Oxygen production device of medical-grade high-temperature molecular sieve membrane adsorption tower and use method of oxygen production device
An oxygen generator and molecular sieve technology, applied in the field of oxygen generators, can solve the problems of poor oxygen production efficiency, low purity, and poor recycling rate of molecular sieves, and achieve improved sterility rate, high oxygen ion conductivity, and high affinity Effect
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[0053] Example 1
[0054] Such as figure 1 As shown, the oxygenation apparatus for the adsorption tower of the medical grade high temperature molecular sieve membrane provided in this example, including the air source access port 1, air compressor 2, C-stage filter 3, air storage tank 4, and T in turn Level filter, A-grade filter, H-class filter, 4 high temperature carbonized ceramic base molecular sieve admix unit 5, vacuum pump 6, oxygen gas tank 7, nitrogen gas tank 8, oxygen gas tank 7 end setting has first Turbine 7-3, the nitrogen gas storage tank 8 is provided with a second stop valve 8-3;
[0055] The vacuum pump 6 is disposed in a high temperature carbonized ceramic-based molecular sieve suction unit 5, and the high-temperature carbonized ceramic-based molecular sieve suction unit 5 and the oxygen storage tank 7 communicate through oxygen shunt pipe 7-2, high temperature carbonized ceramic-based molecular sieve suction unit 5 and nitrogen gas collector 8 Connect through t...
Example Embodiment
[0084] Example 2
[0085] The difference between the embodiments provided in this example is only that the apparatus provided in this embodiment contains three high-temperature carbonized ceramic-based molecular sieve abscissions unit 5.
[0086] In this embodiment, the molecular sieve employed the molecular sieve used in the adsorption tower of the apparatus, the preparation of the material, according to the weight of the weight, including the following ingredients:
[0087]
[0088] The diameter of the nano carboxymethylcellulose of 475 is 65 nm in this example.
[0089] Where said BA 0.3 CE 0.7 CO 0.2 FE 0.8 O Minding method of hollow fiber membrane, including the following steps:
[0090] S1: Add 17.5 parts by weight of EDTA to a water-soluble EDTA ammonium salt solution having a concentration of 3.3 m concentration to a water-soluble EDTA solution in an aqueous solution of a concentration of 3.3 m concentration.
[0091] S2: Mixed bacl in accordance with 3: 7: 2: 8 2 CECL 3...
Example Embodiment
[0112] Example 3
[0113] The difference from the embodiment provided in this example is only that the apparatus provided in this embodiment contains two high-temperature carbonized ceramic-based molecular sieve suction unit 5.
[0114] In this embodiment, the molecular sieve employed the molecular sieve used in the adsorption tower of the apparatus, the preparation of the material, according to the weight of the weight, including the following ingredients:
[0115]
[0116] The diameter of the polymerization of 450 is 80 nm in the diameter of the polymerization of 450.
[0117] BA 0.1 CE 0.9 CO 0.1 FE 0.9 O 0.5 Preparation method of hollow fiber membranes, including the following steps:
[0118] S1: Add 15 parts of EDTA to a water-soluble EDTA ammonium salt solution having a concentration of 3 m concentration to form 15 parts of an aqueous solution of 4%.
[0119] S2: Mixed Bacl in the molar ratio of 1: 9: 1: 9 2 CECL 3 CoCl 2 FECL 3 The powder, then mixed with 20 parts of sodi...
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