Abstract

AbstractThe sections in this article areIntroductionCatalystsCatalyst Acid StrengthCatalyst StructureShape Selectivity and Diffusional RestrictionXylenesAromatic Feedstocks and Reformate SeparationsXylene SeparationsToluene Conversion to BenzeneXylene IsomerizationFundamentals of Xylene IsomerizationEthylbenzene Conversion in Xylene Isomerization ProcessesEthylbenzene Hydrocracking Processes in Xylene IsomerizationEthylbenzene Hydroisomerization Processes in Xylene IsomerizationEthylbenzene Disproportionation Processes in Xylene IsomerizationMethylaromatics TransalkylationFundamental Aspects of Methylaromatics TransalkylationMethylaromatics Transalkylation Catalysts and Process ChemistryMethylaromatics Transalkylation ProcessesSelective Toluene Disproportionation (STDP)Shape Selectivity inSTDPSelective Toluene Disproportionation ProcessesEthylbenzene and Cumene TransalkylationCatalysts for Ethylbenzene and Cumene TransalkylationFeeds and Products of Ethylbenzene and Cumene TransalkylationEthylbenzene and Cumene Transalkylation Processesp‐DiethylbenzeneDiisopropylbenzeneMechanisms of Aromatic TransformationsRelative Reactivity of AlkylaromaticsInitiation of Alkylaromatic Conversion ChemistryUnimolecular Aromatic Conversion ChemistryBimolecular Aromatic Conversion ChemistryProcess Implications of Alkylaromatic Transformation MechanismsXylene IsomerizationConversion of Ethylbenzene to XylenesMethylaromatic TransalkylationEthylbenzene Disproportionation to DiethylbenzeneMethylnaphthalene and Dimethylnaphthalene Isomerization and TransalkylationOlefin Reactivity and Coking in Transformations of AlkylaromaticsLight and Heavy Product Distributions in Selective Toluene Disproportionation (STDP)Byproduct Formation in Ethylbenzene and Cumene TransalkylationCatalyst CokingConclusions

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