Commodity Production Costs Report
Chloroprene Production from Butadiene
Chloroprene Operating Costs & Plant Construction Costs
This report analyses the economics of Chloroprene production from butadiene and chlorine in the United States, via a typical vapor phase butadiene chlorination process. Initially, butadiene is first chlorinated producing two isomers, 1,4-dichloro-2-butene and 3,4-dichloro-1-butene. Then, 1,4-isomers are isomerized to 3,4 isomer. This chemical is finally dehydrochlorinated in the presence of caustic soda producing chloroprene.
The report provides a comprehensive study of Chloroprene production and related Chloroprene production cost, covering three key aspects: a complete description of the Chloroprene production process examined; an in-depth analysis of the related Chloroprene plant capital cost (Capex); and an evaluation of the respective Chloroprene plant operating costs (Opex).
The Chloroprene 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 Chloroprene 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 Chloroprene 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): ?

Product
Chloroprene. Chloroprene is a synthetic monomer used in the production of neoprene rubber, known for its resistance to heat, oil, and chemicals. Neoprene is widely used in the automotive and construction industries for seals, hoses, and insulation. Chloroprene is produced via the chlorination of butadiene and is stored as a liquid. Its polymerization yields neoprene rubber, which is prized for its durability and versatility in a range of harsh environments.
Raw Materials
Butadiene. Butadiene is a commodity mainly produced as a byproduct of ethylene crackers. More specifically, it is extracted from the C4 hydrocarbons stream in naphtha-based crackers. The largest single use of butadiene is in the production of SBR and styrene-butadiene latexes.
Chlorine. Chlorine figures among the most important chemical commodities. It is an indispensable intermediate in the chemical industry, employed in the manufacture of a multitude of end products (e.g. materials of construction, solvents, pesticides, etc). Most of chlorine produced on commercial scale is based on electrolysis of aqueous sodium chloride (brine), which also generates caustic soda and hydrogen as co-products (chlor-alkali processes).
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Professional report based on Q3 2024 economic data, ensuring timely evaluations.
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Content Highlights
Plant Capital Cost Summary
Summary outlining the capital cost required for building the Chloroprene 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 Chloroprene 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 Chloroprene 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 Chloroprene 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 Chloroprene Production Cost Reports

Chloroprene Production from Acetylene
This report presents the economics of Chloroprene production from acetylene and hydrogen chloride in the United States. In the process examined, acetylene is dimerized to monovinyl acetylene (MVA), which is then reacted with hydrogen chloride to generate a chloroallene intermediate. Finally the chloroallene is rearranged to Chloroprene.
Details: 40 kta United States-based plant | Q3 2024 | 107 pages | Issue A | From $999 USD
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