Benzene Production from Light Oil
Benzene Production Costs Report | Issue E | Q2 2024
Report Details |
200 kta United States-based plant | Q2 2024 | 107 pages | Delivered in PDF |
This report presents a cost analysis of a 200 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 shows a techno-economic analysis of Benzene production from light oil using a hydrodealkylation process similar to Lummus Litol technology. The light oil feedstock used is a product from coal coking process. A C6-C8 fraction is separated. Then, diolefins and styrene are hydrogenated. The effluent is finally converted to benzene by hydrodealkylation. The plant is assumed to be located in the United States.
The report provides a comprehensive study of Benzene production and related Benzene production cost, covering three key aspects: a complete description of the Benzene production process examined; an in-depth analysis of the related Benzene plant capital cost (Capex); and an evaluation of the respective Benzene plant operating costs (Opex).
The Benzene 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 Benzene 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 Benzene 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 Schematic
The process under analysis comprises three major sections: (1) Purification; (2) Reactions; and (3) Hydrogen Treatment.
Reactions. Initially, the coke-oven light oil is fractionated for the removal of C5- and C9+ fractions from the feedstock. The feed is then combined with recycled (unconverted) aromatics, forming a mixture that is vaporized with hot hydrogen and fed to a pre-treatment reactor. In the pre-treatment reactor, diolefins, cyclic diolefins, and styrene are selectively hydrogenated in the presence of a catalyst (cobalt molybdate on alumina), and a portion of thiophene and other sulfur compounds are converted to H2S. The hydrogenated effluent from the pre-treatment reactor is heated and subsequently fed to the fixed-bed reactors, where hydrocracking, dehydrogenation, and dealkylation reactions are carried out in the presence of chromia-alumina catalyst. Dealkylation reactions are exothermic, so the reaction temperature is controlled by recycling cold hydrogen between reactors.
Purification. The resulting effluent from the Dealkylation reactors is cooled and fed to a flash drum for the recovery of hydrogen. The liquid outlet is stabilized, clay treated, and then fractionated to obtain a finished benzene product.
Hydrogen Treatment. The gaseous stream from the flash drum is fed to the bottom of a multi-stage absorber column to remove residual hydrocarbons from the hydrogen-rich feed stream, avoiding the build-up of impurities in the process. The washed hydrogen-rich gas is mixed with a reformer-grade hydrogen makeup stream and then compressed and heated before being mixed with the feed mixture.
Up-to-date PDF Report
Professional report based on Q2 2024 economic data, ensuring timely evaluations.
Multiple Use Cases
Ideal for investment screening, feasibility studies, cost estimates, and research planning.
Proven Methodology
Developed using a consistent methodology honed over a decade, ensuring reliable cost analyses.
Compact
$799 USD
Production Process Information
Process Consumptions
Labor Requirements
Plant Capital Cost Summary
Operating Cost Summary
Production Costs Datasheet
Pages | Tables | Images
Read-only Online PDF Format
Updated with Q2 2024 Data
DETAILED
$1,599 USD
Production Process Information
Process Consumptions
Labor Requirements
Plant Capital Cost Summary
Operating Cost Summary
Production Costs Datasheet
Plant Capital Cost Details
Operating Cost Details
Pages | Tables | Images
Downloadable PDF Format
Updated with Q2 2024 Data
PREMIUM
MOST POPULAR
$2,699 USD
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
Pages | Tables | Images
Print-enabled PDF Format Add-on
Updated with Q2 2024 Data
Share with Co-workers
Technical Support via Email
Content Highlights
Plant Capital Cost Summary
Summary outlining the capital cost required for building the Benzene 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 Benzene 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 Benzene 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 Benzene 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 Benzene Production Cost Reports
Benzene Production from Reformate
This report presents the economics of Benzene production from reformate in the United States using a typical sulfolane liquid-liquid extraction process. The solvents extracts first the aromatics from the reformate. The aromatics are then stripped and separated into benzene, toluene and mixed xylenes.
Details: 350 kta United States-based plant | Q2 2024 | 107 pages | Issue A From $799 USD
The cost analyses presented in this report target a 350 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 (Liquid-Liquid Extraction Process)
This study presents the economics of Benzene production from pyrolysis gasoline (pygas) in the United States. This study reviews a typical liquid-liquid extraction process. In the also called solvent extraction, mixed xylenes and a C5 stream are obtained as by-products.
