Permeation and separation performance of a diglycolamine-liquid membrane was studied for CO
2/CH
4 and CO
2/N
2 mixed gases. An original support system for a liquid membrane under vacuum-mode permeation was developed using a surface-treated hydrophobic microporous membrane, termed a surface-soaked liquid membrane. A flat membrane module with a 180 mm square membrane surface was made. A diglycolamine/triethylene glycol (50 wt%) liquid membrane of around 8 μm thickness was formed on the surface of the membrane module. Permeation experiments with CO
2 mixed gases were conducted under conditions of atmospheric pressure feed-side and vacuum pressure of 4–5 kPa permeate-side. The amine liquid membrane preferentially transported the CO
2 component. The separation factor of CO
2 was 30 for CO
2/CH
4 and 40 for CO
2/N
2. The permeability of CO
2 increased at low concentration or low partial pressure. This diglycolamine liquid membrane will be applicable for separation or removal of a low concentration CO
2, e.g., CO
2 in the air. Besides the permeation experiments, equilibrium absorption of CO
2/N
2 gas into the amine liquid was measured by a gravitation method. The measured permeabilities used to assess the solution-diffusion model for gas permeation through a liquid membrane. The model is applicable to the permeation of N
2, which has a low solubility. For the highly soluble CO
2 gas, the model did not match the measured permeability value but may account for the permeability increase at low partial pressure.
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