Production Cost Report
ICC - Is Bespoken: 0
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ICC - Issue: L
ICC - Volume: 35
ICC - Report ID: 035-L
ICC - Report Location: United States
ICC - Is Popular: 0
ICC - Is Developed: 0
ICC - Title: Bio-Paraxylene Production from Glucose (Fermentation Process)
ICC - Show Overview: 1
ICC - Report Location ID: 1
ICC - Plant Capacity Unit ID: 14
ICC - Volume Reports List: 035-A,035-B,035-C,035-D,035-E,035-F,035-G,035-H,035-I,035-J,035-K,035-L
ICC - Related Reports List: 370-A,044-B,044-C
ICC - Report Location Code: USA
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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/035-L.jpg
ICC - Process Overview Text: <h6>Product</h6> <p><b>Paraxylene</b>. p-Xylene, or paraxylene is the most important commercial isomer among the xylenes group. Almost all of its production is converted to Terephthalic Acid and dimethyl terephthalate. p-Xylene is primarily manufactured by naphtha catalytic reforming, followed by separation of the xylenes isomers, crystallization or absorption for pxylene separation.</p> <h6>Raw Material</h6> <p><b>Glucose Syrup</b>. Glucose (C6H12O6), also known as D-glucose and dextrose, is the most abundant sugar in nature. Commercial glucose products are available in both dry and syrup forms in a variety of purities and concentrations. Glucose uses include pharmaceuticals, food, chemicals and fuels. This compound is used as raw material in fermentative processes for the production of vitamins, organic acids, antibiotics, amino acids, enzymes, and polysaccharides.</p>
ICC - Process Schematic Image: //cdn.intratec.us/images/icc/process-schematics/035-L.jpg
ICC - Short Description: This study approaches an economic analysis of p-Xylene production from glucose syrup in the United States. In this process, glucose is fermented to isobutanol intermediate, which is then converted to p-Xylene through dehydration, dimerization and dehydrocyclization.
ICC - Main Product: p-Xylene
ICC - Plant Capacity: 100.00
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Bio-Paraxylene Production from Glucose (Fermentation Process)

p-Xylene Production Costs Report | Issue L | Q2 2024

Production Cost Report

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100 kta United States-based plant   |   Q2 2024   |   107 pages   |   Delivered in PDF

This report presents a cost analysis of a 100 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

Labor Requirements

Plant Capital Cost Summary

Operating Cost Summary

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

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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

Costs in Different Countries Add-on

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Content Highlights

Plant Capital Cost Summary

Summary outlining the capital cost required for building the p-Xylene 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 p-Xylene 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 p-Xylene 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 p-Xylene 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 p-Xylene Production Cost Reports

Bio-Paraxylene Production from Raw Sugar

This report provides an economics of p-Xylene production from raw sugar (sucrose) considering a plant located in Germany. Initially, sucrose is hydrolyzed into glucose and fructose, which are converted to sorbitol. Sorbitol is then reacted in condensation section forming p-Xylene.

Details: 180 kta Germany-based plant   |   Q2 2024   |   107 pages   |   Issue A   From $1,199 USD

The cost analyses presented in this report target a 180 kta (kilo metric ton per annum per annum) Germany-based plant. For those interested in cost analyses considering other plant capacities and/or locations, Intratec offers a customized analysis as an optional feature.

Paraxylene from Mixed Xylenes (Only Adsorption and Isomerization)

This report examines the costs related to a typical process for p-Xylene production from mixed xylenes via adsorption and isomerization in the United States. The remaining xylenes as well as the ethylbenzene are isomerized and recycled to the adsorption unit.

Details: 1,100 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue B   From $799 USD

The cost analyses presented in this report target a 1,100 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.

Paraxylene from Mixed Xylenes (Ethylbenzene Dealkylation)

It presents the economics of a process for p-Xylene production from mixed xylenes in the United States, via isomerization followed by ethylbenzene (EB) dealkylation. In this process, a mixture of C8 aromatics is sent to an adsorption unit for the recovery of p-Xylene. The remaining xylenes are isomerized to equilibrium and the EB is dealkylated to benzene by-product.

Details: 1,100 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue C   From $799 USD

The cost analyses presented in this report target a 1,100 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.

