US1381719A - Centrifugal gas-cleaning apparatus - Google Patents
Centrifugal gas-cleaning apparatus Download PDFInfo
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- US1381719A US1381719A US429667A US42966720A US1381719A US 1381719 A US1381719 A US 1381719A US 429667 A US429667 A US 429667A US 42966720 A US42966720 A US 42966720A US 1381719 A US1381719 A US 1381719A
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- gases
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- head
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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
- B03C3/04—Plant or installations having external electricity supply dry type
- B03C3/14—Plant or installations having external electricity supply dry type characterised by the additional use of mechanical effects, e.g. gravity
- B03C3/15—Centrifugal forces
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C9/00—Combinations with other devices, e.g. fans, expansion chambers, diffusors, water locks
- B04C2009/001—Combinations with other devices, e.g. fans, expansion chambers, diffusors, water locks with means for electrostatic separation
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- 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
Definitions
- FRANK a more, or srnusnnvrrnn, onro, AND ARTHUR r. nnsrarr, or WILKINS- BURG, PENNSYLVANIA.
- This invention relates to centrifugal head members adapted to be used in gas cleaning apparatus of the form used in separating liquid particles from gaseous and fluid streams by electrical precipitation, and has for its principal object the provision of such a head, having means for increasing the efiectiveness of. the ionization. forces in the cleaner, 1
- - Cleaners of the type to which our invention belongs comprise opposing electrode s stems having tubular collecting electrodes.
- centrifugal heads have been applied in or near the tops of the tubular collecting electrodes, having helical vanes forming helical passages to cause a swirling action of the gases as they enter between the electrodes.
- Fig. 2 is a similar view of a sli htl modified form of apparatus. g y
- Fig. 3 is a horizontal sectional view on the line Ill-III of Fig. 2.
- the numeral 2 designates a casing having a receiving chamher 3 at its upper end (shown broken away in the drawi gs). l
- the casing 2 is adapted to house or contain.
- a suitable opposing electrode system which forms a series of ionization fields.
- Such system is composed of a discharge electrode a arranged concentrically within a tubular collecting electrode 5.
- Thedischarge electrode 4 is preferably in the form of a rod having edges spaced along its periphery forming fields composed of individual ionization zones, and having its upper end pointed or beveled as at e.
- the collecting electrode 5 is formed of a plurality of tube sections, each" section being of less diameter than the preceding section, and being so arranged that the smaller section telescopes an appreciable distance within the preceding larger section, thus forming exits or traps 5 to allow the escape of the collected matter from the section of the electrode immediately preceding or above the Cooling or refrigerating jackets 8 are concentrically arranged around each of the sections of the collecting electrode 5 to cause a condensing of the vapors carried in the gases being cleaned, forming a fog-like mist of liquid particles, and to generally lower the temperature of the gases as they pass through the, ionization zones formed in the space between the electrodes.
- the jackets 8 are each provided with inlet pipes 9 and out:
- our invention relates particularly to this member together with the other novel fea-.
- the uncleaned gases will enter-the chamber 3 at the upper end of the casing under pressure, and will be forced to pass through the passages formed by the helical vanes 15 and the opening 14 in the head 11.
- the passages formed by the vanes 15 being comparatively large, the major portion of the gases will pass therethrough and will be given a whirling movement.
- a small or lead stream of the gases will flow through the unrestricted small opening 14 and impinge directly on the upper pointed end 4 ofthe discharge electrode 4.
- the major portion of the gases will pass through the passages formed by the helical vanes and will, therefore, have a swirling or centrifugal movement.
- This centrifugal movement has a tendencg 0 throw off the heavier particles carrie the gases due to the mechanical forces.
- This is materially aided by the forces of the initial ionization zone formed by the lead, stream of gases.
- the successive ionization zones will continue to clean the gases of all liquid particles as .they pass through betweenthe electrodes.
- a pipe 20 is passed through a second passage or aperture 14* to the one side of the aperture or passage 14, and is provided at its lower end with nozzles 14".
- Pipe 20 leads from a suitable source of fluid supply, the fluid preferably being of a similar nature to that carried in suspension in the gases, and which it is desired to remove.
