US3061994A - Dust collector device - Google Patents

Dust collector device Download PDF

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Publication number
US3061994A
US3061994A US63288A US6328860A US3061994A US 3061994 A US3061994 A US 3061994A US 63288 A US63288 A US 63288A US 6328860 A US6328860 A US 6328860A US 3061994 A US3061994 A US 3061994A
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hopper
tube
gases
flanges
tubes
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US63288A
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Lauritz E Mylting
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Allen Sherman Hoff Co
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Allen Sherman Hoff Co
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04CAPPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C5/00Apparatus in which the axial direction of the vortex is reversed
    • B04C5/24Multiple arrangement thereof
    • B04C5/28Multiple arrangement thereof for parallel flow

Definitions

  • outer tubes it has been customary to provide a lower deck which carried the outer tubes and which was carried by the upper end of the solids collecting hopper, a conduit to carry gases to and from said tubes, and, between the inlet and outlet of the gas carrying duct, to provide an upper deck which suspended the inner tubes with their lower end portions projecting into the outer tubes. It has been proposed to provide tubes with flanges which were to be welded together to form the lower deck.
  • the present invention aims to overcome those disadvantages and achieves that aim by means of a new simplied and less expensive construction.
  • FiGURE 1 is a fragmentary, vertical sectional view of one form of apparatus embodying the present inven tion;
  • FiGURE 2 is a fragmentary plan view taken on line 2--2 of FIGURE 1;
  • FIGURE 3 is a fragmentary side elevational View of one of the flanged tubes of FIGURES 1 and 2.
  • the drawings show a cyclone unit including a collecting hopper 1 which is rectangular in horizontal section in its upper portion and has a bottom discharge opening (not shown), a conduit 2 for conducting gases to and from the hopper and a bafe 3 which is spaced above the top of the hopper and which divides the conduit 2 into an inlet chamber 5 and an outlet chamber 6.
  • Means is provided in the upper part of the hopper for separating line solids from gases flowing through conduit 2 and chamber 5.
  • This means includes a plurality of tube units, each consisting of an inner tube 10 and an outer tube 11.
  • Each inner tube extends down through the bale 3 and at its upper end is supported thereby, as by ring 12, and at its lower end projects into the upper end of the outer tube 11 and is connected thereto.
  • each tube unit is supported solely from baille 3.
  • the inner tube is of smaller diameter than the outer tube and thus an annular space is provided between the tubes of each unit through which gases and solids may flow downwardly.
  • means is provided in each annular space for giving the descending gases a swirling motion to facilitate the separation of the solids from the gases.
  • the illustrated means for producing this swirling action is the spiral vane 13 which is connected to the inner tube, spans the annular space and is connected to the outer tube.
  • the lower ends of the outer tubes 11 are preferably frusto-conical, as indicated at 14.
  • Means is provided for insuring that substantially all flow of gases into or out of the hopper will take place through the tube units.
  • This means comprises llanges 16 attached to, and extending outwardly from, the upper ends of the outer tubes 11, a filler 17 closing the upper end of the hopper around the several tube units and resting on ange 18 of the hopper; and packing filling the spaced between the adjacent flanges and between the flanges of the outermost tube units and the ller.
  • Each flange 16 is provided with an encircling groove 19 in which suitable packing 20, such as asbestos rope and the like, is disposed and a corresponding groove is provided in the filler to cooperate with the grooves in the adjacent flanges.
  • the flanges 16 are hexagonal and the filler 17 is rectangular to lit the top of the hopper, as shown in FIGURE 2, but the flanges may be of any desired configuration, and the hopper may also be of any desired horizontal cross sectional shape.
  • Apparatus for removing line solids from gases comprising a collecting hopper, a conduit for conducting gases to and from the upper end of said hopper, a baille spaced from the top of the hopper and dividing the conduit into inlet and outlet chambers, means including a plurality of tube units in the upper part of the hopper for separating iine solids from gases flowing through said inlet chamber, each of said units including an inner tube supported by and extending down through said baille and into said hopper, and an outer tube secured to the lower end portion of the inner tube and defining an annular space about the inner tube, and means for insuring that substantially all the gases flowing through the conduit will pass through said units, said flow-insuring means including flanges extending outwardly from the upper end portions of the outer tubes, a gas impervious filler closing the upper end of the hopper and surrounding the tube units and packing between the several anges and between the filler and the flanges adjacent thereto.
  • Apparatus for removing fine solids from gases comprising a collecting hopper, a conduit for conducting gases to and from the upper end of said hopper, a bale spaced from the top of the hopper and dividing the conduit into inlet and outlet chambers, means including a plurality of tube units in the upper part of the hopper for separating fine solids from gases tlowing through said inlet chamber, each of said units including an inner tube supported by and extending down through said bale and into said hopper, an outer tube around the lower end portion of the inner tube and defining an annular space about the latter, and a spiral vane spanning said space and connecting the two tubes together, and means for insuring that substantially all the gases owing in the conduit will pass through said units, said flow-insuring means including anges extending outwardly from the upper end portions of the outer tubes, a gas impervious filler closing the upper end of the hopper and surrounding the tube units and packing between the several anges and between the iller and the anges adjacent thereto.
  • Apparatus for removing tine solids from gases comprising a collecting hopper, a conduit for conducting gases to and from the upper end of said hopper, a bale spaced from the top of the hopper and dividing the conduit into inlet and outlet chambers, means including a plurality of tube units in the upper part of the hopper for separating ne solids from gases owing through said conduit, each of said units including an inner tube supported by and extending down through said bale and into the hopper and an outer tube in the hopper, secured to the lower end portion of the inner tube and defining an annular space about the latter, flanges extending outwardly from the upper ends of said outer tubes and having peripheral grooves for packing, a gas impervious l'ler closing the upper end of the hopper, surrounding the tube units and having a groove in its inner periphery, and packing filling said grooves and serving to prevent ow of gases between the flanges and between the flanges and ller.

