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Process for removing hydrogen by cryogenic distillation in the production of high purity nitrogen

机译:在高纯度氮气生产中通过低温蒸馏除去氢气的方法

摘要

A process for removing hydrogen by cryogenic distillation in the production of high purity nitrogen, which comprises:a) feeding a compressed, cleaned and dried feed mixture (12) comprising oxygen and nitrogen, which has been cooled to about the dew point thereof, to a first distillation column 13, whereby said nitrogen 16 is extracted at the top of said distillation column as a liquid, and a liquid stream rich is oxygen 17 is extracted at the bottom of said first distillation column;b) extracting a minor fraction of the gas 30 at the top of the first distillation column, the minor fraction containing the lighter impurities;c) expanding said liquid nitrogen at the top of the first distillation column into a second distillation column 14 at an intermediate level, said second distillation column being operated at a pressure sufficiently lower than the pressure of said first distillation column to provide a sufficient temperature difference in a condenser-reboiler located between the first and second distillation columns;d) vaporizing the liquid stream rich is oxygen in the overhead condenser 4 of the second distillation column 14 against the condensing vapor at the top of the second distillation column to form a condensate at the top of the second distillation column, and returning said condensate to the top of the second distillation column as reflux;e) extracting a minor fraction of the gas 31 at the top of the second distillation column containing substantially all lighter impurities; andf) vaporizing the liquid at the bottom of the second distillation column 14 by heat exchange with the condensing gas at the top of the first distillation column 13, and recovering as product a fraction of the liquid 24, a fraction of the vaporized liquid 29 or both, the product containing substantially no lighter air impurities.
机译:一种在生产高纯氮的过程中通过低温蒸馏除去氢的方法,该方法包括:a)将已冷却至大约露点的包含氧气和氮气的压缩,清洁和干燥的进料混合物(12)进料至第一蒸馏塔13,由此在所述蒸馏塔的顶部提取所述氮气16作为液体,在所述第一蒸馏塔的底部提取富含氧气的液流17; b)在第一蒸馏塔的顶部提取少量的气体30,所述少量的气体包含较轻的杂质; c)在第一蒸馏塔的顶部将所述液氮膨胀至中间水平的第二蒸馏塔14,所述第二蒸馏塔在足以低于所述第一蒸馏塔的压力的压力下操作以提供足够的温度差在位于第一蒸馏塔和第二蒸馏塔之间的冷凝器-再沸器中; d)在所述塔顶冷凝器4中蒸发富含氧气的液体流相对于第二蒸馏塔顶部的冷凝蒸气冷凝蒸馏塔14,以在第二蒸馏塔顶部形成冷凝液,并将所述冷凝液作为回流返回第二蒸馏塔的顶部; e)提取少量馏分在第二蒸馏塔顶部的气体31中基本上含有所有较轻的杂质; f)通过与第一蒸馏塔13顶部的冷凝气体进行热交换使第二蒸馏塔14底部的液体汽化,并回收一部分液体24,一部分汽化液体29或两者均基本上不含较轻的空气杂质。

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