Low pressure re-absorber and its integration with sulfur-rich solvent flash drum or sulfur-rich solvent stripper in an absorption unit
A low pressure re-absorber is integrated with a sulfur-rich solvent flash drum or a sulfur-rich solvent stripping column in a solvent acid gas removal process that provides for sufficient sulfur concentration for the downstream sulfur recovery unit. In another aspect of the invention, carbon dioxide containing or carbon dioxide rich gas streams that are at a lower temperature relative to a lean solvent stream are used to cool those lean solvent streams and then optionally to cool other process streams, to save energy consumption.
1. A process for treating a gas stream using solvent comprising sending a feed gas stream to a sulfur absorption unit to produce a sulfur-rich solvent stream and a sulfur-lean gas stream, sending the sulfur-rich solvent stream to a re-absorber unit and then to a sulfur-rich solvent flash drum, sending the overhead gas from the sulfur-rich solvent flash drum to the re-absorber unit, and feeding a solvent stream to the top of the re-absorber unit to produce a re-absorber overhead gas stream that is lean in sulfur.
2. The process of claim 1 wherein the sulfur-lean gas stream from the sulfur absorption unit is sent to a carbon dioxide absorption section to further remove carbon dioxide.
3. The process of claim 1 wherein the process operates without nitrogen stripping in the re-absorber unit.
4. The process of claim 1 wherein the re-absorber unit and the sulfur-rich solvent flash drum operate at pressures so that there is no compressor required to send the overhead gas from the sulfur-rich solvent flash drum to the re-absorber unit.
5. The process of claim 1 wherein there is one or more heat exchangers and/or one or more coolers between the overhead of the sulfur-rich solvent flash drum and the re-absorber to cool the overhead gas from the sulfur-rich solvent flash drum.
6. The process of claim 1 wherein said re-absorber unit operates at a pressure in the range from about atmospheric pressure to about two-thirds of the operating pressure of the sulfur absorption unit.
7. The process of claim 1 wherein the solvent fed to the top of the re-absorber is a solvent that is lean in sulfur and loaded with carbon dioxide.
8. The process of claim 1 wherein the solvent fed to the top of the re-absorber is a solvent that is lean in sulfur and lean in carbon dioxide.
9. The process of claim 1 wherein a lean-rich heat exchanger is used in the liquid line from the re-absorber to the sulfur-rich solvent flash drum where the sulfur-rich solvent is heated by the lean solvent.
10. The process of claim 1 wherein the overhead gas stream from the re-absorber is used to cool the lean solvent and/or to cool other process streams.
11. A process for treating a gas stream using solvent comprising sending a feed gas stream to a sulfur absorption unit to produce a sulfur-rich solvent stream and a sulfur-lean gas stream, sending the sulfur-rich solvent stream to a separation unit, sending the overhead gas from the separation unit to a re-absorber unit, and feeding a solvent stream to the top of the re-absorber unit to produce a re-absorber overhead gas stream that is lean in sulfur wherein the solvent fed to the top of the re-absorber is a solvent that is lean in sulfur and loaded with carbon dioxide.