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  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)

Description

Nov. 6, 1962 MYLTING DUST COLLECTOR DEVICE Filed Oct. 18. 1960 United States Patent Office 3,061,994 Patented Nov. 6, 1962 3,061,994 DUST CGLLECTOR DEVICE Lanritz E. Myiting, Ardmore, Pa., assignor to The Allen Sherman Hoff Company, Wynnewood, Pa., a corpora-v tion of Pennsylvania Filed (ict. 18, 196), Ser. No. 63,288 3 Claims. (Cl. 55-346) outer tubes, it has been customary to provide a lower deck which carried the outer tubes and which was carried by the upper end of the solids collecting hopper, a conduit to carry gases to and from said tubes, and, between the inlet and outlet of the gas carrying duct, to provide an upper deck which suspended the inner tubes with their lower end portions projecting into the outer tubes. It has been proposed to provide tubes with flanges which were to be welded together to form the lower deck.
These prior devices possessed certain disadvantages. For example, when a lower deck plate was used it was dimcult and expensive to align the tube receiving openings in the upper and lower decks so closely that the inner and outer tubes would be concentric. If the flanges of the outer tubes were to be welded together, the aligning problem would be aggravated by the tendency of the welded flanges to warp, distort or shift the position of the outer tubes out of alignment with the inner tubes. Moreover, the assembly of the tubes in the two decks or replacement of any of the tubes could not be carried out effectively or efficiently in the field.
The present invention aims to overcome those disadvantages and achieves that aim by means of a new simplied and less expensive construction.
The entire steel deck which supported the outer tubes in prior devices is eliminated together with the aligning problem inherent therewith, and the new combined inner and outer tube units may be more easily installed either in the shop or in the field and individual tube units may be easily replaced without disturbing adjacent tube units. Also the new tube units can be nested more closely than in prior devices and hence more tubes and more gas cleaning capacity is provided in a given space. These advantages are novel and afford considerable economies in construction and operation.
The present invention will be better understood from the following specification and the accompanying drawings in which:
FiGURE 1 is a fragmentary, vertical sectional view of one form of apparatus embodying the present inven tion;
FiGURE 2 is a fragmentary plan view taken on line 2--2 of FIGURE 1; and
FIGURE 3 is a fragmentary side elevational View of one of the flanged tubes of FIGURES 1 and 2.
The drawings show a cyclone unit including a collecting hopper 1 which is rectangular in horizontal section in its upper portion and has a bottom discharge opening (not shown), a conduit 2 for conducting gases to and from the hopper and a bafe 3 which is spaced above the top of the hopper and which divides the conduit 2 into an inlet chamber 5 and an outlet chamber 6.
Means is provided in the upper part of the hopper for separating line solids from gases flowing through conduit 2 and chamber 5. This means includes a plurality of tube units, each consisting of an inner tube 10 and an outer tube 11. Each inner tube extends down through the bale 3 and at its upper end is supported thereby, as by ring 12, and at its lower end projects into the upper end of the outer tube 11 and is connected thereto. Thus each tube unit is supported solely from baille 3.
The inner tube is of smaller diameter than the outer tube and thus an annular space is provided between the tubes of each unit through which gases and solids may flow downwardly. Preferably, means is provided in each annular space for giving the descending gases a swirling motion to facilitate the separation of the solids from the gases. The illustrated means for producing this swirling action is the spiral vane 13 which is connected to the inner tube, spans the annular space and is connected to the outer tube. The lower ends of the outer tubes 11 are preferably frusto-conical, as indicated at 14.
Means is provided for insuring that substantially all flow of gases into or out of the hopper will take place through the tube units. This means, as illustrated, comprises llanges 16 attached to, and extending outwardly from, the upper ends of the outer tubes 11, a filler 17 closing the upper end of the hopper around the several tube units and resting on ange 18 of the hopper; and packing filling the spaced between the adjacent flanges and between the flanges of the outermost tube units and the ller. Each flange 16 is provided with an encircling groove 19 in which suitable packing 20, such as asbestos rope and the like, is disposed and a corresponding groove is provided in the filler to cooperate with the grooves in the adjacent flanges. When the tube units are assembled in filler 17, and the packing 20 lills and is compressed in the opposed grooves 19 of the flanges and filler, the flow of gases between the several flanges and between the flanges and the filler will be substantially prevented.
