DATTA HYDRO CHEM (P) LTD. I S O 9 0 0 1 : 2 0 1 5 QUALITY MANAGEMENT SYSTEMS
D H C P L INTRODUCTION COMPANY PROFILE • MAVDIKAR GROUP of company. • Extensive experience of THREE decades in the trading & transportation of Petro-Chemicals. • Manufactures Specialty Petro-Chemicals solvents like PENTANE & HEXANE since July 2002. T H E FA C T O R Y I S S I T U AT E D I N A F U L LY D E V E L O P E D C H E M I C A L Z O N E AT K U R K U M B H M I D C , D I S T. P U N E , M A H A R A S H T R A , I N D I A . I S O 9 0 0 1 : 2 0 1 5
D H C P L MANUFACTURING PROCESS The plant designed for fractionating (Distilling) various types & grades of Hydrocarbon solvents into various • types & grades of Specialty petroleum Solvents (Industrial Grade) which are used in various types of chemical Industries such as Paints, Textile, Printing Inks, etc. operate on batch wise basis. The details of the plant operation are described in the following paragraphs. The plant contains distillation column special type of packing material for better mass transfer & separation. • The manufacturing process involves following stages: • Charging Hydrocarbon Solvents / Chemicals from storage tank to distillation kettle. • Heating of Hydrocarbon Solvents / Chemicals by hot thermic fluid slowly. • Vapors are then passed through the Distillation column. • Vapor formed during the process is collected in Cooling water Condenser, where the vapor are condensed • and then passed through the Product Cooler & Bottoms Condenser and a part of it through the Vent Condenser. Collection of different fractions of Hydrocarbon Solvents from distillation column in bulk storage tanks. • Different fractions are collected at different temperature range as per customer’s requirement. As per the requirements from customers the specific fraction is blended to formulate to the required • specialty petroleum solvents ****************************************************************************** I S O 9 0 0 1 : 2 0 1 5
D H C P L OPERATIONS Raw pentane is tested in unloaded in storage tanks after measurements. • Raw Pentane is charged into Kettle as per required batch size. • Thermic fluid & Cooling water circulation is started for process. • Top temperature of distillation column is maintained at specific temperature where pentane is separated and • satisfies specification of end user mainly this product is name under D Sol Pentane. Further after recovery of pentane, N- hexane fraction is separated by maintaining specific temperature in • process where N Hexane reach fraction is separated and satisfies specification of end user mainly this product is name under D Sol N Hexane. At different stage of process during the production of D Sol Pentane & D Sol N Hexane , a intermediate • fraction is collected which is mainly a mixture of impure Pentane and Hexane majorly and blended to satisfies end user requirement in paint and thinner industry to get cheaper hydrocarbon solvent, this product is name under D Sol 50. As and when specific requirement of Petroleum Ether is received and alternate or equivalent mixture of • above pentane and hexane stream is so formulated to give boiling point result of required specification of 40 60 and vice versa with 50 70, the indicator 40 60 and 50 70 , is nothing but define the range of boiling point of blend of pentane and hexane stream with some addition of specific fraction from pentane and hexane production process, and satisfies specification of end user mainly this product is name under D Sol Petroleum Ether 40 60 and D Sol Petroleum Ether 50 70. Similarly other product DSOL Pentane CP-IP-95 & DSOL Pentane CP-IP-75 is produce by distillation of crude • Cyclopentane and formulated with D Sol Pentane to required specification to satisfy end user requirement in appliance industry. I S O 9 0 0 1 : 2 0 1 5
D H C P L FLOW CHART RAW MATERIAL 1)CYCLOPENTANE SOURCE SUPPLIER 2)PENTANE CONDENSATE FROM GAIL , HPL & IMPORT 3)PENTANE PLUS LPG REFINERY FRACTIONAL DISTILLATION MANUFACTURING PROCESS PENTANE 1 COMMERCIAL N PENTANE ISO PENTANE PENTANE 2 HEXANE COMMERCIAL / FOOD GRADE HEXANE PETROLEUM ETHER 3 SPECIAL BOILING POINT SOLVENTS 40:60, 60:80, 40:80 & 55/115 I S O 9 0 0 1 : 2 0 1 5
D H C P L TO PRODUCT INDIGNEOUS QUALITY PRODUCTS • Dsol Pentane • Dsol N Hexane • Dsol Pentane CPIP 95 • Dsol Pentane CPIP 75 • Dsol Petroleum Ether 40 60 • Dsol Petroleum Ether 50 70 I S O 9 0 0 1 : 2 0 1 5
