US2730195A - Gas cleaning method - Google Patents

Gas cleaning method Download PDF

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US2730195A
US2730195A US464948A US46494854A US2730195A US 2730195 A US2730195 A US 2730195A US 464948 A US464948 A US 464948A US 46494854 A US46494854 A US 46494854A US 2730195 A US2730195 A US 2730195A
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carrier gas
compounds
electrodes
gas
collecting
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US464948A
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Lawrence M Roberts
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Research Corp
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Research Corp
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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/02—Plant or installations having external electricity supply
    • B03C3/16—Plant or installations having external electricity supply wet type
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S55/00—Gas separation
    • Y10S55/38—Tubular collector electrode

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  • This invention relates to a new and improved methodfor treating and cleaning gases. It is particularly directed to a gas treating and cleaning method wherein gases issuing from aluminum electric furnaces employing plastic pitch type electrodes and containing substantial quantities of fluorine compounds, carbon compounds and tar products are subjected to a succession of cooperating cleaning and treating operations in a single housing.
  • the invention has particular application to the production of aluminum from alumina by the Soderberg process wherein the electrolytic cell is provided with a continuous self-baking electrode.
  • the single electrode for the electrolytic cell is formed essentially from plastic pitch.
  • the pitch is added to a hopper at the top of a single, large rectangular, aluminum mantle or casing extending from the cell to a platform thereabove.
  • the plastic pitch is added to the hopper and flows downward toward the metallic bath in the base portion of the cell.
  • the plastic pitch in approaching the metallic bath is baked by the heat from the cell forming a solid carbon mass. As the carbon in the baked electrode is consumed at the lower end of the anode during electrolysis, more plastic pitch mix is added at the top, and the mantle or shell is added to from time to time, so that the operation is continuous.
  • the fluorine, tar and pitch compounds may then be disposed of in any suitable manner or the fluorine, tar and pitch compounds may be separatedly recovered from the aqueous slurry for subsequent use.
  • 10 generally designates a vertically extending stack into which a carrier gas stream containing the suspended fluorine compounds, carbon compounds and tar products issuing from one or more aluminum electric furnaces is discharged at the lower end.
  • the stack is cylindrical in cross section and constructed of wood or other material to prevent corrosion by the fluorine compounds.
  • the form of the apparatus shown in the drawings is particuiarly suited for installation in existing stacks for discharg ing the gases issuing from the electric furnaces to atmosphere.
  • one or more scrubber sections 12 for removing the greater portion of fluorine compounds and for humidifying the carrier gas.
  • a series of aqueous sprays comprising pipes 14 and 16 having spray heads 18 and 20 positioned at spaced intervals therealong.
  • two sets of spray devices are shown separated by a gas distributing baflle device 22 with the sprays of each unit projecting in a generally vertical direction in opposed relationship.
  • the gas distributing baflle plate 22 also aids in providing a high velocity means for obtaining intimate contact of the washing liquid with the gas stream flowing upwardly therethroug
  • an electrostatic precipitation section 24 Positioned above the gas washing and humidifying section 12 is an electrostatic precipitation section 24.
  • a plurality of cylindrical collecting electrodes 26 In the electrostatic precipitation section of the apparatus there is provided a plurality of cylindrical collecting electrodes 26, upper header sheet 28, lower header sheet 30, and a plurality of discharge electrodes 32.
  • the collecting electrodes 26 as shown in the drawing are hexagonal and provided with drip points 34 as described and claimed in U. S. Patent No. 2,592,508, I. Phyl, issued April 8, 1952.
  • the collecting pipes, however, may be square or round as is well known in the art.
  • the collecting electrodes 32 are suspended from bus bar 36 insulatedly supported at its ends by insulators 38 and 40 mounted in insulator compartments 42 and 44 secured to the outer wall of the stack 10.
  • Insulator 38 is provided with a high tension inlet conduit 46 which is connected to a suitable source of high voltage electricity.
  • the lower ends of the discharge electrodes 32 are attached to a retaining frame 48 to secure the electrodes from lateral displacement and from swinging from side to side in the gas stream.
  • the supporting frame 43 is secured to the stack by means of insulators 50 and 52 positioned within insulator compartments 54 and 56 which are similet in construction to the insulator compartment 42 and 44.
  • aqueous spray devices 58 Positioned above the electrostatic section 24 is one or more aqueous spray devices 58 which generally comprises a conduit 60 having a plurality of downwardly projecting spray heads 62.
  • the liquid spray device 58 has three primary functions. It aids in the humidification of the gas stream, it provides a source of water for collecting fluorine compounds not collected in the scrubber section 12, and provides a film of liquid for entraining the precipitated carbon and tar products in the electrostatic precipitation section 24;
  • bafiies or grills 64- and 66 Positioned above the spray'section 58 and at the upper most portion of the stack 10 are bafiies or grills 64- and 66 which maybe provided to preventstack' cross winds from effecting the distrlbution'of the gases within the precipitator.
  • the gases issuing from aluminum electric furnaces employing plastic pitch type electrodes are suspended in a stream of carrier gas and'discharged into the'lower end of stack 10.
  • Thegases entering the lower end of stack It) pass upwardly through the scrubber section 12' where a substantial portion of the fluorine compounds'are removed and the gas streamis humidified.
  • tlie gases pass up through the'tower into the electrostaticprecipitation section 24 where the tars, pitches and carbon compounds are collected along the inside surfaces ofthe collecting electrode pipes 26;
  • the precipitated material is removed from. the inner surfaces of the collecting electrodesby theflow ofwater down the pipes issuing from the upper spray headsr62.
  • the method of collecting fume containing substantial quantitiesofzfluorine compounds, carbon compounds and tar products issuing" from aluminum electric furnaces employing plastic pitch type electrodes comprising the steps of entraining the fume in a stream ofcarrier gas, removing a substantial portion of the fluorine compounds from said carrier gas stream-by subjecting the gas to an aqueous spray whereby the carrier gas is humidified, subjecting the carrier gas stream to electrical precipitation between discharge electrodes and complementary collecting electrodes continuously flushed with an aqueous medium to remove suspended particles from said gas in the form ofan aqueous slurry, and thereafter subjecting the gas to an aqueous spray whereby the remainder of the fluorine compounds are removed from said carrier gas stream, and passingsaid carrier gas stream to the atmosphere.

