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This feasibility study presents an analysis of Maleic Anhydride production from n-butane in the United States using a process similar to the one developed by Huntsman. In this process, maleic anhydride is produced by the partial oxidation reaction of n-butane with oxygen carried out in a fixed-bed reactor, using a vanadium–phosphorus oxide (VPO) catalyst supported on silica. The reactor effluent is directed to a solvent-based recovery system for Maleic Anhydride separation.
This study presents an economic analysis of Maleic Anhydride production from n-butane in the United States using a process similar to the one developed by Scientific Design. In this process, Maleic Anhydride is produced by the partial oxidation reaction of n-butane with oxygen carried out in two fixed-bed reactors, using vanadium–phosphorus oxide (VPO) catalyst supported on silica. The Maleic Anhydride formed is recovered in an aqueous-based system.
This study provides a techno-economic analysis of a process for Maleic Anhydride production from benzene in the United States. This process highlights a benzene oxidation to maleic anhydride in a fixed-bed reactor combined with an aqueous-based recovery system.
This report provides the economics of a process similar to CB&I Lummus ALMA for Maleic Anhydride production from n-butane in the United States. The process examined in this report uses a fluid bed reactor. In this case, the recovery system is solvent-based. This process is similar to Lummus ALMA.
This study reviews the economics of a process for Maleic Anhydride production from butenes. In the process examined, Maleic Anhydride is produced by the oxidation of n-butenes with air in a fluidized-bed reactor. The economic analysis performed is based on a plant constructed in the United States.