System for separating gas
An improved system for separating gas from a process stream by providing a stripping unit at the overhead stream of a fractionation column to selectively and effectively remove the gas using a stripping fluid without providing a dedicated light-ends separations unit. The stripper unit may be connected to the reflux drum at the overhead stream. The system for separating gas further achieves greater thermodynamic efficiency by means of a split column design using mechanical vapor recompression with the reboiler and condenser integrated in a falling-film evaporator- or thermosiphon-type vapo-condenser.
1. A system for separating a gas from a process stream, the system comprising:
a separation unit configured to receive the process stream of a chemical process and to separate at least one component of the process stream, the separation unit comprising a first heat exchanger located at an overhead portion of the separation unit and receiving an overhead stream of the process stream from the overhead portion of the separation unit, the first heat exchanger being configured for condensing at least a portion of the overhead stream of the process stream;
a stripper unit configured to receive the condensed portion of the overhead stream of the process stream from the first heat exchanger, the stripper unit being configured for separating the gas from the condensed portion of the overhead stream of the process stream by introducing at least one stripping fluid thereunto; and
wherein the separation unit is a split column comprising a relatively high-pressure column and a relatively low-pressure column, the system further comprising a second heat exchanger, wherein the first heat exchanger is located at an overhead portion of the relatively low-pressure column, and the second heat exchanger is located at an overhead portion of the relative high-pressure column.
2. The system for separating a gas from a process stream of claim 1 , wherein the process stream comprises CO 2 , water, and methanol.
3. The system for separating a gas from a process stream of claim 1 , wherein the chemical process is a methanol synthesis process.
4. The system for separating a gas from a process stream of claim 3 , wherein the chemical process is a methanol synthesis process that synthesizes methanol from CO 2 and H 2 .
5. The system for separating a gas from a process stream of claim 1 , wherein the at least one stripping fluid comprises at least one of gaseous N 2 or H 2 .
6. The system for separating a gas from a process stream of claim 1 , wherein at least one waste gas stream comprising a portion of the at least one stripping fluid and a portion of the separated gas is generated.
7. The system for separating a gas from a process stream of claim 6 , wherein the at least one waste gas stream is generated from the stripper unit and is recycled upstream.
8. The system for separating a gas from a process stream of claim 6 , wherein the at least one waste gas stream is scrubbed of entrained methanol before venting to atmosphere.
9. The system for separating a gas from a process stream of claim 6 , wherein the at least one stripping fluid is a reactant of the chemical process.
10. The system for separating a gas from a process stream of claim 1 , wherein the stripper unit comprises a gas sparger.
11. The system for separating a gas from a process stream of claim 1 , wherein the stripper unit comprises a reflux drum.
12. The system for separating a gas from a process stream of claim 11 , wherein the stripper unit comprising the reflux drum comprises an integrated stripper/reflux drum which comprises a stripper section and the reflux drum.
13. The system for separating a gas from a process stream of claim 11 , wherein a reflux stream and a non-reflux stream extend and flow downstream from the reflux drum, wherein the separation unit receives the reflux stream.
14. The system for separating a gas from a process stream of claim 1 , wherein the stripper unit is associated with the relatively low-pressure column, the system further comprising a second stripper unit, wherein the second stripper unit is associated with the relatively high-pressure column.
15. The system for separating a gas from a process stream of claim 1 , wherein the second heat exchanger located at the overhead portion of the relatively high-pressure column also serves as a reboiler for a bottom stream of the relatively low-pressure column.
16. A system for separating a gas from a process stream, the system comprising:
a separation unit configured to receive the process stream of a chemical process and to separate at least one component of the process stream, the separation unit comprising a first heat exchanger located at an overhead portion of the separation unit and receiving an overhead stream of the process stream from the overhead portion of the separation unit, the first heat exchanger being configured for condensing at least a portion of the overhead stream of the process stream;
a stripper unit configured to receive the condensed portion of the overhead stream of the process stream from the first heat exchanger, the stripper unit being configured for separating the gas from the condensed portion of the overhead stream of the process stream by introducing at least one stripping fluid thereunto; and
wherein the separation unit is a split column comprising a relatively high-pressure column and a relatively low-pressure column, the system further comprising a second heat exchanger, wherein the first heat exchanger is located at an overhead portion of the relatively low-pressure column, and the second heat exchanger is located at an overhead portion of the relative high-pressure column to condense an overhead stream of the relatively high-pressure column, wherein the second heat exchanger also serves as a reboiler for a bottom stream of the relatively low-pressure column.
17. A method for separating a gas from a process stream, the method comprising the steps of:
providing a separation unit configured to receive a process stream of a chemical process and to separate at least one component of the process stream, wherein the separation unit is a split column comprising a relatively high-pressure column and a relatively low-pressure column;
providing a first heat exchanger at an overhead portion of the relatively low-pressure column of the separation unit, and a second heat exchanger at an overhead portion of the relative high-pressure column, the first heat exchanger being configured for condensing at least a portion of an overhead stream of the process stream from the relatively low-pressure column; and
providing a stripper unit configured to receive the condensed portion of the overhead stream of the process stream from the first heat exchanger, the stripper unit separating a gas from the condensed portion of the overhead stream by introducing at least one stripping fluid thereto.
18. The method for separating a gas from a process stream of claim 17 , wherein the second heat exchanger located at the overhead portion of the relatively high-pressure column also serves as a reboiler for a bottom stream of the relatively low-pressure column.
19. The method for separating a gas from a process stream of claim 17 , wherein a second stripper unit is provided associated with the relatively high-pressure column, the method further comprising providing a condensed portion of an overhead stream of the process stream from the second heat exchanger, the second stripper unit separating a gas from the condensed portion of the overhead stream from the second heat exchanger by introducing at least one stripping fluid thereto.
20. The method for separating a gas from a process stream of claim 17 , wherein at least one of the stripper unit or the second stripper unit comprises a reflux drum integrated with the stripper unit or the second stripper unit.