Compact radial platen arrangement for radiant syngas cooler
View Patent ↗A radiant synthesis gas (syngas) cooler used to contain and cool the synthesis gas produced by a coal gasification process used in an IGCC power plant employs a compact radial platen arrangement which is less prone to fouling and/or plugging issues.
1. A synthesis gas cooler for extracting heat from synthesis gas produced by a gasification process, comprising:
a shell having a synthesis gas inlet and a synthesis gas outlet;
a fluid-cooled flue contained within the shell for receiving synthesis gas;
a combination of at least one quench means and at least one convective heat transfer means, wherein the combination of the at least one quench means and the at least one convective heat transfer means extends from a position vertically above to a position adjacent the synthesis gas outlet, the combination of the at least one quench means and the at least one convective heat transfer means designed to form a quench zone designed to cool and humidify the synthesis gas prior to exit thereof through the synthesis gas outlet;
fluid-cooled radiant heat transfer surface partially extending within the flue for cooling the synthesis gas;
a dip tube, wherein the dip tube has an inner and outer surface; and
means for conveying the synthesis gas from the flue to the synthesis gas outlet,
wherein the combination of the dip tube, the at least one quench means and the at least one convective heat transfer means extends from a position vertically above the synthesis gas outlet through a position adjacent the synthesis gas outlet to a position vertically below the synthesis gas outlet,
wherein the at least one convective heat transfer means is formed from a plurality of horizontally oriented tubes, wherein the plurality of horizontally oriented tubes are formed so as to surround the outer surface of the dip tube,
wherein the at least one quench means is formed from a plurality of nozzles mounted to the inner surface of the dip tube, and
wherein the fluid-cooled radiant heat transfer surface comprises at least two sets of platens, a first set of platens having a first radial length and a second set of platens having a second radial length where the first radial length is longer than the second radial length.
2. The synthesis gas cooler according to claim 1 , wherein the first set and second set of platens are arranged in an alternating manner.
3. The synthesis gas cooler according to claim 1 , wherein the ratio of the radial lengths of the first set of platens to the radial lengths of the second set of platens is in the range of about 1:0.15 to about 1:0.8.
4. The synthesis gas cooler according to claim 3 , wherein the ratio of the radial lengths of the first set of platens to the radial lengths of the second set of platens is in the range of about 1:0.25 to about 1:0.75.
5. The synthesis gas cooler according to claim 4 , wherein the ratio of the radial lengths of the first set of platens to the radial lengths of the second set of platens is in the range of about 1:0.4 to about 1:0.6.
6. The synthesis gas cooler according to claim 1 , wherein the total number of radial platens is in the range of about 20 to about 60.
7. The synthesis gas cooler according to claim 6 , wherein the total number of radial platens is in the range of about 25 to about 55.
8. The synthesis gas cooler according to claim 7 , wherein the total number of radial platens is in the range of about 30 to about 50.
9. The synthesis gas cooler according to claim 8 , wherein the total number of radial platens is in the range of about 35 to about 45.
10. The synthesis gas cooler according to claim 1 , wherein the at least one quench means is formed from at least one quench spray level.
11. The synthesis gas cooler according to claim 10 , wherein at least one quench spray level is formed from multiple spray nozzles designed to supply a fluid into an area surrounding the at least one quench means.
12. The synthesis gas cooler according to claim 1 , wherein the at least one convective heat transfer means is formed from one or more banks of tubes wherein each individual tube is oriented in a horizontal plane.
13. A synthesis gas cooler for extracting heat from synthesis gas produced by a gasification process, comprising:
a shell having a synthesis gas inlet and a synthesis gas outlet;
a fluid-cooled flue contained within the shell for receiving synthesis gas;
a combination of at least one quench means and at least one convective heat transfer means, wherein the combination of the at least one quench means and the at least one convective heat transfer means extends from a position vertically above to a position adjacent the synthesis gas outlet, the combination of the at least one quench means and the at least one convective heat transfer means designed to form a quench zone designed to cool and humidify the synthesis gas prior to exit thereof through the synthesis gas outlet;
fluid-cooled radiant heat transfer surface partially extending within the flue for cooling the synthesis gas;
a dip tube, wherein the dip tube has an inner and outer surface; and
means for conveying the synthesis gas from the flue to the synthesis gas outlet,
wherein the combination of the dip tube, the at least one quench means and the at least one convective heat transfer means extends from a position vertically above the synthesis gas outlet through a position adjacent the synthesis gas outlet to a position vertically below the synthesis gas outlet,
wherein the at least one convective heat transfer means is formed from a plurality of horizontally oriented tubes, wherein the plurality of horizontally oriented tubes are formed so as to surround the outer surface of the dip tube,
wherein the at least one quench means is formed from a plurality of nozzles mounted to the inner surface of the dip tube, and
wherein the fluid-cooled radiant heat transfer surface comprises at least three sets of platens, a first set of platens having a first radial length, a second set of platens having a second radial length, and a third set of platens having a third radial length, where the first radial length is longer than the second radial length and the second radial length is longer than the third radial length.
