Commodity Production Costs Report
Bio-Paraxylene Production from Glucose (Catalytic Process)
p-Xylene Operating Costs & Plant Construction Costs
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.
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 Materials
Ethylene. Ethylene is known as a key building block for the petrochemical industry, being one of the largest-volume petrochemical produced worldwide. It is widely used as chemical intermediate in the production of several end products, including plastics, resins and fibers. Ethylene is largely produced by thermal cracking of petroleum-based feedstocks, in the presence of steam. It is stored in a liquid state under high pressure or at low temperatures. However, ethylene is, most of times, directly supplied to its consumers.
Hydrogen. The hydrogen molecule, H2, is the normal state of pure hydrogen, even though hydrogen can be found in its atomic form under specific conditions. It is a very stable molecule, not usually reactive under normal conditions. Essentially, molecular hydrogen is produced industrially by three different methods: hydrocarbons steam reforming, hydrocarbons partial oxidation and water electrolysis. Hydrogen can also be obtained as a by-product recovered in processes such as the manufacture of styrene from ethylbenzene.
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
Ethylene Production from Ethane
This report presents the economics of Polymer Grade (PG) Ethylene production from ethane in the United States. In the process under analysis, ethane is thermally cracked in pyrolysis furnaces through the use of steam, yielding Ethylene. A hydrogen-rich gas is generated as by-product.
Details: 1200 kta United States-based plant | Q3 2024 | 107 pages | Issue B | From $799 USD
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
Hydrogen Production from Natural Gas (Partial Oxidation Process)
This study provides a techno-economic study of Hydrogen production from natural gas in the United States. In this analysis, natural gas is submitted to a thermal partial oxidation process, producing syngas, which is passed through a shift converter to enrich the Hydrogen output.
Details: 25 MM Nm3/y United States-based plant | Q3 2024 | 107 pages | Issue C | From $799 USD
Ethylene Production from Naphtha (Low Severity Steam Cracking)
This report presents the economics of a naphtha-based steam cracker, equipped with an electricity cogeneration unit. In this process, naphtha is thermally cracked at low severity conditions, maximizing propylene to Ethylene ratio. The analysis is based on a plant located in Germany.
Details: 800 kta Germany-based plant | Q3 2024 | 107 pages | Issue A | 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
Hydrogen Production from Natural Gas (Steam Reforming)
This report provides an economic analysis of Hydrogen production from natural gas in the United States using a steam reforming process. Initially, methane present in natural gas is cracked with steam generating syngas. Then, the carbon monoxide from syngas is reacted with steam, producing carbon dioxide and additional hydrogen.
Details: 1000 MM Nm3/y United States-based plant | Q3 2024 | 107 pages | Issue A | 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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