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PROCESS FOR SEPARATING AND RECYCLING REFINERY DRY GAS

机译:分离和回收炼油厂干气的过程

摘要

A process for separating and recycling refinery dry gas. At least a one-stage pressure swing adsorption unit is provided; at least two adsorption beds filled with an adsorbent are disposed in the one-stage pressure swing adsorption unit; the adsorption beds operate alternately according to set time sequence steps; each adsorption bed at least sequentially undergoes process steps such as adsorption, reduced pressure equalization, concentration, reverse exhaust, vacuumizing, pre-adsorption, increased pressure equalization, and final charging. Two material flows, i.e., C2+ component product gas and hydrogen-rich product gas having a C2+ component concentration of greater than 92v% and a recovery rate of greater than 92%, can be obtained after dry feed gas is separated by a pressure swing adsorption unit. Compared with the prior art, the process has simpler procedures, lower investment and operation cost, and higher yield of C2+ components and product purity; if necessary, the dry feed gas can be separated by the one-stage pressure swing adsorption unit and a two-stage pressure swing adsorption unit to obtain three material flows, i.e., C2+ component product gas, hydrogen product gas, and fuel gas.
机译:一种分离和回收炼厂干气的方法。至少设有一级变压吸附单元。一级变压吸附单元中至少装有两个装有吸附剂的吸附床。吸附床按照设定的时间顺序交替运行;每个吸附床至少依次经历诸如吸附,减压均衡,浓缩,反向排气,抽真空,预吸附,增加的压力均衡和最终装料的处理步骤。两种物质流,即C 2 +组分气和C 2 +组分浓度大于92v%且回收率更高的富氢气通过变压吸附装置分离干燥的进料气后,可得到小于92%的碳。与现有技术相比,该工艺过程更简单,投资和操作成本更低,C 2 +组分的收率更高,产品纯度更高。如有必要,可以通过一级变压吸附单元和二级变压吸附单元分离干燥的进料气,以获得三股物料流,即C 2 +组分产物气,氢气产品气和燃料气。

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