Coke plant including exhaust gas sharing
View Patent ↗A coke plant includes multiple coke ovens where each coke oven is adapted to produce exhaust gases, a common tunnel fluidly connected to the plurality of coke ovens and configured to receive the exhaust gases from each of the coke ovens, multiple standard heat recovery steam generators fluidly connected to the common tunnel where the ratio of coke ovens to standard heat recovery steam generators is at least 20:1, and a redundant heat recovery steam generator fluidly connected to the common tunnel where any one of the plurality of standard heat recovery steam generators and the redundant heat recovery steam generator is adapted to receive the exhaust gases from the plurality of ovens and extract heat from the exhaust gases and where the standard heat recovery steam generators and the redundant heat recovery steam generator are all connected in parallel with each other.
1. A system for coking coal comprising:
a plurality of coke ovens, wherein each coke oven includes: an oven chamber; an uptake duct in fluid communication with the oven chamber, the uptake duct being configured to receive exhaust gases from the oven chamber; an uptake damper in fluid communication with the uptake duct, the uptake damper being positioned by an actuator to any one of a plurality of positions including fully opened and fully closed;
a common tunnel fluidly connected to the plurality of coke ovens and being configured to receive the exhaust gases from each of the coke ovens;
a plurality of standard heat recovery steam generators fluidly connected to the common tunnel, wherein a heat recovery steam generator damper is in fluid communication with each standard heat recovery steam generator and configured to be positioned by an actuator to any one of a plurality of positions between open and closed;
a redundant heat recovery steam generator fluidly connected to the common tunnel and including a heat recovery steam generator damper in fluid communication with the redundant heat recovery steam generator that is configured to be positioned by an actuator to any one of a plurality of positions between open and closed;
wherein the standard heat recovery steam generators, the redundant heat recovery steam generator, and the associated heat recovery steam generator dampers are all fluidly connected in parallel with each other and configured to engage a gas sharing mode wherein exhaust gases are rerouted through the common tunnel from at least one of the standard heat recovery steam generators or the redundant heat recovery steam generator to other standard heat recovery steam generators or the redundant heat recovery steam generator; and
a controller configured to initiate the gas sharing mode by providing a position instruction to at least one of the actuators to cause the at least one actuator to alter the position of at least one of the uptake dampers or heat recovery steam generator dampers to thereby maintain a target draft within the system for coking coal when an operating capacity of at least one of the plurality of standard heat recovery steam generators is reduced.
2. The system for coking coal of claim 1 , wherein, during the gas sharing mode, operating conditions at a location within the common tunnel comprises a common tunnel draft of at least 0.7 inches of water.
3. The system for coking coal of claim 2 , wherein, during the gas sharing mode, operating conditions within each of the plurality of ovens comprises an oven draft of at least 0.1 inches of water.
4. The system for coking coal of claim 2 , wherein, during the gas sharing mode, operating conditions at the location within the common tunnel comprises a common tunnel draft of at least 1.0 inches of water.
5. The system for coking coal of claim 4 , wherein, during the gas sharing mode, operating conditions within each of the plurality of ovens comprises an oven draft of at least 0.1 inches of water.
6. The system for coking coal of claim 2 , wherein, during the gas sharing mode, operating conditions at the location within the common tunnel comprises a common tunnel draft of at least 2.0 inches of water.
7. The system for coking coal of claim 6 , wherein, during the gas sharing mode, operating conditions within each of the plurality of ovens comprises an oven draft of at least 0.1 inches of water.
8. The system for coking coal of claim 1 , wherein each of the plurality of coke ovens comprises,
a pressure sensor configured to detect an oven draft, the controller being in communication with the at least one actuator and with the pressure sensor, the controller configured to provide position instructions to the at least one actuator in response to the oven draft detected by the pressure sensor.
9. The system for coking coal of claim 8 , wherein the controller is configured to provide the position instruction to the at least one actuator to cause the at least one actuator to alter the position of an uptake damper to thereby maintain the oven draft at least at 0.1 inches of water.
10. The system for coking coal of claim 9 , wherein the operating conditions at a location within the common tunnel comprises a common tunnel draft of at least 0.7 inches of water.
11. The system for coking coal of claim 9 , wherein the operating conditions at a location within the common tunnel comprises a common tunnel draft of at least 1.0 inches of water.
12. The system for coking coal of claim 9 , wherein the operating conditions at a location within the common tunnel comprises a common tunnel draft of at least 2.0 inches of water.
