Commodity Production Costs Report
Epichlorohydrin Production from Acrolein
Epichlorohydrin Operating Costs & Plant Construction Costs
This report provides a techno-economic study of an early stage process for Epichlorohydrin production from acrolein in the United States. The process examined is a non-commercial route based on Dow Chemical patents.
The report provides a comprehensive study of Epichlorohydrin production and related Epichlorohydrin production cost, covering three key aspects: a complete description of the Epichlorohydrin production process examined; an in-depth analysis of the related Epichlorohydrin plant capital cost (Capex); and an evaluation of the respective Epichlorohydrin plant operating costs (Opex).
The Epichlorohydrin 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 Epichlorohydrin 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 Epichlorohydrin plant operating costs analysis covers operating expenses, including variable costs like raw materials and utilities, and fixed costs such as maintenance, labor, and depreciation.
Product
Epichlorohydrin. Epichlorohydrin is a key raw material in the production of epoxy resins and glycerol, widely used in coatings, adhesives, and elastomers. It is valued for its reactivity and versatility in chemical manufacturing. Epichlorohydrin is produced by reacting allyl chloride with hypochlorous acid. It is stored as a liquid and must be handled with care due to its hazardous nature.
Raw Material
Acrolein. Acrolein is a highly reactive aldehyde used as an intermediate in the production of acrylic acid, methionine, and biocides. It is also utilized as a herbicide and in water treatment to control microbial growth. Acrolein is produced through the oxidation of propylene and is stored as a volatile liquid. Its reactivity with nucleophiles makes it a critical building block in chemical synthesis, especially for polymer and agrochemical applications.
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Professional report based on Q2 2025 economic data, ensuring timely evaluations.
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Ideal for investment screening, feasibility studies, cost estimates, and research planning.
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Content Highlights
Plant Capital Cost Summary
Summary outlining the capital cost required for building the Epichlorohydrin 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 Epichlorohydrin 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 Epichlorohydrin 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 Epichlorohydrin 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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Other Epichlorohydrin Production Cost Reports
Epichlorohydrin from Propylene (Allyl Chloride Intermediate)
This feasibility study provides an economic analysis of Epichlorohydrin (ECH) production from propylene and chlorine in the United States. Initially, propylene is chlorinated, generating allyl chloride, which is reacted with hypochlorous acid, formed by chlorine dispersion in water. Finally, the glycerol dichlorohydrins generated are hydrolyzed with calcium hydroxide, yielding ECH.
Details: 80 kta United States-based plant | Q2 2025 | 107 pages | Issue B | From $1,199 USD
Epichlorohydrin from Propylene (Allyl Alcohol Intermediate)
This study presents a techno-economic analysis of Epichlorohydrin production from propylene and chlorine in the United States. In this process, propylene is subjected to an acetoxylation reaction, followed by hydrolysis, generating allyl alcohol, which is then chlorinated, yielding glycerol dichlorohydrins. Finally, the glycerol dichlorohydrins generated are reacted with calcium hydroxide, yielding Epichlorohydrin.
Details: 110 kta United States-based plant | Q2 2025 | 107 pages | Issue C | From $1,199 USD
Epichlorohydrin Production from Glycerol and Hydrogen Chloride
This study provides an economic analysis of Epichlorohydrin production from glycerol in the United States. Initially, glycerol is reacted with hydrogen chloride in a hydrochlorination reaction, generating dichlorohydrins (DCH). Then, the DCH is hydrolyzed by caustic soda, yielding epichlorohydrin (ECH).
Details: 100 kta United States-based plant | Q2 2025 | 107 pages | Issue D | From $799 USD
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Other Related Production Cost Reports
Epoxy Phenol Novolac Resin Production
This report presents a techno-economic study of a process for Epoxy Phenol Novolac Resin production from phenol, formaldehyde and epichlorohydrin in a plant constructed in the United States. The process examined comprises two main steps: condensation of phenol and formaldehyde to produce phenol novolac resin; and (2) epoxidation of the phenol novolac resin with epichlorohydrin to form Epoxy Phenol Novolac Resin.
Details: 3 kta United States-based plant | Q2 2025 | 107 pages | Issue D | From $799 USD
Liquid and Solid Epoxy Resins Production
This report presents the economics of Liquid and Solid Epoxy Resins production from epichlorohydrin and bisphenol A (BPA) considering a United States-based facility. In this process, epichlorohydrin and BPA are reacted in the presence of an aqueous sodium hydroxide solution to form Liquid Epoxy Resin. The resulting resin is purified and further reacted with BPA to produce the Solid Epoxy Resin. Part of the Liquid Epoxy Resin obtained is also sold as co-product.
Details: 20 kta United States-based plant | Q2 2025 | 107 pages | Issue A | From $799 USD
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