Search for a Commodity and Check Solutions Offered
Refine Results
Results 1 - 10 of 10
This report also presents the economics of Benzene production from toluene in the United States. This assessment depicts a conventional toluene disproportionation process (TDP).
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.
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.
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.
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.
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.
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
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.
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.
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).