annexure – a details of products sr. no. proposed … · annexures to form – 1 & pfr for...

62
Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality and Agro Chemicals intermediates] by M/s Prerana Agrochem Pvt Limited, Plot No. 824/18, GIDC Jhagadia, Dist. Bharuch, Gujarat ANNEXURE – A DETAILS OF PRODUCTS Sr. No. PROPOSED PRODUCT CAS NO. QUANTITY [MT/ANNUM] Group Reduction 3600 1 2,5 Dichloro Aniline [2,5 DCA] 95-82-9 2 2,3 Dichloro Aniline[2,3-DCA] 608-27-5 3 3,4 Dichloro Aniline [3,4 DCA] 95-76-1 4 3,5 Dichloro Aniline[3,5-DCA] 626-43-7 5 P-Chloro Aniline [PCA] 106-47-8 6 M-Chloro Aniline [MCA] 108-42-9 7 2,4,5 Trichloro Aniline [2,4,5 TCA] 636-30-6 Hydrolysis of Amine 1200 8 2,5 Dichloro Phenol [2,5 DCP] 583-78-8 9 2,3 Dichloro Phenol [2,3 DCP] 576-24-9 10 3,4 Dichloro Phenol [3,4 DCP] 95-77-2 11 3,5 Dichloro Phenol [3,5 DCP] 591-35-5 CNP & CAP Group 600 12 4 Chloro-2-Nitro Phenol [4 CNP] 89-64-5 13 2 Chloro-4-Nitro Phenol [2 CNP] 619-08-9 14 4 Chloro-2-Amino Phenol [4 CAP] 95-85-2 15 2 Chloro-4-Amino Phenol [2 CAP] 3964-52-1 16 5-Chloro-2-Amino Phenol [5 CAP] 28443-50-7 Nitro-Amino Phenol Group 300 17 4-Nitro-2-Amino Phenol [4-NAP] 99-57-0 18 5-Nitro-2-Amino Phenol [5-NAP] 121-88-0 Alkyl Bromide 360 19 N-Propyl Bromide [N-Pr Br] 106-94-5 20 N-Hexyl Bromide [N-Hex Br] 111-25-1 HQ Group 240 21 5-Chloro-8-Hydroxy Quinoline [5 HQ] 130-16-5 22 8 Hydroxy Quinoline [8 HQ] 148-24-3 Speciality Chemicals 23 Iodo Chloro Hydroxy Quinoline [IODO] 130-26-7 60 24 2-Mercapto Benzaimidazole 583-39-1 600 25 2-Mercapto-5-Methoxybenzimidazole 37052-78-1 600 26 4-Nitro-2,5 Dichloro Aniline [2,5 DCPNA] 6627-34-5 240

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Page 1: ANNEXURE – A DETAILS OF PRODUCTS Sr. No. PROPOSED … · Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality and Agro Chemicals intermediates] by

Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality andAgro Chemicals intermediates] by M/s Prerana Agrochem Pvt Limited, Plot No. 824/18,

GIDC Jhagadia, Dist. Bharuch, Gujarat

ANNEXURE – A

DETAILS OF PRODUCTS

Sr. No. PROPOSED PRODUCT CAS NO. QUANTITY[MT/ANNUM]

Group Reduction

3600

1 2,5 Dichloro Aniline [2,5 DCA] 95-82-92 2,3 Dichloro Aniline[2,3-DCA] 608-27-53 3,4 Dichloro Aniline [3,4 DCA] 95-76-14 3,5 Dichloro Aniline[3,5-DCA] 626-43-75 P-Chloro Aniline [PCA] 106-47-86 M-Chloro Aniline [MCA] 108-42-97 2,4,5 Trichloro Aniline [2,4,5 TCA] 636-30-6

Hydrolysis of Amine

12008 2,5 Dichloro Phenol [2,5 DCP] 583-78-89 2,3 Dichloro Phenol [2,3 DCP] 576-24-9

10 3,4 Dichloro Phenol [3,4 DCP] 95-77-211 3,5 Dichloro Phenol [3,5 DCP] 591-35-5

CNP & CAP Group

600

12 4 Chloro-2-Nitro Phenol [4 CNP] 89-64-513 2 Chloro-4-Nitro Phenol [2 CNP] 619-08-914 4 Chloro-2-Amino Phenol [4 CAP] 95-85-215 2 Chloro-4-Amino Phenol [2 CAP] 3964-52-116 5-Chloro-2-Amino Phenol [5 CAP] 28443-50-7

Nitro-Amino Phenol Group30017 4-Nitro-2-Amino Phenol [4-NAP] 99-57-0

18 5-Nitro-2-Amino Phenol [5-NAP] 121-88-0Alkyl Bromide

36019 N-Propyl Bromide [N-Pr Br] 106-94-520 N-Hexyl Bromide [N-Hex Br] 111-25-1

HQ Group24021 5-Chloro-8-Hydroxy Quinoline [5 HQ] 130-16-5

22 8 Hydroxy Quinoline [8 HQ] 148-24-3Speciality Chemicals

23 Iodo Chloro Hydroxy Quinoline[IODO] 130-26-7 60

24 2-Mercapto Benzaimidazole 583-39-1 60025 2-Mercapto-5-Methoxybenzimidazole 37052-78-1 600

26 4-Nitro-2,5 Dichloro Aniline [2,5DCPNA] 6627-34-5 240

Page 2: ANNEXURE – A DETAILS OF PRODUCTS Sr. No. PROPOSED … · Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality and Agro Chemicals intermediates] by

Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality andAgro Chemicals intermediates] by M/s Prerana Agrochem Pvt Limited, Plot No. 824/18,

GIDC Jhagadia, Dist. Bharuch, Gujarat

27 2-Chloro-1,4-Phenylene Diamine [2,5DCPPD] 20103-09-7 240

28 6-Chloro-M-Toludine-4-Sulfonic Acid[CLT Acid] 88-53-9 300

29 4-Sulfomido Phenyl Hydrazine HCl [4SPH-HCl] 27918-19-0 120

30 3-Methoxy-4-Amino-Azobenzene-3’-Sulfonic Acid [Yellow Base] 6300-07-8 120

31 5 Chloro – 2- Benzaxolone[Chlorzoxazone] 95-25-0 300

32 Cloquintocet Mexyl - Safener 99607-70-2 480TOTAL OF PRODUCTS ------ 9360 =

780 MT/month

Page 3: ANNEXURE – A DETAILS OF PRODUCTS Sr. No. PROPOSED … · Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality and Agro Chemicals intermediates] by

Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality andAgro Chemicals intermediates] by M/s Prerana Agrochem Pvt Limited, Plot No. 824/18,

GIDC Jhagadia, Dist. Bharuch, Gujarat

ANNEXURE – B

DETAILS OF PRODUCT WISE RAW MATERIAL CONSUMPTION

Sr. No. Product Name Raw material MT/MT

1 2,5 DICHLOROANILINE [2,5 DCA]

2,5 DCNB 1.282Iron Powder 1.026Hydrochloric Acid 0.077C S Lye 0.064Water 0.833

2 2,3 DICHLOROANILINE [2,3 DCA]

2,3 DCNB 1.282Iron Powder 1.026Hydrochloric Acid 0.077C S Lye 0.064Water 0.833

3 3,4 DICHLOROANILINE [3,4 DCA]

3,4 DCNB 1.282Iron Powder 1.026Hydrochloric Acid 0.077C S Lye 0.064Water 0.833

4 3,5 DICHLOROANILINE [3,5 DCA]

