“…Thus, the concept of decreasing the local oxygen concentration by distributed dosing to avoid series reactions forming CO and CO 2 has proven to be successful applying ceramic membranes. For further information see Hamel et al , 2003 ;Thomas, Klose, and Seidel -Morgenstern, 2001 .…”
Section: Comparison Between Pbr and Pbmr Using Ceramic Membranes In Amentioning
“…Thus, the concept of decreasing the local oxygen concentration by distributed dosing to avoid series reactions forming CO and CO 2 has proven to be successful applying ceramic membranes. For further information see Hamel et al , 2003 ;Thomas, Klose, and Seidel -Morgenstern, 2001 .…”
Section: Comparison Between Pbr and Pbmr Using Ceramic Membranes In Amentioning
“…Hydrogen productivity in methanol conversion process dependent on membrane porous structure and orientation (T = 300 8C, feeding Ar flux was 80 cm 3 / min, methanol feeding is 0.1 cm 3 /min, under total feed pressure 1.3-1.7 bar). for multilayer porous membranes was observed, recently [13], with gas permeance differences 3-10%. It is explained by consideration of the boundary conditions.…”
Section: Resultsmentioning
confidence: 82%
“…The temperature of the gas in the membrane diffusion cell is controlled by using the thermocouple [7] of the thermostat. Two manometers are used to control gas pressure: before and after the membrane [4,13]. Gas permeation through the membrane [6] was measured by flow meter [9].…”
Section: Methodsmentioning
confidence: 99%
“…The scheme of membrane diffusion cell which consists of: source of gas (1, 2), dryer (3), manometers(4,13), diffusion cell…”
“…In this work, the DGM consisting in Knudsen diffusion and viscous flow mechanisms was adopted to describe the mass transfer of permeate molecules through porous hollow fiber support. [24][25][26] The flux of the components i in Knudsen region is described by Eq. 14…”
A multi-layer series-resistance mass transfer model was developed to simulate mass transfer behaviors of water/ethanol mixture through hollow fiber NaA zeolite membranes. The mass transfer through zeolite layer was described by Maxwell-Stefan mechanism based on adsorption and diffusion parameters obtained from molecular simulation. The mass transfer through asymmetric hollow fiber support was described by dusty gas model involving Knudsen diffusion and viscous flow. It was found that the sponge-like layer of support besides of zeolite layer made an important contribution to overall membrane transfer resistance while the finger-like layer had less effect. When permeate pressure shifted from 0.2 to 7.5 kPa, the mass transfer resistance contribution of sponge-like layer varied from 27.1 to 17.8%. Effects of microstructure parameters of support on mass transfer through membrane were investigated extensively. Large pore size and thin thickness for sponge-like layer of support were beneficial to improve water permeation flux.
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