Reformate Production from Naphtha via Semi-Regeneration Process

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Analysis Basis : Germany

Period of Analysis : Q1 2020

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This study reviews the costs associated with Reformate production from naphtha via a semi-regeneration process. In a typical semi-regenerative reforming unit, treated naphtha feed is combined with recycled hydrogen gas and heat exchanged against reactor effluent. The combined feed is then raised to reaction temperature in the charge heater and sent to the reactor section. Down-flow or radial-flow reactors are arranged in a conventional side-byside pattern. The catalyst deactivates over time at reaction conditions. After the catalyst has deactivated to the point where the desired product can no longer be achieved, the unit is taken off-line, the reactors are purged of hydrocarbons and the catalyst is regenerated.

 

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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