Combined recovery of hydrogen and hydrocarbon liquids from hydrogen-containing gases
View Patent ↗A pressure differential of a feed gas ( 110 ) between a compressor ( 120 ) and expander ( 160 ) is employed to cool the feed gas to condense and remove at least a portion of one component to produce a partially depleted feed gas from which another component may then be removed. In especially preferred aspects, the feed gas comprises C 2 -C 5 hydrocarbons and hydrogen, wherein the hydrocarbons are condensed in the cooler and hydrogen is removed using a pressure swing adsorption unit ( 180 ).
1. A plant comprising:
a compressor that is configured to compress a feed gas comprising a first component and a second component, and to thereby form a compressed feed gas having a first pressure;
a cooler coupled to the compressor, wherein the cooler is configured to receive and cool the compressed feed gas to a temperature sufficient to condense at least part of the first component in the compressed feed gas;
a first separator that is configured to separate the cooled compressed feed gas into a first vapor portion and a first liquids portion, and an expander that is configured to expand the first vapor portion to a second pressure to thereby allow formation of an expanded stream; and
a second separator that is configured to separate the expanded stream into a second liquids portion and a second vapor portion, wherein the cooler is configured to allow the second vapor portion to provide refrigeration to the compressed feed gas.
2. The plant of claim 1 further comprising a pressure swing adsorption unit that is configured to receive the second vapor portion to allow for removal of the second component from the feed gas.
3. The plant of claim 2 wherein second separator is configured to receive the first liquids portion, and wherein the second liquids portion predominantly comprises the second component.
4. The plant of claim 3 wherein the compressor and the expander are mechanically coupled to each other.
5. The plant of claim 3 wherein the first component comprises a C 2 -C 5 hydrocarbon, and wherein the second component comprises hydrogen.
6. The plant of claim 5 wherein the pressure swing adsorption unit comprises a hydrogen pressure swing adsorption unit.
7. The plant of claim 1 wherein the compressor is configured to compress the feed gas to a pressure of about 470 psia to about 510 psia, and wherein the expander is configured to expand the compressed feed gas to a pressure of about 380 psia to about 420 psia.
8. A plant that is configured to allow use of a pressure differential of a feed gas between a compressor and an expander to thereby allow for cooling the feed gas to a temperature that is sufficient to condense at least a portion of a first component of the feed gas and to thereby produce a partially depleted feed gas, wherein the plant is further configured to allow removal of a second component of the feed gas from the partially depleted feed gas using a pressure swing adsorption unit.
9. The plant of claim 8 wherein the pressure differential is between about 70 psia and about 130 psia.
10. The plant of claim 9 wherein the first component comprises a C 2 -C 5 hydrocarbon, and wherein the second component comprises hydrogen.
11. The plant of claim 10 wherein the plant is further configured to allow use of the partially depleted feed gas as refrigerant for cooling of the feed gas.
12. The plant of claim 10 wherein the pressure swing adsorption unit is a hydrogen pressure swing adsorption unit.
13. A method of separating a first component and a second component from a feed gas, comprising:
compressing the feed gas from pressure P 0 to pressure P 1 , and further compressing the feed gas from pressure P 1 to pressure P 2 ;
cooling the feed gas at pressure P 2 to a temperature sufficient to condense at least a portion of the first component of the feed gas;
separating the cooled feed gas in a first separator into a first vapor portion and a first liquid portion comprising the first component, and expanding the first vapor portion in an expander to pressure P 1 , thereby producing a cooled expanded product; and
separating the cooled and expanded product in a second separator into a second vapor portion comprising the second component and a second liquid portion comprising the first component, wherein the second vapor portion provides refrigeration for the cooling of the compressed feed gas at pressure P 2 .
14. The method of claim 13 wherein pressure P 0 is between about atmospheric pressure and about 200 psia.
15. The method of claim 14 wherein pressure P 1 is between about 200 psia and about 700 psia.
16. The method of claim 15 wherein pressure P 2 is between about 400 psia and about 800 psia.
17. The method of claim 13 the first component comprises a C 2 -C 5 hydrocarbon, and wherein the second component comprises hydrogen.