Description

Jan. 10, 1956 1.. M. ROBERTS 2,730,195
GAS CLEANING METHOD Filed Oct. 27, 1954 ea e4 e2 3 f 58 44 HHHHHHHH H LX036 F k 1% IZ A' 7 1711' In It? 17m r fi L 42 as L L J -fl w ULILILIULIUUUULIUUULIUUUULI 5o 20 \ul \lm 1w WW W! \h [l l1 ['1 Fl Fl I1 221 INVENTOR LAWRENCE M. ROBERTS K ZUZZQZ/ ATTORNEY GAS CLEANING METHOD Lawrence M. Roberts, Bound Brook, N. J., assignor to Research Corporation, New York, N. Y., a corporation of New York Application ()ctober 27, 1954, Serial No. 464,948 3 Claims. (Cl. 183-121) This invention relates to a new and improved methodfor treating and cleaning gases. It is particularly directed to a gas treating and cleaning method wherein gases issuing from aluminum electric furnaces employing plastic pitch type electrodes and containing substantial quantities of fluorine compounds, carbon compounds and tar products are subjected to a succession of cooperating cleaning and treating operations in a single housing.
The invention has particular application to the production of aluminum from alumina by the Soderberg process wherein the electrolytic cell is provided with a continuous self-baking electrode.
Generally the single electrode for the electrolytic cell is formed essentially from plastic pitch. The pitch is added to a hopper at the top of a single, large rectangular, aluminum mantle or casing extending from the cell to a platform thereabove. The plastic pitch is added to the hopper and flows downward toward the metallic bath in the base portion of the cell. The plastic pitch in approaching the metallic bath, is baked by the heat from the cell forming a solid carbon mass. As the carbon in the baked electrode is consumed at the lower end of the anode during electrolysis, more plastic pitch mix is added at the top, and the mantle or shell is added to from time to time, so that the operation is continuous.
While the particular advantage of this process is that it does away with the necessity for a separate plant for the production of the large carbon electrodes the volatile components of the plastic pitch have brought about a substantial air pollution problem. As the plastic pitch electrode is baked, the metallic bath volatizes the volatile components of the pitch, which rise through the body thereof and are expelled through ports on the side of the cell or through an outlet at the top. The gases issuing from these ports contain in addition to fluorine products, carhon compounds, tars and pitches.
It is therefore a primary object of the present invention to provide a method of collecting fume containing substantial quantities of fluorine compounds, carbon compounds and tar products issuing from aluminum electric furnaces employing plastic pitch type electrodes which generally comprises the steps of entraining the fume in a stream of carrier gas, removing'a substantial portion of the fluorine compound from said carrier gas stream by subjecting the gas to an aqueous spray whereby the carrier gas is humidified, and thereafter subjecting the carrier gas stream to electrical precipitation between discharge electrodes and complementary collecting electrodes continuously flushed with an aqueous medium to remove suspended particles from said gas in the form of an aqueous slurry.
The fluorine, tar and pitch compounds may then be disposed of in any suitable manner or the fluorine, tar and pitch compounds may be separatedly recovered from the aqueous slurry for subsequent use.
Further objects of the present invention are to provide such a method that is highly efiicient, economical and nited States Patent" 2 readily adaptable for installation in existing stacks for directing the gases issuing for such electric furnaces to atmosphere.
The invention will be more particularly described with reference to the accompanying drawings showing a preferred form of the apparatus which may be very advantageously employed in the method of the present invention.
Referring to the drawings, 10 generally designates a vertically extending stack into which a carrier gas stream containing the suspended fluorine compounds, carbon compounds and tar products issuing from one or more aluminum electric furnaces is discharged at the lower end. Preferably the stack is cylindrical in cross section and constructed of wood or other material to prevent corrosion by the fluorine compounds. However, the form of the apparatus shown in the drawings is particuiarly suited for installation in existing stacks for discharg ing the gases issuing from the electric furnaces to atmosphere.
At the lower end of the stack downstream from the gas stream entrance is provided one or more scrubber sections 12 for removing the greater portion of fluorine compounds and for humidifying the carrier gas. Within the scrubber section are arranged a series of aqueous sprays comprising pipes 14 and 16 having spray heads 18 and 20 positioned at spaced intervals therealong. In the form of the apparatus illustrated in the drawing two sets of spray devices are shown separated by a gas distributing baflle device 22 with the sprays of each unit projecting in a generally vertical direction in opposed relationship.