Paraxylene from Mixed Xylenes (P-Xylene Crystallization)

This report analyses the economics of a process for p-Xylene production from mixed xylenes in the United States. In this process, a mixture of C8 aromatics is sent to a crystallization recovery unit for p-Xylene separation. The remaining xylenes are isomerized to equilibrium and the EB is dealkylated to benzene by-product.

Details: 1,100 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue D   From $799 USD

The cost analyses presented in this report target a 1,100 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.

Paraxylene from Mixed Xylenes (O-Xylene Recovery)

It presents the economics of a typical process for p-Xylene production from mixed xylenes in the United States. In this process, o-xylene is also generated as by-product.

Details: 600 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue E   From $799 USD

The cost analyses presented in this report target a 600 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.

Paraxylene from Toluene (STDP with Pentasil Zeolite Catalyst)

This report examines the costs related to a process for p-Xylene production from toluene in the United States. In this study, p-Xylene is produced via a selective toluene disproportionation process. High-purity benzene is also obtained as by-product.

Details: 400 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue F   From $799 USD

The cost analyses presented in this report target a 400 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.

Paraxylene from Toluene (STDP with Aluminosilicate Zeolite Catalyst)

This study presents the economics of a toluene disproportionation process similar to PxMax developed by ExxonMobil for p-Xylene production in the United States.

Details: 450 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue G   From $799 USD

The cost analyses presented in this report target a 450 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.

Paraxylene from Toluene (Conventional TDP)

This report presents the economics of p-Xylene production from toluene in the United States. In this study, p-Xylene is generated via a typical toluene disproportionation process (TDP).

Details: 450 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue H   From $1,199 USD

The cost analyses presented in this report target a 450 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.

Paraxylene from Toluene and C9 Aromatics (TDP and Transalkylation)

This report examines the costs of a typical disproportionation and transalkylation process for p-Xylene production from toluene and C9 aromatics in the United States. Benzene is obtained as by-product.

Details: 450 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue I   From $1,199 USD

The cost analyses presented in this report target a 450 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.

Paraxylene from Toluene and C9 Aromatics (Transalkylation)

This report presents the economics of a typical transalkylation process for p-Xylene production from Toluene and C9 aromatics in the United States.

Details: 450 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue J   From $1,199 USD

The cost analyses presented in this report target a 450 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-Paraxylene Production from Glucose (Catalytic Process)

This report examines the costs of p-Xylene production from glucose syrup in the United States. Initially, glucose is converted to hydroxymethylfurfural (HMF), which reacts with hydrogen to produce dimethylfuran (DMF). Finally, DMF reacts with ethylene using hexane as a solvent, yielding paraxylene.

Details: 200 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue K   From $999 USD

The cost analyses presented in this report target a 200 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-Paraxylene Production from Glucose (Fermentation Process)

This study approaches an economic analysis of p-Xylene production from glucose syrup in the United States. In this process, glucose is fermented to isobutanol intermediate, which is then converted to p-Xylene through dehydration, dimerization and dehydrocyclization.

Details: 100 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue L   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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Other Related Production Cost Reports

Purified Terephthalic Acid from p-Xylene (Conventional Process)

This study presents the economics of Purified Terephthalic Acid (PTA) production using p-xylene as the process feedstock. The study approaches the construction of a plant in the United States employing a conventional catalytic oxidation process. In this process, p-xylene is oxidized to terephthalic acid (TPA). The TPA is subjected to separation and drying steps, and then sent to hydrogenation to obtain PTA as the final product.

Details: 700 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue B   From $799 USD

The cost analyses presented in this report target a 700 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.

Purified Terephthalic Acid from p-Xylene (BP Technology)

This assessment presents the economics of Purified Terephthalic Acid (PTA) production from p-xylene. The economic analysis is based in a plant located in the United States. The process examined in this report is similar to BP X Technology. In this process, p-xylene is oxidized to terephthalic acid, which is hydrogenated to obtain PTA. Drying and storage of crude terephthalic acid is not necessary.

Details: 700 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue C   From $799 USD

The cost analyses presented in this report target a 700 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.

Glucose Syrup Production

This report presents the economics of Glucose Syrup production from shelled corn. In this process, shelled corn is passed through a wet milling process to recover the corn starch, which, in turn, passes through two subsequent hydrolysis steps for the generation of glucose. The economic analysis performed assumes a plant located in the United States.

Details: 40 kta United States-based plant   |   Q2 2024   |   107 pages   |   Issue A   From $799 USD

The cost analyses presented in this report target a 40 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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