3,5 DCNB 1.282Iron Powder 1.026Hydrochloric Acid 0.077C S Lye 0.064Water 0.833

5 PARA-CHLORO ANILE[PCA]

4-CNB 1.341Iron Powder 1.307Hydrochloric Acid 0.102C S Lye 0.081Water 1.064

6 META-CHLOROANILE [3-MCA]

3-CNB 1.341Iron Powder 1.307Hydrochloric Acid 0.102C S Lye 0.081Water 1.064

7 2,4,5 TRICHLOROANILINE [2,4,5 TCA]

2,4,5 TCNB 1.252Iron Powder 0.849Hydrochloric Acid 0.064C S Lye 0.05Water 0.683

8 2,5 DICHLOROPHENOL [2,5 DCP]

2,5 DCA 1.06Sulfuric Acid 1.2Nitrosyl Sulfuric Acid 2.085Water 1.8

9 2,3 DICHLOROPHENOL [2,3 DCP]

2,3 DCA 1.06Sulfuric Acid 1.2Nitrosyl Sulfuric Acid 2.085

Page 4: ANNEXURE – A DETAILS OF PRODUCTS Sr. No. PROPOSED … · Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality and Agro Chemicals intermediates] by

Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality andAgro Chemicals intermediates] by M/s Prerana Agrochem Pvt Limited, Plot No. 824/18,

GIDC Jhagadia, Dist. Bharuch, GujaratWater 1.8

10 3, 4 DICHLOROPHENOL [3,4 DCP]

3,4 DCA 1.06Sulfuric Acid 1.2Nitrosyl Sulfuric Acid 2.085Water 1.8

11 3, 5 DICHLOROPHENOL [3,5 DCP]

3,5 DCA 1.06Sulfuric Acid 1.2Nitrosyl Sulfuric Acid 2.085Water 1.8

12 4-Chloro-2-NitroPhenol [4-CNP]

2,5 DCNB 1.25C S Lye 1.328Hydrochloric Acid 1.563Water 12.5

13 2-CHLORO-4-NITROPHENOL [2-CNP]

3,4 DCNB 1.25C S Lye 1.328Hydrochloric Acid 1.563Water 12.5

14 4-CHLORO-2-AMINOPHENOL [4-CAP]

2,5 DCNB 1.923C S Lye 4.447Hydrochloric Acid 3.25Iron Powder 2.043Activated Charcoal 0.072Additives 0.014Water 13.221

15 2-CHLORO-4-AMINOPHENOL [2-CAP]

3,4 DCNB 1.923C S Lye 4.447Hydrochloric Acid 3.25Iron Powder 2.043Activated Charcoal 0.072Additives 0.014Water 13.221

16 5-CHLORO-2-AMINOPHENOL [5-CAP]

2,4 DCNB 1.923C S Lye 4.447Hydrochloric Acid 3.25Iron Powder 2.043Activated Charcoal 0.072Additives 0.014Water 13.221

17 & 18

4-NITRO-2-AMINOPHENOL [4-NAP] AND

5-NITRO-2-AMINOPHENOL [5-NAP]

O-Aminophenol 0.762Acetic Acid 0.441Solvent Toluene 0.699Solvent EDC 0.699Sulfuric Acid 1.413Nitric Acid 0.629C S Lye 0.653Water 3.846

19 N-PROPYL BROMIDE N-Propanol 0.541Hydrobromic Acid 2.676

Page 5: ANNEXURE – A DETAILS OF PRODUCTS Sr. No. PROPOSED … · Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality and Agro Chemicals intermediates] by

Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality andAgro Chemicals intermediates] by M/s Prerana Agrochem Pvt Limited, Plot No. 824/18,

GIDC Jhagadia, Dist. Bharuch, GujaratSulfuric Acid 0.18Soda Ash 0.023Water 0.901

20 N-HEXYL BROMIDE

N-Propanol 0.68Hydrobromic Acid 1.98Sulfuric Acid 0.133Soda Ash 0.017Water 0.667

215-CHLORO-8-

HYDROXYQUINOLINE[5-CHQ]

4-CAP 1.227Glycerine 1.25Sulfuric Acid 1.977Acetic Acid 0.145C S Lye [for pH] 2.773Water 20

228-

HYDROXYQUINOLINE[8-HQ]

2-Amino Phenol 1.158Glycerine 0.825Sulfuric Acid 1.305Acetic Acid 0.096C S Lye [for pH] 1.836Water 21.215

235-CHLORO-7-IODO-8-HYDROXYQUINOLINE

[IODO]

4-CAP 0.871Glycerine 0.887Sulfuric Acid 1.403Acetic Acid 0.103C S Lye [for pH] 2.935Iodine 0.403Water 24.323

24 2 MERCAPTOBENZIMIDAZOLE

O-Phenyle Diamine 0.8Carbon Disulfide 0.7Caustic Soda Lye 1.32Hydrochloric Acid 0.9Activated Charcoal 0.02Water 5.6

25

5-METHOXY-2MERCAPTO

BENZIMIDAZOLE[5M-2-MBI]

4-M-2-Nitro Aniline 1.017Sodium Hydrosulfide 1.100Carbon Disulfide 0.565Caustic Soda Lye 0.908Hydrochloric Acid [30%] 0.400Activated Charcoal 0.025Water [Total] 5.089

264-NITRO-2,5

DICHLORO ANILINE[2,5 DCPNA]

2,5 Dichloro Aniline 0.868Acetyl Chloride 0.42Solvent:Toluene 1Solvent: EDC 1Sulfuric Acid 1.085Nitric Acid 0.475C S Lye 0.475Water 3.559

Page 6: ANNEXURE – A DETAILS OF PRODUCTS Sr. No. PROPOSED … · Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality and Agro Chemicals intermediates] by

Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality andAgro Chemicals intermediates] by M/s Prerana Agrochem Pvt Limited, Plot No. 824/18,

GIDC Jhagadia, Dist. Bharuch, Gujarat

272-CHLORO 1,4

PHENYLENE DIAMINE[2-CL-1,4-PDA]

2-Chloro-4-Nitroaniline 1.311Iron Powder 1.167Hydrochloric Acid 0.091C S Lye 0.076Water 0.947

28 2-Chloro-5-Toludine-4-Sulfonic Acid [CLT]

Toluene 0.871Sulfuric Acid 2.249Nitric Acid 0.811HCl Solution 0.532Chlorine 0.74Feric Chloride 0.004Iron Powder 0.533Soda Ash 0.03Salts 1Water 10.39

294-SULFOMIDO

PHENYL HYDRAZINEHCL [4-SPHHCL]

n-Acetylsulfanilyl Cl 1.592Ammonia Soln 1.857C S Lye 1Sodium Nitrite 0.406Sodium Bisulfite 1Soda Ash 0.25Hydrochloric Acid [2 Lot] 3.75Hydro Salt 0.005Carbon 0.008Water 13

30

3-METHOXY-4-AMINO-

AZOBENZENE-3'-SULFONIC ACID[YELLOW BASE]

O-Anisidine 0.556Formaldehyde 0.733SBS 0.439Metanilic Acid 0.806Hydrochloric Acid 0.972Sodium Nitrite 0.322Sulfamic Acid 0.556Sodium Acetate 1.111C S Lye 0.278Salt 1.556Ice 4.167Water 12.361

315 Chloro - 2-Benzaxolone

[Chlorzoxazone]

4-CAP 1Urea 1.75Acetic Acid 1.824HCl [30 %] 3.04C S Lye 0.6Methanol 1.6Carbon 0.01Water 4.4