- the fluid is forced through the pipe 20 and nozzles 14* and becomes mixed with the gases coming through the passage .14, and is forced or precipitated outward with said gases into the stream of oncoming unclean After the partlcles have been ionized by either of the above apparatus and they are precipitated against the collecting electrodes, they will escape through the traps 6 onto the collecting partitions 7 where they are retained until drawn off through the outlets 7.
- head member adapted to cause a mechanical centrifugal movement to the major portion ofthe gases, said head comprising a bod portion having a relativel small cenaperture theret ugh, and a plurality of he ical vanes formed on the outer peri hery of said body portion forming'helica passages, the major portion of the gases beingadapted to pass through said helical passages and a minor being adapted to pass through sai smallcentrally arranged aperture forming a lead stream. a '3.
- a receiving chamber for the ortlon having a plurality of traps spaced.
- a discharge electrode centrally cipitating particles from gaseous streams
- An apparatus for separating particles from gaseous and fluid streams by electri cal precipitation comprising the combination-with a casing, of a tubular collecting electrode arranged within said casing'and arranged Within said collecting electrode, and a centrifugal head member adapted to impart a mechanical centrifugal movement tothe major portionof the gases, said head being arranged within said collecting electrode and above said discharge electrode,-
Description
F. R. McGEE AND A. F. NESBITA CENTRIFUGAL GAS CLEANING APPARATUS.
APPLICATION FILED DEC. I0. 1920.
Patented June 14, 1921.
jflaenfirs: 6%
Wines-sea UNITED STATES PATENT oEElcE.
FRANK a. more, or srnusnnvrrnn, onro, AND ARTHUR r. nnsrarr, or WILKINS- BURG, PENNSYLVANIA.
CENTBIFUGAL GAS-CLEANING APIEARATUS.
S Specification of letters Patent.
Application filed December 10, 1920. Serial No. 429,667.
T 0 all whom it may concern Be it known that we, FRANK R. MCGEE and ARTHUR F. Nnsnr'r, citizens of the ful Improvements in Centrifugal Gas-Clean ing Apparatus, of which the following is a specification.
This invention relates to centrifugal head members adapted to be used in gas cleaning apparatus of the form used in separating liquid particles from gaseous and fluid streams by electrical precipitation, and has for its principal object the provision of such a head, having means for increasing the efiectiveness of. the ionization. forces in the cleaner, 1
- Cleaners of the type to which our invention belongs, comprise opposing electrode s stems having tubular collecting electrodes.
eretofore, suitable centrifugal heads have been applied in or near the tops of the tubular collecting electrodes, having helical vanes forming helical passages to cause a swirling action of the gases as they enter between the electrodes.
It is the object of our present invention to improve this construction of centrifugal head by providing a centrally arranged direct lead opening in the head to permit a small. amount of dirty vapor laden gases to enter and impinge directly on the top of the discharge electrode, thereby causing an initial ionization of these gases in advance of the main volume and setting up an outward precipitating movement of the liquid or collected vapor particles which will materially aid in the separation of the particles from the main flo embodying our invention, and,
Fig. 2 is a similar view of a sli htl modified form of apparatus. g y
'Fig. 3 is a horizontal sectional view on the line Ill-III of Fig. 2.
Referring to the drawings, the numeral 2 designates a casing having a receiving chamher 3 at its upper end (shown broken away in the drawi gs). l
The casing 2 is adapted to house or contain.
a suitable opposing electrode system which forms a series of ionization fields. Such system is composed of a discharge electrode a arranged concentrically within a tubular collecting electrode 5.
Thedischarge electrode 4 is preferably in the form of a rod having edges spaced along its periphery forming fields composed of individual ionization zones, and having its upper end pointed or beveled as at e.