14. The synthesis gas cooler according to claim 13 , wherein the first set, second set and third set of platens are arranged in an alternating manner.
15. The synthesis gas cooler according to claim 13 , wherein the ratio of the radial lengths of the first set of platens to the second set of platens to the third set of platens is in the range of about 1:0.5:0.15 to about 1:0.8:0.6.
16. The synthesis gas cooler according to claim 15 , wherein the ratio of the radial lengths of the first set of platens to the second set of platens to the third set of platens is in the range of about 1:0.6:0.25 to about 1:0.75:0.5.
17. The synthesis gas cooler according to claim 16 , wherein the ratio of the radial lengths of the first set of platens to the second set of platens to the third set of platens is in the range of about 1:0.66:0.5.
18. The synthesis gas cooler according to claim 13 , wherein the total number of radial platens is in the range of about 20 to about 60.
19. The synthesis gas cooler according to claim 18 , wherein the total number of radial platens is in the range of about 25 to about 55.
20. The synthesis gas cooler according to claim 19 wherein the total number of radial platens is in the range of about 30 to about 50.
21. The synthesis gas cooler according to claim 13 , wherein the at least one quench means is formed from at least one quench spray level.
22. The synthesis gas cooler according to claim 21 , wherein at least one quench spray level is formed from multiple spray nozzles designed to supply a fluid into an area surrounding the at least one quench means.
23. The synthesis gas cooler according to claim 13 , wherein the at least one convective heat transfer means is formed from one or more banks of tubes wherein each individual tube is oriented in a horizontal plane.
24. A synthesis gas cooler for extracting heat from synthesis gas produced by a gasification process, comprising:
a shell having a synthesis gas inlet and a synthesis gas outlet;
a fluid-cooled flue contained within the shell for receiving synthesis gas;
a combination of at least one quench means and at least one convective heat transfer means, wherein the combination of the at least one quench means and the at least one convective heat transfer means extends from a position vertically above to a position adjacent the synthesis gas outlet, the combination of the at least one quench means and the at least one convective heat transfer means designed to form a quench zone designed to cool and humidify the synthesis gas prior to exit thereof through the synthesis gas outlet;
fluid-cooled radiant heat transfer surface partially extending within the flue for cooling the synthesis gas;
a dip tube, wherein the dip tube has an inner and outer surface, and
means for conveying the synthesis gas from the flue to the synthesis gas outlet,
wherein the combination of the dip tube, the at least one quench means and the at least one convective heat transfer means extends from a position vertically above the synthesis gas outlet through a position adjacent the synthesis gas outlet to a position vertically below the synthesis gas outlet,
wherein the at least one convective heat transfer means is formed from a plurality of horizontally oriented tubes, wherein the plurality of horizontally oriented tubes are formed so as to surround the outer surface of the dip tube,
wherein the at least one quench means is formed from a plurality of nozzles mounted to the inner surface of the dip tube, and
wherein the fluid-cooled radiant heat transfer surface comprises at least four sets of platens, a first set of platens having a first radial length, a second set of platens having a second radial length, a third set of platens having a third radial length, and a fourth set of platens having a fourth radial length, where the first radial length is longer than the second radial length, the second radial length is longer than the third radial length, and the third radial length is longer than the fourth radial length.
25. The synthesis gas cooler according to claim 24 , wherein the ratio of the radial lengths of the first set of platens to the second set of platens to the third set of platens to the fourth set of platens is in the range of about 1:0.8:0.5:0.25 to about 1:0.5:0.3:0.15.
26. The synthesis gas cooler according to claim 24 , wherein the first set, the second set, the third set and the fourth set of platens are arranged in an alternating manner.
27. The synthesis gas cooler according to claim 24 , wherein the at least one quench means is formed from at least one quench spray level.
28. The synthesis gas cooler according to claim 27 , wherein at least one quench spray level is formed from multiple spray nozzles designed to supply a fluid into an area surrounding the at least one quench means.
29. The synthesis gas cooler according to claim 24 , wherein the at least one convective heat transfer means is formed from one or more banks of tubes wherein each individual tube is oriented in a horizontal plane.