公开(公告)号：US20140187841A1

公开(公告)日：2014-07-03

申请号：US13728568

申请日：2012-12-27

申请人： UOP LLC

发明人： Frank S. Rosser ,  Larry D. Awe

IPC分类号： B01D47/02 ,  C07C7/11

CPC分类号： B01D53/14 ,  B01D47/02 ,  B01D53/002 ,  B01D53/1487 ,  B01D53/18 ,  B01D2252/205 ,  B01D2256/16 ,  B01D2257/702 ,  C07C7/11 ,  C10G70/043 ,  C10G70/048 ,  Y02P20/132

摘要： Embodiments of apparatuses and methods for separating liquefiable hydrocarbons from H2—, hydrocarbon-containing gas streams are provided. In one example, a method comprises positioning a H2—, hydrocarbon-containing gas stream in an internal volume of a vessel below a heat exchange absorption section. A hydrocarbon-containing liquid stream is positioned in the internal volume above the heat exchange absorption section. The hydrocarbon-containing liquid stream is countercurrent contacted with at least a portion of the H2—, hydrocarbon-containing gas stream along a tube portion of the heat exchange absorption section to separate H2 and C3+ hydrocarbons. The hydrocarbon-containing liquid stream and the at least the portion of the H2—, hydrocarbon-containing gas stream are cooled along the tube portion to facilitate separating H2 and C3+ hydrocarbons.

摘要翻译： 提供了将液化烃与含H2-烃的气流分离的装置和方法的实施例。 在一个实例中，一种方法包括将H2-含烃气流定位在热交换吸收段下方的容器的内部体积中。 含烃液体流定位在热交换吸收部分上方的内部体积中。 含烃液体物流与沿热交换吸收部分的管部分的至少一部分含H2-烃的气流逆流接触以分离H 2和C 3 +烃。 含烃液体物流和至少部分含H2-烃的气流沿着管部分被冷却，以便于分离H 2和C 3+烃。

公开(公告)号：US08882890B2

公开(公告)日：2014-11-11

申请号：US13728568

申请日：2012-12-27

申请人： UOP LLC

发明人： Frank S. Rosser ,  Larry D. Awe

IPC分类号： B01D53/14 ,  B01D53/18 ,  B01D47/02 ,  C07C7/11

CPC分类号： B01D53/14 ,  B01D47/02 ,  B01D53/002 ,  B01D53/1487 ,  B01D53/18 ,  B01D2252/205 ,  B01D2256/16 ,  B01D2257/702 ,  C07C7/11 ,  C10G70/043 ,  C10G70/048 ,  Y02P20/132

摘要： Embodiments of apparatuses and methods for separating liquefiable hydrocarbons from H2-, hydrocarbon-containing gas streams are provided. In one example, a method comprises positioning a H2-, hydrocarbon-containing gas stream in an internal volume of a vessel below a heat exchange absorption section. A hydrocarbon-containing liquid stream is positioned in the internal volume above the heat exchange absorption section. The hydrocarbon-containing liquid stream is countercurrent contacted with at least a portion of the H2-, hydrocarbon-containing gas stream along a tube portion of the heat exchange absorption section to separate H2 and C3+ hydrocarbons. The hydrocarbon-containing liquid stream and the at least the portion of the H2-, hydrocarbon-containing gas stream are cooled along the tube portion to facilitate separating H2 and C3+ hydrocarbons.

摘要翻译： 提供了将液化烃与含H2-烃的气流分离的装置和方法的实施例。 在一个实例中，一种方法包括将H2-含烃气流定位在热交换吸收段下方的容器的内部体积中。 含烃液体流定位在热交换吸收部分上方的内部体积中。 含烃液体物流与沿热交换吸收部分的管部分的至少一部分含H2-烃的气流逆流接触以分离H 2和C 3 +烃。 含烃液体物流和至少部分含H2-烃的气流沿着管部分被冷却，以便于分离H 2和C 3+烃。