The gas distributing baflle plate 22 also aids in providing a high velocity means for obtaining intimate contact of the washing liquid with the gas stream flowing upwardly therethroug Positioned above the gas washing and humidifying section 12 is an electrostatic precipitation section 24. In the electrostatic precipitation section of the apparatus there is provided a plurality of cylindrical collecting electrodes 26, upper header sheet 28, lower header sheet 30, and a plurality of discharge electrodes 32.
The collecting electrodes 26 as shown in the drawing are hexagonal and provided with drip points 34 as described and claimed in U. S. Patent No. 2,592,508, I. Phyl, issued April 8, 1952. The collecting pipes, however, may be square or round as is well known in the art.
The collecting electrodes 32 are suspended from bus bar 36 insulatedly supported at its ends by insulators 38 and 40 mounted in insulator compartments 42 and 44 secured to the outer wall of the stack 10. Insulator 38 is provided with a high tension inlet conduit 46 which is connected to a suitable source of high voltage electricity. The lower ends of the discharge electrodes 32 are attached to a retaining frame 48 to secure the electrodes from lateral displacement and from swinging from side to side in the gas stream. The supporting frame 43 is secured to the stack by means of insulators 50 and 52 positioned within insulator compartments 54 and 56 which are similet in construction to the insulator compartment 42 and 44.
Positioned above the electrostatic section 24 is one or more aqueous spray devices 58 which generally comprises a conduit 60 having a plurality of downwardly projecting spray heads 62. The liquid spray device 58 has three primary functions. It aids in the humidification of the gas stream, it provides a source of water for collecting fluorine compounds not collected in the scrubber section 12, and provides a film of liquid for entraining the precipitated carbon and tar products in the electrostatic precipitation section 24;
Positioned above the spray'section 58 and at the upper most portion of the stack 10 are bafiies or grills 64- and 66 which maybe provided to preventstack' cross winds from effecting the distrlbution'of the gases within the precipitator.
In operation of the apparatus shown in the drawing the gases issuing from aluminum electric furnaces employing plastic pitch type electrodes are suspended in a stream of carrier gas and'discharged into the'lower end of stack 10. Thegases entering the lower end of stack It) pass upwardly through the scrubber section 12' where a substantial portion of the fluorine compounds'are removed and the gas streamis humidified. After leaving the spray or scrubber section, tlie gases pass up through the'tower into the electrostaticprecipitation section 24 where the tars, pitches and carbon compounds are collected along the inside surfaces ofthe collecting electrode pipes 26;
The precipitated material is removed from. the inner surfaces of the collecting electrodesby theflow ofwater down the pipes issuing from the upper spray headsr62.
The liquid from the prccipitator section will then flow through the scrubber section and act as a scrubbing and humidif'ying medium, augmenting the spray devices. 18 andZt'lin the scrubber section 121 From the foregoing description of the present invention it will be seen that" the new method of collecting fume from aluminum electric furnaces employing plastic pitch type electrodes fully accomplishes the aims and objects of the present" invention.
1 claim:
1'. The method of collecting fume containingsubstantial quantities of fluorine compounds, carbon compounds and tar products issuing from aluminum electric furnaces employing plastic pitch type electrodes comprising the steps of entraining the fume in a stream of carrier gas,
removing a substantial portion of the fluorine compounds from" said carrier gas stream by subjecting the'gasto' anaqueous spray whereby the carrier gas is humidified, and thereafter subjecting the carrier gas stream to electrical precipitation between discharge electrodes and complementary collecting electrodes continuously flushed with an aqueous medium to remove suspended particles from said gas in the form of-anaqueous slurry.
2. The method of collecting fume containing substantial quantitiesofzfluorine compounds, carbon compounds and tar products issuing" from aluminum electric furnaces employing plastic pitch type electrodes comprising the steps of entraining the fume in a stream ofcarrier gas, removing a substantial portion of the fluorine compounds from said carrier gas stream-by subjecting the gas to an aqueous spray whereby the carrier gas is humidified, subjecting the carrier gas stream to electrical precipitation between discharge electrodes and complementary collecting electrodes continuously flushed with an aqueous medium to remove suspended particles from said gas in the form ofan aqueous slurry, and thereafter subjecting the gas to an aqueous spray whereby the remainder of the fluorine compounds are removed from said carrier gas stream, and passingsaid carrier gas stream to the atmosphere.
3.- Themethod defined in claim 1 wherein the aqueous medium for flushing the collecting electrodes of the electrostatic. precipitator isemployed to remove a portion of the fluorine compound from the carrier gas stream.
References Cited in the file of this patent UNITED. STATES PATENTS Hedberg et al Feb. 17, 1942 ,White June 29, 1954 OTHER REFERENCES