32. Cloquintocet Mexyl -Safener

2-Heptanol 0.40MCA 0.332

Page 7: ANNEXURE – A DETAILS OF PRODUCTS Sr. No. PROPOSED … · Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality and Agro Chemicals intermediates] by

Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality andAgro Chemicals intermediates] by M/s Prerana Agrochem Pvt Limited, Plot No. 824/18,

GIDC Jhagadia, Dist. Bharuch, GujaratToluene 1.754PTSA 0.0045-Cl-8HQ 0.630Methanol 3.330Water 2.351

Page 8: ANNEXURE – A DETAILS OF PRODUCTS Sr. No. PROPOSED … · Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality and Agro Chemicals intermediates] by

Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality andAgro Chemicals intermediates] by M/s Prerana Agrochem Pvt Limited, Plot No. 824/18,

GIDC Jhagadia, Dist. Bharuch, Gujarat

ANNEXURE – C

DETAILS OF MANUFACTURING PROCESS DESCRIPTION

1.2,5 DICHLORO ANILINE [2,5 DCA]:

Process Description:

2,5 Dichloro Nitro Benzene [2,5 DCNB] is subjected to reduction using IronPowder under acidic condition to form 2,5 Dichloro Aniline. 2,5 DCA thus formedis then suitably isolated from the reaction mixture by means of filtration anddistillation.

Chemical Reaction:

Mass Balance:

Input Qty Output Qty2,5 DCNB 1282 Aqueous Layer 769Iron Powder 1026 Distillation Loss 26Hydrochloric Acid 77 Process Residue 1487C S Lye 64 Product 2,5 DCA 1000Total Water 833

Total 3282 Total 3282

Flow Chart:

Page 9: ANNEXURE – A DETAILS OF PRODUCTS Sr. No. PROPOSED … · Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality and Agro Chemicals intermediates] by

Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality andAgro Chemicals intermediates] by M/s Prerana Agrochem Pvt Limited, Plot No. 824/18,

GIDC Jhagadia, Dist. Bharuch, Gujarat

2. 2,3 DICHLORO ANILINE [2,3 DCA]:

Process Description:

2,3 Dichloro Nitro Benzene [2,3 DCNB] is subjected to reduction using IronPowder under acidic condition to form 2,3 Dichloro Aniline. 2,3 DCA thus formedis then suitably isolated from the reaction mixture by means of filtration anddistillation.

Chemical Reaction:

Mass Balance:

Input Qty Output Qty2,3 DCNB 1282 Aqueous Layer 769Iron Powder 1026 Distillation Loss 26Hydrochloric Acid 77 Process Residue 1487C S Lye 64 Product 2,3 DCA 1000Total Water 833

Total 3282 Total 3282

Flow Diagram:

Page 10: ANNEXURE – A DETAILS OF PRODUCTS Sr. No. PROPOSED … · Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality and Agro Chemicals intermediates] by

Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality andAgro Chemicals intermediates] by M/s Prerana Agrochem Pvt Limited, Plot No. 824/18,

GIDC Jhagadia, Dist. Bharuch, Gujarat

3. 3,4 DICHLORO ANILINE [3,4 DCA]:

Process Description:

3,4 Dichloro Nitro Benzene [3,4 DCNB] is subjected to reduction using IronPowder under acidic condition to form 3,4 Dichloro Aniline. 3,4 DCA thus formedis then suitably isolated from the reaction mixture by means of filtration anddistillation.

Chemical Reaction:

Mass Balance:

Input Qty Output Qty3,4 DCNB 1282 Aqueous Layer 769Iron Powder 1026 Distillation Loss 26Hydrochloric Acid 77 Process Residue 1487C S Lye 64 Product 3,4 DCA 1000Total Water 833

Total 3282 Total 3282

Flow Diagram:

Page 11: ANNEXURE – A DETAILS OF PRODUCTS Sr. No. PROPOSED … · Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality and Agro Chemicals intermediates] by

Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality andAgro Chemicals intermediates] by M/s Prerana Agrochem Pvt Limited, Plot No. 824/18,

GIDC Jhagadia, Dist. Bharuch, Gujarat

4. 3,5 DICHLORO ANILINE [3,5 DCA]:

Process Description:

3,5 Dichloro Nitro Benzene [3,5 DCNB] is subjected to reduction using IronPowder under acidic condition to form 3,5 Dichloro Aniline. 3,5 DCA thus formedis then suitably isolated from the reaction mixture by means of filtration anddistillation.

Chemical Reaction:

Mass Balance:

Input Qty Output Qty3,5 DCNB 1282 Aqueous Layer 769Iron Powder 1026 Distillation Loss 26Hydrochloric Acid 77 Process Residue 1487C S Lye 64 Product 3,5 DCA 1000Total Water 833

Page 12: ANNEXURE – A DETAILS OF PRODUCTS Sr. No. PROPOSED … · Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality and Agro Chemicals intermediates] by

Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality andAgro Chemicals intermediates] by M/s Prerana Agrochem Pvt Limited, Plot No. 824/18,

GIDC Jhagadia, Dist. Bharuch, Gujarat

Total 3282 Total 3282

Flow Diagram:

5. PARA-CHLORO ANILE [PCA]:

Process Description:

4 Chloro Nitro Benzene [4 CNB] is subjected to reduction using Iron Powderunder acidic condition to to form 3 Chloro Aniline. 4 Chloro Aniline thus formed isthen suitably isolated from the reaction mixture by means of filtration anddistillation.

Chemical Reaction:

Mass Balance:

Input Qty Output Qty4-CNB 1341 Aqueous Layer 979Iron Powder 1307 Distillation Loss 26Hydrochloric Acid 102 Process Residue 1890

Page 13: ANNEXURE – A DETAILS OF PRODUCTS Sr. No. PROPOSED … · Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality and Agro Chemicals intermediates] by

Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality andAgro Chemicals intermediates] by M/s Prerana Agrochem Pvt Limited, Plot No. 824/18,

GIDC Jhagadia, Dist. Bharuch, Gujarat

C S Lye 81 Product PCA 1000Total Water 1064

Total 3895 Total 3895

Flow Diagram:

6. META-CHLORO ANILE [3-MCA]:

Process Description:

3 Chloro Nitro Benzene [3 CNB] is subjected to reduction using Iron Powderunder acidic condition to form 3 Chloro Aniline. 3 Chloro Aniline thus formed isthen suitably isolated from the reaction mixture by means of filtration anddistillation.

Chemical Reaction:

Mass Balance:

Input Qty Output Qty

Page 14: ANNEXURE – A DETAILS OF PRODUCTS Sr. No. PROPOSED … · Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality and Agro Chemicals intermediates] by

Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality andAgro Chemicals intermediates] by M/s Prerana Agrochem Pvt Limited, Plot No. 824/18,

GIDC Jhagadia, Dist. Bharuch, Gujarat

3-CNB 1341 Aqueous Layer 979Iron Powder 1307 Distillation Loss 26Hydrochloric Acid 102 Process Residue 1890C S Lye 81 Product MCA 1000Total Water 1064

Total 3895 Total 3895

Flow Diagram:

7. 2,4,5 TRICHLORO ANILINE [2,4,5 TCA]:

Process Description:

3,5 Dichloro Nitro Benzene [3,5 DCNB] is subjected to reduction using IronPowder under acidic condition to form 3,5 Dichloro Aniline. 3,5 DCA thus formedis then suitably isolated from the reaction mixture by means of filtration anddistillation.

