초록 ▼

The present invention relates to methods and apparatuses for the operation of a distillation tower containing a controlled freezing zone and at least one distillation section. The process and tower design are utilized for the additional recovery of hydrocarbons from an acid gas. In this process, a s

The present invention relates to methods and apparatuses for the operation of a distillation tower containing a controlled freezing zone and at least one distillation section. The process and tower design are utilized for the additional recovery of hydrocarbons from an acid gas. In this process, a separation process is utilized in which a multi-component feedstream is introduced into an apparatus that operates under solids forming conditions for at least one of the feedstream components. The freezable component, although typically CO2, H2S, or another acid gas, can be any component that has the potential for forming solids in the separation system. A dividing wall is added to at least a portion of the lower distillation section of the apparatus to effect the separation of at least some fraction of the hydrocarbons in that portion of the tower.

대표청구항 ▼

1. A method for the separation of a feedstream in a distillation tower with a controlled freezing zone comprising: feeding a mixture of at least one acid gas and methane to a lower distillation zone comprising a dividing wall, which extends substantially vertically through the lower distillation zon

1. A method for the separation of a feedstream in a distillation tower with a controlled freezing zone comprising: feeding a mixture of at least one acid gas and methane to a lower distillation zone comprising a dividing wall, which extends substantially vertically through the lower distillation zone to divide the lower distillation zone into a pre-fractionation zone and a product zone;producing in the lower distillation zone an enriched acid gas liquid bottoms stream and a freezing zone vapor feedstream at a temperature and pressure at which substantially no carbon dioxide solids are formed;contacting in the controlled freezing zone the freezing zone vapor feedstream with at least one freezing zone liquid feedstream containing methane at a temperature and pressure wherein both solids containing carbon dioxide and a methane-enriched vapor stream are formed;removing in an upper distillation section an acid gas component from the methane-enriched vapor stream;separating the enriched acid gas liquid bottoms stream into a liquid acid gas stream and a hydrocarbon stream;recovering from a draw tray of the lower distillation zone a portion of the hydrocarbon stream and concentrating the portion of the hydrocarbon stream using an adsorption or membrane system to produce an enriched hydrocarbon product stream and an enriched sour gas stream; andreintroducing the enriched sour gas stream into the lower distillation section. 2. The method of claim 1, wherein separating the enriched acid gas liquid bottoms stream comprises distilling the enriched acid gas liquid bottoms stream. 3. The method of claim 1, wherein the at least one acid gas comprises a mixture of hydrogen sulfide and carbon dioxide. 4. The method of claim 1, wherein the enriched sour gas stream is reintroduced into a prefractionation zone of the lower distillation column. 5. The method of claim 1, wherein the enriched hydrocarbon product stream is further concentrated using a pressure swing adsorption system. 6. A method for the separation of a sour gas feedstream containing methane and carbon dioxide acid gas in a distillation tower comprising: maintaining a lower distillation zone comprising a dividing wall, which extends substantially vertically through the lower distillation zone to divide the lower distillation zone into a pre-fractionation zone and a product zone, said lower distillation zone configured to produce an enriched carbon dioxide liquid bottoms stream and a freezing zone vapor feed stream;maintaining a controlled freezing zone configured to contact the freezing zone vapor feedstream with at least one freezing zone liquid feedstream containing methane at a temperature and pressure whereby both solids-containing carbon dioxide and a methane-enriched vapor stream are formed in the controlled freezing zone;introducing the sour gas feedstream containing methane and carbon dioxide gas into the lower distillation zone;producing the enriched carbon dioxide liquid bottoms stream and the freezing zone vapor feedstream;introducing the freezing zone vapor feedstream into the controlled freezing zone;contacting in the controlled freezing zone the freezing zone vapor feedstream with the at least one freezing zone liquid feedstream;forming in the controlled freezing zone the solids containing carbon dioxide and the methane-enriched vapor stream;melting the solids containing carbon dioxide and introducing a liquid stream containing the melted solids into the lower distillation zone;separating the liquid stream containing the melted solids into a liquid acid gas stream and a hydrocarbon stream;recovering from a draw tray of the lower distillation zone a portion of the hydrocarbon stream and concentrating the portion of the hydrocarbon stream using an adsorption or membrane system to produce an enriched hydrocarbon product stream and an enriched sour gas stream; andreintroducing the enriched sour gas stream into the lower distillation section. 