Commodity Production Costs Report
Toluene Production from Pygas
Toluene Operating Costs & Plant Construction Costs
This study presents the economics of Toluene production from pyrolysis gasoline (pygas) in the United States using a typical liquid-liquid extraction process.
The report provides a comprehensive study of Toluene production and related Toluene production cost, covering three key aspects: a complete description of the Toluene production process examined; an in-depth analysis of the related Toluene plant capital cost (Capex); and an evaluation of the respective Toluene plant operating costs (Opex).
The Toluene 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 Toluene 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 Toluene 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): ?
Products
Toluene, Benzene, Mixed Xylenes, Crude C5s.
Raw Material
Pyrolysis Gasoline.
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Up-to-date Report
Professional report based on Q3 2024 economic data, ensuring timely evaluations.
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Ideal for investment screening, feasibility studies, cost estimates, and research planning.
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Developed using a consistent methodology honed over a decade, ensuring reliable cost analyses.
Report Editions
Content Highlights
Plant Capital Cost Summary
Summary outlining the capital cost required for building the Toluene 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 Toluene 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 Toluene 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 Toluene 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 Toluene Production Cost Reports
Toluene Production from Reformate
This report presents the economics of Toluene production from reformate. The reformate is submitted to a typical sulfolane liquid-liquid extraction, giving a mixture of aromatics, which is further processed to yield pure Toluene. Benzene and mixed xylenes are produced as by-products. The economic analysis presented is based on a plant constructed in the United States.
Details: 350 kta United States-based plant | Q3 2024 | 107 pages | Issue A | From $799 USD
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Other Related Production Cost Reports
Ethylene Propylene Rubber Production
This report analyses the economics of Ethylene Propylene Diene Rubber (EPDM rubber) production from ethylene and propylene in the United States, via a suspension polymerization process using Ziegler-Natta catalyst. Ethylidene norbornene is also used as termonomer to allow vulcanization of the polymer.
Details: 100 kta United States-based plant | Q3 2024 | 107 pages | Issue A | From $799 USD
Toluene Diisocyanate from Toluene (Liquid-Phase Phosgenation)
This report presents the economics of a typical liquid-phase phosgenation process for Toluene Diisocyanate (TDI) production from toluene and chlorine in the USA. Initially, toluene is submitted to a dinitration to produce dinitrotoluene (DNT), which is then hydrogenated to toluenediamine (TDA). This TDA is reacted with phosgene in liquid phase to yield TDI product. The phosgene used is generated from chlorine in an on-site unit.
Details: 220 kta United States-based plant | Q3 2024 | 107 pages | Issue D | From $1,499 USD
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