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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Embodiment 1
[0054] like figure 1 As shown, the oxygen production device of a medical-grade high-temperature molecular sieve membrane adsorption tower provided in this embodiment includes an air source inlet 1, an air compressor 2, a C-level filter 3, an air storage tank 4, and a T Class filter, Class A filter, Class H filter, 4 high-temperature carbonized ceramic-based molecular sieve adsorption units 5, vacuum pump 6, oxygen gas storage tank 7, nitrogen gas storage tank 8, the end of the oxygen gas storage tank 7 is provided with a first The stop valve 7-3, the end of the nitrogen storage tank 8 is provided with a second stop valve 8-3;
[0055] The vacuum pump 6 is set in the high-temperature carbonized ceramic-based molecular sieve adsorption unit 5, the high-temperature carbonized ceramic-based molecular sieve adsorption unit 5 communicates with the oxygen gas storage tank 7 through the oxygen shunt pipeline 7-2, and the high-temperature carbonized ceramic-based molecular sieve adsorp...
Embodiment 2
[0085] The structural difference between this example and Example 1 is only that the device provided by this example contains three high-temperature carbonized ceramic-based molecular sieve adsorption units 5 .
[0086] The raw materials for the preparation of the oxygen-ion conductive carbonized ceramic-based molecular sieve membrane used in the molecular sieve in the adsorption tower of the device provided in this embodiment include the following components in parts by weight:
[0087]
[0088] The diameter of the nano carboxymethyl cellulose sodium with a degree of polymerization of 475 used in this embodiment is 65 nm.
[0089] Among them, the Ba 0.3 Ce 0.7 co 0.2 Fe 0.8 The preparation method of O hollow fiber membrane, comprises the following steps:
[0090] S1: Add 17.5 parts by weight of EDTA to an aqueous solution of ammonium hydroxide with a mass fraction of 26% to form a water-soluble EDTA ammonium salt solution with a concentration of 3.3M;
[0091] S2: Mix...
Embodiment 3
[0113] The structural difference between this example and Example 1 is only that the device provided by this example contains two high-temperature carbonized ceramic-based molecular sieve adsorption units 5 .
[0114] The raw materials for the preparation of the oxygen-ion conductive carbonized ceramic-based molecular sieve membrane used in the molecular sieve in the adsorption tower of the device provided in this embodiment include the following components in parts by weight:
[0115]
[0116] The nano lignosulfonate with a degree of polymerization of 450 used in this example has a diameter of 80 nm.
[0117] Ba 0.1 Ce 0.9 co 0.1 Fe 0.9 o 0.5 The preparation method of hollow fiber membrane comprises the following steps:
[0118] S1: Add 15 parts of EDTA to an aqueous ammonium hydroxide solution with a mass fraction of 25% to form a water-soluble EDTA ammonium salt solution with a concentration of 3M;
[0119] S2: Mix BaCl according to the molar ratio of 1:9:1:9 2 , ...
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