Commodity Production Costs Report
Bio-Paraxylene Production from Glucose (Fermentation Process)
p-Xylene Operating Costs & Plant Construction Costs
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.
The report provides a comprehensive study of p-Xylene production and related p-Xylene production cost, covering three key aspects: a complete description of the p-Xylene production process examined; an in-depth analysis of the related p-Xylene plant capital cost (Capex); and an evaluation of the respective p-Xylene plant operating costs (Opex).
The p-Xylene production process description includes a block flow diagram (BFD), an overview of the industrial site installations, detailing both the process unit and the necessary infrastructure, process consumption figures and comprehensive process flow diagrams (PFD). The p-Xylene plant capital cost analysis breaks down the Capex by plant cost (i.e., ISBL, OSBL and Contingency); owner's cost; working capital; and costs incurred during industrial plant commissioning and start-up. The p-Xylene plant operating costs analysis covers operating expenses, including variable costs like raw materials and utilities, and fixed costs such as maintenance, labor, and depreciation.
Key reference(s): ?
Product
Paraxylene. 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 p-Xylene separation.
Raw Material
Glucose Syrup. 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.
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Professional report based on Q3 2024 economic data, ensuring timely evaluations.
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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
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Other p-Xylene Production Cost Reports
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: 1100 kta United States-based plant | Q3 2024 | 107 pages | Issue C | From $799 USD
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: 1100 kta United States-based plant | Q3 2024 | 107 pages | Issue D | From $799 USD
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 | Q3 2024 | 107 pages | Issue E | From $799 USD
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Other Related Production Cost Reports
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 | Q3 2024 | 107 pages | Issue C | From $799 USD
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 | Q3 2024 | 107 pages | Issue B | From $799 USD
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 | Q3 2024 | 107 pages | Issue A | From $799 USD
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