Research and development of novel CO
2-selective membranes, called molecular gate membranes (MGMs), has been conducted. Unlike conventional CO
2-selective membranes, MGMs show exceptionally high CO
2 separation over H
2. The membranes and the membrane modules were developed for
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Research and development of novel CO
2-selective membranes, called molecular gate membranes (MGMs), has been conducted. Unlike conventional CO
2-selective membranes, MGMs show exceptionally high CO
2 separation over H
2. The membranes and the membrane modules were developed for CO
2 separation at low energy consumption and low cost in pre-combustion processes such as integrated gasification combined cycle (IGCC) and hydrogen production. To date, two candidate membrane materials—poly(ethylene glycol) (PEG)-based and poly(vinyl alcohol) (PVA)-based membranes—have been used. As for PEG-based membrane materials, the effect of operating conditions, such as relative humidity in feed gas and sweep gas and operating pressure, on CO
2 separation performance were investigated. Both CO
2 permeance and selectivity increased with increasing relative humidity on both the feed and permeate sides. The CO
2 permeance increased from the 10
−12 to the 10
−11 order, while the selectivity increased from 2.8 to 25. In addition, it was found that the water vapor permeates from the high to the low relative humidity side with a permeance typically on the order of 10
−8 m
3(STP)m
−2·s
−1·Pa
−1, regardless of the total pressure difference between the feed side and the permeate side. This finding is important in the design of membrane systems. However, we found that PVA-based membranes exhibited superior thin-film coating ability and higher separation performance compared with PEG-based membranes. As for PVA-based materials, membranes that showed high CO
2 separation performance under high-pressure conditions of 2.4 MPa (the supposed pressure in the IGCC process) were successfully prepared. In addition, the technology to prepare MGMs with a large membrane area was developed by a continuous membrane-forming method, and the membrane elements (diameter: 10–20 cm; length: 20–60 cm) were also fabricated. Pre-combustion CO
2 capture tests of the membrane elements were conducted using coal-derived gasification gas, and it was confirmed that the membrane elements were durable against the real gas, which contained components such as H
2S (on the order of 100 ppm) and CO (32.4%).
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