Oleochemical Complex on 27 Acres

100,000 Metric Ton/Year

IMMEDIATELY AVAILABLE - #600369

55,000 Metric Ton/Year Fatty Acid Plant
Splitting, Fatty Acid Distillation, Hydrogenation, Wet Separation And Stearine - #600497

17,000 Metric Ton/Year Glycerine Plant
Refines Soap Lye Crude And Splitters Crude To Produce High Purity Glycerine - #600493

24,000 Metric Ton/Year Esters Plant
Highly Automated And Flexible Batch - #600494

15,000 Metric Ton/Year Triacetin Plant
Highly Automated And Dedicated Continuous - #600496

9,500 Metric Ton/Year Sorbitan Ester (Esterification) Plant
Highly Automated And Flexible Batch - #600495

55,000 Metric Ton/Year Fatty Acid Plant #600497

Splitting, Fatty Acid Distillation, Hydragenatian, Wet Separation And Stearine

• Shut Down: 2009
• Technology: Free And Clear To Practice Anywhere In The World
• Raw Materials:
  • Tallow (Grades 2, 4, and 6)
  • Natural Oils (Coconut, Palm, Palm Kernel and Soya Bean)
• Unit Operations In This Facility Include:
  • (3) Fat Splitting (Hydrolysis) Columns
  • (2) Fatty Acid Vacuum Distillation Units
  • (1) Fat Batch Hardening (Hydrogenation) Unit
  • (1) Fat Separation Unit (Wet Process)
• Major Equipment Includes: (Contact IPP For A Complete Equipment List)
  • (3) 316LSS Splitting Columns
  • 5,600 Lbs/Hr product 316SS Kestner 4-Stage Evaporator
  • (12) 316TiSS Crystallizer Banks
  • 316SS WA5 Mixer
  • 1 M dia. 316SS Krauss Maffei Centrifuge
  • 800 mm dia. 316SS Krauss Maffei Centrifuge
  • (5) 316SS Heine Centrifuges
  • 316SS Dryer Vessel
  • 316SS Reactor Vessel
  • SS Filtration Tank
  • Lurgi Distillation Columns
• Contact IPP For A Process Overview And Process Flow Diagrams
• Complete Documentation Available

Additional Components Available From This Complex

Contact IPP For Details About These And Other Available Components

• Flaking And Bagging Unit
• Tank Farms: (220) SS & CS Tanks From 5,000 To 500,000 Gallon

17,000 Metric Ton/Year Glycerine Plant #600493

Refines Soap Lye Crude And Splitters Crude To Produce High Purity Glycerine

• Built: 2003
• Shut Down: 2009
• Raw Materials: Crude Glycerine
• Product Produced: Pure Glycerine
• Major Equipment Includes: (Contact IPP For A Complete Equipment List)
  • 316LSS Pre-Dryer
  • 316SS Condensing Column
  • 316TiSS Stripping Column
  • 18 M² 316TiSS Buss SMS Luwa Wiped Film Evaporator
  • 2 M² 316TiSS Buss SMS Luwa Wiped Film Evaporator
• Complete Documentation Available

24,000 Metric Ton/Year Esters Plant #600494

Highly Automated And Flexible Batch

• Built: 1998
• Shut Down: 2009
• Raw Materials:
• Fatty Acids
• Alcohols

15,000 Metric Ton/Year Triacetin Plant #600496

Highly Automoted And Dedicated Continuous

• Built: 2009
• Raw Materials: Glycerine, Acetic Acid, Acetic Anhydride
• Major Equipment Includes: (Contact IPP For A Complete Equipment List)
  • Azeotropic Distillation Calum Designed To Operate With Both Liquid & Gaseous Feed
  • 3,500 Liter 316SS/254SS Reactor
  • (2) 2,700 Liter 31655/904LSS Reactors
  • 904LSS Still Column
  • 15.5 M² 904LSS Still Reboiler
• Complete Documentation Available

9,500 Metric Ton/Year Sorbitan Ester (Esterification) Plant #600495

Highly Automated And Flexible Batch

• Shut Down: 2009
• Raw Materials: Fatty Acids, Sorbitol
• Major Equipment Includes: (Contact IPP For A Complete Equipment List)
  • (2) Pressure Reactors (25,000 Liter 316LSS and 15,000 Liter 321SS)
• Complete Documentation Available

Contact IPP For A Complete Description

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