Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: A
ICC - Volume: 362
ICC - Report ID: 362-A
ICC - Report Location: United States
ICC - Is Popular: 0
ICC - Is Developed: 1
ICC - Title: Butyraldehyde from Propylene and Syngas (N/Iso Ratio of 30:1)
ICC - Show Overview: 1
ICC - Report Location ID: 1
ICC - Plant Capacity Unit ID: 14
ICC - Volume Reports List: 362-B,362-C
ICC - Related Reports List: 017-A,376-A
ICC - Report Location Code: USA
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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/362-A.jpg
ICC - Process Overview Text: <h6>Products</h6> <p><b>n-Butyraldehyde</b></p>, <p><b>Isobutyraldehyde</b></p> <h6>Raw Materials</h6> <p><b>Chemicals</b></p>, <p><b>Synthesis Gas</b></p>, <p><b>CG Propylene</b></p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/362-A.jpg
ICC - Process Schematic Text: <p>The process under analysis comprises the following major sections: (1) hydroformylation; (2) catalyst recovery and (3) purification.</p><p>* Hydroformylation. Fresh propylene and syngas are treated to remove impurities that could poison the rhodium catalyst employed in the hydroformylation reaction. The purified raw materials, recycled reactants and recycled catalyst solution are fed to the first of two reactors operating in series. In both reactors, the propylene reacts with carbon monoxide and hydrogen at mild temperatures and low pressures, and in the presence of a homogeneous rhodium-based catalyst with an organophosphite ligand, yielding n-Butyraldehyde as main product and isobutyraldehyde by-product. The catalyst is dissolved in the high-boiling reaction by-products.</p><p>* Catalyst recovery. The liquid effluent from the hydroformylation, containing catalyst components, reaction products, unreacted propylene, as well as aldehyde products with some dissolved gases, is depressurized and fed to a falling-film evaporator. The concentrated catalyst solution obtained from evaporator is recycled to the hydroformylation area, with a small portion directed to a catalyst regeneration step. The vapor from evaporator is partially condensed and the uncondensed gas is recycled to the reactor through a compressor. The condensed liquid stream is sent to the purification steps.</p><p>* Purification. The condensed liquid stream containing the aldehydes from the catalyst recovery is directed to the first of three distillation columns for the purification of n-Butyraldehyde product. In the first column, the stabilizer column, remaining traces of dissolved gases are removed (propylene, propane, and other inert gases) and recycled to the hydroformylation. The bottom stream from the stabilizer column is fed to a second distillation column, where isobutyraldehyde is separated. In the third column, the heavy-ends column, heavies impurities are separated from the n-Butyraldehyde product (with 99 wt% purity), which is finally routed to storage facilities located outside battery limits.</p>
ICC - Short Description: This report presents an economic analysis of n-Butyraldehyde production from propylene and syngas, assuming a plant located in the United States. The process under analysis is a propylene hydroformylation similar to the LP OXO technology jointly licensed by JM Davy and Dow, employing Selector 30 catalyst. The production ratio of n- to iso-butyraldehyde is about 30.
ICC - Main Product: Butyraldehyde
ICC - Plant Capacity: 160.00
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Butyraldehyde from Propylene and Syngas (N/Iso Ratio of 30:1)

Butyraldehyde Production Costs Report | Issue A | Q3 2024

Production Cost Report

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

This report presents a cost analysis of a 160 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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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 Butyraldehyde 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 Butyraldehyde 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 Butyraldehyde 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 Butyraldehyde 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 Butyraldehyde Production Cost Reports

Butyraldehyde from Propylene and Syngas (N/Iso Ratio of 10:1)

This feasibility study approaches n-Butyraldehyde production from propylene and syngas, assuming a plant located in the United States. The process under analysis is a propylene hydroformylation similar to the LP OXO technology jointly developed by JM Davy and Union Carbide, employing Selector 10 catalyst. The production ratio of n- to iso-butyraldehyde is about 10.

Details: 160 kta United States-based plant   |   Q3 2024   |   107 pages   |   Issue B   From $799 USD

The cost analyses presented in this report target a 160 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.

Butyraldehyde from Propylene and Syngas (N/Iso Ratio of 4:1)

This report concerns the costs associated with the production of n-Butyraldehyde from propylene and syngas. The process under analysis is a propylene hydroformylation similar to the technology jointly developed by Rhodia (former Rhône-Poulenc) and Ruhrchemie. The economic analysis presented assumes a plant located in the United States.

Details: 160 kta United States-based plant   |   Q3 2024   |   107 pages   |   Issue C   From $799 USD

The cost analyses presented in this report target a 160 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

Trimethylolpropane Production

This report presents the economics of Trimethylolpropane (TMP) production from formaldehyde and n-butyraldehyde, assuming a plant located in the United States. In the process analyzed, formaldehyde and n-butyraldehyde go through an aldol condensation and a cross-Cannizaro reaction to form Trimethylolpropane, using 2,2-bis(hydroxymethyl)butanal as intermediate.

Details: 20 kta United States-based plant   |   Q3 2024   |   107 pages   |   Issue A   From $1,199 USD

The cost analyses presented in this report target a 20 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.

2-Ethylhexanoic Acid Production from Butyraldehyde

This report presents the economics of 2-Ethylhexanoic Acid production from Butyraldehyde in the United States. In this process, n-butyraldehyde undergoes an aldol condensation reaction yielding 2-ethylhexenal, which is then hydrogenated to form 2-ethylhexanal. The aldehyde is subsequently subjected to an oxidation reaction to produce the 2-Ethylhexanoic Acid.

Details: 60 kta United States-based plant   |   Q3 2024   |   107 pages   |   Issue A   From $1,999 USD

The cost analyses presented in this report target a 60 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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