The collecting electrode 5 is formed of a plurality of tube sections, each" section being of less diameter than the preceding section, and being so arranged that the smaller section telescopes an appreciable distance within the preceding larger section, thus forming exits or traps 5 to allow the escape of the collected matter from the section of the electrode immediately preceding or above the Cooling or refrigerating jackets 8 are concentrically arranged around each of the sections of the collecting electrode 5 to cause a condensing of the vapors carried in the gases being cleaned, forming a fog-like mist of liquid particles, and to generally lower the temperature of the gases as they pass through the, ionization zones formed in the space between the electrodes. The jackets 8 are each provided with inlet pipes 9 and out:
let pipes 10, each of which are provided with suitable regulating valves to permitcirculation of acooling fluid. 7
An improved and novel direction imparthead member ll is mounted within the Patented J une 14, 1921i.
upper end of the collecting chamber, and
our invention relates particularly to this member together with the other novel fea-.
formed around the outer periphery of the' body poltion 12, and have their lower ends contracted forming nozzle-like terminals 15*, of such width that they will snugly abut the inner periphery of the tubular collecting electrode 5 forming helical passages for the incoming gases.
The uncleaned gases will enter-the chamber 3 at the upper end of the casing under pressure, and will be forced to pass through the passages formed by the helical vanes 15 and the opening 14 in the head 11. The passages formed by the vanes 15 being comparatively large, the major portion of the gases will pass therethrough and will be given a whirling movement. However, a small or lead stream of the gases will flow through the unrestricted small opening 14 and impinge directly on the upper pointed end 4 ofthe discharge electrode 4. The efiect of this small or lead stream of gases impinging directly on the point of the discharge electrode will be to initially ionize such stream at a point above the normal ionization zones and, therefore, precipitate the fog or liquid particles with which it is laden toward the surrounding collecting electrode and intothe path of the oncoming gases that have passed between the vanes 15. The effect of precipitating the particles of this initially ionized stream into the path of the oncoming unclean and vapor laden gases will serve a two-fold purpose, first the precipitated fog or liquid particles will form a nucleus for collecting the vapor particles in the oncoming unclean gases, and second it will cause an initial ionization zone at this point of more intensity than could otherwise be formed, therefore, causing a more perfect cleaning of the gases.
As has been said, the major portion of the gases will pass through the passages formed by the helical vanes and will, therefore, have a swirling or centrifugal movement. This centrifugal movement has a tendencg 0 throw off the heavier particles carrie the gases due to the mechanical forces. However this is materially aided by the forces of the initial ionization zone formed by the lead, stream of gases. The successive ionization zones will continue to clean the gases of all liquid particles as .they pass through betweenthe electrodes.
The modification shown in Figs. 2 and 3 is similar in all respects to the construction tra y arranged heretofore described, with the exception that a pipe 20 is passed through a second passage or aperture 14* to the one side of the aperture or passage 14, and is provided at its lower end with nozzles 14". Pipe 20 leads from a suitable source of fluid supply, the fluid preferably being of a similar nature to that carried in suspension in the gases, and which it is desired to remove. The fluid is forced through the pipe 20 and nozzles 14* and becomes mixed with the gases coming through the passage .14, and is forced or precipitated outward with said gases into the stream of oncoming unclean After the partlcles have been ionized by either of the above apparatus and they are precipitated against the collecting electrodes, they will escape through the traps 6 onto the collecting partitions 7 where they are retained until drawn off through the outlets 7.
Various modifications will readily suggest themselves to those skilled in the art.
Therefore it will be understood that'w ,do not WlSh to be limited to the specific constructions shown, except as expressly limited in the appended claims.