Chemical Reaction:

Mass Balance:

Page 15: ANNEXURE – A DETAILS OF PRODUCTS Sr. No. PROPOSED … · Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality and Agro Chemicals intermediates] by

Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality andAgro Chemicals intermediates] by M/s Prerana Agrochem Pvt Limited, Plot No. 824/18,

GIDC Jhagadia, Dist. Bharuch, Gujarat

Input Qty Output Qty2,4,5 TCNB 1252 Aqueous Layer 641Iron Powder 849 Distillation Loss 20Hydrochloric Acid 64 Process Residue 1237C S Lye 50 Product 2,4,5 TCA 1000Total Water 683

Total 2898 Total 2898

Flow Diagram:

8. 2,5 DICHLORO PHENOL [2,5 DCP]:

Process Description:

2,5 Dichloro Aniline [2,5 DCA] is converted to its diazonium compound withNitrosyl Sulfuric Acid in presence of Sulfuric Acid. The reaction is carried outunder very controlled condition of temperature. The Diazonium salt formed isfurther subjected to acidic hydrolysis leading to formation of the product 2,5Dichloro Phenol. The product formed is isolated by means of distillation.

Chemical Reaction:

Page 16: ANNEXURE – A DETAILS OF PRODUCTS Sr. No. PROPOSED … · Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality and Agro Chemicals intermediates] by

Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality andAgro Chemicals intermediates] by M/s Prerana Agrochem Pvt Limited, Plot No. 824/18,

GIDC Jhagadia, Dist. Bharuch, Gujarat

Mass Balance:

Input Qty Output Qty2,5 DCA 1060 Aqueous Layer 1185Sulfuric Acid 1200 Process/Distillation Loss 170Nitrosyl Sulfuric Acid 2085 Distillation Loss 13Water 1800 Distillation Residue 27

Spent Sulfuric Acid 3750Product: 2,5 DCP 1000

Total 6145 Total 6145

Flow Diagram:

9. 2,3 DICHLORO PHENOL [2,3 DCP]:

Process Description:

2,3 Dichloro Aniline [2,3 DCA] is converted to its diazonium compound withNitrosyl Sulfuric Acid in presence of Sulfuric Acid. The reaction is carried outunder very controlled condition of temperature.

The Diazonium salt formed is further subjected to acidic hydrolysis leading toformation of the product 2,3 Dichloro Phenol. The product formed is isolated bymeans of distillation.

Chemical Reaction:

Page 17: ANNEXURE – A DETAILS OF PRODUCTS Sr. No. PROPOSED … · Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality and Agro Chemicals intermediates] by

Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality andAgro Chemicals intermediates] by M/s Prerana Agrochem Pvt Limited, Plot No. 824/18,

GIDC Jhagadia, Dist. Bharuch, Gujarat

Mass Balance:

Input Qty Output Qty2,3 DCA 1060 Aqueous Layer 1185Sulfuric Acid 1200 Process/Distillation Loss 170Nitrosyl Sulfuric Acid 2085 Distillation Loss 13Water 1800 Distillation Residue 27

Spent Sulfuric Acid 3750Product: 2,3 DCP 1000

Total 6145 Total 6145

Flow Diagram:

10. 3, 4 DICHLORO PHENOL [3,4 DCP]:

Process Description:

3,4 Dichloro Aniline [3,4 DCA] is converted to its diazonium compound withNitrosyl Sulfuric Acid in presence of Sulfuric Acid. The reaction is carried outunder very controlled condition of temperature.

The Diazonium salt formed is further subjected to acidic hydrolysis leading toformation of the product 3,4 Dichloro Phenol. The product formed is isolated bymeans of distillation.

Chemical Reaction:

Page 18: ANNEXURE – A DETAILS OF PRODUCTS Sr. No. PROPOSED … · Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality and Agro Chemicals intermediates] by

Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality andAgro Chemicals intermediates] by M/s Prerana Agrochem Pvt Limited, Plot No. 824/18,

GIDC Jhagadia, Dist. Bharuch, Gujarat

Mass Balance:

Input Qty Output Qty3,4 DCA 1060 Aqueous Layer 1185Sulfuric Acid 1200 Process/Distillation Loss 170Nitrosyl Sulfuric Acid 2085 Distillation Loss 13Water 1800 Distillation Residue 27

Spent Sulfuric Acid 3750Product: 3,4 DCP 1000

Total 6145 Total 6145

Flow Diagram:

11. 3, 5 DICHLORO PHENOL [3,5 DCP]:

Process Description:

3,5 Dichloro Aniline [3,5 DCA] is converted to its diazonium compound withNitrosyl Sulfuric Acid in presence of Sulfuric Acid. The reaction is carried outunder very controlled condition of temperature.

The Diazonium salt formed is further subjected to acidic hydrolysis leading toformation of the product 3,5 Dichloro Phenol. The product formed is isolated bymeans of distillation.

Chemical Reaction:

Page 19: ANNEXURE – A DETAILS OF PRODUCTS Sr. No. PROPOSED … · Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality and Agro Chemicals intermediates] by

Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality andAgro Chemicals intermediates] by M/s Prerana Agrochem Pvt Limited, Plot No. 824/18,

GIDC Jhagadia, Dist. Bharuch, Gujarat

Mass Balance:

Input Qty Output Qty3,5 DCA 1060 Aqueous Layer 1185Sulfuric Acid 1200 Process/Distillation Loss 170Nitrosyl Sulfuric Acid 2085 Distillation Loss 13Water 1800 Distillation Residue 27

Spent Sulfuric Acid 3750Product: 3,5 DCP 1000

Total 6145 Total 6145

Flow Diagram:

12.4-Chloro-2-Nitro Phenol [4-CNP]

Process Description:

2,5 Dichloronitrobenzene [2,5 DCNB] is hydrolysed with Sodium Hydroxide ata controlled reaction parameter. After the hydrolysis is completed, ML fromthe reaction mass is decanted and the residual mass is acidified.

The Acidification results into falling out of 4-Chloro-2-Nitro Phenol [4-CNP],which is filtered, washed and dried.

Chemical Reaction:

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Mass Balance:

Input Qty Output Qty2,5 DCNB 1250 Decanted ML 6250C S Lye 1328 ML/WML 9141Hydrochloric Acid 1563 Drying Loss 250Water 12500 Product: 4-CNP 1000

Total 16641 Total 16641

Flow Diagram:

13. 2-CHLORO-4-NITRO PHENOL [2-CNP]:

Process Description:

Take 3,4 Dichloronitrobenzene [3,4 DCNB] is hydrolysed with Sodium Hydroxideat a controlled reaction parameter. After the hydrolysis is completed, ML from thereaction mass is decanted and the residual mass is acidified.

The Acidification results into falling out of 2-Chloro-4-Nitro Phenol [2-CNP], whichis filtered, washed and dried.

Chemical Reaction:

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Mass Balance:

Input Qty Output Qty3,4 DCNB 1250 Decanted ML 6250C S Lye 1328 ML/WML 9141Hydrochloric Acid 1563 Drying Loss 250Water 12500 Product: 2-CNP 1000

Total 16641 Total 16641

Flow Diagram:

14. 4-CHLORO-2-AMINO PHENOL [4-CAP]:

Process Description:

2,5 Dichloronitrobenzene [2,5 DCNB] is hydrolysed with Sodium Hydroxide at acontrolled reaction parameter. After the hydrolysis is completed, ML from thereaction mass is decanted and the residual mass is acidified.

