Gas separating membrane and its utilizing method
A gas separation membrane, helium technology
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Embodiment 1
[0063] In a separable flask, 583.3 g of a solution of polyimide A with a polymer concentration of 12.0 wt % and 250 g of a solution of polyimide B with a polymer concentration of 13.0 wt % were stirred at a temperature of 130 °C for 3 hours to prepare a polyimide blend solution. This blend solution had a polymer concentration of 12.3 wt% and a rotational viscosity of 1500 poise. The polyimide blend solution was used to produce hollow fiber membranes by the aforementioned asymmetric hollow fiber membrane production method. The gas permeability and mechanical properties of this hollow fiber membrane were measured by the aforementioned methods. The results are shown in Table 1.
Embodiment 2
[0065] Using the same mixing method as in Example 1, 400 g of polyimide A solution with a polymer concentration of 12.0 wt % and 400 g of polyimide B solution with a polymer concentration of 13.0 wt % were mixed to prepare a mixed solution. The polymer concentration of this blend solution was 12.5 wt%. This polyimide blend solution was used to produce hollow fiber membranes by the aforementioned asymmetric hollow fiber membrane production method. The gas permeability and mechanical properties of this hollow fiber membrane were measured by the aforementioned methods. The results are shown in Table 1.
Embodiment 3
[0073] Using the same mixing method as in Example 1, 350 g of polyimide C solution with a polymer concentration of 12.0 wt % and 150 g of polyimide B solution with a polymer concentration of 13.0 wt % were mixed to prepare a mixed solution. The polymer concentration of this blend solution was 12.3 wt%. This polyimide blend solution was used to produce hollow fiber membranes by the aforementioned asymmetric hollow fiber membrane production method. The gas permeability and mechanical properties of this hollow fiber membrane were measured by the aforementioned methods. The results are shown in Table 1.
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Abstract
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