Liquid blowdown elimination system

• US 5,035,188 A
• Filed: 09/11/1990
• Issued: 07/30/1991
• Est. Priority Date: 09/11/1990
• Status: Expired due to Fees

• Current Assignee: Koch Glitsch Inc (KOCH Industries Incorporated)
• Original Assignee: IT-McGill Pollution Control Systems Inc.
• Inventors: Newburn, James A., Johnson, Bruce C.
• Primary Examiner(s): Yuen, Henry C.
• Application Number:
  US07/580,773
• Time in Patent Office: 322 Days
• Field of Search: 110/345, 110/215, 110/216
• US Class Current: 110/345
• CPC Class Codes: B01D 53/40 Acidic components B01D53/44 takes precedence
• CPC Class Codes: B01D 53/75 Multi-step processes
• CPC Class Codes: C02F 1/048 Purification of waste water by evaporation
• CPC Class Codes: C02F 2103/18 from the purification of gaseous effluents
• CPC Class Codes: F23G 2202/103 in separate chambers
• CPC Class Codes: F23J 15/006 Layout of treatment plant
• CPC Class Codes: F23J 2215/60 Heavy metals; Compounds thereof
• CPC Class Codes: F23J 2217/101 Baghouse type
• CPC Class Codes: F23J 2219/40 Sorption with wet devices, e.g. scrubbers

Abstract

An improved process for eliminating the liquid blowdown stream from the wet flue gas scrubbing equipment of an incinerator system. The liquid blowdown stream from the main wet scrubbing system is mixed with a hot flue gas slipstream. The water is evaporated and the residual solids are removed, thereby producing a dry waste stream for disposal and a solids-free flue gas slipstream for exhaust.

Claims

1. In an incinerator system in which a flue gas stream is subjected to a wet scrubber system or the like to recover particulate matter and/or acid gases contained in a main flue gas stream and in which is produced a liquid bottom stream and an exhaust overhead flue gas stream, the improvement comprising the steps of:

(a) removing a flue gas slipstream from the main flue gas stream;

(b) combining the flue gas slipstream with a liquid blowdown stream to evaporate the liquid constituent of the liquid blowdown stream and produce a dry effluent slipstream;

(c) removing residual particulates from the dry effluent slipstream to produce a substantially solids-free flue gas slipstream; and

(d) exhausting the substantially solids-free flue gas slipstream.

2. In an incinerator system of claim 1 wherein exhausting of the substantially solids-free flue gas slipstream comprises recombining the substantially solids-free flue gas slipstream with the main flue gas stream at a location immediately downstream from removal of the flue gas slipstream from the main flue gas stream.

3. In an incinerator system of claim 1 wherein exhausting of the substantially solids-free flue gas slipstream comprises recombining the substantially solids-free flue gas slipstream with the main flue gas stream following passage thereof from the wet scrubber system.

4. In an incinerator system of claim 1 wherein exhausting of the substantially solids-free flue gas slipstream comprises recombining the substantially solids-free flue gas slipstream with the scrubbed main flue gas stream.

5. In an incinerator system of claim 1 wherein the improvement further comprises the step of injecting a cooler gas into the dry effluent slipstream as required to maintain the temperature of the dry effluent slipstream at less than about 450°

F.

6. In an incinerator system of claim 1 wherein the main flue gas stream contains acid gases, and wherein the improvement further comprises the step of introducing an acid gas neutralizer into the dry effluent slipstream to react with and neutralize such acid gases.

7. In an incinerator system of claim 1 wherein the main flue gas contains acid gases and wherein the improvement further comprises the step of mixing an acid gas neutralizer with the liquid blowdown stream prior to combining the flue gas slipstream with the liquid blowdown stream in accordance with step (b).

8. In an incinerator system of claim 1 wherein removing residual particulates from the dry effluent stream in accordance with step (c) is carried out by collecting the residual particulates in a baghouse.

9. In an incinerator system of claim 1 wherein removing of the flue gas slipstream from the main flue gas stream in accordance with step (a) and exhausting of the flue gas slipstream in accordance with step (d) are carried out by passing the flue gas slipstream from the point of removal of the flue gas slipstream from the main flue gas stream to the point of exhaust of the substantially solids-free flue gas slipstream.

