Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: E
ICC - Volume: 183
ICC - Report ID: 183-E
ICC - Report Location: United States
ICC - Is Popular: 0
ICC - Is Developed: 1
ICC - Title: Propylene Oxide Production from Propylene and Isobutane
ICC - Show Overview: 1
ICC - Report Location ID: 1
ICC - Plant Capacity Unit ID: 14
ICC - Volume Reports List: 183-A,183-B,183-C,183-D,183-F,183-G
ICC - Related Reports List: 027-G,194-A,021-D
ICC - Report Location Code: USA
ICC - Delivery Times: {"versions":{"1":{"1":{"time":"5","price":0},"2":{"time":"1","price":"299"}},"2":{"1":{"time":"5","price":0},"2":{"time":"1","price":"299"}},"3":{"1":{"time":"7","price":0},"2":{"time":"3","price":"299"}}},"unit":"d"}
ICC - Prices: {"versions":{"1":{"1":"1199","2":"1199","3":"1199"},"2":{"1":"1999","2":"1999","3":"1999"},"3":{"1":"3399","2":"3399","3":"3399"}},"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-E.jpg
ICC - Process Overview Text: <h6>Products</h6> <p><b>Propylene Oxide</b></p>, <p><b>Tert-Butyl Alcohol</b></p> <h6>Raw Materials</h6> <p><b>Chemicals</b></p>, <p><b>Isobutane</b></p>, <p><b>CG Propylene</b></p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/183-E.jpg
ICC - Process Schematic Text: <p>The process under analysis comprises two major sections: (1) Reactions; and (2) Purification.</p><p>Reactions. Isobutane is reacted with oxygen yielding a solution of tertiary butyl hydroperoxide (TBHP) and tertiary butyl alcohol (TBA) by-product. While the reaction is exothermic, reaction conditions are regulated such that the reaction mixture is constantly boiling, so that reaction heat is removed by reaction media vaporization. Accordingly, the oxidation product - a vapor mixture - is removed from the reactor and cooled, in such a way that TBHP, TBA, unreacted isobutane and other readily condensable components are condensed and partially routed to an isobutane recovery step and then to epoxidation reaction system. The second reaction, epoxidation, occurs by mixing the peroxide solution in TBA with propylene. The reaction is carried out in the liquid phase, in the presence of a homogeneous molybdenum catalyst, yielding Propylene Oxide (PO). As in the peroxidation, the heat of epoxidation reaction is removed by the medium vaporization. The epoxidation product is then separated into a distillate stream containing unreacted propylene, propylene oxide and TBA, and a heavy organic stream, comprising high boiling by-products and dissolved molybdenum catalyst. The catalyst-rich stream is submitted to a thermal treatment before being recycled to epoxidation.</p><p>Purification. The distillate from epoxidation reaction system is sent to the propylene column, which strips off propylene, propane and residual light ends from the epoxidation effluent stream. The C3 stream is further treated in a column for recovery of a propylene-rich stream that can be recycled to the epoxidation. The C3-free epoxidation product, in turn, is fed to the TBA recovery, where a crude PO stream is obtained after a TBA-rich stream is separated, treated for impurities removal, and recycled to the epoxidation reaction. The crude PO stream is further purified by means of an extractive distillation process followed by another distillation column, from which high-purity Propylene Oxide is obtained as overheads product.</p><p></p>
ICC - Short Description: 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.
ICC - Main Product: Propylene Oxide
ICC - Plant Capacity: 450.00
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ICC - Images Count: {"versions":{"1":"9","2":"13","3":"22"}}
ICC - Table Count: {"versions":{"1":"22","2":"28","3":"34"}}

Propylene Oxide Production from Propylene and Isobutane

Propylene Oxide Production Costs Report | Issue E | 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

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Labor Requirements

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Production Process Information

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Production Process Information

Process Consumptions

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Plant Capital Cost Summary

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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 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 Hydrogen Peroxide

This report presents the economics of Propylene Oxide (PO) production from polymer grade (PG) propylene and hydrogen peroxide in the United States, similar to the hydrogen peroxide to propylene oxide (HPPO) process jointly developed by Evonik and Uhde.

Details: 450 kta United States-based plant   |   Q3 2024   |   107 pages   |   Issue D   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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Other Related Production Cost Reports

Propylene Glycol from Propylene Oxide

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.

Butanediol Production from Propylene Oxide

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Details: 100 kta United States-based plant   |   Q3 2024   |   107 pages   |   Issue G   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.

Isobutane Production

This report examines the costs incurring from producing Isobutane via catalytic isomerization of n-butane. n-Butane is dehydrogenated to 1-butene, which is then rearranged to isobutylene. Finally, isobutylene is hydrogenated producing isobutane. The economic analysis provided assumes a plant located in the United States.

Details: 850 kta United States-based plant   |   Q3 2024   |   107 pages   |   Issue A   From $999 USD

The cost analyses presented in this report target a 850 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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