Claims (1)

1. THE METHOD OF COLLECTING FUME CONTAINING SUBSTANTIAL QUANTITIES OF FLUROINE COMPOUNDS, CARBON COMPOUNDS AND TAR PRODUCTS ISSUING FROM ALUMINUM ELECTRIC FURNACES EMPLOYING PLASTIC PITCH TYPE ELECTRODES COMPRISING THE STEPS OF ENTRAINING THE FUME IN A STREAM OF CARRIER GAS, REMOVING A SUBSTANTIAL PORTION OF THE FLUORINE COMPOUNDS FROM SAID CARRIER GAS STREAM BY SUBJECTING THE GAS TO AN AQUEOUS SPRAY WHEREBY THE CARRIER GAS IS HUMIDIFIED, AND THEREAFTER SUBJECTING THE CARRIER GAS STREAM TO ELECTRICAL PRECIPITATION BETWEEN DISCHARGE ELECTRODES AND COMPLEMENTARY COLLECTING ELECTRODES CONTINUOUSLY FLUSHED WITH AN AQUEOUS MEDIUM TO REMOVE SUSPENDED PARTICLES FROM SAID GAS IN THE FORM OF AN AQUEOUS SLURRY.
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Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2997132A (en) * 1956-03-23 1961-08-22 Svenska Flaektfabriken Ab Method for the ventilating of plants for the manufacture of aluminium or similar products
DE1184093B (en) * 1962-02-15 1964-12-23 Pechiney Prod Chimiques Sa Method and device for cleaning exhaust gases from aluminum fused-salt electrolysis
DE1255637B (en) * 1959-02-27 1967-12-07 Alusuisse System for the purification of exhaust air from factory halls in which ovens are installed
US3511030A (en) * 1967-02-06 1970-05-12 Cottrell Res Inc Methods and apparatus for electrostatically cleaning highly compressed gases
US3891415A (en) * 1972-01-14 1975-06-24 Nippon Kogei Kogyo Company Lim Electrostatic dust collector for exhaust gases containing fine particles
US5009677A (en) * 1989-09-01 1991-04-23 Fmc Corporation Process for separating particulates in an electrostatic precipitator
US5070893A (en) * 1988-02-06 1991-12-10 Degussa Aktiengesellschaft Apparatus and method for removing washcoat remaining in the channels of freshly coated monolithic or honeycombed catalyst carriers and use of the apparatus
US5165970A (en) * 1990-02-28 1992-11-24 Degussa Aktiengesellschaft Method of coating honeycomb bodies with finely divided solid matter
US6156098A (en) * 1999-02-10 2000-12-05 Richards; Clyde N. Charged droplet gas scrubber apparatus and method
US6579349B1 (en) * 2002-04-08 2003-06-17 Chein-Bang Ting Electrostatic precipitator
US20120222550A1 (en) * 2011-03-01 2012-09-06 Ellis Timothy W Wet electrostatic precipitator and related methods
WO2015125016A1 (en) 2014-02-18 2015-08-27 Ugra S.R.L. Method and apparatus for purifying a gas containing pollutants
US11260401B2 (en) * 2018-10-01 2022-03-01 DOOSAN Heavy Industries Construction Co., LTD Dust collecting module, desulfurizing apparatus having same, and method of installing dust collecting module

