Save 10% on two Benzene Production Cost reports, 20% on three, and 30% on four or more — discounts automatically applied at checkout.
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 | Q1 2026 | Issue A | Detailed | Printable
Companion Reports:
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 | Q1 2026 | Issue B | Detailed | Printable
Companion Reports:
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 | Q1 2026 | Issue C | Detailed | Printable
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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 | Q1 2026 | Issue E | Detailed | Printable
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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 | Q1 2026 | Issue F | Detailed | Printable
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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 | Q1 2026 | Issue G | Detailed | Printable
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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 | Q1 2026 | Issue H | Detailed | Printable
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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 | Q1 2026 | Issue I | Detailed | Printable
Companion Reports:
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 | Q1 2026 | Issue J | Detailed | Printable
Companion Reports:
Summary
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Benzene Production from Pygas (Hydrodealkylation Process)
Detailed Edition | Q1 2026
250 kta @ Q1 2026
Downloadable PDF
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Summary
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Benzene Production from Pygas (Hydrodealkylation Process) Report
Production Costs Report | Detailed Edition$1,599 -
Total$1,599 USD