflor277.27
Mass Balance
Material Balance- Sulfoxaflor Batch size (Final output):1000 Kg
S. No. Name of material Input
Qty(Kg)
Product
output
Qty.(Kg)
Recovery
(Kg)
Losses (Kg) Total
Liquid Other
1. Sulfilimine 1070 EDC EDC Vapour
loss
Aqueous
waste
14200.6
6
4922
428 7850.66
2. Sodium
permanganate
581.97
3. Ethylene dichloride 5350
4. Sodium bisulphite 778.69 1000
5. Water 6420
Total !"#$$.!! 14200.6
6
32. Benzovindiflupyr
Manufacturing Process
Step-1: 3-(Difluoromethyl)-1-methyl-1-H-pyrazol-4-carboxylic acid, is taken in ethylene dichloride
and is reacted with Thionyl chloride, evolved gases are removed by nitrogen purging.
Step-2: The acid chloride is coupled with 1, 2,3, 4-tetrahydro-1,4-methanonaphthalen-5-amine
at room temperature and the product is filtered, washed and dried to get the desired product.
Chemical reaction:
N
N
CH3
O
OH
F
F
+ S
O
Cl Cl
NN
CH3
O
Cl
F
F
+
Step-1
Step-2
NN
CH3
O
Cl
F
F
+
NH2
Cl
Cl
NN
NH
O
CH3
F
F Cl
Cl
3-(difluoromethyl)-1-methyl-1H-pyrazole-4-carboxylic acid
Mass: 176.12
sulfurous dichloride
Mass: 118.97
DMF
3-(difluoromethyl)-1-methyl-1H-pyrazole-4-carbonyl chloride
Mass: 194.56
Mass: 36.46
3-(difluoromethyl)-1-methyl-1H-pyrazole-4-carbonyl chloride
Mass: 194.56
9-(dichloromethylidene)-1,2,3,4-tetrahydro-1,4-methanonaphthalen-5-amine
Mass: 240.13Mass: 398.23
N-[9-(dichloromethylidene)-1,2,3,4-tetrahydro-1,4-methanonaphthalen-5-yl]-3-(difluoromethyl)-1-methyl-1H-pyrazole-4-carboxamide
+ ClH
Mass: 36.46
ClH + S
O
OSulferdioxide64
Mass Balance
MATERIAL BALANCE- Benzovindiflupyr Batch size (Final output): 1000 Kg
S.
No.
Name of
Material
Input
Qty.
(Kg)
Products
out put
Qty. (Kg)
Recovery
(Kg)
Losses (Kg) Total
Liquid Others
4709.58
1. EDC 1672
1000
EDC EDC
vapour
loss
HCL
2. Carboxylic acid 557.33 1505
115.5
3. DMF 5.57
4. Triethylamine 320.28 167 SO2
5. SOCl2 395.40
6. DCMTMPA 759.00 202.5
7. Water 1000
Aqueous
waste
1719.58
Total 4709.58 4709.58
33. FLUOPRAM TECHNICAL
Manufacturing Process
Step-1: 2-(Trifluoromethyl) benzoic acid (TFBC), is taken in ethylene dichloride and is reacted with
Thionyl chloride, evolved gases are removed by nitrogen purging.
Step-2: 3-chloro-5-(trifluoromethyl)-2-ethylacetamide-pyridinyl with water under stirrer heat reaction
mass at 40-45°C. Started addition of hydrochloric acid in two hours.
Reaction mass heat up to reflux for 3-4 hours. Cool to 30°C, added two times EDC in mass under
stirrer for one hour, reaction mass taken for layer separation, organic layer concentrate under vacuum
distillation. Obtained crude material taken for next step.
Step-3: The acid chloride is coupled with Intermediate at room temperature and the product is
filtered, washed and dried to get the desired product.
Chemical reaction:
FF
F
O
OH
+
F F
F
O
ClS
OO+S
O
ClCl
Step-1
Step-2
F
FF O
Cl
+
N
F
F
FCl
NH
OCH3
ON
F
FF Cl
NH
F
FF
ClHOH2 N
F
F
F
Cl
NH2
+CH3
O
OH
+ N
F
F
F
Cl
NH2
+ ClH
Step-3
+ ClH
chloro tri fluro methyl 2-pyridine ethanamine266.64
Acetic acid60.05
Cat
NaOH
Trifluoromethyl banzoic acid190.11
Thionyl chloride119 Acid chloride
208.56
sulpher dioxide64
Hydrochloric acid36.5
Acid chloride208.56
Water18 Intermediate
224.61
intermediate224.61
Fluopyram396.71
Hydrochloric acid36.5
Mass Balance
MATERIAL BALANCE- Fluopyram Batch size (Final output): 1000 Kg
S.
