Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: A
ICC - Volume: 17
ICC - Report ID: 017-A
ICC - Report Location: United States
ICC - Is Popular: 0
ICC - Is Developed: 1
ICC - Title: Trimethylolpropane Production
ICC - Show Overview: 1
ICC - Report Location ID: 1
ICC - Plant Capacity Unit ID: 14
ICC - Volume Reports List: 017-A
ICC - Related Reports List: 110-B,110-A,214-E,174-B,174-A,362-A
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/017-A.jpg
ICC - Process Overview Text: <h6>Products</h6> <p><b>Trimethylolpropane</b></p>, <p><b>Sodium Formate</b></p> <h6>Raw Materials</h6> <p><b>Chemicals</b></p>, <p><b>Formalin</b></p>, <p><b>Caustic Soda</b></p>, <p><b>Formic Acid</b></p>, <p><b>n-Butyraldehyde</b></p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/017-A.jpg
ICC - Process Schematic Text: <p>The process under analysis comprises four major sections: (1) reaction; (2) TMP separation ; (3) TMP purification; and (4) sodium formate recovery.</p><p>* Reaction. Initially, fresh and recycled aqueous solution of formaldehyde, n-butyraldehyde and the sodium hydroxide catalyst solution are fed to a reactor to produce Trimethylolpropane and sodium formate. The output from the reactor is subsequently mixed with formic acid to neutralize the excess of sodium hydroxide used in the reaction. </p><p>* TMP separation. The neutralized solution is then fed to a stripper column wherein excess of formaldehyde fed in the reaction is recovered and recycled to the reactor. The solution, containing the TMP product is then concentrated by evaporation and sent to an extraction column where TMP is separated from sodium formate by-product by means of extraction with ethyl acetate.</p><p>* TMP purification. The purification section consists of two distillation columns for the removal of light-end impurities and heavy-end impurities. Purified TMP melt is converted into flakes and finally packed.</p><p>* Sodium formate recovery. The aqueous sodium formate stream separated from TMP is passed through evaporation, crystallization, centrifugation and drying steps for obtaining sodium formate as by-product. </p>
ICC - Short Description: 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.
ICC - Main Product: Trimethylolpropane
ICC - Plant Capacity: 20.00
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ICC - Images Count: {"versions":{"1":"9","2":"13","3":"22"}}
ICC - Table Count: {"versions":{"1":"22","2":"28","3":"34"}}

Trimethylolpropane Production

Trimethylolpropane Production Costs Report | Issue A | Q3 2024

Production Cost Report

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

This report presents a cost analysis of a 20 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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Plant Capital Cost Summary

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Production Costs Datasheet

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Operating Cost Details

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Content Highlights

Plant Capital Cost Summary

Summary outlining the capital cost required for building the Trimethylolpropane 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 Trimethylolpropane 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 Trimethylolpropane 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 Trimethylolpropane 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 Trimethylolpropane 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.

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

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Sodium Hydroxide Production from Sodium Chloride (Diaphragm Process)

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TMP-Propylene Oxide Polyether Production

This report presents the economics of TMP-Propylene Oxide Polyether production in the United States. In this process, Polyether is produced from propylene oxide using trimethylolpropane (TMP) as starter in the base-catalyzed alkoxylation reaction.

Details: 50 kta United States-based plant   |   Q3 2024   |   107 pages   |   Issue E   From $799 USD

The cost analyses presented in this report target a 50 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 30:1)

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.

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