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This report presents the economics of an industrial process for 1-Hexene production from ethylene, assuming a trimerization process similar to the one owned by Chevron Philips. The economic analysis is based on a plant operating in the United States.
This analysis approaches the economics of 1-Hexene production from raffinate-2, based on a process similar to the CPT Process licensed by Lummus. Initially, 2-butene from raffinate-2 is isomerized to 1-butene. Then, 1-butene is reacted with itself to form 3-hexene and ethylene. The 3-hexene is finally isomerized to 1-hexene. The analysis considers a facility erected in the United States.
In this report, it is approached the economics of 1-Hexene production via extractive distillation from synthetic fuels (synfuels), using an industrial process similar to the technology owned by Sasol. The economic analysis assumes a plant located in the United States.