Maleic Anhydride Production from Benzene
Maleic Anhydride Production Costs Report | Issue D | Q4 2024
Report Details |
80 kta United States-based plant | Q4 2024 | 107 pages |
This report presents a cost analysis of a 80 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.
Report Abstract
This study provides a techno-economic analysis of a process for Maleic Anhydride production from benzene in the United States. This process highlights a benzene oxidation to maleic anhydride in a fixed-bed reactor combined with an aqueous-based recovery system.
The report provides a comprehensive study of Maleic Anhydride production and related Maleic Anhydride production cost, covering three key aspects: a complete description of the Maleic Anhydride production process examined; an in-depth analysis of the related Maleic Anhydride plant capital cost (Capex); and an evaluation of the respective Maleic Anhydride plant operating costs (Opex).
The Maleic Anhydride 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 Maleic Anhydride 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 Maleic Anhydride plant operating costs analysis covers operating expenses, including variable costs like raw materials and utilities, and fixed costs such as maintenance, labor, and depreciation.
Process Overview

Product
Maleic Anhydride. Maleic anhydride is a multifunctional chemical intermediate which find application in many fields of industrial chemistry. It is an important raw material used in the manufacture of polyester resins, lubricant additives, plasticizers, surface coatings, copolymers, and agricultural chemicals. It is produced by vapor-phase oxidation of n-butane (most common route) or benzene.
Raw Material
Benzene. Benzene (C6H6) is a flammable and volatile liquid. As the most simple aromatic hydrocarbon, it is used as an intermediate to produce many important chemicals, such as styrene (raw material for polystyrene and synthetic rubber), cyclohexane (used in nylon production), alkylbenzenes (used in detergent industry), aniline (used to produce dyes and polyurethanes), and chlorobenzenes. Also, benzene is used to produce pharmaceuticals, specialty chemicals, plastics, and pesticides. It occurs naturally in crude oil and coal tar.
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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
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Content Highlights
Plant Capital Cost Summary
Summary outlining the capital cost required for building the Maleic Anhydride 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 Maleic Anhydride 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 Maleic Anhydride 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 Maleic Anhydride 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 Maleic Anhydride Production Cost Reports
Maleic Anhydride from Butane (Fixed-Bed Reactor + Solvent-Based Recovery)
This feasibility study presents an analysis of Maleic Anhydride production from n-butane in the United States using a process similar to the one developed by Huntsman. In this process, maleic anhydride is produced by the partial oxidation reaction of n-butane with oxygen carried out in a fixed-bed reactor, using a vanadium–phosphorus oxide (VPO) catalyst supported on silica. The reactor effluent is directed to a solvent-based recovery system for Maleic Anhydride separation.
Details: 60 kta United States-based plant | Q4 2024 | 107 pages | Issue A From $799 USD
The cost analyses presented in this report target a 60 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.
Maleic Anhydride from Butane (Two Fixed-Bed Reactors + Aqueous-Based Recovery)
This study presents an economic analysis of Maleic Anhydride production from n-butane in the United States using a process similar to the one developed by Scientific Design. In this process, Maleic Anhydride is produced by the partial oxidation reaction of n-butane with oxygen carried out in two fixed-bed reactors, using vanadium–phosphorus oxide (VPO) catalyst supported on silica. The Maleic Anhydride formed is recovered in an aqueous-based system.
Details: 50 kta United States-based plant | Q4 2024 | 107 pages | Issue B From $799 USD
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.
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Butanediol Production from Maleic Anhydride
This report presents an economic analysis of 1,4-Butanediol (BDO) production from maleic anhydride in the United States using a process similar to the one proposed by JM Davy. Initially, maleic anhydride is reacted with methanol to produce dimethyl maleate (DMM). The DMM is then hydrogenated to BDO.
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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.
Benzene Production from Pygas (Extractive Distillation Process)
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The cost analyses presented in this report target a 250 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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This analysis presents the economics of Benzene production from pyrolysis gasoline (pygas) in the United States using a typical hydrodealkylation process. Initially, pygas is fractionated into 3 hydrocarbon cuts. The C6-C8 fraction is then directed to the hydrodealkylation step, in which the aromatics content in the process stream are converted into benzene
Details: 250 kta United States-based plant | Q4 2024 | 107 pages | Issue D From $799 USD
The cost analyses presented in this report target a 250 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.
Succinic Acid Production from Maleic Anhydride
This report analyses the economics of a Succinic Acid production from maleic anhydride. In this process, maleic anhydride is first hydrogenated to produce succinic anhydride, which is then hydrated to produce Succinic Acid. The economic analysis presented is based on a plant constructed in the United States.
Details: 30 kta United States-based plant | Q4 2024 | 107 pages | Issue J From $1,199 USD
The cost analyses presented in this report target a 30 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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