Regenerative fume-incinerator with on-line burn-out and wash-down system

• US 20040123880A1
• Filed: 12/09/2003
• Published: 07/01/2004
• Est. Priority Date: 12/10/2002
• Status: Active Grant

• Current Assignee: Pro-Environmental Incorporated
• Original Assignee: Pro-Environmental Incorporated
• Inventors: Chiles, Joseph David, Kirkland, John G., Cabarlo, Agustin, Vij, Anu D., Yerkes, Jeffrey J.
• Granted Patent: US 7,017,592 B2
• Time in Patent Office: Days
• US Class Current: 134/22.18
• CPC Class Codes: F23G 7/068 using regenerative heat recovery means

Abstract

A method and apparatus for on-line wash-down of a heat sink media bed in a regenerative heat exchanger of a regenerative fume incinerator is disclosed. When a heat sink media bed requires cleaning, the selected regenerative heat exchanger is cooled while the remaining regenerative heat exchangers are operated in their normal mode of operation. When the selected media bed reaches a temperature which is less than the thermal-shock temperature of the media material, a cleaning fluid is sprayed on the media surfaces through spray-pipes which are installed within the media bed. After the media surfaces are washed down, the selected regenerative heat-exchanger is reverted back to its normal mode of operation. The regenerative heat exchanger can also be automatically burnt-out of deposited gasifiable matter prior to the wash-down. Random or sequential burn-out and wash-down of the regenerative heat-exchangers can be performed. The apparatus can also be used to suppress fires within the media bed by spraying cold water on the media bed when a rapid rise in temperature is detected within the media bed.

Claims

1. ) A Regenerative Fume Incinerator for cleaning a polluted gas, the Regenerative Fume Incinerator comprising:

a combustion chamber which receives the polluted gas and oxidizes the oxidizable pollutants therein to produce a cleansed gas; and

a plurality of regenerative heat exchangers, each regenerative heat exchanger comprising

a regenerative heat exchanger compartment having a hot end and a cold end, the hot end of the regenerative heat exchanger compartment configured for fluid communication with the combustion chamber, the regenerative heat exchanger compartment further comprising a heat sink media bed located in between the hot and cold ends of the regenerative heat exchanger compartment in the path of flow of the polluted gas and the cleansed gas and a deposited matter removal means for dislodging deposited matter from the surface of the heat sink media within the regenerative heat exchanger compartment, the deposited matter removal means comprising at least one spray pipe containing a cleaning-fluid, the cleaning fluid being at a pressure greater than the gas pressure within the regenerative heat exchanger compartment, the spray pipe located within the heat sink media bed to direct the cleaning fluid therein toward at least some of the surfaces of the heat sink media to physically dislodge the deposited matter thereon, and a flow control means for the selective introduction of the polluted gas into the regenerative heat exchanger compartment and for the selective removal of the cleansed gas from the regenerative heat exchanger compartment, the flow control means being located at the cold end of the regenerative heat exchanger and configured for fluid communication with the cold end of the regenerative heat exchanger compartment.

2. ) The Regenerative Fume Incinerator of claim 1, which further comprises a first temperature measuring means located within the heat sink media bed.

3. ) The Regenerative Fume Incinerator of claim 1, wherein the heat sink media bed is divided into an upper heat sink media bed section and a lower heat sink media bed section and the deposited matter removal means is located in the space between the upper heat sink media bed section and the lower heat sink media bed section.

4. ) The Regenerative Fume Incinerator of claim 3 which further comprises a first temperature measuring means located within the space between the upper heat sink media bed section and the lower heat sink media bed section.

5. ) The Regenerative Fume Incinerator of claim 1, wherein the cleaning fluid is water.

6. ) The Regenerative Fume Incinerator of claim 1, wherein the cleaning fluid is steam.

7. ) The Regenerative Fume Incinerator of claim 1, wherein the cleaning fluid is air.

8. ) The Regenerative Fume Incinerator of claim 1, which further comprises a second temperature measuring means located in the cold end of the regenerative heat exchanger compartment.

9. ) The Regenerative Fume Incinerator of claim 2, which further comprises a second temperature measuring means located in the cold end of the regenerative heat exchanger compartment.

