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Publication numberUS3673768 A
Publication typeGrant
Publication dateJul 4, 1972
Filing dateOct 17, 1969
Priority dateOct 17, 1969
Publication numberUS 3673768 A, US 3673768A, US-A-3673768, US3673768 A, US3673768A
InventorsGerald D Leonard
Original AssigneeCottrell Res Inc
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Jacketed precipitator apparatus
US 3673768 A
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Description  (OCR text may contain errors)

United States Patent 1151 3,673,768

Leonard July 4, 1972 1 JACKETED PRECIPITATOR 1,391,436 9/1921 Welch 55/148 x APPARATUS 1,473,806 11/1923 Bradley 1,884,085 10/1932 Miller [72] lnventor. Gerald D. Leonard, Millstone, NJ. 2,615,530 lo/lgsz Hodson a M [73] Assignee: Research-Cottrell, lnc., Bridgewater g g i v owie Townsh'p 3,233,702 3/1966 De Seversky .55/120 x 22 Filed: 061. 17, 1969 FOREIGN PATENTS OR APPLICATIONS 211 Appl. N().I 869,447

550,372 12/1922 France ..55/l46 Related US. Application Data 120,994 12/1918 Great Britain 1.55/ l 46 [63] Continuation of Ser. No. 607,839, .Ian. 6, 1967, abandoned.

[52] U.S.Cl. ..55/135, 55/146,55/D1G. 38 [51 Int. Cl. ..B03c 3/01 [58] Field of Search... ..55/146 [56] References Cited UNITED STATES PATENTS 1,379,897 5/1921 Bradley ..55/10l X Primary ExaminerDennis E. Talbert, Jr. Attorney-Stowe" & Stowell ABSTRACT An improved electrostatic precipitator having a temperature regulated precipitator chamber for the treatment of particle laden gases.

1 Claim, 2 Drawing Figures PATENTEUJUH I972 FIG. I

INVENTOR. GERALD D. LEONARD J ACKETED PRECIPITATOR APPARATUS This is a continuation application of Ser. No. 607,839, filed Jan. 6, 1967, now abandoned.

in a preferred form the present invention relates to a hollow-jacketed electrostatic precipitator gas treatment chamber provided with means for passing a flow of a heated gas through such jacket to prevent or reduce the condensation of the gas under treatment onto the interior walls of the chamber.

An excessive temperature difierential between the particleladen gases under treatment and the walls of a gas treatment precipitator chamber through which such gases flow will cause condensation of moisture from the gas stream upon the chamber walls, with the deposition of gas products and suspended particulate matter carried within the gases.

Such deposition upon the chamber walls is undesirable in that deleterious condensation products may build up which may reduce the precipitator efficiency and also act to corrode and erode the chamber walls, particularly when the gases contain matter such as phosphorous, sulphur, nitrates, or the like.

It is accordingly an object of the present invention to prevent undesirable condensation upon the interior walls of an electrostatic precipitator chamber.

A more specific object of this invention is to prevent undue temperature fall of the precipitator chamber walls by providing an external jacket over the same; passing a heated gas through such jacket; and/or supplementing such a flow of temperature-regulating heated gas by a flow of heated gas over the internal chamber walls.

The above and further objects and advantages of the invention will become apparent upon consideration of the detailed description of a preferred embodiment of the invention which follows, when taken with the accompanying drawings wherein:

FIG. 1 is a diagrammatic representation showing in elevation and partial section a system for treating particle-laden gases utilizing the present invention; and

' FIG. 2 is a view taken on line 2 2 ofa portion of FIG. 1.

In the drawings reference numeral generally designates an electrostatic precipitator through which hot particle-laden gases from a furnace 12 flow for ultimate discharge through vertical stack 14.

Arrows 16 indicate the gas flow from fumace to stack, which is by way of the fumace-outlet to precipitator-inlet flue 18; through precipitator 10; and then through the precipitator-outlet to stack-inlet flue 20.

The precipitator 10 includes treatment electrode sets 22 consisting of tubular ground potential collecting electrodes 21 and fine wire discharge electrodes 23 which pass axially through each of the collector tubes 21. The discharge electrodes 23 are suspended by an insulator and bus arrangement 60, and charged from the usual voltage source (not shown). Electrodes 22 occupy the major area within treatment chamber 24. The gas cleaner illustrated in FIG. 1 may be utilized in treating paper mill gases, for example, and to this end precipitator 10 is shown with a sump 26; a return flow conduit 28 leading to a black liquor inlet 30 to the recovery boiler (not shown) within furnace 12.

While tubular collecting electrodes have been specifically shown in the drawings any form of electrodes may be employed with the jacketed housing without changing the basic objects of the invention.

The walls of treatment chamber 24 are preferably formed of mild steel for ease of manufacture and assembly. However, for example, in the treatment of paper mill gases corrosion of the chamber walls due to condensation of sodium sulphite gases from the recovery boiler is to be avoided. Rather than form the chamber walls of a more expensive and less workable corrosion-resistant metal the present invention proposes to regulate the temperature on both sides of chamber walls 24.

To this end a spaced jacket 32, which also may be formed of mild steel, is provided which surrounds chamber walls 24. It is spaced from walls 24 by means of plurality of channel members 34. Support members 36 bear the weight of precipitator l0, and an outer insulation shield 40 may be optionally provided to maintain a more uniform temperature within treatment chamber 24.

The channel spacer members 34 have openings therein, as illustrated, to provide a closed jacket surrounding the treatment chamber; through which jacket heated air flows as indicated by the arrows 42.