We claim:
1. In an apparatus for separating foreign particles from gaseous streams, the combicipitating particles from gaseous streams, a
head member adapted to cause a mechanical centrifugal movement to the major portion ofthe gases, said head comprising a bod portion having a relativel small cenaperture theret ugh, and a plurality of he ical vanes formed on the outer peri hery of said body portion forming'helica passages, the major portion of the gases beingadapted to pass through said helical passages and a minor being adapted to pass through sai smallcentrally arranged aperture forming a lead stream. a '3. In an apparatus for electrically prenation with a receiving chamber for the ortlon having a plurality of traps spaced. along its length, a discharge electrode centrally cipitating particles from gaseous streams, the combination with a tubular collecting electrode and a discharge electrode centrally arranged within said collecting electrode, of a centrifugal head member adapted to impart a mechanical centrifugal movement to the major portion of the gases, said head being arranged within said collecting electrode and above said ldischarge electrode, and comprising a cylindrical body portion having a relatively small centrally arranged unrestricted aperture ,therein adapted to admit a small lead flow of uncleaned gases through the head to impinge directly upon the upper end of the dis-. charge electrode, and a plurality of helical vanes formed on the outer periphe I of said body portion adapted to abut the inner periphery of said collecting electrode, thereby forming helical passages through which the major portion of said gases are adapted to pass. i
.4. An apparatus for separating particles from gaseous and fluid streams by electri cal precipitation, comprising the combination-with a casing, of a tubular collecting electrode arranged within said casing'and arranged Within said collecting electrode, and a centrifugal head member adapted to impart a mechanical centrifugal movement tothe major portionof the gases, said head being arranged within said collecting electrode and above said discharge electrode,-
and comprising a cylindrical body portion having a relatively small centrally arranged unrestricted aperture therein adapted toadmit a small lead flow of uncleaned gases through the head .to impinge directly upon the upper end of the discharge electrode, and a plurallty of helical vanes formed on the outer periphery of said body portion trode and into the path of said first body.
-6. The method of precipitating particles from gaseous fluids, comprising, first, in-
passing the gases into a chamber, dividing said ases into two flow bodies, passing one of said bodies through helical assages imparting a mechanical centri gal whirl thereto, and'then passing it through ionization zones in the space between a discharge electrode and a collecting electrode, and passing said other body directly against said discharge electrode, causing an initial ionization thereof, and precipitating the particles therefrom toward said collecting electrode and into the path of said first flow body, thereby forming a nucleus for the par I ticles of, and initially ionizing, said first named flow body.
I In ,testimony whereof we have hereunto signed our names.
FRANK R. McGEE. ARTHUR r. NESBIT.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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US429667A US1381719A (en) | 1920-12-10 | 1920-12-10 | Centrifugal gas-cleaning apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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US429667A US1381719A (en) | 1920-12-10 | 1920-12-10 | Centrifugal gas-cleaning apparatus |
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US1381719A true US1381719A (en) | 1921-06-14 |
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US429667A Expired - Lifetime US1381719A (en) | 1920-12-10 | 1920-12-10 | Centrifugal gas-cleaning apparatus |
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Cited By (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2594805A (en) * | 1945-06-26 | 1952-04-29 | Garrett Corp | Air cleaner |
US2615530A (en) * | 1949-11-25 | 1952-10-28 | Air Preheater | Liquid cleaned precipitator |
US2740493A (en) * | 1953-12-30 | 1956-04-03 | Research Corp | Gas cleaning method and apparatus |