13. The system for coking coal of claim 1 , further comprising:
a plurality of crossover ducts, wherein each crossover duct is connected to the common tunnel at an intersection and each crossover duct is connected to one of the group consisting of the standard heat recovery steam generators and the redundant heat recovery steam generator.
14. The system for coking coal of claim 13 , wherein the operating conditions within each of the plurality of ovens comprises an oven draft of at least 0.1 inches of water.
15. The system for coking coal of claim 14 , wherein the operating conditions at one or more of the intersections comprises an intersection draft of at least 0.7 inches of water.
16. The system for coking coal of claim 14 , wherein the operating conditions at one or more of the intersections comprises an intersection draft of at least 1.0 inches of water.
17. The system for coking coal of claim 14 , wherein the operating conditions at one or more of the intersections comprises an intersection draft of at least 2.0 inches of water.
18. The system for coking coal of claim 1 , further comprising:
a second plurality of coke ovens, wherein each coke oven is adapted to produce exhaust gases;
a second common tunnel fluidly connected to the second plurality of coke ovens and being configured to receive the exhaust gases from each of the second plurality of coke ovens; and
a crossover duct connected to the common tunnel, the second common tunnel, the plurality of standard heat recovery steam generators, and the redundant heat recovery steam generator.
19. The system for coking coal of claim 18 , wherein the ratio of coke ovens to standard heat recovery steam generators is at least 60:1.
20. The system for coking coal of claim 1 , further comprising:
a second plurality of coke ovens, wherein each coke oven is adapted to produce exhaust gases;
a second common tunnel fluidly connected to the second plurality of coke ovens and being configured to receive the exhaust gases from each of the second plurality of coke ovens; and
a first crossover duct connected to the first common tunnel, the plurality of standard heat recovery steam generators, and the redundant heat recovery steam generator; and
a second crossover duct connected to the second common tunnel, the plurality of standard heat recovery steam generators, and the redundant heat recovery steam generator.
21. The system for coking coal of claim 1 , further comprising:
a crossover duct, wherein each of the standard heat recovery steam generators and the redundant heat recovery steam generator is fluidly connected to the common tunnel by the crossover duct.
22. The system for coking coal of claim 21 , wherein the ratio of coke ovens to standard heat recovery steam generators is at least 60:1.
23. The system for coking coal of claim 1 , wherein the redundant heat recovery steam generator is one of a plurality redundant heat recovery steam generators fluidly connected to the common tunnel.
24. A system for coking coal comprising:
a plurality of coke ovens, wherein each coke oven includes: an oven chamber; an uptake duct in fluid communication with the oven chamber, the uptake duct being configured to receive exhaust gases from the oven chamber; an uptake damper in fluid communication with the uptake duct, the uptake damper being positioned by an actuator to any one of a plurality of positions including fully opened and fully closed;
a common tunnel fluidly connected to the plurality of coke ovens and being configured to receive the exhaust gases from each of the coke ovens;
a plurality of standard heat recovery steam generators fluidly connected to the common tunnel; wherein a heat recovery steam generator damper is in fluid communication with each standard heat recovery steam generator and configured to be positioned by an actuator to any one of a plurality of positions between open and closed;
a redundant heat recovery steam generator fluidly connected to the common tunnel and including a heat recovery steam generator damper in fluid communication with the redundant heat recovery steam generator that is configured to be positioned by an actuator to any one of a plurality of positions between open and closed;
wherein the standard heat recovery steam generators, the redundant heat recovery steam generator, and the associated heat recovery steam generator dampers are all fluidly connected in parallel with each other and configured to engage a gas sharing mode wherein exhaust gases are rerouted through the common tunnel from at least one of the standard heat recovery steam generators or the redundant heat recovery steam generator to other standard heat recovery steam generators or the redundant heat recovery steam generator;
a plurality of crossover ducts, wherein each of the heat recovery steam generators and the redundant heat recovery steam generator is connected to the common tunnel by one of the plurality of crossover ducts and wherein the ratio of ovens to crossover ducts is at least 50:3; and
a controller configured to initiate the sharing mode by providing a position instruction to at least one of the actuators to cause the at least one actuator to alter the position of at least one of the uptake dampers or heat recovery steam generator dampers to thereby maintain a target draft within the system for coking coal when an operating capacity of at least one of the plurality of standard heat recovery steam generators is reduced.
25. The system for coking coal of claim 24 , wherein the ratio of ovens to crossover ducts is at least 60:1.