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2273194A (en) * 1941-03-11 1942-02-17 Research Corp Gas cleaning
US2682313A (en) * 1952-10-29 1954-06-29 Research Corp Alternating current ion-filter for electrical precipitators

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2273194A (en) * 1941-03-11 1942-02-17 Research Corp Gas cleaning
US2682313A (en) * 1952-10-29 1954-06-29 Research Corp Alternating current ion-filter for electrical precipitators

Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2997132A (en) * 1956-03-23 1961-08-22 Svenska Flaektfabriken Ab Method for the ventilating of plants for the manufacture of aluminium or similar products
DE1255637B (en) * 1959-02-27 1967-12-07 Alusuisse System for the purification of exhaust air from factory halls in which ovens are installed
DE1184093B (en) * 1962-02-15 1964-12-23 Pechiney Prod Chimiques Sa Method and device for cleaning exhaust gases from aluminum fused-salt electrolysis
US3511030A (en) * 1967-02-06 1970-05-12 Cottrell Res Inc Methods and apparatus for electrostatically cleaning highly compressed gases
US3891415A (en) * 1972-01-14 1975-06-24 Nippon Kogei Kogyo Company Lim Electrostatic dust collector for exhaust gases containing fine particles
US5070893A (en) * 1988-02-06 1991-12-10 Degussa Aktiengesellschaft Apparatus and method for removing washcoat remaining in the channels of freshly coated monolithic or honeycombed catalyst carriers and use of the apparatus
US5009677A (en) * 1989-09-01 1991-04-23 Fmc Corporation Process for separating particulates in an electrostatic precipitator
US5165970A (en) * 1990-02-28 1992-11-24 Degussa Aktiengesellschaft Method of coating honeycomb bodies with finely divided solid matter
US6156098A (en) * 1999-02-10 2000-12-05 Richards; Clyde N. Charged droplet gas scrubber apparatus and method
US6579349B1 (en) * 2002-04-08 2003-06-17 Chein-Bang Ting Electrostatic precipitator
US20120222550A1 (en) * 2011-03-01 2012-09-06 Ellis Timothy W Wet electrostatic precipitator and related methods
US8790444B2 (en) * 2011-03-01 2014-07-29 Rsr Technologies, Inc. Wet electrostatic precipitator and related methods
US20150040759A1 (en) * 2011-03-01 2015-02-12 Rsr Technologies, Inc. Wet electrostatic precipitator and related methods
US9821320B2 (en) * 2011-03-01 2017-11-21 Rsr Technologies, Inc. Wet electrostatic precipitator and related methods
WO2015125016A1 (en) 2014-02-18 2015-08-27 Ugra S.R.L. Method and apparatus for purifying a gas containing pollutants
US11260401B2 (en) * 2018-10-01 2022-03-01 DOOSAN Heavy Industries Construction Co., LTD Dust collecting module, desulfurizing apparatus having same, and method of installing dust collecting module

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