A heater 44 maybe located adjacent the precipitator in order to heat the fresh temperature-regulating air for the jacket formed by precipitator walls 24 and jacket walls 32. Heated air from the heater outlet duct 46 is circulated through the jacket by means of a blower fan 50 and a supply duct 48. The temperature-regulating air enters the jacket via a peripheral input manifold 52; passes along the outer surface of walls 24; and exits via output manifold 54. A plurality of branch ducts 56 interconnect the manifolds with the jacket.

A closed recirculating system is illustrated for the temperature-regulating air; the output manifold 54 being connected back to the heater by the return duct 58. In accordance with known practice the several ducts 46, 48 and 58 should be graduated in cross-section; and the several branch ducts 56, either entry, or exit, or both, should be provided with adjustable throttling valves (not shown); in order that a uniform flow of the jacketing air is achieved.

Further in accordance with known practice make-up air may be introduced into the recirculating temperature-regulating system, for example, by means of inlet duct 45 having a damper-controlled means 47 positioned ahead of blower fan 50. Heater 44 may be provided with suitable temperature regulator control means.

In FIG. 1 it will be noted that the suspension means for the gas treatment electrodes 22 enters the chamber roof panel 24 through an opening below insulator 60. Bleed air from the jacket flows into the interior of the precipitator at this point as indicated by the curved arrows.

Such bleed air serves to prohibit condensation upon the insulator and the gas treatment electrodes, as well as the chamber roof and side panels 24.

The heater 44 may be of any conventional design and may be gas or oil fired or electrically or steam heated. In general the heater 44 for the air would not comprise a flue gas type heat exchanger as with a flue gas heated heat exchanger the incoming air temperature to the jacket would be lower than the flue gas temperature and may not therefore prevent condensation from the gas stream upon the chamber walls of the precipitator.

EXAMPLE In an installation for a paper mill precipitator the following operating values were found to eliminate unwanted condensation upon the interior precipitator walls:

Heater 44 output temperature: 340 F. Blower fan 50: 5400 cfm.

Input manifold 52: 5400 cfm. at 300 F. Output manifold 54: 4800 cfrn. at 250-300 F. Bleed air into chamber: 600 cfm. at 300 F.

Make-up air into system: 600 cfrn. Ambient Operation of the hollow-jacketed electrostatic precipitator should be apparent from the foregoing description and example, although certain modifications, equivalents and changes may occur to those skilled in the art. Accordingly, the invention is only to be limited as defined by the appended claims.

What is claimed is:

1. A gas treatment electrostatic precipitator comprising a double wall vertical shell having inner and outer spacedly arranged tubular side walls, said inner wall circumscribingly defining a gas treatment chamber, means at the lower end of the shell for supporting the shell and closing off the treatment chamber and the space between the side walls, a double wall top housing arrangement at the top of the shell closing ofi' the shell and constituting transverse top projections of the side walls, said top wall arrangement defining an insulator chamber disposed in free and open communication with the space between the side walls, said insulator chamber being closed off from the treatment chamber with only a bleed passage between the insulator chamber and the treatment chamber, spacedly arranged discharge and collecting electrodes positioned in said treatment chamber, electrical conductor means passing through the insulator chamber and into the treatment chamber for energizing the electrodes, inlet conduit means directingly conveying particle laden gas to be treated into the treatment chamber to flow between the spacedly arranged discharge and collecting electrodes, outlet conduit means in communication with the treatment chamber for conveying the treated gas out from the treatment chamber, heater means for heating a clean gas that is distinct from the treated gas, inlet means communicated between the heater means and the space between the walls of the shell for conveying the heated clean gas into said space so that the gas comes in intimate contact with the exterior surface of the inner wall of the shell, outlet means communicated with said space at a point remote 'from the inlet means for withdrawing the heated gas from the space between the walls and being connected with the heater means for returning the withdrawn gas to the heater means, said heater means being in substantially closed fluid path with said gas inlet means and said gas outlet means, said bleed passage between the insulator chamber and the treatment chamber permitting a portion of the heated clean gas to enter from the insulator chamber into the treatment chamber around the electrodes and into contact with the interior of the shell walls, conduit means for conveying a make up gas to the closed fluid path of the heater means in advance of the heater means to replace the bleed portion of said gas, spacer members connected between the inner and outer side walls of the shell for spacing the walls apart and having openings therethrough through which the heated clean gas pases in a controlled manner and means for forcefully moving the heated clean gas from said gas outlet to said gas inlet means.

Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US3818682 *Sep 25, 1972Jun 25, 1974Owens Illinois IncFlue gas temperature control system
US3830039 *Jun 8, 1973Aug 20, 1974Knapsack AgProcess and apparatus for continuous work-up of phosphorus-containing residues
US3989482 *Aug 16, 1974Nov 2, 1976Polysius AgMethod for the removal of dust from exhaust gases
US4462973 *Jun 27, 1983Jul 31, 1984Fmc CorporationColor change from yellow to balck
US4678484 *Jul 7, 1986Jul 7, 1987Metallgesellschaft AktiengesellschaftElectrofilter
US4846857 *Oct 14, 1987Jul 11, 1989Mitsubishi Jukogyo Kabushiki KaishaElectric dust collector with electrode supporter therefor
US5003774 *Oct 27, 1989Apr 2, 1991Kerr-Mcgee Chemical CorporationApparatus for soot removal from exhaust gas
U.S. Classification96/74, 55/DIG.380
International ClassificationB03C3/82
Cooperative ClassificationY10S55/38, B03C3/82
European ClassificationB03C3/82