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method of removing oxygen from u0431u0443u0442u0430u0434u0438u0435u043du0430 c hydrocarbon flows

机译:从 u0431 u0443 u0442 u0430 u0434 u0438 u0435 u043d u0430 c烃流中去除氧气的方法

摘要

describes the way to obtain u0431u0443u0442u0430u0434u0438u0435u043du0430 of n - butane with the following steps: a) preparation of a gas flow containing n - butane; b) food by gas adequate flow and containing n - butane, at least one first u0434u0435u0433u0438u0434u0440u0438u0440u0443u044eu0449u0435u0439 zone and u043du0435u043eu043au0438u0441u043bu0438u0442u0435u043bu044cu043du043eu0433u043e catalytic u0434u0435u0433u0438u0434u0440u0438u0440u043eu0432u0430u043du0438u044f n - butane, which are u0433u0430u0437u043eu0432u044b in stream b containing n - butane, 1 - u0431u0443u0442u0435u043d, 2 - u0431u0443u0442u0435u043du044b, butadiene, hydrogenif necessary, water vapor, if necessary, carbon oxide and, if necessary, inert gases; (g) the feed gas flow f, which includes bhutan, u0431u0443u0442u0435u043du044b, boo u0442u0430u0434u0438u0435u043d and received from a gas flow containing oxygen gas b, and at least one second u0434u0435u0433u0438u0434u0440u0438u0440u0443u044eu0449u0435u0439 zone and u043eu043au0438u0441u043bu0438u0442u0435u043bu044cu043du043eu0433u043e u0434u0435u0433u0438u0434u0440u0438u0440u043eu0432u0430u043du0438u044f 1 - and 2 - u0431u0443u0442u0435u043du0430 u0431u0443u0442u0435u043du043eu0432 and receive the gas flow g, containing n - butane.not that u0431u0443u0442u0435u043d (s) 1 and 2 u0431u0443u0442u0435u043du044b, butadiene, water vapor, if necessary, carbon oxides, hydrogen, if necessary and, if necessary, inert gases; and (h) ood u0430u043bu0435u043du0438u0435 residual oxygen contained in a gas stream (g, through the catalytic stage combustionat which oxygen transforms with part or all of the separated hydrogen d2 and / or further by feeding hydrogen to obtain flow u0435u0449u0435u0441u0442u0432 h, depleted of oxygen and the fact that the phase h) are in the presence of a catalyst which comprises a monolith, which shows u043au0430u0442u0430u043bu0438u0442u0438u0447u0435u0441u043a and the inert material of low wet - surface, and a layer of catalystwhich caused the monolith and contains u043eu043au0441u0438u0434u043du044bu0439 material carrier, at least one noble metal selected from the group consisting of noble metals gr u0443u043fu043fu044b viii of periodic system of elements, if necessary, tin
机译:描述了通过以下步骤获得正丁烷的方法:a)制备含正丁烷的气流; b)气体充分流动且含有正丁烷,至少一个第一 u0434 u0435 u0433 u0438 u0434 u0440 u0438 u0440 u0443 u044e u0449 u0435 u0439区域和 u043d u0435 u043e u043a u0438 u0441 u043b u0438 u0442 u0435 u043b u044c u043d u043e u0433 u043e催化 u0434 u0435 u0433 u0438 u0434 u0434 u0440 u0438 u0440 u043e u0432 u043d u0438 u044f n-丁烷,它们是包含n-丁烷1- u0431 u0443 u0442 u0435 u043d,2- u0431 的流b中的 u0433 u0430 u0437 u043e u0432 u044b丁二烯,氢(如果需要),水蒸气(如果需要),二氧化碳和(如果需要)惰性气体; (g)原料气流f,其中包括不丹, u0431 u0443 u0442 u0435 u043d u044b,boo u0442 u0430 u0434 u0438 u0435 u043d并从包含氧气b的气流中接收,至少一秒钟 u0434 u0435 u0433 u0438 u0434 u0440 u0438 u0440 u0443 u044e u0449 u0435 u0439区域和 u043e u043a u0438 u0441 u0441 u0431 u043b u0438 u0442 u0435 u043b u044c u043d u043e u0433 u043e u0434 u0435 u0433 u0438 u0434 u0440 u0438 u0440 u043e u0432 u0430 u043d u0438 u044f 1和2- u0431 u0443 u0442 u0435 u043d u0430 u0431 u0443 u0442 u0435 u043d u043e u0432并接收包含正丁烷的气流g,不是 u0431 u0443 u0442 u0435 u043d(s)1和2丁二烯,水蒸气(如果需要),碳氧化物,氢气(如果需要)以及(如果需要)惰性气体; (h)气流中所含的残余氧(g,通过催化阶段燃烧,在该催化阶段燃烧中,氧与部分或全部分离出的氢d2和//转化,或者进一步由进料氢气以获得流量,氧气流失,并且相h)存在于包含整体催化剂的催化剂中,该事实表明 u043a u0430 u0442 u0430 u043b u0438 u0442 u0438 u0447 u0435 u0441 u043a的惰性材料,以及一层引起整体结构并包含 u043e u043a u0441 u0438 u0434 u043d的催化剂层材料载体,选自元素周期系统的至少一种贵金属,包括贵金属gr,锡,必要时是锡

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