A kind of oxygen generator of medical grade high temperature molecular sieve membrane adsorption tower and using method thereof
An oxygen generator and molecular sieve technology, applied in the field of oxygen generators, can solve the problems of low purity, poor oxygen preparation efficiency, poor molecular sieve recycling rate, etc., and achieve high oxygen ion conductivity, high affinity, and improve sterility. Effect
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Embodiment 1
[0054] like figure 1 As shown, the oxygen generator 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, a T Class filter, Class A filter, Class H filter, 4 high temperature carbonized ceramic base molecular sieve adsorption units 5, vacuum pump 6, oxygen gas storage tank 7, nitrogen gas storage tank 8, the end of oxygen gas storage tank 7 is provided with a first The closing valve 7-3, the end of the nitrogen gas storage tank 8 is provided with a second closing valve 8-3;
[0055] The vacuum pump 6 is arranged in the high-temperature carbonized ceramic-based molecular sieve adsorption unit 5, the high-temperature carbonized ceramic-based molecular sieve adsorption unit 5 is connected with the oxygen gas storage tank 7 through the oxygen shunt pipeline 7-2, and the high-temperature carbonized ceramic-based molecular sieve adsorpti...
Embodiment 2
[0085] The only difference in structure between this embodiment and Embodiment 1 is that the device provided in this embodiment contains three high-temperature carbonized ceramic-based molecular sieve adsorption units 5 .
[0086] The raw materials for the preparation of oxygen ion conductive carbonized ceramic-based molecular sieve membranes used in the molecular sieve in the adsorption tower of the device provided in this embodiment, in parts by weight, include the following components:
[0087]
[0088] The diameter of the nanometer sodium carboxymethyl cellulose with a polymerization degree of 475 used in this example 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: adding 17.5 parts by weight of EDTA to an ammonium hydroxide aqueous solution with a mass fraction of 26% to form a water-soluble EDTA ammonium salt solution with a concentration of 3.3M;
[0091...
Embodiment 3
[0113] The only difference in structure between this embodiment and Embodiment 1 is that the device provided in this embodiment 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, in parts by weight, include the following components:
[0115]
[0116] The diameter of the nano-lignosulfonate with a polymerization degree of 450 used in this example is 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: adding 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 in a molar ratio of 1:9:1:9 2 ...
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