10. ) The Regenerative Fume Incinerator of claim 2 which further comprises a control means to perform on-line wash-down of the heat sink media in at least one of the regenerative heat exchangers of the Regenerative Fume Incinerator, the Regenerative Fume Incinerator control means comprising an algorithm to perform the following steps:

(a) freeze the regenerative heat exchanger in a heat sink media cooling mode of operation while allowing the other regenerative heat exchangers to operate in their normal modes of operation,

(b) read the measured temperature from the first temperature measuring means and continue to freeze the regenerative heat exchanger in the heat sink media cooling mode of operation until the measured temperature is less than a predetermined value,

(c) operate the flow control means of the selected regenerative heat exchanger to substantially stop the flow of the polluted and cleansed gases into and out of the regenerative heat exchanger,

(d) start the flow of the cleaning fluid into the spray pipe of the deposited matter removal means in the regenerative heat exchanger to dislodge at least some of the deposited matter from the surface of the heat sink media within the selected regenerative heat exchanger,

(e) stop the flow of the cleaning fluid into the spray-pipe of the deposited matter removal means of the regenerative heat exchanger after a predetermined period of time.

(f) operate the flow control means to maintain the regenerative heat exchanger in a heat sink media heating mode of operation while monitoring the temperature measured by the first temperature measuring means of the regenerative heat exchanger, and

(g) revert the regenerative heat exchanger back into the normal mode of operation when the temperature measured within the heat sink media of the regenerative heat exchanger by the first temperature measuring means of the regenerative heat exchanger reaches a predetermined level.

11. ) The Regenerative Fume Incinerator of claim 10, wherein the algorithm of the Regenerative Fume Incinerator control means automatically repeats sequential steps (a) to (g) in at least one of the remaining regenerative heat exchangers.

12. ) The Regenerative Fume Incinerator of claim 10, wherein the algorithm of the Regenerative Fume Incinerator control means automatically repeats sequential steps (a) to (g) in each of the remaining regenerative heat exchangers.

13. ) The Regenerative Fume Incinerator of claim 10, further comprising a second temperature measuring means located in the cold end of the regenerative heat exchanger compartment and wherein the algorithm further performs steps (i) to (iv) described below prior to performing steps (a) to (g):

(i) freeze the regenerative heat exchanger in a heat sink media heating mode of operation while maintaining the other regenerative heat exchangers in their normal mode of operation,

(ii) read the measured temperature from the second temperature sensing means of the regenerative heat exchanger and continue to freeze the selected regenerative heat exchanger in the heat sink media heating mode of operation while the measured temperature is less than a predetermined value,

(iii) stop the operation of the regenerative heat exchanger in the heat sink media heating mode of operation when the measured temperature is at least equal to the predetermined temperature, and

(iv) operate the regenerative heat exchanger compartment in a heat sink media cooling mode of operation.

14. ) The Regenerative Fume Incinerator of claim 13, wherein the regenerative heat exchanger control means automatically repeats sequential steps (i) to (iv) and (a) to (g) in at least one of the remaining regenerative heat exchangers.

15. ) The Regenerative Fume Incinerator of claim 13, wherein the regenerative heat exchanger control means automatically repeats sequential steps (i) to (iv) and (a) to (g) in each of the remaining regenerative heat exchanger s.

16. ) A Regenerative Fume Incinerator control system to perform on-line wash-down of the heat sink media in a regenerative heat exchanger of a Regenerative Fume Incinerator, the regenerative heat exchanger having at least one cleaning fluid spray-pipe and a first temperature measuring means, both located within the heat sink media bed of the regenerative heat exchanger, the regenerative heat exchanger further having a second temperature measuring means located under the heat sink media bed of the regenerative heat exchanger, the regenerative heat exchanger further having a flow control means for the selective introduction of the polluted gas into the regenerative heat exchanger compartment and for the selective removal of the cleansed gas from the regenerative heat exchanger compartment, the flow control means being located at the cold end of the regenerative heat exchanger and configured for fluid communication with the cold end of the regenerative heat exchanger compartment, the Regenerative Fume Incinerator control system comprising an algorithm to perform the following steps:

(a) freeze the regenerative heat exchanger in a heat sink media cooling mode of operation while maintaining the other regenerative heat exchangers in their normal mode of operation,

(b) read the measured temperature from the first temperature measuring means and continue to freeze the selected regenerative heat exchanger in the heat sink media cooling mode of operation until the measured temperature is less than a predetermined value,