7. The method of claim 6, further comprising: condensing at least a portion of the methane-enriched vapor stream and forming the at least one freezing zone liquid feedstream with at least a portion of the condensed vapor stream; andrecovering at least a portion of the remainder of the methane-enriched vapor stream as a methane-enriched product stream. 8. The method of claim 6, wherein the lower distillation zone comprises a dividing wall column configured to separate the feedstream containing methane and carbon dioxide into a low boiler fraction, an intermediate boiler fraction, and a high boiler fraction. 9. The method of claim 8, wherein the intermediate boiler fraction comprises the hydrocarbon stream. 10. The method of claim 8, wherein the higher boiler fraction comprises the liquid acid gas stream. 11. The method of claim 8, wherein the low boiler fraction comprises methane. 12. The method of claim 6, further comprising: maintaining an upper distillation zone configured to produce the at least one freezing zone liquid feedstream and an overhead vapor stream and operated at a temperature and a pressure at which substantially no carbon dioxide solids are produced within the upper distillation zone;condensing at least a portion of the overhead vapor stream and recycling at least a portion of the condensed overhead vapor stream as reflux in the upper distillation zone; andrecovering at least a portion of the remainder of the overhead vapor stream as a methane-enriched product stream. 13. A distillation tower for the separation of a feedstream containing methane and carbon dioxide acid gas comprising: a lower distillation zone comprising: a dividing wall, which extends substantially vertically through the lower distillation zone to divide the lower distillation zone into a pre-fractionation zone and a product zone, both of the zones opening at both ends of the dividing wall in common zones above and below the dividing wall, wherein an enriched carbon dioxide liquid bottoms stream and a freezing zone vapor feedstream are produced at a temperature and pressure at which substantially no carbon dioxide solids are formed;a side draw tray outlet configured to receive a hydrocarbon stream separated from the enriched carbon dioxide liquid bottoms stream; andan adsorption or membrane device in fluid communication with the side draw outlet, wherein the adsorption or membrane device is configured to separate the hydrocarbon stream into an enriched hydrocarbon product stream and an enriched sour gas stream;a reintroduction inlet in fluid communication with the absorption or membrane device to reintroduce the enriched sour gas stream into the lower distillation section;an inlet to the lower zone of the distillation tower for a feedstream containing methane and carbon dioxide acid gas;a controlled freezing zone wherein a freezing zone liquid feedstream containing methane is contacted with the freezing zone vapor feedstream at a temperature and pressure wherein both solids containing carbon dioxide and a methane-enriched vapor stream are formed; andan upper distillation section wherein an acid gas component from the methane-enriched vapor stream is removed. 14. The distillation tower of claim 13, wherein the dividing wall comprises a corrosion-resistant material. 15. The distillation tower of claim 14, wherein the corrosion resistant-material is polytetrafluoroethylene. 16. The distillation tower of claim 13, wherein the dividing wall comprises a corrosion-resistant metallic material. 17. The distillation tower of claim 16, wherein the corrosion-resistant metallic material comprises a chromium-nickel containing stainless steel. 18. The distillation tower of claim 13, wherein the lower distillation zone comprises between eight and twelve theoretical stages. 19. The distillation tower of claim 13, wherein the lower distillation zone comprises at least two thermally-coupled sections. 20. The distillation tower of claim 13, wherein the dividing wall is convex relative to the pre-fractionation zone. 21. The distillation tower of claim 13, wherein the dividing wall is concave relative to the pre-fractionation zone. 22. The distillation tower of claim 13, wherein the adsorption or membrane device comprises adsorptive materials selective for the enriched hydrocarbon product stream. 23. The distillation tower of claim 22, wherein the adsorptive materials are selected from the group consisting of silica gels, zeolites, or composites thereof. 24. The distillation tower of claim 13, wherein the adsorption or membrane device comprises a permeable membrane selective for the hydrocarbon product stream.