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- W2280565564 abstract "Abstract– A mathematical model has been developed for removal of carbon dioxide from synthesis gas into amine-promoted hot potash solution. In this model a gas–liquid reaction system is proposed based on the surface renewal theory. The mass transfer mechanism accompanied by a chemical reaction is mathematically treated in a new way in order to use its results to develop the model conveniently. An iteration procedure is given to solve the boundary value differential equation system numerically. The predicted data of the model were consistent with the plant data of Shiraz Petrochemical Complex, indicating the validity of the model. The influences of the important model parameters such as amine addition and operating pressure on the absorption performance are also studied. The addition of piperazine to potash solution carbonate increases the rate of CO2 absorption, which has been discussed in this paper." @default.
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- W2280565564 date "2004-01-01" @default.
- W2280565564 modified "2023-09-27" @default.
- W2280565564 title "MODELING AND SIMULATION OF INDUSTRIAL CARBON DIOXIDE ABSORBER USING AMINE-PROMOTED POTASH SOLUTION" @default.
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