The Acidified mass is then subjected to conventional reduction using IronPowder. After completion of reduction Iron Sludge separated out. The residualfiltrate is treated with activated charcoal, followed by Charcoal removal and

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adding other additives along with pH adjustment is then filtered, washedanddried.

Chemical Reaction:

Mass Balance:

Input Qty Output Qty2,5 DCNB 1923 Iron Sludge 4808C S Lye 4447 Carbon Residue 144Hydrochloric Acid 3250 Drying Loss 923Iron Powder 2043 Waste Water [ML/WML] 18096Activated Charcoal 72 Product: 4-CAP 1000Additives 14Water 13221

Total 24971 Total 24971

Flow Diagram:

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15. 2-CHLORO-4-AMINO PHENOL [2-CAP]:

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Process Description:

3,4 Dichloronitrobenzene [3,4 DCNB] is hydrolysed with Sodium Hydroxide at acontrolled reaction parameter. After the hydrolysis is completed, ML from thereaction mass is decanted and the residual mass is acidified.

The Acidified mass is then subjected to conventional reduction using IronPowder. After completion of reduction Iron Sludge separated out. The residualfiltrate is treated with activated charcoal, followed by Charcoal removal andadding other additives along with pH adjustment is then filtered, washed anddried.

Chemical Reaction:

Mass Balance:

Input Qty Output Qty3,4 DCNB 1923 Iron Sludge 4808C S Lye 4447 Carbon Residue 144Hydrochloric Acid 3250 Drying Loss 923Iron Powder 2043 Waste Water [ML/WML] 18096Activated Charcoal 72 Product: 2-CAP 1000Additives 14Water 13221

Total 24971 Total 24971

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Flow Diagram:

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16. 5-CHLORO-2-AMINO PHENOL [5-CAP]:

Process Description:

2,4 Dichloronitrobenzene [2,4 DCNB] is hydrolysed with Sodium Hydroxide at acontrolled reaction parameter. After the hydrolysis is completed, ML from thereaction mass is decanted and the residual mass is acidified.

The Acidified mass is then subjected to conventional reduction using IronPowder. After completion of reduction Iron Sludge separated out. The residualfiltrate is treated with activated charcoal, followed by Charcoal removal andadding other additives along with pH adjustment is then filtered, washed anddried.

Chemical Reaction:

Mass Balance:

Input Qty Output Qty2,4 DCNB 1923 Iron Sludge 4808C S Lye 4447 Carbon Residue 144Hydrochloric Acid 3250 Drying Loss 923Iron Powder 2043 Waste Water [ML/WML] 18096Activated Charcoal 72 Product: 5-CAP 1000Additives 14Water 13221

Total 24971 Total 24971

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Flow Diagram:

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17. & 18. 4-NITRO-2-AMINO PHENOL [4-NAP] AND 5-NITRO-2-AMINO PHENOL[5-NAP]:

Process Description:

2,4 Dichloronitrobenzene [2,4 DCNB] is hydrolysed with Sodium Hydroxide at acontrolled reaction parameter. After the hydrolysis is completed, ML from thereaction mass is decanted and the residual mass is acidified.

The Acidified mass is then subjected to conventional reduction using IronPowder. After completion of reduction Iron Sludge separated out. The residualfiltrate is treated with activated charcoal, followed by Charcoal removal andadding other additives along with pH adjustment is then filtered, washed anddried.

Chemical Reaction:

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Mass Balance:

Input Qty Output QtyO-Aminophenol 762 Toluene recovered 685Acetic Acid 441 Recovered EDC 686Solvent Toluene 699 Spent Acid 1713Solvent EDC 699 Total Aqueous Waste 5014Sulfuric Acid 1413 Distillation Losses 43Nitric Acid 629 Product: 4-NAP & 5-NAP 1000C S Lye 653Total Water 3846

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Total 9142 Total 9142

Flow Diagram:

19. N-PROPYL BROMIDE:

Process Description:

N-Propyl Alcohol is reacted with Hydrobromic Acid in presence of Sulfuric Acid atelevated temperature resulting in formation of N-Propyl Bromide. The N-PropylBromide thus formed is taken out from the reaction mass by means of distillationand then washed with Soda Ash Solution and Water.

The Washed Organic mass of N-Propyl Bromide is then subjected to distillationfor obtaining pure N-Propyl Bromide.

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Chemical Reaction:

Mass Balance:

Input Qty Output QtyN-Propanol 541 Water from Distillation 901Hydrobromic Acid 2676 Reaction ML 1441Sulfuric Acid 180 Mother Liquor 482Soda Ash 23 Washing Liquor 459Water 901 Distillation Loss 18

Distillation Residue 18Product: N-Propyl Bromide 1000

Total 4320 Total 4320

Flow Diagram:

20. N-HEXYL BROMIDE:

Process Description:

N-Hexyl Alcohol is reacted with Hydrobromic Acid in presence of Sulfuric Acid atelevated temperature resulting in formation of N-Hexyl Bromide. The N-HexylBromide thus formed is taken out from the reaction mass by means of distillationand then washed with Soda Ash Solution and Water.

The Washed Organic mass of N-p\Hexyl Bromide is then subjected to distillationfor obtaining pure N-Hexyl Bromide.

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Chemical Reaction:

Mass Balance:

Input Qty Output QtyN-Propanol 680 Water from Distillation 667Hydrobromic Acid 1980 Reaction ML 1067Sulfuric Acid 133 Mother Liquor 363Soda Ash 17 Washing Liquor 347Water 667 Distillation Loss 13

Distillation Residue 20Product: N-Hexyl Bromide 1000

Total 3477 Total 3477

Flow Diagram:

21. 5-CHLORO-8-HYDROXYQUINOLINE [5-CHQ]:

Process Description:

4-Chloro-2-Amino Phenol is reacted with Glycerine leading to cyclization inpresence of Sulfuric Acid. The reaction leads to form 5-Chloro-8-Hydroxyquinoline; the excess of 4-CAP is removed by distillation.

The residual mass diluted with water and pH adjusted with C S Lye followed byfiltration and washing. The wet cake dried to obtain product 5-Chloro-8-

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Hydroxyquinoline [5-CHQ]

Chemical Reaction:

Mass Balance:

Input Qty Output Qty4-CAP 1227 Rec 4-CAP 273Glycerine 1250 ML/WML 25736Sulfuric Acid 1977 Water Evaporation 364Acetic Acid 145 Product: 5-CHQ 1001C S Lye [for pH] 2773Water in Total 20000

Total 27373 Total 27373

Flow Diagram:

22.8-HYDROXYQUINOLINE [8-HQ]:

Process Description:

2-Amino Phenol is reacted with Glycerine leading to cyclization in presence ofSulfuric Acid. The reaction leads to form 8-Hydroxyquinoline; the excess of 2-Amino Phenol is removed by distillation.

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The residual mass diluted with water and pH adjusted with C S Lye followed byfiltration and washing. The wet cake dried to obtain product 8-Hydroxyquinoline[8-HQ]

Chemical Reaction:

Mass Balance:

Input Qty Output Qty2 Amino Phenol 1158 Rec 4-CAP 260Glycerine 825 ML/WML 24757Sulfuric Acid 1305 Water Evaporation 418Acetic Acid 96 Product: 8-HQ 1000C S Lye [for pH] 1836Water in Total 21215

Total 26435 Total 26435

Flow Diagram:

23.5-CHLORO-7-IODO-8-HYDROXYQUINOLINE [IODO]:

Process Description:

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4-Chloro-2-Amino Phenol is reacted with Glycerine leading to cyclization inpresence of Sulfuric Acid. The reaction leads to form 5-Chloro-8-Hydroxyquinoline; the excess of 4-CAP is removed by distillation.

