Hail tower for gas-vapor separations
A device and process for removing vapors from a gas is disclosed. A tower is provided. Sub-cooled pellets are distributed by the solids distributor across a horizontal cross-section of the tower. A process gas, comprising a product vapor, passes through the gas inlet. The product vapor and the sub-cooled pellets comprise the same material. The product vapor and the sub-cooled pellets agglomerate as the product vapor desublimates onto the sub-cooled pellets, forming product pellets and a vapor-depleted gas. A crushing device, a screening device, and a solids heat exchanger are provided. A portion of the product pellets are recycled as sub-cooled pellets to the solids distributor by crushing and screening the portion of the product pellets to the size distribution of the sub-cooled pellets and cooling the portion of the product pellets to produce the sub-cooled pellets.
1. A process for removing vapors from a gas comprising:
providing a tower comprising a solids distributor and a gas outlet in a top portion of the tower and a solids outlet and a gas inlet in a bottom portion of the tower;
passing sub-cooled pellets through the solids distributor, the solids distributor distributing the sub-cooled pellets across a horizontal cross-section of the tower, the sub-cooled pellets comprising a size distribution;
passing a process gas through the gas inlet, the process gas comprising a product vapor, the product vapor and the sub-cooled pellets comprising the same material;
agglomerating the product vapor and the sub-cooled pellets as the product vapor desublimates onto the sub-cooled pellets, forming product pellets and a vapor-depleted gas;
passing the product pellets out of the solids outlet and the vapor-depleted gas out of the gas outlet;
recycling a portion of the product pellets as sub-cooled pellets to the solids distributor by a process comprising:
crushing and screening the portion of the product pellets to the size distribution of the sub-cooled pellets; and,
cooling the portion of the product pellets in a solids heat exchanger to produce the sub-cooled pellets.
2. The process of claim 1 , wherein the process gas comprises flue gas, syngas, producer gas, natural gas, steam reforming gas, hydrocarbons, light gases, refinery off-gases, organic solvents, steam, ammonia, or combinations thereof.
3. The process of claim 2 , wherein the vapor comprises carbon dioxide, nitrogen oxide, sulfur dioxide, nitrogen dioxide, sulfur trioxide, hydrogen sulfide, hydrogen cyanide, water, mercury, hydrocarbons, or combinations thereof.
4. The process of claim 3 , wherein the solids distributor comprises a screen, a vibrating screen, a plurality of solid inlets situated evenly around a circumference of the top portion of the tower, or a combination thereof.
5. The process of claim 3 , further comprising providing an auger that passes the sub-cooled pellets to the solids distributor.
6. The process of claim 5 , further comprising providing a plurality of towers in series, each of the plurality of towers connected by augers that convey solids.
7. The process of claim 3 , further comprising providing a lock hopper after the solids outlet and a lock hopper before the solids distributor to maintain pressure in the tower while passing solids into and out of the tower.
8. The process of claim 3 , wherein the solids heat exchanger comprises a plate-type solid heat exchanger, a horizontal bulk solid heat exchanger, a fluidized-bed heat exchanger, or combinations thereof.
9. The process of claim 3 , wherein the crushing step is accomplished by a crusher, grinder, other comminution device, or combinations thereof.
10. The process of claim 9 , wherein the screening step is accomplished by a tumbler screen, a circle-throw vibrating screen, a high-frequency vibrating screen, a gyratory screen, a trommel screen, or combinations thereof.
11. A device for removing vapors from a gas comprising:
a tower comprising a solids distributor and a gas outlet in a top portion of the tower and a solids outlet and a gas inlet in a bottom portion of the tower, wherein:
sub-cooled pellets pass through the solids distributor, the solids distributor distributing the sub-cooled pellets across a horizontal cross-section of the tower, the sub-cooled pellets comprising a size distribution;
a process gas passes through the gas inlet, the process gas comprising a product vapor, the product vapor and the sub-cooled pellets comprising the same material;
the product vapor and the sub-cooled pellets agglomerate as the product vapor desublimates onto the sub-cooled pellets, forming product pellets and a vapor-depleted gas;
the product pellets pass out of the solids outlet and the vapor-depleted gas passes out of the gas outlet; and,
a crushing device, a screening device, and a solids heat exchanger, wherein a portion of the product pellets are recycled as sub-cooled pellets to the solids distributor by crushing and screening the portion of the product pellets in the crushing device and screening device, respectively, to the size distribution of the sub-cooled pellets and cooling the portion of the product pellets in a solids heat exchanger to produce the sub-cooled pellets.
12. The device of claim 11 , wherein the process gas comprises flue gas, syngas, producer gas, natural gas, steam reforming gas, hydrocarbons, light gases, refinery off-gases, organic solvents, steam, ammonia, or combinations thereof.
13. The device of claim 12 , wherein the vapor comprises carbon dioxide, nitrogen oxide, sulfur dioxide, nitrogen dioxide, sulfur trioxide, hydrogen sulfide, hydrogen cyanide, water, mercury, hydrocarbons, or combinations thereof.
14. The device of claim 11 , wherein the solids distributor comprises a screen, a vibrating screen, a plurality of solid inlets situated evenly around a circumference of the top portion of the tower, or a combination thereof.
15. The device of claim 11 , further comprising providing an auger that passes the sub-cooled pellets to the solids distributor.
16. The device of claim 15 , further comprising a plurality of towers in series, each of the plurality of towers connected by augers that convey solids.
17. The device of claim 11 , further comprising providing a lock hopper after the solids outlet and a lock hopper before the solids distributor to maintain pressure in the tower while passing solids into and out of the tower.
18. The device of claim 11 , wherein the solids heat exchanger comprises a plate-type solid heat exchanger, a horizontal bulk solid heat exchanger, a fluidized-bed heat exchanger, or combinations thereof.
19. The device of claim 11 , wherein the crushing device comprises a crusher, grinder, other comminution device, or combinations thereof.
20. The device of claim 19 , wherein the screening device comprises a tumbler screen, a circle-throw vibrating screen, a high-frequency vibrating screen, a gyratory screen, a trommel screen, or combinations thereof.