초록 ▼

The invention provides systems and methods for separating ethane and heavier hydrocarbons from a natural gas stream. In aspects of the invention, an adsorption unit is integrated with a cryogenic gas processing plant in order to overcome methane recovery limitations by sending the tail gas from the

The invention provides systems and methods for separating ethane and heavier hydrocarbons from a natural gas stream. In aspects of the invention, an adsorption unit is integrated with a cryogenic gas processing plant in order to overcome methane recovery limitations by sending the tail gas from the adsorption unit to the cryogenic gas processing plant to recover methane that would otherwise be lost.

대표청구항 ▼

1. A system for treating raw natural gas comprising: (i) a raw natural gas stream formed by diverting a fraction of a main raw natural gas feed stream;(ii) an adsorption unit configured to receive the raw natural gas stream and produce a first stream comprising methane and enriched in natural gas li

1. A system for treating raw natural gas comprising: (i) a raw natural gas stream formed by diverting a fraction of a main raw natural gas feed stream;(ii) an adsorption unit configured to receive the raw natural gas stream and produce a first stream comprising methane and enriched in natural gas liquids and a second stream comprising methane and depleted in natural gas liquids;(iii) a compressor or pump configured to receive and increase the pressure of the first stream to produce a gas processing plant feed stream; and(iv) a gas processing plant configured to receive the gas processing plant feed stream, wherein the gas processing plant comprises: (a) a secondary main raw natural gas feed stream formed by the portion of the main raw natural gas feed stream remaining after diversion of the raw natural gas feed stream;(b) a first heat exchanger configured to receive and cool the secondary main raw natural gas feed stream to produce a cooled feed stream;(c) a separation unit configured to receive the cooled feed stream and separate it into a vapor feed stream and a liquid feed stream;(d) an expander configured to receive and expand a portion of the vapor feed stream to form a main demethanizer feed stream;(e) a second heat exchanger configured to receive and condense a portion of the vapor feed stream, a portion of the cooled feed stream, a portion of a demethanizer overhead stream, or any combination thereof to form a demethanizer reflux stream; and(f) a demethanizer configured to receive the main demethanizer feed stream, the liquid feed stream, and the methanizer reflux stream and produce the demethanizer overhead stream comprising methane and a demethanizer bottoms stream comprising natural gas liquids; andwherein the system further comprises a third heat exchanger configured to receive and cool the gas processing plant feed stream before the gas processing plant feed stream is combined with the liquid feed stream to form a combined demethanizer feed stream and the combined demethanizer feed stream is fed directly to the demethanizer. 2. The system of claim 1, wherein the raw natural gas stream comprises at least 60% methane by volume. 3. The system of claim 1, wherein the raw natural gas stream comprises less than 2% carbon dioxide by volume. 4. The system of claim 1, wherein the raw natural gas stream comprises less than 100 ppm water vapor by volume. 5. The system of claim 1, wherein the pressure of the raw natural gas stream is greater than 700 psia. 6. The system of claim 1, wherein the adsorption unit is a pressure swing adsorption unit. 7. The system of claim 6, wherein the lowest pressure in the pressure swing adsorption unit during any single cycle is 1 atm. 8. The system of claim 1, wherein the beds of the adsorption unit have a length to diameter ratio less than 1.5.