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In the present study, we investigated the effects of module substitution on the properties of Ngb.
Effects of module packing fractions and Reynolds numbers as well as the transverse and longitudinal pitches of the fibers on the mean Nusselt, Sherwood numbers and friction factors for air flow and water flow are analyzed.
A controlled experiment was designed and conducted to evaluate the effects of module design characteristics on information recall, satisfaction, disorientation, and task workload, and the implications for E-Training.
A pure gas test carried out using H2 and He confirmed that there were no effects of module configuration in gas permeation behavior, indicating that the upscale of the separation capacity by numbering-up of membranes using our module design was successful.
Here we evaluated the effects of module M1 on the translocation properties of wild-type Mb.
Next, to examine the effects of module M1 attachment on the secondary structure of globin, we measured the far UV CD spectra of the ferric forms of chimeric Mb, human wild-type Mb and zebrafish wild-type Ngb.
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The effectiveness of gas-sparging was found to be greater with one membrane module type, clearly highlighting the effect of module design on process efficiency.
The model was subsequently used to compare the effect of module length and number of stages on the design performance of a 110,000 m3/day NF plant.
Mutual shading and masking between collector rows; effect of module temperature; and power loss of the conducting cables are taken into account.
The validated model was then used to investigate the geometric effect of module design on the shell-side flow and consequent absorption performance.
A commercially available PTFE (polytetrafluoroethylene) membrane was used in direct contact membrane distillation (DCMD) to investigate the effect of module dimensions on performance.
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