Commodity Production Costs Report

Reformate from Naphtha (Continuous Catalyst Regeneration)

Reformate Operating Costs & Plant Construction Costs

800 kta United States-based plant | 107 Pages | Issue A | Q3 2024
Starting at $799 USD | See Report Editions Prices

This feasibility study is about Reformate production from naphtha in the United States. The process evaluated is a continuous catalyst regeneration (CCR) process similar to the UOP CCR Platforming technology. In this process, naphtha is reformed through a series of reactions, in which paraffins are converted to aromatics.

The report provides a comprehensive study of Reformate production and related Reformate production cost, covering three key aspects: a complete description of the Reformate production process examined; an in-depth analysis of the related Reformate plant capital cost (Capex); and an evaluation of the respective Reformate plant operating costs (Opex).

The Reformate production process description includes a block flow diagram (BFD), an overview of the industrial site installations, detailing both the process unit and the necessary infrastructure, process consumption figures and comprehensive process flow diagrams (PFD). The Reformate plant capital cost analysis breaks down the Capex by plant cost (i.e., ISBL, OSBL and Contingency); owner's cost; working capital; and costs incurred during industrial plant commissioning and start-up. The Reformate plant operating costs analysis covers operating expenses, including variable costs like raw materials and utilities, and fixed costs such as maintenance, labor, and depreciation.

Key reference(s): ?

Reformate Production Cost Report Process Schematic

The process under analysis comprises three major sections: (1) Naphtha treatment; (2) Reforming; and (3) Purification.

Naphtha treatment. Naphtha is combined with hydrogen-rich recycle gas and fed to a fired heater, where it is vaporized and raised to the hydrotreatment reaction temperature. Impurities that could contaminate and deactivate catalysts used in reforming reactions are hydrogenated and removed. The reactions take place in the vapor phase, with a reduced hydrogen consumption. A large part of this gas has to be recycled to that reactor. The liquid hydrocarbon stream from the separation step is then steam-stripped, for the removal of light impurities.

Reforming. Heated purified naphtha stream is fed to the first of radial-flow reactors arranged in a vertical stack. All reforming reactions take place in the presence of catalysts consisting of a higher-density alumina support, with tailored pore structure and re-optimized metal/acid balance, activated with platinum. While all reactions are endothermic, between each reaction stage the charge is reheated to reaction temperature by means of an interheater. Catalysts are continually withdrawn from the bottom of the reactor stack and fed to a vessel where the accumulated coke is burned off, which deactivates them over time.

Purification. The outlet from the reactors is then fed to a Gas/Liquid Separator, in which it is split into vapor and liquid products. The vapor phase, rich in hydrogen produced from reforming, is recycled to the reaction and to the hydrotreatment section while the surplus hydrogen produced is sold as a by-product. The liquid phase is sent to a column where Reformate is separated from liquified petroleum gas by-product and other light hydrocarbons.

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  • Production Process Information
  • Process Consumptions
  • Labor Requirements
  • Plant Capital Cost Summary
  • Operating Cost Summary
  • Production Costs Datasheet
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 80 Pages | 22 Tables | 9 Images

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Table of Contents


Features
  • Production Process Information
  • Process Consumptions
  • Labor Requirements
  • Plant Capital Cost Summary
  • Operating Cost Summary
  • Production Costs Datasheet
  • Plant Capital Cost Details
  • Operating Cost Details
  • See All Features

 90 Pages | 28 Tables | 13 Images

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Updated with Q3 2024 Data

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Table of Contents


Features
  • Production Process Information
  • Process Consumptions
  • Labor Requirements
  • Plant Capital Cost Summary
  • Operating Cost Summary
  • Production Costs Datasheet
  • Plant Capital Cost Details
  • Operating Cost Details
  • Plant Cost Breakdowns
  • Plant Capacity Assessment
  • Process Flow Diagrams
  • Costs in Different Countries Add-on
  • See All Features

  • 107 Pages | 34 Tables | 22 Images
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  • Updated with Q3 2024 Data
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Content Highlights

Plant Capital Cost Summary

Summary outlining the capital cost required for building the Reformate production plant examined.

Plant Capital Cost Details

Detailing of fixed capital (ISBL, OSBL & Owner’s Cost), working capital and additional capital requirements.

Plant Cost Breakdowns

Breakdown of Reformate process unit (ISBL) costs and infrastructure (OSBL) costs; plant cost breakdown per discipline.

Operating Costs Summary

Summary presenting the operating variable costs and the total operating cost of the Reformate production plant studied.

Operating Cost Details

Detailing of utilities costs, operating fixed costs and depreciation.

Plant Capacity Assessment

Comparative analysis of capital investment and operating costs for different Reformate plant capacities.

Production Process Information

Block Flow Diagram, descriptions of process unit (ISBL) and site infrastructure (OSBL).

Process Consumptions

Raw materials and utilities consumption figures, by-products credits, labor requirements

Process Diagrams

Process flow diagrams (PFD), equipment list and industrial site configuration

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Benzene Production from Reformate

This report presents the economics of Benzene production from reformate in the United States using a typical sulfolane liquid-liquid extraction process. The solvents extracts first the aromatics from the reformate. The aromatics are then stripped and separated into benzene, toluene and mixed xylenes.

Details: 350 kta United States-based plant | Q3 2024 | 107 pages | Issue A | From $799 USD

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This report presents the economics of Toluene production from reformate. The reformate is submitted to a typical sulfolane liquid-liquid extraction, giving a mixture of aromatics, which is further processed to yield pure Toluene. Benzene and mixed xylenes are produced as by-products. The economic analysis presented is based on a plant constructed in the United States.

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