Process for recovering CF4 and C2F6 from a gas
A C2F6, CO2 technology, applied in the field of aluminum production, can solve problems such as the increase of anode polarization voltage
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Embodiment 1
[0072] Contains CF 4 、C 2 f 6 and N 2 The gas flow was in contact with the polyimide asymmetric composite hollow fiber membrane at various temperatures to determine the CF 4 、C 2 f 6 and N 2 relative permeability. This gas flow has a constant flow rate of 170 sccm. The pressure of the feed gas stream was maintained at 3 bar. The permeability of each of these components is shown in Figure 2. As can be seen from Figure 2, CF 4 / N 2 and C 2 f 6 / N 2 The selectivity is 300.
[0073] Based on the above selectivity, the single-stage membrane separation unit was simulated by computer. Concentration and pressure of feed, permeate and retentate, and CF 4 / C 2 f 6 The recoveries are shown in Table 1.
[0074] Feed
Embodiment 2
[0076] Using the feed concentrations and pressures listed in Table 2, the procedure of Example 1 was repeated. The simulation results are also listed in Table 2.
[0077] Feed
Embodiment 3
[0079] A typical smelting plant with 100 smelting tanks has an exhaust gas flow of 3Nm 3 / h. The procedure of Example 1 was repeated with this gas flow. The feed concentrations and pressures and simulation results for this stream are listed in Table 3.
[0080] Feed
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