Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: A
ICC - Volume: 287
ICC - Report ID: 287-A
ICC - Report Location: United States
ICC - Is Popular: 0
ICC - Is Developed: 1
ICC - Title: Neopentyl Glycol Production
ICC - Show Overview: 1
ICC - Report Location ID: 1
ICC - Plant Capacity Unit ID: 14
ICC - Related Reports List: 174-A,246-C,246-A,174-B
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":"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/287-A.jpg
ICC - Process Overview Text: <h6>Product</h6> <b>Neopentyl Glycol</b></p></b></p> <h6>Raw Materials</h6> <p><b>Hydrogen</b></p>, <p><b>Chemicals</b></p>, <p><b>Formalin</b></p>, <p><b>Isobutyraldehyde</b></p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/287-A.jpg
ICC - Process Schematic Text: <p>The process under analysis comprises three major sections: (1) Aldol Condensation; (2) Hydrogenation; and (3) Purification.</p><p>Aldol Condensation. An aldol reactor is fed with an aqueous solution of formaldehyde, isobutyraldehyde and triethylamine. In such reactor, an aldol condensation reaction between isobutyraldehyde and formaldehyde is carried out in the presence of triethylamine catalysts. The output from the aldol condensation reactor, containing crude hydroxypivaldehyde, is submitted to extraction with octanol and distillation for the recovery of a purified hydroxypivaldehyde. </p><p>Hydrogenation. The purified hydroxypivaldehyde is fed to a loop-type reactor, along with hydrogen gas. There, a reaction between hydroxypivaldehyde and hydrogen takes place, in the presence of Raney nickel catalysts. Such hydrogenation reaction yields a mixture containing crude Neopentyl Glycol, which is then submitted to a saponification step. In the saponification, the hydrogenation product is mixed with caustic soda, in such a way that the precursors still present in the stream are converted to Neopentyl Glycol.</p><p>Purification. In this section, the stream rich in Neopentyl Glycol and a stream containing residual NPG content are fed to an extractor. Water is used as solvent for Neopentyl Glycol removal. The aqueous phase from the extraction is fed to a distillation column, which further separates a mixture of Neopentyl Glycol and water from salt impurities. The Neopentyl Glycol and water mixture is fed to the last column, which further purifies the NPG. High-purity Neopentyl Glycol withdrawn from column bottom is routed to a finishing step and stored. </p><p></p>
ICC - Short Description: This report presents the economics of Neopentyl Glycol production from isobutyraldehyde, formaldehyde and hydrogen, assuming a conventional industrial process, located in the United States. In this process, formaldehyde and isobutyraldehyde are reacted via aldol condensation to form hydroxypivaldehyde, which is then converted to Neopentyl Glycol via catalytic hydrogenation.
ICC - Main Product: Neopentyl Glycol
ICC - Plant Capacity: 60.00
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ICC - Table Count: {"versions":{"1":"22","2":"28","3":"34"}}

Neopentyl Glycol Production

Neopentyl Glycol Production Costs Report | Issue A | Q2 2024

Production Cost Report

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60 kta United States-based plant   |   Q2 2024   |   107 pages

This report presents a cost analysis of a 60 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

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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

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Content Highlights

Plant Capital Cost Summary

Summary outlining the capital cost required for building the Neopentyl Glycol 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 Neopentyl Glycol 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 Neopentyl Glycol 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 Neopentyl Glycol 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

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