PropertyValue
http://www.w3.org/1999/02/22-rdf-syntax-ns#type
http://www.w3.org/ns/prov#value
  • When the isomerization processes are integrated with separation processes such as adsorption or distillation, which separate the effluent from the isomerization reactor into higher and lower octane segments, the final product from the integrated process typically has an octane of about 90 RON. In accordance with the present invention processes are provided for the adsorption and isomerization of a
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