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- W2592786360 abstract "The oxidative coupling of methane (OCM) allows for the catalytic conversion of methane into longer hydrocarbons, especially ethylene. Given its low yield and large number of byproducts the whole process concept needs to be optimized thoroughly. This contribution focuses on modeling and optimizing a hybrid system for the removal of CO2 from the OCM product gas, which consists of an absorption desorption unit and a two-stage gas separation membrane system. The absorption is modeled based on equilibrium data for Monoethanolamine and experimental data of the mini-plant built at Berlin University of Technology. A standard model using measured permeances is implemented for the membrane. The whole system is modelled in MOSAIC and automatically exported to AMPL, wherein simulations and optimization are carried out using IPOPT. The two-stage membrane system upstream to the absorption allows for the reduction of the product loss, i.e. ethylene, and decreases the energy required for the removal of CO2 compared to the single-stage membrane system even further." @default.
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- W2592786360 date "2013-06-01" @default.
- W2592786360 modified "2023-09-27" @default.
- W2592786360 title "Optimization of a Membrane-Absorption-Hybrid System for Removal of CO2 from OCM Gas" @default.
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- W2592786360 hasPublicationYear "2013" @default.
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