The residual mass diluted with water and pH adjusted with C S Lye followed byfiltration and washing. The wet cake is further taken for Iodination with Iodine.

The Iodination is carried out under controlled parameter in alkaline condition. TheIodinated mass is then subjected to filtration and washing. The wet cake obtainedis dried to obtain product IODO.

Chemical Reaction:

Mass Balance:

Input Qty Output Qty4-CAP 871 Rec 4-CAP 194Glycerine 887 ML/WML 29313Sulfuric Acid 1403 Evaporation Loss 419Acetic Acid 103 Product: IODO 1000C S Lye [for pH] 2935Iodine 403Water in Total 24323

Total 30926 Total 30926

Flow Diagram:

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24. 2 MERCAPTO BENZIMIDAZOLE:

Process Description:

O-Phenylene Diamine is reacted with Carbon Disulfide along with SodiumHydroxide leading to form 2-Mercapto Benzimidazole which is isolated byfiltration and further washed.

The wet cake of 2-Mercapto Benzimidazole is converted to its alkali salt, treatedwith activated charcoal and then again acidified to obtain 2-MercaptoBenzimidazole. The product is filtered and dried. Is further dried to obtained 2-MBI.

Chemical Reaction:

Mass Balance:

Input Qty Output QtyO-Phenylen Diamine 800 Mother Liquor [Total] 6190Carbon Disulfide 700 Washing Liquor

[Total]1710

Caustic Soda Lye 1320 Water of Evaporation 400Hydrochloric Acid 900 Charcoal Residue 40Activated Charcoal 20 Product 2-MBI 1000Water 5600

Total 9340 Total 9340

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Flow Diagram:

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25. 5-METHOXY-2 MERCAPTO BENZIMIDAZOLE[5M-2-MBI]

Process Description:

4-Methoxy-2-Nitroaniline is reacted with Sodium Hydrosulfide leading to reductionreaction to yield. 4-Methoxy-2-Amino Aniline.

4-Methoxy-2-Amino Aniline is further reacted with Carbon Disulfide in presence ofSodium hydroxide to give 2-Mercapto-5-Methoxy Benzimidazole.

The wet cake of 2-Mercapto-5-Methoxy Benzimidazole is converted to its alkalisalt, treated with activated charcoal and then again acidified to obtained 2-Mercapto-5-Methoxy Benzimidazole. The product is filtered and dried is furtherdried to obtained 2-Mercapto-5-Methoxy Benzimidazole.

Chemical Reaction:

Mass Balance:

Input Qty Output Qty4-M-2-Nitro Aniline 1017 Mother Liquor [Total] 6352Sodium Hydrosulfide 1100 Washing Liquor [Total] 1252Carbon Disulfide 565 carbon Residue 51Caustic Soda Lye 908 Water of Evaporation 450Hydrochloric Acid [30%] 400 Product 5M2MBI Dried 1000Activated Charcoal 25Water [Total] 5089

Total 9105 Total 9105

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Flow Diagram:

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26. 4-NITRO-2,5 DICHLORO ANILINE [2,5 DCPNA]:

Process Description:

Step I: 2,5 Dichloroanaline is reacted with Acetyl Chloride in solvent Tolueneleading to formation of 2,5 Dichloro Acetanilide. The reaction mass is washedwith water and Toluene recovered for reuse.

Step II: The residual mass of previous step [2,5 Dichloro Acetanilide] is subjectedto Nitration with Nitric Acid in presence of Sulfuric Acid and using EDC assolvent. After completion of Nitration, EDC is recovered by distillation and spentacid separated from the residual mass followed by washing.

Step III: 4-Nitro-2,5 Dichloro Acetanilide formed through Nitration is finallysubjected to alkaline hydrolysis in EDC leading to form desired product 4-Nitro-2,5 Dichloro Aniline [4-N-2,5 DCA]. The product is isolated by washing andrecovering EDC.

Chemical Reaction:

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Mass Balance:

Input Qty Output Qty2,5 Dichloro Aniline 868 HCl Solution - By Product 655Acetyl Chloride 420 Spent Acid 1315Solvent: Toluene 1000 Aqueous Layer in Total 3912Solvent: EDC 1000 Recovered Toluene 975Sulfuric Acid 1085 Loss in Toluene Recovery 25Nitric Acid 475 Recovered EDC 975C S Lye 475 Loss in EDC Recovery 25Water in Total 3559 Product: 4-N-2,5 DCA 1000

Total 8882 Total 8882

Flow Diagram:

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27. 2-CHLORO 1,4 PHENYLENE DIAMINE [2-CL-1,4-PDA]:

Process Description:

2-Chloro-4-Nitro Benzene [2-C-4NA] is subjected to reduction using Iron Powderunder acidic condition to form 2-Chloro 1,4 Phenylene Diamine . 2-Chloro 1,4Phenylene Diamine thus formed is then suitably isolated from the reactionmixture by means of filtration and distillation.

Chemical Reaction:

Mass Balance:

Input Qty Output Qty2-Chloro-4-Nitroaniline 1311 Aqueous Layer for 871Iron Powder 1167 Distillation Loss 30Hydrochloric Acid 91 Process Residue [Iron Sludge] 1689C S Lye 76 Product 2-Cl-1,4-PDA 1000Water [Total] 947

Total 3591 Total 3591

Flow Diagram:

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28.2-Chloro-5-Toludine-4-Sulfonic Acid [CLT]

Process Description:

2-Chloro-4-Nitro Benzene [2-C-4NA] is subjected to reduction using Iron Powderunder acidic condition to form 2-Chloro 1,4 Phenylene Diamine . 2-Chloro 1,4Phenylene Diamine thus formed is then suitably isolated from the reactionmixture by means of filtration and distillation.

Chemical Reaction:

Mass Balance:

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Flow Diagram:

Input Qty Output QtyToluene 871 30 % HCl Solution 1271Sulfuric Acid 2249 Iron Sludge 1065Nitric Acid 811 Total Aqueous 13365HCl Solution 532 Drying Loss 457Chlorine 740 Product: 1000Feric Chloride 4Iron Powder 533Soda Ash 30Salts 1000Water [Total] 10390

Total 17158 Total 17158

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29. 4-SULFOMIDO PHENYL HYDRAZINE HCL [4-SPHHCL]:

Process Description:

N-Acetylsulfanilyl chloride is reacted with Ammonia resulting to N-AcetylsulfanilylAmide, which is next hydrolysed with Sodium Hydroxide leading to form N-Sulfanilyl Amide.

N-Sulfaniyl Amide thus formed is isolated by filtration is then subjected todiazotization using Sodium Nitrate and then acidified with Hydrochloric acidleading to form N-Sulfanilyl Phenyl Hydrazine Hydrochloride. N-Sulfanilyl PhenylHydrazine Hydrochloride thus formed is isolated as crude material is then purifiedand filtered followed by drying.

Chemical Reaction:

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Mass Balance:

Input Qty Output Qtyn-Acetylsulfanilyl Cl 1592 Total Aqueous Water 21185Ammonia Solution 1857 Carbon Residue 16C S Lye 1000 Loss of Drying 666Sodium Nitrite 406 Product 1001Sodium Bisulfite 1000Soda Ash 250Hydrochloric Acid [2 Lot] 3750Hydro Salt 5Carbon 8Total Water 13000

Total 22867 Total 22867

Flow Diagram:

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30.3-METHOXY-4-AMINO-AZOBENZENE-3'-SULFONIC ACID [YELLOW BASE]:

Process Description:

Metanilic Acid is diazotized using Sodium Nitrite under suitable condition. Thediazonium ion formed is further coupled with O-Anisidine followed by hydrolysisto yield 3-Methoxy-4-Amino Azobenzene-3'- Sulfonic Acid [Yellow Base]. Yellowbase formed thus is isolated by filtration followed by drying.

