Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: A
ICC - Volume: 183
ICC - Report ID: 183-A
ICC - Report Location: United States
ICC - Is Popular: 0
ICC - Is Developed: 1
ICC - Title: Propylene Oxide Production from Propylene and Chlorine
ICC - Show Overview: 1
ICC - Report Location ID: 1
ICC - Plant Capacity Unit ID: 14
ICC - Volume Reports List: 183-B,183-C,183-D,183-E,183-F,183-G
ICC - Related Reports List: 027-G,111-B,021-D,111-A
ICC - Report Location Code: USA
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ICC - Prices: {"versions":{"1":{"1":"799","2":"799","3":"799"},"2":{"1":"1599","2":"1599","3":"1599"},"3":{"1":"2699","2":"2699","3":"2699"}},"currency":"USD"}
ICC - Plant Capacity Unit Name: kilo metric ton per annum
ICC - Plant Capacity Unit Short Name: kta
ICC - Process Overview Image: //cdn.intratec.us/images/icc/process-overview/183-A.jpg
ICC - Process Overview Text: <h6>Products</h6> <p><b>Propylene Oxide</b></p>, <p><b>Dichloropropane</b></p> <h6>Raw Materials</h6> <p><b>Chemicals</b></p>, <p><b>Chlorine</b></p>, <p><b>CG Propylene</b></p>, <p><b>Cell Liquor</b></p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/183-A.jpg
ICC - Process Schematic Text: <p>The process under analysis comprises three major sections: (1) Hypochlorination; (2) Epoxidation; and (3) Purification.</p><p>Hypochlorination. Initially, fresh, gaseous polymer grade propylene and chlorine are mixed with water, forming an aqueous solution. Such compounds react producing propene – chloronium complex, an intermediate which reacts with water yielding hydrochloric acid and propylene chlorohydrin (PCH) isomers. The gaseous effluent from the reactor is fed to a separator, which separates a solution containing PCH from the vent gas. The PCH solution is directed to the Epoxidation, while the vent gas is passed through a caustic scrubber and released.</p><p>Epoxidation. The PCH solution and a caustic solution (from a chlor-alkali unit) are fed to a saponifier, where a dehydrochlorination reaction takes place. Here, the PCH is converted to propylene oxide (PO) while organic impurities are stripped from the brine. The brine from saponifier bottom is directed to a treatment step, while a stream containing PO from saponifier overhead is routed to purification steps.</p><p>Purification. The stream rich in PO is distilled in a first column for obtaining a crude propylene oxide stream, removed from overhead. A solution containing 1,2-dichloropropane (DCP) from column bottom is decanted, yielding a DCP-rich stream and water. In a second column, residual light ends are stripped off from the crude PO stream and burned for fuel. The column’s bottom product is fed to a third column, which further purifies the PO from impurities. A 99.9 wt% Propylene Oxide is condensed and stored. Heavy ends are burned for fuel. The DCP-rich stream is treated for the neutralization, and for the removal of epoxidation by-products and other heavy components. The brine stream from Epoxidation and the wastewater from the first column are treated and returned to the chlor-alkali facility.</p><p></p>
ICC - Short Description: This report presents the economics of Propylene Oxide (PO) production from chemical grade (CG) propylene and chlorine in the United States. In the process under analysis, propylene and chlorine react, yielding chlorohydrin intermediate, which is then dehydrochlorinated to produce PO. Dichloropropane is generated as by-product.
ICC - Main Product: Propylene Oxide
ICC - Plant Capacity: 450.00
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Propylene Oxide Production from Propylene and Chlorine

Propylene Oxide Production Costs Report | Issue A | Q3 2024

Production Cost Report

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450 kta United States-based plant   |   Q3 2024   |   107 pages

This report presents a cost analysis of a 450 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.

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Production Process Information

Process Consumptions

Labor Requirements

Plant Capital Cost Summary

Operating Cost Summary

Production Costs Datasheet

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Production Process Information

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Production Costs Datasheet

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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

Costs in Different Countries Add-on

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Content Highlights

Plant Capital Cost Summary

Summary outlining the capital cost required for building the Propylene Oxide 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 Propylene Oxide 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 Propylene Oxide 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 Propylene Oxide 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 Propylene Oxide Production Cost Reports

Propylene Oxide Production from Propylene and Isobutane

This report examines the costs related to Propylene Oxide (PO) production from chemical grade (CG) propylene and isobutane in the United States. The process is similar to LyondellBasell process. In this process, isobutane is oxidized to produce t-butyl hydroperoxide, which reacts with propylene to produce PO.

Details: 450 kta United States-based plant   |   Q3 2024   |   107 pages   |   Issue E   From $1,199 USD

The cost analyses presented in this report target a 450 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.

Propylene Oxide from Propylene and Hydrogen (Indirect Oxidation)

This report analyses the economics of Propylene Oxide (PO) production from polymer grade (PG) propylene and hydrogen in the United States. The process used is a direct epoxidation similar to AIST/Nippon Shokubai process. Initially, hydrogen is directy oxidized with oxygen to hydrogen peroxide. The peroxide converts propylene into propylene oxide.

Details: 250 kta United States-based plant   |   Q3 2024   |   107 pages   |   Issue G   From $1,199 USD

The cost analyses presented in this report target a 250 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 analyses the economics of Propylene Glycol production from propylene oxide in the United States, via a typical hydration process. In this analysis, propylene oxide is hydrolyzed to propylene glycol. Dipropylene glycol is produced as by-product.

Details: 200 kta United States-based plant   |   Q3 2024   |   107 pages   |   Issue D   From $799 USD

The cost analyses presented in this report target a 200 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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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.

Chlorine Production from Sodium Chloride (Membrane Process)

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Details: 500 kta United States-based plant   |   Q3 2024   |   107 pages   |   Issue A   From $799 USD

The cost analyses presented in this report target a 500 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.

Chlorine Production from Sodium Chloride (Diaphragm Process)

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Details: 550 kta United States-based plant   |   Q3 2024   |   107 pages   |   Issue B   From $799 USD

The cost analyses presented in this report target a 550 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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