No
Name of
Material
Input
Qty.
(Kg)
Product
s out put
Qty.
(Kg)
Recovery
Kg
Losses (Kg) Total
Liquid Others
1 EDC
1690
1000
EDC
EDC
vapour
loss
HCL
6147.16
2 DFMPCA 563.64 1555 135 108.21
3 DMF 5.63 Acetic acid SO2
4 SOCl2 370.31 191.04 189.74
5. Chloro
trifluoromethyl
pyridine
ethaneamine
849
Aqueous
waste
6 Hydrochloric
acid 387
2968.17
7 Water 2163
8 Sodium
hydroxide 118.58
Total 6147.16 6147.16
34. Dinetofuron technical
Manufacturing Process
3-Aminomethyl tetrahydrofuron with water under stirrer added sodium hydroxide, sodium chloride
and diethylnitrosourea reaction at 0-5 °C. Maintain for 10 h and the product is filtered, washed and
dried to get the desired product.
Chemical Reaction:
O
NH2
+
CH3
N
O
CH3
NH
N O
O
O
N
NH
CH3
NH
N
O
O
+ CH3 OH
3-Amino methyl tetrahydrofuron101.15
Dimethylnitroso urea133.11
NaOH
NaCL
Dinetofuron202.21
Methanol32
Mass balance
Material Balance- Dinetofuron Batch size (Final output): 1000 Kg
S.
No
Name of
Material
Input
Qty.
(Kg)
Product
s out
put Qty.
(Kg)
Recovery
Losses Total
Liquid Others
3463.6
1. 3-Amino methyl
tetrahydrofuron 610.02
1000
Methanol Aqueous
waste
2. Dimethylnitroso
urea 842.87
192.62 2270.94
3. Sodium
hydroxide 237.67
4. Sodium chloride 553
5. Water 1220
Total 3463.56 3463.56
35. Bentazone Technical
Manufacturing Process
2-Amino benzoic acid is charged in to ethylene dichloride and reacted with isopropyl amine
and chlorosulphonic acid at room temperature for 6 h. Washed with water and concentrate
EDC under vacuum and filtered dried to get the desired product.
Chemical Reaction:
NH2 O
OCH3 +
NH2
CH3CH3
+ Cl S
O
O
OH
O
NCH3
NH
S O
O
+ H Cl + CH3 OH + OH2
2-Amino banzoic acid methyl ester151.16
Isopropylamine59.11
chlorosulphonic acid116.5
Bentazone240.27
36.5
3218
Mass Balance
Material Balance- Bantazone Batch size (Final output): 1000 Kg
S.
No
Name of
Material
Input
Qty.
(Kg)
Products
out put
Qty. (Kg)
Recovery
Kg
Losses (Kg) Total
Liquid Others
5396.42
1. Amino benzoic
acid 741
1000
EDC Aqueou
s waste HCL
2. Isopropyl amine 304.22
2045.16
1837.6 178.92
3. Chlorosulphonic
acid
628.20 EDC Methan
ol
4. EDC 2223
177.84 156.9
5. Water 1500
Total 5396.42 5396.42
36. Saflufenacil
Manufacturing process
2-chloro-5-[2,6-dioxo-4-(trifluoromethyl)-3,6-dihydropyrimidin-1(2H)-yl]-4-fluoro-N[methyl(propan-
2-yl) sulfamoyl]benzamide in to toluene and added catalyst under stirring and added dimethyl
sulphate at room temperature for 3 h and digest 40-45 °C. The desired product is filtered, washed and
dried to get the desired product.
Chemical Reaction
NNH
F
F
FO
OF Cl
NH
O
S
O
ON
CH3
CH3CH3
+
O
S
OO
O
CH3CH3
NN
F
F
FO
OF Cl
NH
O
S
O
ON
CH3
CH3CH3
CH3+
CH3 O
SO
O
OH
2-chloro-5-[2,6-dioxo-4-(trifluoromethyl)-3,6-dihydropyrimidin-1(2H)-yl]-4-fluoro-N-[methyl(pr
opan-2-yl)sulfamoyl]benzamide486.82
Dimethyl sulphate126
Saflufenacil501.85
Methyl hydrogen sulfate112
Mass Balance Material Balance- Saflufenacil Batch size (Final output): 1000 Kg
S.
No
Name of
Material
Input Qty.
