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Paper presents the results of simulation of recycle membrane contactor system (RMC) for biogas separation and air dehumidification application.
In the present work we studied the use of a membrane contactor system for simultaneous absorption of H2S and CO2 from a gas mixture similar to natural gas.
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A simplified version of the model is developed to enable fast design and scale up assessment of membrane contactor systems.
The experiments with membrane contactor systems demonstrated effective air-drying (Tdew point = −30 °C) under high gas flow to liquid carrier flow ratio (G/L = 103) with membrane absorber and desorber temperature difference about ΔT = 30 °C.
This paper presents theoretical and experimental study of humidity control and independently carbon dioxide removal from indoors conditions by means of the pilot recycle membrane contactor air conditioning system (MCACS).
BCTR took a perforated pipe as sparger, while MCTR employed a membrane contactor as the whole mass transfer system.
The location of the reaction zone in the catalytic membrane contactor was determined for two-phase reaction system.
The process has been investigated in both batch and flow conditions, where the latter approach employs a Teflon AF-2400 tube-in-tube gas–liquid membrane contactor to deliver ethylene to the reaction system.
The results show that the well-designed woven fabric membrane contactor as well as the pilot membrane degassing system can effectively remove dissolved oxygen, show low pressure drop and no effect on RO water quality.
The experimental findings for these systems show that a hollow fiber membrane contactor can be used successfully as a model contactor for the determination of various gas liquid physico-chemical properties.
A range of these technologies are reviewed, amongst others, optimized absorption systems, the application of gas/liquid membrane contactors and developmental adsorbent systems.
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