Reformate Production from Naphtha via Catalyst Regeneration Process

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Analysis Basis : Germany

Period of Analysis : Q1 2020

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The study presents reformate production from naphtha through continuous catalyst regeneration process. Stacking of reactor with catalyst allows the catalyst to flow from the top reactor to the bottom reactor due to gravity. A partially deactivated catalyst is continuously withdrawn, transferred to the CCR regenerator from the bottom of the reactor stack, regenerated, and then transferred again to the top of the first reactor to complete the catalyst circulation cycle. Hydrotreated naphtha feed is intermixed with recycled hydrogen gas, and heat exchanged with the reactor effluent. The charge heater heats the intermixed feed up to the reaction temperature which is then sent to the first reactor section. The effluent from the last reactor is heat exchanged with the intermixed feed, cooled, and finally separated into vapor and liquid products using a separator, thus forming reformate.


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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