US2741331A (en) * | 1952-03-19 | 1956-04-10 | Sfindex | Electrostatic gas precipitation |
US2748888A (en) * | 1952-03-27 | 1956-06-05 | Apra Precipitator Corp | Vortex-electrostatic gas cleaner |
US2983332A (en) * | 1956-11-02 | 1961-05-09 | Vicard Pierre Georges | Process and apparatus for the purification of gases |
US3357159A (en) * | 1966-09-06 | 1967-12-12 | Koppers Co Inc | Dust concentrator |
US5041145A (en) * | 1990-05-15 | 1991-08-20 | Niles Parts Co., Ltd. | Bridged stream corona generator |
US5066316A (en) * | 1989-10-06 | 1991-11-19 | Niles Parts Co., Ltd. | Exhaust gas purifying apparatus |
US5084078A (en) * | 1990-11-28 | 1992-01-28 | Niles Parts Co., Ltd. | Exhaust gas purifier unit |
US5591253A (en) * | 1995-03-07 | 1997-01-07 | Electric Power Research Institute, Inc. | Electrostatically enhanced separator (EES) |
US5922111A (en) * | 1994-08-30 | 1999-07-13 | Omi Kogyo Co., Ltd. | Electrostatic precipitator |
US20040168573A1 (en) * | 2001-07-16 | 2004-09-02 | Ragne Svadil | Air cleaner |
US20050000361A1 (en) * | 2003-07-02 | 2005-01-06 | Industrial Technology Research Institute | Adjustable eddy electrostatic precipitator |
US6964698B1 (en) * | 2004-06-07 | 2005-11-15 | Balcke-Durr Gmbh | Gas supply for electrostatic filter and electrostatic filter arrangement |
US7156902B1 (en) * | 2005-05-04 | 2007-01-02 | Electric Power Research Institute | Wet electro-core gas particulate separator |
US20190056300A1 (en) * | 2015-11-13 | 2019-02-21 | Virginia Commonwealth University | Curved classifiers and classification methods |
-
1920
- 1920-12-10 US US429667A patent/US1381719A/en not_active Expired - Lifetime
Cited By (23)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2594805A (en) * | 1945-06-26 | 1952-04-29 | Garrett Corp | Air cleaner |
US2615530A (en) * | 1949-11-25 | 1952-10-28 | Air Preheater | Liquid cleaned precipitator |
US2741331A (en) * | 1952-03-19 | 1956-04-10 | Sfindex | Electrostatic gas precipitation |
US2748888A (en) * | 1952-03-27 | 1956-06-05 | Apra Precipitator Corp | Vortex-electrostatic gas cleaner |
US2740493A (en) * | 1953-12-30 | 1956-04-03 | Research Corp | Gas cleaning method and apparatus |
US2983332A (en) * | 1956-11-02 | 1961-05-09 | Vicard Pierre Georges | Process and apparatus for the purification of gases |
US3357159A (en) * | 1966-09-06 | 1967-12-12 | Koppers Co Inc | Dust concentrator |
US5066316A (en) * | 1989-10-06 | 1991-11-19 | Niles Parts Co., Ltd. | Exhaust gas purifying apparatus |
US5041145A (en) * | 1990-05-15 | 1991-08-20 | Niles Parts Co., Ltd. | Bridged stream corona generator |
US5084078A (en) * | 1990-11-28 | 1992-01-28 | Niles Parts Co., Ltd. | Exhaust gas purifier unit |
US5922111A (en) * | 1994-08-30 | 1999-07-13 | Omi Kogyo Co., Ltd. | Electrostatic precipitator |
US5591253A (en) * | 1995-03-07 | 1997-01-07 | Electric Power Research Institute, Inc. | Electrostatically enhanced separator (EES) |
US5683494A (en) * | 1995-03-07 | 1997-11-04 | Electric Power Research Institute, Inc. | Electrostatically enhanced separator (EES) |
US20040168573A1 (en) * | 2001-07-16 | 2004-09-02 | Ragne Svadil | Air cleaner |
US7048787B2 (en) * | 2001-07-16 | 2006-05-23 | Ragne Svadil | Air cleaner |
US20050000361A1 (en) * | 2003-07-02 | 2005-01-06 | Industrial Technology Research Institute | Adjustable eddy electrostatic precipitator |
US6962620B2 (en) * | 2003-07-02 | 2005-11-08 | Industrial Technology Research Institute | Adjustable eddy electrostatic precipitator |
US6964698B1 (en) * | 2004-06-07 | 2005-11-15 | Balcke-Durr Gmbh | Gas supply for electrostatic filter and electrostatic filter arrangement |
US20050268784A1 (en) * | 2004-06-07 | 2005-12-08 | Thomas Davis | Gas supply for electrostatic filter and electrostatic filter arrangement |
AU2005202330B2 (en) * | 2004-06-07 | 2009-12-03 | Howden Rothemühle GmbH. | Gas supply for electrostatic filters and electrostatic filter arrangement |
US7156902B1 (en) * | 2005-05-04 | 2007-01-02 | Electric Power Research Institute | Wet electro-core gas particulate separator |
US20190056300A1 (en) * | 2015-11-13 | 2019-02-21 | Virginia Commonwealth University | Curved classifiers and classification methods |
US10845288B2 (en) * | 2015-11-13 | 2020-11-24 | Virginia Commonwealth University | Curved classifiers and classification methods |
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