(c) operate the flow control means of the regenerative heat exchanger to stop the flow of the polluted and cleansed gases into and out of the regenerative heat exchanger,

(d) start the flow of the cleaning fluid into the spray-pipe of the regenerative heat exchanger to dislodge the deposited matter from the surface of the heat sink media within the regenerative heat exchanger,

(e) stop the flow of the cleaning fluid into the spray-pipe of the regenerative heat exchanger after a predetermined period of time,

(f) operate the flow control means of the regenerative heat exchanger in the heat sink media heating mode of operation while monitoring the temperature measured by the first temperature measuring means within the regenerative heat exchanger, and

(g) revert the selected regenerative heat exchanger back into the normal mode of operation when the temperature measured within the heat sink media of the regenerative heat exchanger by the first temperature measuring means of the regenerative heat exchanger reaches a predetermined value.

17. ) The Regenerative Fume Incinerator control system of claim 16, wherein the algorithm automatically repeats sequential steps (a) to (g) in at least one of the remaining regenerative heat exchangers.

18. ) The Regenerative Fume Incinerator control system of claim 16, wherein the algorithm automatically repeats sequential steps (a) to (g) in each of the remaining regenerative heat exchangers.

19. ) The Regenerative Fume Incinerator control system of claim 16, wherein the algorithm further performs steps (i) to (iv) described below prior to performing steps (a) to (g):

(i) freeze the selected regenerative heat exchanger in the heat sink media heating mode of operation while maintaining the other regenerative heat exchangers in their normal mode of operation,

(ii) read the measured temperature from the second temperature sensing means within the regenerative heat exchanger compartment of the selected regenerative heat exchanger and continue to freeze the regenerative heat exchanger in the heat sink media heating mode of operation while the measured temperature is less than a predetermined value,

(iii) stop the operation of the regenerative heat exchanger in the heat sink media heating mode of operation when the measured temperature is at least equal to a predetermined value, and

(iv) operate the regenerative heat exchanger compartment in the heat sink media cooling mode of operation.

20. ) The Regenerative Fume Incinerator control system of claim 19 wherein the algorithm automatically repeats sequential steps (i) to (iv) and (a) to (g) in at least one of the remaining regenerative heat exchangers.

21. ) The Regenerative Fume Incinerator control system of claim 19 wherein the algorithm automatically repeats sequential steps (i) to (iv) and (a) to (g) in each of the remaining regenerative heat exchangers.

22. ) A method of washing the heat sink media in a regenerative heat exchanger of a Regenerative Fume Incinerator, the regenerative heat exchanger having at least one spray pipe installed within it, the spray pipe connected to a source of cleaning fluid, the spray orifices on the spray pipe being directed towards the surface of the heat sink media within the regenerative heat exchanger, the method comprising the following steps:

(a) cooling the heat sink media to a temperature which is sufficient to prevent thermal shock to the heat sink media; and

(b) introducing the cleaning fluid into the spray-pipe to wash the surface of the heat sink media.

23. ) The heat sink media washing method of claim 22, wherein the cleaning fluid is water.

24. ) The heat sink media washing method of claim 22, wherein the cleaning fluid is steam.

25. ) The heat sink media washing method of claim 22, wherein the cleaning fluid is compressed air.

26. ) The heat sink media washing method of claim 22, wherein the temperature to prevent thermal shock to the heat sink media is less than 500 degrees Fahrenheit.

27. ) The heat sink media washing method of claim 22, wherein the temperature to prevent thermal shock to the heat sink media is in the range of 200 to 500 degrees Fahrenheit.

28. ) The heat sink media washing method of claim 22, further including the step of burning out the heat sink media before execution of steps (a) to (b).

29. ) A method of suppressing fires within a regenerative heat exchanger of a Regenerative Fume Incinerator, the regenerative heat exchanger containing regenerative heat sink media, the regenerative heat exchanger further having at least one spray pipe and at least one temperature measuring device installed within it, the spray-pipe connected to a source of water, the spray orifices on the spray-pipe being directed towards the surface of the heat sink media within the regenerative heat exchanger, the method comprising the following steps:

i) monitoring the temperature within the regenerative heat exchanger indicated by the temperature measuring device; and

ii) introducing the water into the spray-pipe when the monitored temperature reaches a pre-determined high level.

30. ) The fire suppression method of claim 29, wherein the pre-determined high level of the monitored temperature is at least 600 degrees F.