MEMBRANE HEAT TREATMENT METHOD
    2.
    发明公开

    公开(公告)号:US20230356153A1

    公开(公告)日:2023-11-09

    申请号:US18352377

    申请日:2023-07-14

    Abstract: A membrane heat treatment method includes a process of raising the temperature of a membrane to an intermediate heating temperature (step S21), a process of heating and keeping the membrane at the intermediate heating temperature (step S22), a process of raising the temperature of the membrane to a main heating temperature higher than the intermediate heating temperature (step S23), and the process of heating and keeping the membrane at the main heating temperature (step S24). A first recovery amount R1 that is a difference in permeability of the membrane between after step S22 and before step S21 is 50% or more and 95% or less of a second recovery amount R2 that is a difference in permeability of the membrane between after step S24 and before step S21.

    MIXED GAS SEPARATION METHOD AND MIXED GAS SEPARATION APPARATUS

    公开(公告)号:US20240100474A1

    公开(公告)日:2024-03-28

    申请号:US18524431

    申请日:2023-11-30

    Abstract: A mixed gas separation method includes a step of supplying a mixed gas to the separation membrane and causing a gas with high permeability in the mixed gas to permeate through the separation membrane. In the step, when ΔP is a difference between a gas pressure on the primary side of the separation membrane, i.e., a feed pressure, and a gas pressure on the secondary side of the separation membrane, i.e., a permeate pressure, and A is a Joule-Thomson coefficient, a difference ΔT between a gas temperature on the primary side of the separation membrane, i.e., a feed temperature, and a gas temperature on the secondary side of the separation membrane, i.e., a permeate temperature, is made less than 90% of A·ΔP by setting the Nu number in the mixed gas to be greater than or equal to 2 and less than or equal to 10.

    GAS SEPARATION METHOD AND ZEOLITE MEMBRANE

    公开(公告)号:US20230026226A1

    公开(公告)日:2023-01-26

    申请号:US17931925

    申请日:2022-09-14

    Abstract: A gas separation method includes supplying a mixed gas to a zeolite membrane complex and permeating a high permeability gas through the zeolite membrane complex to separate the high permeability gas from other gases. The mixed gas includes a high permeability gas and a trace gas that is lower in concentration than the high permeability gas. The molar concentration of a first gas included in the trace gas in the mixed gas is higher than the molar concentration of a second gas included in the trace gas in the mixed gas. The adsorption equilibrium constant of the first gas on the zeolite membrane is less than 60 times that of the high permeability gas. The adsorption equilibrium constant of the second gas on the zeolite membrane is 400 times or more that of the high permeability gas.

    GAS SEPARATION METHOD AND ZEOLITE MEMBRANE

    公开(公告)号:US20230018523A1

    公开(公告)日:2023-01-19

    申请号:US17931918

    申请日:2022-09-14

    Abstract: A gas separation method includes supplying a mixed gas to a zeolite membrane complex and permeating a high permeability gas through the zeolite membrane complex to separate the high permeability gas from other gases. The mixed gas includes a high permeability gas and a trace gas that is lower in concentration than the high permeability gas. The trace gas contains an organic substance whose molar concentration in the mixed gas is higher than or equal to 1.0 mol %. The adsorption equilibrium constant of the organic substance on the zeolite membrane is less than 150 times the adsorption equilibrium constant of the high permeability gas.

    SEPARATION MEMBRANE MODULE
    9.
    发明申请

    公开(公告)号:US20230073866A1

    公开(公告)日:2023-03-09

    申请号:US18045485

    申请日:2022-10-11

    Abstract: A separation membrane module includes a separation membrane complex having a support and a separation membrane provided on the support, a housing container for housing the separation membrane complex, and a sealing member existing between a supporting surface provided inside the housing container and a supported surface of the separation membrane complex, being in close contact with the supporting surface and the supported surface. A first static friction coefficient between the sealing member and the supported surface and/or a second static friction coefficient between the sealing member and the supporting surface are/is not higher than 0.5. A value obtained by multiplying the first static friction coefficient and/or the second static friction coefficient by a compressive force [N] of the sealing member and dividing the product by a mass [kg] of the separation membrane complex is larger than 0.7.

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