Production Cost Report
ICC - Is Bespoken: 0
ICC - Main References: ?
ICC - Issue: A
ICC - Volume: 224
ICC - Report ID: 224-A
ICC - Report Location: United States
ICC - Is Popular: 0
ICC - Is Developed: 1
ICC - Title: Polybutylene Terephthalate Production
ICC - Show Overview: 1
ICC - Report Location ID: 1
ICC - Plant Capacity Unit ID: 14
ICC - Related Reports List: 027-A,027-B,050-A,050-B
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/224-A.jpg
ICC - Process Overview Text: <h6>Products</h6> <p><b>Polybutylene Terephthalate</b></p>, <p><b>Methanol</b></p>, <p><b>Tetrahydrofuran</b></p> <h6>Raw Materials</h6> <p><b>Chemicals</b></p>, <p><b>Butanediol</b></p>, <p><b>Dimethyl Terephthalate</b></p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/224-A.jpg
ICC - Process Schematic Text: <p>The process under analysis comprises two major sections: (1) Polymerization and (2) Recovery System.</p><p>Polymerization. Dimethyl terephthalate and butanediol (BDO) are mixed in the Paste System and, together with the catalyst, are fed into the Tower Reactor, in the Esterification section. The product from esterification and recovered BDO are fed into another section of the Tower Reactor, where post-esterification and pre-polymerization processes occur, through cascade reaction cups. The resulting pre-polymer is led to the Polycondensation reactor, where the catalyst and other additives are fed. Monomers, oligomers, and short-chain polymers are condensed in order to form long-chain Polybutylene Terephthalate (PBT), releasing BDO, recovered in a distillation column (BDO Recovery). All the light unreacted reagents and side products of esterification and polycondensation – mainly methanol, tetrahydrofuran (THF), and water – are sent to THF Recovery. After polymerization, PBT is sent to Finishing steps, in which it is pelletized, homogenized, and packed. </p><p>Recovery System. Products and unreacted reagents from polymerization are directed to a light-ends column present in the THF Recovery system. The light gas from the top of the column, containing THF, water, and methanol, passes through a second column operating at a higher pressure. Thanks to the change in pressure, the azeotrope properties are shifted, and high-purity THF is obtained as a bottom by-product. The new azeotrope is recycled to the first column of THF Recovery. At the bottom of this first column, methanol, BDO, and water are stripped off and directed to the BDO Recovery column, where BDO is recovered at the bottom. Finally, methanol is separated from water in the Methanol Purification column as an overhead product. Water and impurities leave the system as wastewater.</p>
ICC - Short Description: This report presents the economics of Polybutylene Terephthalate (PBT) production from dimethyl terephthalate (DMT) in the United States, via a typical transesterification/polycondensation process. In this process, DMT is transesterified with 1,4-butanediol followed by polycondensation, yielding PBT.
ICC - Main Product: Polybutylene Terephthalate
ICC - Plant Capacity: 65.00
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Polybutylene Terephthalate Production

Polybutylene Terephthalate Production Costs Report | Issue A | Q4 2024

Production Cost Report

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65 kta United States-based plant   |   Q4 2024   |   107 pages

This report presents a cost analysis of a 65 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

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Operating Cost Details

Plant Cost Breakdowns

Plant Capacity Assessment

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Content Highlights

Plant Capital Cost Summary

Summary outlining the capital cost required for building the Polybutylene Terephthalate 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 Polybutylene Terephthalate 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 Polybutylene Terephthalate 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 Polybutylene Terephthalate 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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Bio-Butanediol Production from Glucose (Direct Fermentation)

This report presents the economics of bio-based 1,4-Butanediol (BDO) production from glucose syrup in a plant located in the United States. This process, similar to the one proposed by Genomatica, consists in a direct fermentation of glucose syrup, producing BDO, which is then submitted to purifying steps.

Details: 75 kta United States-based plant   |   Q4 2024   |   107 pages   |   Issue A   From $799 USD

The cost analyses presented in this report target a 75 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.

Bio-Butanediol from Glucose (Succinic Acid as Intermediate)

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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.

Dimethyl Terephthalate from p-Xylene and Methanol

This report examines the costs related to Dimethyl Terephthalate (DMT) production from p-xylene and methanol in the United States, via typical oxidation and esterification processes. In this process, operations theoretically take place in alternate oxidation and esterification (with methanol) phases. P-xylene is oxidized to p-toluic acid, which is converted to p-methyl toluate, then to methyl terephthalate and ,finally, to DMT.

Details: 100 kta United States-based plant   |   Q4 2024   |   107 pages   |   Issue A   From $1,199 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.

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It presents the economics of Dimethyl Terephthalate (DMT) production from toluene and methanol in a plant located in the United States. Toluene is converted to p-xylene via a catalytic disproportionation process similar to ExxonMobil PxMax. The p-xylene is oxidized to p-toluic acid, which is esterified with methanol to generate DMT.

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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.

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