Allyl Chloride Production
Allyl Chloride Production Costs Report | Issue A | Q2 2024
Report Details |
100 kta United States-based plant | Q2 2024 | 107 pages | Delivered in PDF |
This report presents a cost analysis of a 100 kta (kilo metric ton per annum) United States-based plant. You can add a customized cost analysis, assuming another location (country), when ordering a premium edition of this report.
Report Abstract
This report presents a techno-economic analysis of a typical chlorination process for Allyl Chloride production from chlorine and propylene considering a plant constructed in the United States.
The report provides a comprehensive study of Allyl Chloride production and related Allyl Chloride production cost, covering three key aspects: a complete description of the Allyl Chloride production process examined; an in-depth analysis of the related Allyl Chloride plant capital cost (Capex); and an evaluation of the respective Allyl Chloride plant operating costs (Opex).
The Allyl Chloride 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 Allyl Chloride 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 Allyl Chloride plant operating costs analysis covers operating expenses, including variable costs like raw materials and utilities, and fixed costs such as maintenance, labor, and depreciation.
Process Schematic
The process under analysis comprises three major sections: (1) Chlorination; (2) Propylene Recovery; and (3) Product Treatment.
Chlorination. The liquid propylene is sent to an evaporator, being vaporized and preheated to the chlorination reaction temperature. It is then fed, along with chlorine, to an adiabatic reactor, where the chlorination reaction is carried out, producing allyl chloride and by-products.
Propylene Recovery. The reactor effluent is cooled and routed to the Prefractionator, where HCl and unreacted propylene are separated from chloropropenes, dichloropropenes, chloropropanes and heavier compounds. The Prefractionator overhead stream, containing HCl and propylene, is passed in countercurrent with demineralized water in the HCL Absorber, forming a hydrochloric acid solution with 32% purity that is stored. The off-gas, mostly propylene, is sent to Caustic Wash, which removes residual HCl. The washed propylene is compressed and routed to a decanter and dried by adsorption for water removal. Part of dried propylene is returned to the feed, and the remainder is recycled to the Prefractionator.
Product Treatment. The bottom stream from the Prefractionator, rich in Allyl Chloride, is directed to the Light-ends Column, which strips components lighter than Allyl Chloride, that are burned for fuel. The bottom product of this column is sent to the Purification Column, where Allyl Chloride is removed form the top, condensed and routed to storage, while its bottom is sent to Dichloropropene Column. This last distillation step separates dichlorides, collected from the top and sent to storage, from heavy components that are burned for fuel.
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Production Process Information
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Production Costs Datasheet
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Production Process Information
Process Consumptions
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Operating Cost Summary
Production Costs Datasheet
Plant Capital Cost Details
Operating Cost Details
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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
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Content Highlights
Plant Capital Cost Summary
Summary outlining the capital cost required for building the Allyl Chloride 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 Allyl Chloride 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 Allyl Chloride 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 Allyl Chloride 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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