The process of CO2 absorbed in a hollow fiber membrane absorber was studied. For the non-wetted mode
the mathematical model of mass transfer in the membrane absorber was derived. The solution method for nonlinear partial differential equations was given by using T-model difference scheme. For water
NaOH
monoethanolamines (MEA) and 2-amino-2 -methyl-1-propanol (AMP) as absorbents
the process of CO2 absorbed in hollow fiber membrane absorber was simulated. In addition
the absorption of CO2by an aqueous mixture of AMP-MEA was also investigated. For CO2 absorbed into 0.6 mol8226;L-1 NaOH solution
the result of simulation agreed well with the experimental data.
Experiment and analysis of ammonia escape from decarburization absorbent inhibited by NHD
Simulation of process for butanone-toluene solvent recovering in dewaxing of complex oil and/or wax mixtures replaced by a pseudo-single heavy component
Process simulation of methyl acetate hydrolysis via catalytic distillation
Numerical simulation on performances of rough-cut cyclone in FCC disengager
From multi-scale to meso-scale:new challenges for simulation of complex processes in chemical engineering