Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: A
ICC - Volume: 275
ICC - Report ID: 275-A
ICC - Report Location: United States
ICC - Is Popular: 0
ICC - Is Developed: 1
ICC - Title: Isononanol Production from Octenes (Rhodium Catalyst)
ICC - Show Overview: 1
ICC - Report Location ID: 1
ICC - Plant Capacity Unit ID: 14
ICC - Volume Reports List: 275-B
ICC - Related Reports List: 277-A,246-A,246-C
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/275-A.jpg
ICC - Process Overview Text: <h6>Product</h6> <b>Isononanol</b></p></b></p> <h6>Raw Materials</h6> <p><b>Hydrogen</b></p>, <p><b>Chemicals</b></p>, <p><b>Mixed Octenes</b></p>, <p><b>Synthesis Gas</b></p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/275-A.jpg
ICC - Process Schematic Text: <p>The process under analysis comprises three major sections: (1) Hydroformylation; (2) Hydrogenation; and (3) Purification.</p><p>Hydroformylation. The Hydroformylation is comprised of a series of four water cooled reactors. The first reactor receives mixed octenes from the Feed Tank and rhodium catalyst in form of salt, as well as fresh or recycled pressurized synthesis gas. The effluent of one reactor is cooled down in heat exchangers before being routed to the subsequent reactor, which is also fed with synthesis gas. The octenes react with the carbon monoxide and hydrogen contained in the synthesis gas to form the corresponding aldehydes with chain length of 9 carbons.</p><p>Hydrogenation. The crude product flows to an intermediate vessel, where pressure is reduced and hydrogen and carbon monoxide dissolved in the liquid phase are released. The reaction product is passed through a series of ion exchange resin beds that absorb the rhodium contained in this stream. Then, the spent rhodium salt proceeds to be recovered for the hydroformylation reaction to keep the process economically feasible. The rhodium-free aldehyde-olefin mixture is mixed with pressurized hydrogen. The aldehydes are catalytically hydrogenated in the presence of a copper/zinc catalyst to form the isononyl alcohols with high selectivity.</p><p>Purification. The crude alcohol stream formed is sent to three columns for purification. Light and heavy ends are used as fuel, and aldehydes are recycled to hydrogenation. Finally, the alcohol stream is still passed through a hydrorefining step in the presence of hydrogen and a nickel based catalyst. This step serves to remove trace levels of unsaturation, as well as convert any remaining aldehyde into the corresponding alcohol.</p>
ICC - Short Description: This report presents an economic study of Isononanol production from octenes in the presence of a rhodium catalyst. It assumes a plant located in the United States using a process similar to Johnson Matthey OXO alcohols process. Initially, octenes are submitted to hydroformylation to form the respectives C9 aldehydes. The aldehydes are then hydrogenated to the corresponding C9 alcohols.
ICC - Main Product: Isononanol
ICC - Plant Capacity: 220.00
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Isononanol Production from Octenes (Rhodium Catalyst)

Isononanol Production Costs Report | Issue A | Q3 2024

Production Cost Report

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

This report presents a cost analysis of a 220 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

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Production Costs Datasheet

Plant Capital Cost Details

Operating Cost Details

Plant Cost Breakdowns

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Content Highlights

Plant Capital Cost Summary

Summary outlining the capital cost required for building the Isononanol 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 Isononanol 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 Isononanol 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 Isononanol 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 Isononanol Production Cost Reports

Isononanol Production from Octenes (Cobalt Catalyst)

In this report, the economics of Isononanol production from octenes is analyzed based on a typical cobalt catalyst process, assuming a plant located in the United States. Initially, octenes are submitted to hydroformylation to form the respectives C9 aldehydes. The aldehydes are then hydrogenated to the corresponding C9 alcohols.

Details: 220 kta United States-based plant   |   Q3 2024   |   107 pages   |   Issue B   From $799 USD

The cost analyses presented in this report target a 220 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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Hydrogen Production from Natural Gas (Steam Reforming)

This report provides an economic analysis of Hydrogen production from natural gas in the United States using a steam reforming process. Initially, methane present in natural gas is cracked with steam generating syngas. Then, the carbon monoxide from syngas is reacted with steam, producing carbon dioxide and additional hydrogen.

Details: 1,000 MM Nm3/y United States-based plant   |   Q3 2024   |   107 pages   |   Issue A   From $799 USD

The cost analyses presented in this report target a 1,000 MM Nm3/y (MM Nm3 per year 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.

Hydrogen Production from Natural Gas (Partial Oxidation Process)

This study provides a techno-economic study of Hydrogen production from natural gas in the United States. In this analysis, natural gas is submitted to a thermal partial oxidation process, producing syngas, which is passed through a shift converter to enrich the Hydrogen output.

Details: 25 MM Nm3/y United States-based plant   |   Q3 2024   |   107 pages   |   Issue C   From $799 USD

The cost analyses presented in this report target a 25 MM Nm3/y (MM Nm3 per year 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.

Octenes Production from Butenes

This report presents an economic analysis for the production of Mixed Octenes starting from butenes. In this process, butenes are dimerized to octenes, using an organometalic catalyst. The study concerns a plant based on a process similar to Axens Dimersol-X and located in the United States.

Details: 240 kta United States-based plant   |   Q3 2024   |   107 pages   |   Issue A   From $799 USD

The cost analyses presented in this report target a 240 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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