Details: 400 kta United States-based plant | Q2 2024 | 107 pages | Issue B 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.
Benzene Production from Pygas (Extractive Distillation Process)
This report examines the costs related to Benzene production from pyrolysis gasoline (pygas) in the United States using a typical extractive distillation process. Initially, pygas is fractionated into 3 hydrocarbon cuts. The C6s fraction is then fed to an extractive distillation system, using N-formylmorpholine (NFM) as solvent. to recover benzene.
Details: 250 kta United States-based plant | Q2 2024 | 107 pages | Issue C 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.
Benzene Production from Pygas (Hydrodealkylation Process)
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 | Q2 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.
Benzene Production from Light Oil
This study shows a techno-economic analysis of Benzene production from light oil using a hydrodealkylation process similar to Lummus Litol technology. The light oil feedstock used is a product from coal coking process. A C6-C8 fraction is separated. Then, diolefins and styrene are hydrogenated. The effluent is finally converted to benzene by hydrodealkylation. The plant is assumed to be located in the United States.
Details: 200 kta United States-based plant | Q2 2024 | 107 pages | Issue E From $799 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.
Benzene from Toluene (Conventional Toluene Disproportionation)
This report also presents the economics of Benzene production from toluene in the United States. This assessment depicts a conventional toluene disproportionation process (TDP).
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.
Benzene from Toluene (Selective Toluene Disproportionation)
It presents the economics of a selective toluene disproportionation process (STDP) for Benzene production in the United States. In the STDP, toluene is converted into benzene and xylenes (mainly, p-xylene). The reaction is carried out with a zeolitic catalyst, in a hydrogen atmosphere to minimize coke formation and side reactions.
Details: 250 kta United States-based plant | Q2 2024 | 107 pages | Issue G 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.
Benzene Production from Toluene & Heavy Aromatics
This report shows the costs associated with Benzene production from toluene and heavy aromatics in the United States using a typical transalkylation process. In this process, toluene and heavy aromatics are converted to Benzene and xylenes (co-product).
Details: 250 kta United States-based plant | Q2 2024 | 107 pages | Issue H 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.
Benzene from Toluene (Hydrodealkylation)
This study presents the economic analysis for the construction of an industrial plant for Benzene production from toluene in the United States. This study reviews a toluene hydrodealkylation (THDA) technology similar to Houdry's Detol. In this process, toluene is converted over a fixed-bed catalyst into Benzene.
Details: 250 kta United States-based plant | Q2 2024 | 107 pages | Issue I 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.
Benzene Production from Naphtha
This study provides the economics of Benzene production from naphtha in the United States using an integrated aromatics complex, which involves the co-production of p-Xylene. In this process, naphtha is reformed, and the reformate is separated into Benzene, xylenes and toluene, which undergoes disproportionation, forming the other two products.
Details: 450 kta United States-based plant | Q2 2024 | 107 pages | Issue J From $1,499 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.
Could Not Find the Report You Need?
Obtain a Bespoke Report
Get a report targeting the process in which you are interested
See Offer Details
Understand Bespoke Reports and how you can easily order them
Check Editions & Pricing
Complete a brief form and see a quotation for your Bespoke Report
Other Related Production Cost Reports
Cyclohexane from Benzene and Hydrogen (Liquid-Phase Process)
This feasibility study shows the economics of Cyclohexane production from benzene using a liquid phase hydrogenation process in the presence of a nickel-based catalyst. The economic analysis presented is based on a plant constructed in the United States.
Details: 200 kta United States-based plant | Q2 2024 | 107 pages | Issue A From $799 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.
Nitrobenzene Production from Benzene (NORAM)
This report presents the economics of Nitrobenzene production from benzene and nitric acid in the United States. The process analyzed in this report is similar to NORAM's adiabatic benzene nitration process, which uses a plug-flow nitrator containing jet-impingement elements.
Details: 530 kta United States-based plant | Q2 2024 | 107 pages | Issue A From $799 USD
The cost analyses presented in this report target a 530 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.
+800 Reports Developed, Targeting +250 Commodities
Best-in-Class Reports
Analysis of capital and operating costs of commodity production processes. Prices starting at $799 USD
Vast Report Library
858 independent and up-to-date reports examining embryonic and established production processes
Free Sample Reports
Quickly understand the structure and depth of content of our professional reports