Epichlorohydrin Production from Glycerol and Sodium Chloride
Epichlorohydrin Production Costs Report | Issue F | 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 the economics of Epichlorohydrin (ECH) production from glycerol and sodium chloride in the United States. Initially, brine is decomposed electrolytically in a membrane cell, producing chlorine, caustic soda and hydrogen. The hydrogen and chlorine react forming hydrogen chloride (HCl). Finally, glycerol is reacted with HCl, generating dichlorohydrins (DCH), which are hydrolyzed to ECH by the caustic soda.
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.
Process Overview
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 Materials
Sodium Chloride. Sodium chloride (NaCl) is the salt naturally occurring in sea water. Sodium chloride (as aqueous solution, i.e., brine or solid) is widely used in the chemical industry as a feedstock for the production of chlorine, sodium hydroxide, and other sodium-based compounds through electrolysis.
Glycerol. Crude glycerol is a byproduct of biodiesel production, containing impurities like methanol and soaps. It is used in animal feed, as a raw material for chemical synthesis, and in biogas production. Collected from transesterification processes, it is stored as a viscous liquid. Purification can yield refined glycerol for pharmaceuticals and personal care products.
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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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Production Costs Datasheet
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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 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
Other Epichlorohydrin Production Cost Reports
Epichlorohydrin Production from Allyl Chloride
This report presents a economic analysis of Epichlorohydrin production from allyl chloride and chlorine in the United States using a typical hypochlorination process. Initially, allyl chloride is reacted with hypochlorous acid, formed by chlorine dispersion in water. The glycerol dichlorohydrins generated are then treated with calcium hydroxide to promote epoxidation, yielding ECH.
Details: 75 kta United States-based plant | Q2 2024 | 107 pages | Issue A From $799 USD
The cost analyses presented in this report target a 75 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.
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 2024 | 107 pages | Issue B From $1,199 USD
The cost analyses presented in this report target a 80 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.
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 2024 | 107 pages | Issue C From $1,199 USD
The cost analyses presented in this report target a 110 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.
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 2024 | 107 pages | Issue D From $799 USD
The cost analyses presented in this report target a 100 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.
Epichlorohydrin Production from Acrolein
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.
Details: 75 kta United States-based plant | Q2 2024 | 107 pages | Issue E From $799 USD
The cost analyses presented in this report target a 75 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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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.
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