Chemical Reaction:

Page 51: ANNEXURE – A DETAILS OF PRODUCTS Sr. No. PROPOSED … · Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality and Agro Chemicals intermediates] by

Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality andAgro Chemicals intermediates] by M/s Prerana Agrochem Pvt Limited, Plot No. 824/18,

GIDC Jhagadia, Dist. Bharuch, Gujarat

Mass Balance:

Input Qty Output QtyO-Anisidine 556 Overall Aqueous Water 22428Formaldehyde 733 Loss of Drying 428SBS 439 Product: Yellow Base 1000Metanilic Acid 806Hydrochloric Acid 972Sodium Nitrite 322Sulfamic Acid 556Sodium Acetate 1111C S Lye 278Salt 1556Ice 4167Water 12361

Total 23856 Total 23856

Flow Diagram:

Page 52: ANNEXURE – A DETAILS OF PRODUCTS Sr. No. PROPOSED … · Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality and Agro Chemicals intermediates] by

Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality andAgro Chemicals intermediates] by M/s Prerana Agrochem Pvt Limited, Plot No. 824/18,

GIDC Jhagadia, Dist. Bharuch, Gujarat

31. 5 CHLORO - 2- BENZAXOLONE [Chlorzoxazone]

Process Description:

4-Chloro Amino Phenol [4-CAP] is charged along with HCl, Urea, Acetic Acid andWater & heated to specific elevated temperature till completion of the reaction.The mass is then filtered.

The wet cake is then dissolved in dilute C S Lye and Carbon added followed byfiltration. The filtrate is again treated with HCl solution for isolation of productwhich in turn is further re-crystallized by Methanol for final purification. ThePurified wet cake is then dried to obtain product Chlorzoxazone.

Methanol obtained as ML is further taken for distillation and recycled insubsequent batches.

Chemical Reaction:

Page 53: ANNEXURE – A DETAILS OF PRODUCTS Sr. No. PROPOSED … · Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality and Agro Chemicals intermediates] by

Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality andAgro Chemicals intermediates] by M/s Prerana Agrochem Pvt Limited, Plot No. 824/18,

GIDC Jhagadia, Dist. Bharuch, Gujarat

Mass Balance:

Input Qty Output Qty4-CAP 1000 Overall Aqueous Water 10784Urea 1750 Methanol ML for Recycle 2100Acetic Acid 1824 Carbon Residue 40HCl [30 %] 3040 Drying Loss 300C S Lye 600 Product: Chlorzoxazone 1000Methanol 1600Carbon 10Water 4400

Total 14224 Total 14224

Flow Diagram:

Page 54: ANNEXURE – A DETAILS OF PRODUCTS Sr. No. PROPOSED … · Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality and Agro Chemicals intermediates] by

Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality andAgro Chemicals intermediates] by M/s Prerana Agrochem Pvt Limited, Plot No. 824/18,

GIDC Jhagadia, Dist. Bharuch, Gujarat

Page 55: ANNEXURE – A DETAILS OF PRODUCTS Sr. No. PROPOSED … · Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality and Agro Chemicals intermediates] by

Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality andAgro Chemicals intermediates] by M/s Prerana Agrochem Pvt Limited, Plot No. 824/18,

GIDC Jhagadia, Dist. Bharuch, Gujarat

32. Cloquintocet Mexyl

Process Description:

2-Heptanol is reacted with Monochloro Acetic Acid in Toluene as solvent with aidof P-Toluene sulfonic acid yielding the ester 2-Methyl Hexyl Chloroformatealong with liberation of water which is removed from the reaction mass. Thereaction mass is washed with water and further taken for next step of CloquintocetMexyl synthesis.

2-Methyl Hexyl Chloroformate in Toluene is reacted with 5-Chloro-8-Hydroxyquinoline along with Potassium Carbonate leading to formation ofCloquintocet Mexyl with generation of Potassium salts. The Potassium salt andorganic layer washed with water. Toluene recovered from organic layer and theresidual mass crystallized in Methanol followed by filtrate and drying. Methanolrecycled after recovery.

Chemical Reaction:

Stage I: Preparation of 2-Methyl hexyl Chloroformate

Stage II: Preparation of Cloquintocet Mexyl

+

Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality andAgro Chemicals intermediates] by M/s Prerana Agrochem Pvt Limited, Plot No. 824/18,

GIDC Jhagadia, Dist. Bharuch, Gujarat

32. Cloquintocet Mexyl

Process Description:

2-Heptanol is reacted with Monochloro Acetic Acid in Toluene as solvent with aidof P-Toluene sulfonic acid yielding the ester 2-Methyl Hexyl Chloroformatealong with liberation of water which is removed from the reaction mass. Thereaction mass is washed with water and further taken for next step of CloquintocetMexyl synthesis.

2-Methyl Hexyl Chloroformate in Toluene is reacted with 5-Chloro-8-Hydroxyquinoline along with Potassium Carbonate leading to formation ofCloquintocet Mexyl with generation of Potassium salts. The Potassium salt andorganic layer washed with water. Toluene recovered from organic layer and theresidual mass crystallized in Methanol followed by filtrate and drying. Methanolrecycled after recovery.

Chemical Reaction:

Stage I: Preparation of 2-Methyl hexyl Chloroformate

Stage II: Preparation of Cloquintocet Mexyl

+

Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality andAgro Chemicals intermediates] by M/s Prerana Agrochem Pvt Limited, Plot No. 824/18,

GIDC Jhagadia, Dist. Bharuch, Gujarat

32. Cloquintocet Mexyl

Process Description:

2-Heptanol is reacted with Monochloro Acetic Acid in Toluene as solvent with aidof P-Toluene sulfonic acid yielding the ester 2-Methyl Hexyl Chloroformatealong with liberation of water which is removed from the reaction mass. Thereaction mass is washed with water and further taken for next step of CloquintocetMexyl synthesis.

2-Methyl Hexyl Chloroformate in Toluene is reacted with 5-Chloro-8-Hydroxyquinoline along with Potassium Carbonate leading to formation ofCloquintocet Mexyl with generation of Potassium salts. The Potassium salt andorganic layer washed with water. Toluene recovered from organic layer and theresidual mass crystallized in Methanol followed by filtrate and drying. Methanolrecycled after recovery.

