Membrane separator

1 . A separation system, comprising:

a membrane separator configured to receive two or more fluid streams, wherein the membrane separator comprises a hollow fiber membrane comprising:

a first set of fibers configured to transfer one or more components from a first gas stream into a shell side volume; and

a second set of fibers configured to transfer the one or more components from the shell side volume into a second gas stream.

2 . The separation system of claim 1 ,

wherein the two or more fluid streams comprise the first gas stream and a liquid sorbent stream, and

wherein the membrane separator comprises a membrane contactor configured to absorb the one or more components from the first gas stream into a liquid sorbent of the liquid sorbent stream in the shell side volume.

3 . The separation system of claim 2 , wherein the membrane contactor is configured to desorb at least a portion of the one or more components from the liquid sorbent into the second gas stream.

4 . The separation system of claim 3 ,

wherein the membrane contactor is a first membrane contactor configured to desorb a first portion of the one or more components from the liquid sorbent into the second gas stream, and

wherein the separation system comprises a second membrane contactor configured to desorb a second portion of the one or more components from the liquid sorbent into a product stream.

5 . The separation system of claim 3 ,

wherein the first set of fibers is positioned at least partially upstream of the second set of fibers with respect to a flow of the liquid sorbent, and

wherein the membrane separator is configured to maintain a temperature of the liquid sorbent proximate to the first set of fibers higher than a temperature of the liquid sorbent proximate to the second set of fibers.

6 . The separation system of claim 5 , further comprising one or more heat traces configured to heat the liquid sorbent.

7 . The separation system of claim 1 ,

wherein the two or more fluid streams comprise the first gas stream and the second gas stream, and

wherein the membrane separator comprises a membrane gas separator configured to transfer the one or more components from the first gas stream into the second gas stream via the shell side volume.

8 . The separation system of claim 7 , wherein the first set of fibers and the second set of fibers have a different permeability to the one or more components.

9 . The separation system of claim 7 , wherein the membrane gas separator comprises a membrane dehumidifier configured to transfer water vapor from the first gas stream into the second gas stream via the shell side volume.

10 . The separation system of claim 9 , wherein the separation system further comprises one or more membrane contactors configured to:

absorb the one or more components from the first gas stream into a liquid sorbent; and

desorb at least a portion of the one or more components from the liquid sorbent into a product stream.

11 . The separation system of claim 1 , wherein the membrane separator further comprises:

a housing;

a first tubesheet set coupled to the first set of fibers; and

a second tubesheet set coupled to the second set of fibers.

12 . The separation system of claim 11 , wherein the housing, the first tubesheet set, and the second tubesheet set define:

a first inlet plenum and a first outlet plenum fluidically coupled to the first set of fibers,

a second inlet plenum and a second outlet plenum fluidically coupled to the second set of fibers, and

the shell side volume.

13 . A method, comprising:

receiving, by a first set of fibers of a hollow fiber membrane of a membrane separator, a first gas stream that includes one or more components, wherein the membrane separator receives two or more fluid streams;

transferring, by the first set of fibers, the one or more components from the first gas stream into a shell side volume;

transferring, by a second set of fibers of the hollow fiber membrane, at least a portion of the one or more components from the shell side volume into a second gas stream; and

discharging, by the second set of fibers, the second gas stream from the hollow fiber membrane.

14 . The method of claim 13 ,

wherein the two or more fluid streams comprise the first gas stream and a liquid sorbent stream,

wherein the membrane separator comprises a membrane contactor, and

wherein transferring the one or more components from the first gas stream into a shell side volume comprises absorbing the one or more components from the first gas stream into a liquid sorbent of the liquid sorbent stream in the shell side volume.

15 . The method of claim 14 , wherein transferring at least a portion of the one or more components from the shell side volume into the second gas stream comprises desorbing at least a portion of the one or more components from the liquid sorbent into the second gas stream.

16 . The method of claim 15 ,

wherein the membrane contactor is a first membrane contactor,

wherein a first portion of the one or more components is desorbed from the liquid sorbent into the second gas stream by the first membrane contactor, and

wherein a second portion of the one or more components is desorbed from the liquid sorbent into a product stream by a second membrane contactor.

17 . The method of claim 15 ,

wherein the first set of fibers is positioned at least partially upstream of the second set of fibers with respect to a flow of the liquid sorbent, and

wherein the method further comprises maintaining a temperature of the liquid sorbent proximate to the first set of fibers higher than a temperature of the liquid sorbent proximate to the second set of fibers.

18 . The method of claim 13 ,

wherein the two or more fluid streams comprise the first gas stream and the second gas stream,

wherein the membrane separator comprises a membrane gas separator, and

wherein transferring the one or more components from the first gas stream into a shell side volume and transferring at least a portion of the one or more components from the shell side volume into the second gas stream comprises transferring the one or more components from the first gas stream into the second gas stream via the shell side volume.

19 . The method of claim 18 ,

wherein the membrane gas separator comprises a membrane dehumidifier, and

wherein transferring the one or more components from the first gas stream into the second shell stream via the shell side volume comprises transferring water vapor from the first gas stream into the second gas stream via the shell side volume.

20 . The method of claim 19 , further comprising:

absorbing the one or more components from the first gas stream into a liquid sorbent; and

desorbing at least a portion of the one or more components from the liquid sorbent into a product stream.