Isopropyl Alchohol Production from Acetone

  • Report Summary
  • Optional Analyses & Support

Analysis Basis : Germany

Period of Analysis : Q3 2019

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This report provides the cost structure of isopropyl alcohol production by hydrogenation of crude acetone. In this process- hydrogenation of acetone is carried out in the liquid phase over a fixed bed reactor, in the presence of catalysts such as Raney nickel. Minute quantities of by-products like diisopropyl ether, methyl isobutyl ketone, and 4-methyl-pentan-2-ol are obtained in this reaction. A sustainable way of carrying out this reaction is the ‘bionic leaf’ method involving splitting of water by sunlight, and with the help of biocatalyst bacteria to produce hydrogen.

 

The project economic analysis provided in the report discusses a Germany-based plant and encorporates:

 

  • Manufacturing Process
    • Process Flow
    • Material Flow
    • Material Balance
  • Raw Material and Product/s Specifications
    • Raw Material Consumption
    • Product and Co-Product Generation
    • Capital Investment
  • Land and Site Cost
    • Offsites/Civil Works
    • Equipment Cost
    • Auxiliary Equipment Cost
    • Contingency
    • Engineering and Consulting Charges
    • Working Capital
  • Variable Cost
    • Raw Material
    • Utilities
  • Fixed Cost
    • Labor Requirement & Wages
    • Overhead Expenses
    • Maintenance Charges
  • Financing Costs
    • Interest on Working Capital
    • Interest on Loans
  • Depreciation Charges
  • General Sales and Admin Costs
  • Production Cost Summary

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