Chemical Reaction:

Stage I: Preparation of 2-Methyl hexyl Chloroformate

Stage II: Preparation of Cloquintocet Mexyl

+

Page 56: ANNEXURE – A DETAILS OF PRODUCTS Sr. No. PROPOSED … · Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality and Agro Chemicals intermediates] by

Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality andAgro Chemicals intermediates] by M/s Prerana Agrochem Pvt Limited, Plot No. 824/18,

GIDC Jhagadia, Dist. Bharuch, Gujarat

Mass Balance:

Flow Diagram:

Input Qty Output Qty2-Heptanol 408 Overall Aqueous Water 2491MCA 332 Residual Potassium Salt 684Toluene 1754 Toluene Recovered 1719PTSA 4 Methanol Recycle 27095-Cl-8HQ 630 Evaporation Loss 207Methanol 3333 Product 1000Water for Process 2351Total 8811 Total 8811

Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality andAgro Chemicals intermediates] by M/s Prerana Agrochem Pvt Limited, Plot No. 824/18,

GIDC Jhagadia, Dist. Bharuch, Gujarat

Mass Balance:

Flow Diagram:

Input Qty Output Qty2-Heptanol 408 Overall Aqueous Water 2491MCA 332 Residual Potassium Salt 684Toluene 1754 Toluene Recovered 1719PTSA 4 Methanol Recycle 27095-Cl-8HQ 630 Evaporation Loss 207Methanol 3333 Product 1000Water for Process 2351Total 8811 Total 8811

Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality andAgro Chemicals intermediates] by M/s Prerana Agrochem Pvt Limited, Plot No. 824/18,

GIDC Jhagadia, Dist. Bharuch, Gujarat

Mass Balance:

Flow Diagram:

Input Qty Output Qty2-Heptanol 408 Overall Aqueous Water 2491MCA 332 Residual Potassium Salt 684Toluene 1754 Toluene Recovered 1719PTSA 4 Methanol Recycle 27095-Cl-8HQ 630 Evaporation Loss 207Methanol 3333 Product 1000Water for Process 2351Total 8811 Total 8811

Page 57: ANNEXURE – A DETAILS OF PRODUCTS Sr. No. PROPOSED … · Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality and Agro Chemicals intermediates] by

Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality andAgro Chemicals intermediates] by M/s Prerana Agrochem Pvt Limited, Plot No. 824/18,

GIDC Jhagadia, Dist. Bharuch, Gujarat

Page 58: ANNEXURE – A DETAILS OF PRODUCTS Sr. No. PROPOSED … · Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality and Agro Chemicals intermediates] by

Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality andAgro Chemicals intermediates] by M/s Prerana Agrochem Pvt Limited, Plot No. 824/18,

GIDC Jhagadia, Dist. Bharuch, Gujarat

ANNEXURE – D

DETAILS OF WATER CONSUMPTION & WASTE WATER GENERATION

Sr.no.

PURPOSE Water Consumption,KL/day

Waste WaterGeneration, KL/day

1. Domestic 10 9.02. Industriala. Process 109 137b. Boiler 12 3c. Cooling 12 3d. Washing 5 5e. Scrubber 1 1f. Gardening 5 0

TOTAL [ 2 ] 144 149TOTAL [ 1 + 2 ] 154 158

Note: Domestic waste water will be disposed in to Septic tank/Soak pit

WATER BALANCE DIAGRAM

Total Water Requirement[154 KL/Day]

Domestic[10.0 KL/Day]

Industrial[139KL/Day]

Gardening[5.0 KL/Day]

Boiler[12 KL/Day]

Cooling[12 KL/Day]

Washing& Scrubber[6 KL/Day]

Process[109 KL/Day]

Domestic W/W[9.0 KL/Day]

Disposal through soakpit / septic tank

ETP

Waste water[149 KL/Day]

Treated w.w Sent to JhagadiaPipeline

Page 59: ANNEXURE – A DETAILS OF PRODUCTS Sr. No. PROPOSED … · Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality and Agro Chemicals intermediates] by

Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality andAgro Chemicals intermediates] by M/s Prerana Agrochem Pvt Limited, Plot No. 824/18,

GIDC Jhagadia, Dist. Bharuch, Gujarat

Flow Diagram of ETP

Raw Effluent Screen ChamberOil and Grease

TrapCollection CumNeutralization

tank

Primary SettlingTank

SecondaryTreatment

Treated w.w Send toJhagadia Pipeline

Secondary SettlingTank

Tertiary Treatment

Page 60: ANNEXURE – A DETAILS OF PRODUCTS Sr. No. PROPOSED … · Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality and Agro Chemicals intermediates] by

Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality and AgroChemicals intermediates] by M/s Prerana Agrochem Pvt Limited, Plot No. 824/18, GIDC

Jhagadia, Dist. Bharuch, Gujarat

ANNEXURE – EDETAILS OF HAZARDOUS WASTE

Sr.No.

Name of HazardousWaste

Category Quantity

/[Annum]

Mode of Disposal

1. Used/Spent oil 5.1 0.6 KL Collection, Storage, Transportationand Given to GPCB registeredreprocessor.

2. Used Filters/Filter Cloths &Materials /Hy-FlowMaterial / Used Carbon etc

36.2 12 MT Collection, storage, Transportationand Disposal at BEIL- Incineration.

3. Distillation Residue 20.3 64 MT Collection, Storage, Transportationand Disposal to Incineration / Co-Processing.

4. Process residue[ Iron Sludge ]

26.1 10000 MT Collection, Storage,Decontamination, Transportationand sent to cement manufactures /at common TSDF.

5. ETP Sludge 35.3 200 MT Collection, Storage, Transportation,and disposal at common TSDF / co-processing.

6. Discarded drumsDiscarded Bags/Liners

33.1 75000 Nos.360000Nos.

Collection, Storage,Decontamination Transportationand Sold to GPCB authorized users.

7. Spent solvent 20.2 Max. 18,500MT

Collection, storage and reusedwithin the plant premises

8. Fly-Ash --- 300 MT Collection, Storage, Transportationand send to Brick manufacture orLow lying area.

9. Hydrochloric Acid [30%][CAS-7647-01-0]

--- 539 MT Collection, Storage, transportationand sell to authorized users.

10. Spent Acid [70%][CAS-7664-93-9]

--- 5330 MT Collection, Storage, transportationand sell to authorized users.

11. Sodium Hydrosulfide[NaSH] Solution[CAS-16721-80-5]

--- 2316 MT Collection, Storage, transportationand sell to authorized users.

Page 61: ANNEXURE – A DETAILS OF PRODUCTS Sr. No. PROPOSED … · Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality and Agro Chemicals intermediates] by

Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality andAgro Chemicals intermediates] by M/s Prerana Agrochem Pvt Limited, Plot No. 824/18,

GIDC Jhagadia, Dist. Bharuch, Gujarat

ANNEXURE – F

DETAILS OF AIR POLLUTION CONTROL MEASURES

Details of Flue Gas Emission

Sr.No.

StackAttached to

Capacity Name of fuel &its consumption

APCM StackHeight

Parameter

1. Boiler 3 MT Solid Fuel500 Kg/Hour

MulticycloneSeparator

+Bag filter

+Water Scrubber

30 m

SPM ≤ 150 mg/Nm3

SO2 ≤ 100 mg/Nm3

NOx ≤ 50 mg/Nm3

2. Thermic FluidHeater [2 Nos.]

2 LakhKcal

[each]

Natural Gas116 m3/Hrs.

-- 15 m

3. DG Set [ Foremergencypurpose only]

225 KVA Diesel40 Ltr./Hr

-- 10 m

Details of Process Gas Emission

Sr.No.

Stack Attached to Stack Height Air Pollution controlsystem

Parameter

1. Process Reactor-1 10 m Water & Alkali Scrubber HCl ≤ 20 mg/Nm3

2. Process Reactor-2 10 m Alkali Scrubber SO2 ≤ 100 mg/Nm3

NOx ≤ 50 mg/Nm3

3. Process Reactor-3 12m Alkali Scrubber H2S ≤45 mg/Nm3

Page 62: ANNEXURE – A DETAILS OF PRODUCTS Sr. No. PROPOSED … · Annexures to Form – 1 & PFR for Proposed Project for manufacturing of [Speciality and Agro Chemicals intermediates] by