D H C P L EQUIPMENT PROCESS:- Distillation Column(C-101 & C-201), Kettle Reboiler(E-101 & TH-201), Reflex Drum, Condenser, Product cooler, Bottom Cooler, Receivers, Process Intermediate tanks, Final Finished Product and Raw Material Storage tanks. CONTROL SYSTEM:- DCS Control System FM series . UTILITY :- Thermo Pack, Thermic Fluid Heater – (Thermax Pune) Cyclotherm - VTCY Series Boiler (Thermax Pune ) Cooling Tower ( M Square Engineer) Air Compressor (Ingersoll Rand) Nitrogen Blanketing Vacuum Pump (Toshniwal) DG set Eco Friendly (Kirloskar) Fire Fighting Equipment's.(Entire System) I S O 9 0 0 1 : 2 0 1 5
D H C P L QC/QA • Quality Assurance LABORATORY in House. • Controlled input Raw Materials, Intermediates & Finished Products. • Required tests are based on ASTM, UOP& BIS standards . • Analysis carried out in PPM level accuracy. • Modern Equipment :- Ø Ultra Fast Trace Gas Chromatograph Make by Thermo Fisher. Ø UV 3000+ Double beam Ø Metrohm KF Coulometer (Swiss made) Ø Distillation unit, Hydrometer... etc. Ø Electrometric Autotitrator ( Bromine index) Ø Karl Fischer Autotitrator (Moisture) Ø Sulphur content analysis unit. Ø Nitrogen content analysis unit. I S O 9 0 0 1 : 2 0 1 5
D H C P L QC/QA Ø Latest Gas Chromatograph Analyzer To Analyze • CO (Carbon Monoxide) • CO2 (Carbon di Oxide) • O2 (Oxygen) • Low Oxygenate viz :- 1. Diethyl ether 2.Isovaleraldehyde 3.Valeraldehyde 4. Acetaldehyde 5.Methyle pert. Butyl ether 6.Disoprpylether 7.Butyraldehyde 8.Propylether 9.Methnol 10. Acetone 11.Propanol 12. Tert.amyl methyl ether 13. 2-Butanone 14. Ethanol. 15.Propylether 16.Propanol 17. Tert. Butanol 18.Ethanol 19.1- Butanol I S O 9 0 0 1 : 2 0 1 5
D H C P L QC/QA Ø Electrometric Auto Titrator ( Bromine index) Ø Karl Fischer Auto Titrator Moisture) Ø Sulphur content analysis unit. Ø Spectrophotometer. ( LAB INDIA) Ø Shaw Meter for Due Point. Ø Metrohm KF Coulometer (Swiss Made) Ø Distillation unit, Hydrometer.. etc. I S O 9 0 0 1 : 2 0 1 5
D H C P L QUALITY MANAGEMENT SYSTEM ISO 9001:2015 by World wide • recognized Accredited certification Body DNV. DEVELOPMENT • MANUFACTURE AND SUPPLY OF SPECIALTY HYDROCARBON SOLVENTS LIKE ALKANE ISO 9001:2015 QUALITY MANAGEMENT SYSTEMS I S O 9 0 0 1 : 2 0 1 5
sales 45.00 40.00 35.00 30.00 25.00 20.00 15.00 10.00 5.00 - C A P I T A L I N V E S T M E N T I N I N R : - 4 2 C R I S O 9 0 0 1 : 2 0 1 5
D H C P L VISION AND ACHIEVMENT VISION • To establish as a “World Class Company” in the field of Pentane Products. • To achieve continuous profitable business growth • Stake holder satisfaction & pride • Fulfillment of social obligations ACHIEVEMENT • Established an in-house R&D, which lead to the development of an OWN TECHNOLOGY for producing Pentane and Hexane quality Products. • Fulfillment of QUALITY PRODUCTS as per customer requirement. • Certification awarded by world renowned certification authority DNV as ISO 9001:2015 QMS certified company, being first in India among Pentane manufacturers. • First DCS CONTROL fully automatic plant. I S O 9 0 0 1 : 2 0 1 5
D H C P L A D D I T I O N A L F A C I L I T I E S u COMPANY OWN DEDICATED ROAD TANKER. TO AVOID ANY SPECIALLY DESIGNED AND APPROVED BY PESO CONTAMINATIONS IN FOR ONLY PENTANE LOGISTIC . PRODUCT DEDICATED ROAD PENTANE TANKER u IN HOUSE DIGITAL 60 MT WEIGH BRIDGE TO ENSURE TO ENSURE RIGHT & TRUE AND CORRECT MEASURMENT OF PRODUCT . ACCURATE WEIGHT u ECOFREINDLY EQUIPMENT USED TO AVOID FOSSIEL CYCLOTHERM- VTCY SERIES FUEL IN PRODUCTION. FOR ECOFREINDLY FUEL u DG SET AND ONLINE UPS INSTALLED TO ENSURE UNINTERRUPTED POWER SMOOTH OPERATION.
D H C P L I N D U S T R I A L S A F E T Y – U s u a l l y i n a H yd ro ca r b o n h a n d l i n g a n d p ro c e s s i n g In d u st r y A c c i d e nt s ta ke p l a c e d u e to G a s L e a ka ge & E l e c t r i ca l Fa u l t s i n t h e O P E R AT I O N A L A R EA S . – A s o n to d ay t h e co nve nt i o n a l p ra c t i c e to f i n d o u t l e a ka ge i s N OT S U F F I C E N T TO P I N P O I N T T H E E X AC T FAU LTS . – Re p o r t o f te st i n g s e r v i c e s ta ke s m o re t i m e a n d i s a l ways w i t h t h e l i m i tat i o n to t h e s at u rat i o n o f G A S VO LU M E . – Re p o r t p ro d u c e d by s e r v i c e p rov i d e r a re m o st o f t h e t i m e i n CO N F U S I O N w i t h t h e a c t u a l f i e l d o p e rato rs , S afe ty o f f i c e rs , S e n i o r M a n a ge m e nt a n d th e M o st I m p o r ta nt P r in c ip le M a n u fa c tu re r / S u p p lie r o f th at p a r tic u la r Pa r t o r Eq u ip m e nt . I S O 9 0 0 1 : 2 0 1 5
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