(Kg)
Products
out put
Qty. (Kg)
Recovery
(Kg)
Losses (Kg) Total
Liquid Others 5793.66
1. Starting
Material 1143.2
1000
Toluene
Toluene
Vapour
loss
Aqueous
waste
2. Toluene 3429.6 3120.93
308.66 1100.67
3. Dimethyl
sulphate 353
Methyl
hydrogen
Sulphate
4. Catalyst
22.86
5. 10% NaOH
Solution 845 263.4
Total 5793.66 5793.66
37. Clomazone
Manufacturing process:
Charged in reactor ethylene dichloride and 1-chloro-2-(chloromethyl)benzene under stirrer with
triethylamine, isoxazolidinone. Reaction mass maintained at 0 °C for 24 h to give final products of
Clomazone. Acidic water and solvent was recovered to get desired Clomazone technical.
Chemical reaction:
NH
O
CH3
CH3
O
+
Cl
ClN
O
CH3
CH3
OCl
+ ClH
Step-1
Mass: 115.13
4,4-dimethyl-1,2-oxazolidin-3-one
Mass: 161.02
1-chloro-2-(chloromethyl)benzene
Mass: 239.69
2-[(2-chlorophenyl)methyl]-4,4-dimethyl-1,2-oxazolidin-3-one
Mass: 36.46
Mass Balance
MATERIAL BALANCE-Clomazone Batch size (Final output): 1000 Kg
S. No Name of Material Input
Qty. (Kg)
Products
output Qty.
(Kg)
Recovery Losses
Total Liquid Others
1 EDC 3750.87
1000
EDC Water mL EDC
6791.62
2 Isoxazolidinone 600.41 3375.78 1266.52 375.09
3 Dichloromethylben
zene 856.25 TEA HCL
4 Triethylamine 554.09 554.09 190.14
5 Hydrochloric acid 30.00 HCL
6 Water 1000 30.00
Total 6791.62 6791.62
38. Tembortione
Manufacturing process
Charged in reactor acetonitrile and Benzoic acid Cyclohexen ester under stirrer with triethylamine
Cynoacetone. Reaction mass maintained at 30 °C for 24 h to give final products of Tembortione.
Recovered solvent, given acidic water wash to get crystallized Tembortione technical.
Chemical reaction:
O
O
O
Cl S
O
O
CH3
O
F
FF
O
Cl
S OO
CH3
O
F
F
F
O
O
Mass: 440.81
3-oxocyclohex-1-en-1-yl 2-chloro-4-(methanesulfonyl)-3-[(2,2,2-trifluoroethoxy)methyl]benzoate
2-{2-chloro-4-(methanesulfonyl)-3-[(2,2,2-trifluoroethoxy)methyl]benzoyl}cyclohexane-1,3-dione
Mass: 440.81
catalyst
Mass Balance
MATERIAL BALANCE- Tembortione Batch size (Final output): 1000 Kg
S.
No Name of Material
Input
Qty. (Kg)
Products
output
Qty. (Kg)
Recovery
Kg
Losses (Kg) Total
Liquid Others
1 ACN 4623.53
1000
ACN Aqueous
waste ACN
7441.16
2 Benzoic
acidcyclohexen 1176.47
3 Cynoacetone 58.82 4161.17 1641.16
462.35 4 Triethylamine 58.82
Organic
waste 5 Hydrochloric acid 23.52
6 Water 1500 176.48
Total 7441.16 7441.16
39. Sulfentrazone technical
Manufacturing process:
2-(5-amino-2,4-dichlorophenyl)-4-(difluoromethyl)-5-methyl-2,4-dihydro-3H-1,2,4-triazol-3-one in
toluene under stirrer with Methane sulfonyl chloride. Reaction mass maintained at 120 °C for 12 h to
give final products of Sulfentrazone. Recovered half volume of toluene and cool to room temperature
filtered and dried to get final desired compound.
Chemical reaction:
++ ClH
Step-1
Methanesulfonyl chloride114.55
36.46
Cl
Cl
NH2
N
N
N
F
F
CH3
OCH3
S
O
O
Cl
Cl
Cl
NH
N
N
N
F
F
CH3
O
S
O
CH3O
Sulfentrazone387.19
ADMDT309.10
Mass Balance
MATERIAL BALANCE- Sulfentrazone Batch size (Final output): 1000 Kg
S.
No Name of Material
Input
Qty. (Kg)
Products
output
Qty. (Kg)
Recovery Losses
Total Liquid Others
1 Toluene 3990.28
1000
Toluene Toluene Organic
waste
5293.87
2 ADMDT
939.19
3591.25
399.02 205.81
3 Methane sulfonyl
chloride 355.02
Triphen
ylphosp
hine
HCL
4 Triphenylphosphine 9.38
9.38
88.41
Total 5293.87 5293.87
40. Lambda Cyhalothrin technical
41. Bifenthrin Technical
42. Cypermethrin Technical
Reaction Scheme