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N2-ADSORBENT AND O2/N2 SEPARATION USING THE SAME

机译:相同的N2吸附剂和O2 / N2分离

摘要

PURPOSE:To easily obtain a product O2 in reduced power consumption, by perforing adsorption and regeneration under cooling by using an N2-adsorbent prepared by applying heat treatment to sodium faujasite having an alumina sol adhered thereto. CONSTITUTION:1wt% or more of an alumina sol is added to sodium faujasite represented by Na-X or Na-Y and the resulting mixture is subjected to heat treatment at 450 deg.C or more to form a low temp. N2-adsorbent which is, in turn, allowed to pack two or more of adsorbing towers 8, 8'. Compressed, dehumidified and purified air is sent to the adsorbing tower 8 at pressure ranging from atmospheric pressure to 3 ata through flowlines 3', 6 to adsorb N2 with the N2-adsorbent 9 while high purity O2 or O2-enriched air is recovered as a product through a tank 13. A part of this O2 is sent to the adsorbing tower 8' through a pressure reducing valve 15 and the internal pressure of the tower 8' is reduced to 0.5-0.08 ata to regenerate the adsorbent 9'. After regeneration, the air flowline 6 is changed over to an air flowline 6'. In addition, a freezer 20 is provided to the flowline 3 and the adsorbing towers 8, 8' are set to a cooling condition equal to or less than a room temp.
机译:目的:通过使用N2吸附剂在冷却条件下进行吸附和再生,以降低功耗,轻松获得产品O2,该N2吸附剂是通过对附着有氧化铝溶胶的八面酸钠进行热处理而制得的。组成:将1wt%或更多的氧化铝溶胶添加到以Na-X或Na-Y表示的八面沸石钠中,然后将所得混合物在450℃或更高的温度下进行热处理以形成低温。 N 2吸附剂又可以填充两个或多个吸附塔8、8'。压缩,除湿和净化后的空气通过流路3',6在大气压至3 ata的压力下输送到吸附塔8,通过N2吸附剂9吸附N2,同时回收高纯度的O2或富含O2的空气产物O 2通过罐13通过减压阀15被送至吸附塔8',塔8'的内部压力降低至0.5-0.08ata,以再生吸附剂9'。在再生之后,将空气流线6转换成空气流线6'。另外,在流水线3上设置有冷冻室20,吸附塔8、8'被设定为等于或小于室温的冷却条件。

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