10. In an incinerator system of claim 9 wherein the improvement further comprises the step of mixing an acid gas neutralizer with the liquid blowdown stream prior to combining the flue gas slipstream with the liquid blowdown stream in accordance with step (b).

11. In an incinerator system of claim 9 wherein the main flue gas stream contains acid gases, and wherein the improvement further comprises the step of mixing the acid gas neutralizer with the dry effluent stream produced in accordance with step (b) prior to removing the residual particulates from the dry effluent stream in accordance with step (c).

12. In an incinerator system of claim 1 wherein the main flue gas stream contains particulate matter characterized as toxic metals and wherein the improvement further comprises introducing a chemical component into the dry effluent slipstream to react with and thereby precipitate such toxic metals.

13. In an incinerator system of claim 1 wherein the flue gas stream contains particulate matter characterized as toxic metals and wherein the improvement further comprises the step of mixing a chemical component with the liquid blowdown stream to react with the toxic metals and form a precipitate prior to combining the flue gas slipstream with the liquid blowdown stream in accordance with step (b).

14. In an incinerator system wherein a quench liquid is combined with a main flue gas stream in a scrubber operation to recover solids contained in the main flue gas stream and in which a liquid blowdown stream and an exhaust overhead flue gas stream are produced, the improvement comprising a system for eliminating or minimizing the liquid blowdown stream which comprises:

means for removing a flue gas slipstream from the main flue gas stream;

means for combining the flue gas slipstream with the liquid blowdown stream to evaporate the scrubber liquid from the liquid blowdown stream and thereby produce a dry effluent slipstream;

means for removing residual particulates from the dry effluent stream to produce a substantially solids-free flue gas slipstream; and

means for exhausting the substantially solids-free flue gas slipstream.

15. In an incinerator system of claim 14 wherein the means for removing the flue gas slipstream from the main flue gas stream comprises a fan communicating with the flue gas slipstream.

16. In an incinerator system of claim 14 wherein the means for removing the flue gas slipstream diverts a portion of the main flue gas stream as a flue gas slipstream.

17. In an incinerator system of claim 14 wherein the means for removing the dry particulates from said dry effluent waste stream comprises a baghouse.

18. In an incinerator system of claim 17 wherein the improvement further comprises means for injecting air into the dry effluent stream as required to maintain the dry effluent stream at a temperature of less than about 450°

F.

19. In an incinerator system of claim 14 wherein the improvement further comprises means for introducing into the flue gas slipstream an acid gas neutralizer to react with and neutralize acid gases present in the flue gas.

20. In an incinerator system of claim 14 wherein the improvement further comprises a mixer for mixing the acid gas neutralizer with the liquid blowdown stream.

21. In an incinerator system of claim 14 wherein the improvement further comprises means for introducing a dry acid gas neutralizer into the dry effluent slipstream upstream of the means for removing the residual particulates from the dry effluent slipstream.

22. In an incinerator system in which a main flue gas stream contains particulates or acid gases, the improvement adapted to eliminate or minimize liquid blowdown and comprising the steps of:

(a) removing a flue gas slipstream from the main flue gas stream;

(b) scrubbing the remaining flue gas with a quench liquid to produce a liquid bottom stream having a liquid blowdown stream and an exhaust overhead flue gas stream;

(c) combining the flue gas slipstream with the liquid blowdown stream to evaporate the liquid from the liquid blowdown stream to produce a dry effluent slipstream;

(d) removing residual particulates from the dry effluent slip stream to produce a substantially solids-free flue gas slipstream; and

(e) exhausting the substantially solids-free flue gas slipstream.

23. In an incinerator system of claim 22 wherein the improvement further comprises the step of introducing an acid gas neutralizer into the flue gas slipstream to react with and neutralize said acid gases.

24. In an incinerator system of claim 22 wherein the particulates in the main flue gas stream include toxic metals and wherein the improvement further comprises the step of introducing a chemical component into the flue gas slipstream to react with and precipitate the toxic metals.