Vinyl Chloride Production from Ethylene Dichloride
Vinyl Chloride Production Costs Report | Issue A | Q4 2024
Report Details |
500 kta United States-based plant | Q4 2024 | 107 pages |
This report presents a cost analysis of a 500 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 the economics of Vinyl Chloride production from ethylene dichloride (EDC) in the United States using a typical thermal cracking process. In the process under analysis, EDC is thermally cracked to produce Vinyl Chloride, also generating hydrogen chloride as a by-product.
The report provides a comprehensive study of Vinyl Chloride production and related Vinyl Chloride production cost, covering three key aspects: a complete description of the Vinyl Chloride production process examined; an in-depth analysis of the related Vinyl Chloride plant capital cost (Capex); and an evaluation of the respective Vinyl Chloride plant operating costs (Opex).
The Vinyl 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 Vinyl 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 Vinyl 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) Thermal Cracking; (2) VCM Purification; and (3) EDC Recovery.
Thermal Cracking. The EDC from the EDC Tank is mixed with recycled EDC and is preheated, vaporized and subsequently cracked in a pyrolysis furnace heated by fuel combustion. The cracking reaction is endothermic and generates VCM, HCl, by-products of various chemical structures and coke. The furnace operates at temperatures above 480 °C and pressure of about 16 bar. Cracking rates of up to 60% are achieved, with selectivity to VCM greater than 98%.
VCM Purification. The output from the pyrolysis furnace, containing the VCM produced, is quenched to minimize coke formation. The overhead from the quench is sent to the HCl Column. Hydrogen chloride stream recovered in column overhead is sent to a section, where acetylene impurity is hydrogenated. After, it is sent to the consumer. The column bottoms, comprising unconverted EDC and VCM, are fed to a VCM column, where VCM is separated from unconverted EDC. Residual HCl present in VCM stream is removed in a stripper and recycled to the first column, while VCM product is stored.
EDC Recovery. Unreacted EDC is fed to the High-Boil column, for high-boiling compounds removal. The bottom product from the High-Boil column and the bottom product from quench are fed to the Vacuum Column, where more EDC is recovered. EDC streams are recycled to cracking, while heavies is sent to a waste disposal system.
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Production Process Information
Process Consumptions
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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 Vinyl 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 Vinyl 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 Vinyl 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 Vinyl 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
Other Vinyl Chloride Production Cost Reports
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This study reviews the costs associated with Vinyl Chloride production directly from ethane and chlorine. The process examined is an early stage process similar to that developed by European Vinyls Corporation, now owned by INEOS. The process is a direct ethane to vinyl chloride monomer route. The economic assessment assumes an industrial plant in the United States.
Details: 500 kta United States-based plant | Q4 2024 | 107 pages | Issue B From $1,199 USD
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Vinyl Chloride Production from Acetylene
This feasibility study reviews a typical hydrochlorination process for Vinyl Chloride production from acetylene. In this process, anhydrous hydrogen chloride is reacted in vapor phase with acetylene over a mercuric chloride catalyst producing Vinyl Chloride. The economic analysis presented is based on the construction of an industrial plant in the United States.
Details: 280 kta United States-based plant | Q4 2024 | 107 pages | Issue C From $799 USD
The cost analyses presented in this report target a 280 kta (kilo metric ton per annum per annum) United States-based plant. For those interested in cost analyses considering other plant capacities and/or locations, Intratec offers a customized analysis as an optional feature.
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