초록 ▼

A gas separation process that utilizes ejector recycle with a membrane separation step in combination with a second separation step. The second separation step may be a second membrane separation, or may involve a different type of separation process. At least a portion of the non-product (i.e. resi

A gas separation process that utilizes ejector recycle with a membrane separation step in combination with a second separation step. The second separation step may be a second membrane separation, or may involve a different type of separation process. At least a portion of the non-product (i.e. residue) stream withdrawn from the second separation step is directed back to the ejector to form a processing loop. The ejector drives the gas flow in the loop and recycles the non-product stream to the first separation step.

대표청구항 ▼

1. A gas separation process, comprising: (a) providing an ejector including a motive gas inlet, a suction gas inlet, and a mixed gas outlet;(b) passing to the motive gas inlet a motive gas comprising a gas mixture that includes at least a first gas component and a second gas component that is differ

1. A gas separation process, comprising: (a) providing an ejector including a motive gas inlet, a suction gas inlet, and a mixed gas outlet;(b) passing to the motive gas inlet a motive gas comprising a gas mixture that includes at least a first gas component and a second gas component that is different from the first gas component;(c) passing a suction gas to the suction gas inlet;(d) withdrawing from the mixed gas outlet a mixed gas comprising the motive gas and the suction gas;(e) providing a first membrane having a first feed side and a first permeate side, wherein the first membrane is selective to the first gas component relative to the second gas component;(f) passing the mixed gas across the first feed side;(g) withdrawing from the first permeate side a first permeate stream that is enriched in the first gas component relative to the mixed gas;(h) withdrawing from the first feed side a first residue stream that is depleted in the first gas component relative to the mixed gas;(i) providing a second membrane having a second feed side and a second permeate side, wherein the second membrane is selective to the second gas component relative to the first gas component;(j) passing the first residue stream across the second feed side;(k) withdrawing from the second permeate side a second permeate stream that is enriched in the second gas component relative to the first residue stream;(l) withdrawing from the second feed side a second residue stream that is depleted in the second gas component relative to the first residue stream; and(m) passing at least a portion of the second residue stream back to the ejector as the suction gas.