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Brief description of the recovery of 1996 in a gaseous effluent hydrocarbon, with the implementation of a membrane reactor.

机译:使用膜反应器对1996年在气态废气中的回收进行了简要说明。

摘要

In order to recover the hydrogen in a gaseous effluent rich in hydrocarbons, it implements a process which comprises: - a step (a) in which it causes a gaseous effluent rich in hydrocarbons in contact with the upstream face of a selective membrane to the hydrogen, at a pressure p1; - a step (b), in which circulates a stream containing one or more compound (s) of the unsaturated (s) in contact with the downstream face of said membrane, at a pressure p2 is lower than p1, and in the presence of a catalyst, so as to be at least in part, the said (or these) compound (s) of the unsaturated (s) by means of at least a portion of the hydrogen passing by permeation of said upstream face to the downstream face of the said selective membrane; - a step (c) in which it conveys the flow containing the (or) compound (s) of hydrogenated (s) in step (b). the method may further include a step (d) in which a dehydrogenation reaction of the (or) compound (s) of hydrogenated (s) being transported to the step (c), so as to recover at least a portion of the hydrogen consumed by the hydrogenation step (b).
机译:为了回收富含烃的气态流出物中的氢,其实施了一种方法,该方法包括:-步骤(a),在该步骤中,使富含烃的气态流出物与选择性膜的上游面接触而产生氢。 ,压力为p1; -步骤(b),其中使包含与所述膜的下游面接触的一种或多种不饱和化合物的一种或多种化合物的料流在压力p2低于p1且存在下的条件下循环。通过至少一部分通过所述上游面渗透到所述下游面的氢而至少部分地使所述不饱和化合物中的所述(或这些)化合物成为催化剂。所述选择性膜; -步骤(c),其中在步骤(b)中输送包含(一种或多种)氢化化合物的物流。该方法可以进一步包括步骤(d),其中将(一种或多种)氢化化合物(一种或多种)的脱氢反应输送到步骤(c),以便回收至少一部分消耗的氢。通过氢化步骤(b)。

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