Preferably, the flanges 16 are hexagonal and the filler 17 is rectangular to lit the top of the hopper, as shown in FIGURE 2, but the flanges may be of any desired configuration, and the hopper may also be of any desired horizontal cross sectional shape.
Having thus described this invention in such full, clear, concise and exact terms as to enable any person skilled in the art to which it pertains to make and use the same, and having set forth the best mode contemplated of carrying out this invention, I state that the subject matter which I regard as being my invention is particularly pointed out and distinctly claimed in what is claimed, it being understood that equivalents or modifications of, or substitutions for, parts of the above specifically described embodiment of the invention may be made without departing from the scope of the invention as set forth in what is claimed.
What is claimed is:
1. Apparatus for removing line solids from gases comprising a collecting hopper, a conduit for conducting gases to and from the upper end of said hopper, a baille spaced from the top of the hopper and dividing the conduit into inlet and outlet chambers, means including a plurality of tube units in the upper part of the hopper for separating iine solids from gases flowing through said inlet chamber, each of said units including an inner tube supported by and extending down through said baille and into said hopper, and an outer tube secured to the lower end portion of the inner tube and defining an annular space about the inner tube, and means for insuring that substantially all the gases flowing through the conduit will pass through said units, said flow-insuring means including flanges extending outwardly from the upper end portions of the outer tubes, a gas impervious filler closing the upper end of the hopper and surrounding the tube units and packing between the several anges and between the filler and the flanges adjacent thereto.
2. Apparatus for removing fine solids from gases comprising a collecting hopper, a conduit for conducting gases to and from the upper end of said hopper, a bale spaced from the top of the hopper and dividing the conduit into inlet and outlet chambers, means including a plurality of tube units in the upper part of the hopper for separating fine solids from gases tlowing through said inlet chamber, each of said units including an inner tube supported by and extending down through said bale and into said hopper, an outer tube around the lower end portion of the inner tube and defining an annular space about the latter, and a spiral vane spanning said space and connecting the two tubes together, and means for insuring that substantially all the gases owing in the conduit will pass through said units, said flow-insuring means including anges extending outwardly from the upper end portions of the outer tubes, a gas impervious filler closing the upper end of the hopper and surrounding the tube units and packing between the several anges and between the iller and the anges adjacent thereto.
3. Apparatus for removing tine solids from gases comprising a collecting hopper, a conduit for conducting gases to and from the upper end of said hopper, a bale spaced from the top of the hopper and dividing the conduit into inlet and outlet chambers, means including a plurality of tube units in the upper part of the hopper for separating ne solids from gases owing through said conduit, each of said units including an inner tube supported by and extending down through said bale and into the hopper and an outer tube in the hopper, secured to the lower end portion of the inner tube and defining an annular space about the latter, flanges extending outwardly from the upper ends of said outer tubes and having peripheral grooves for packing, a gas impervious l'ler closing the upper end of the hopper, surrounding the tube units and having a groove in its inner periphery, and packing filling said grooves and serving to prevent ow of gases between the flanges and between the flanges and ller.
References Cited in the file of this patent UNITED STATES PATENTS 1,909,184 Lissman May 16, 1933 2,662,610 Heinrich Dec. 15, 1953 2,904,130 Chapler Sept. 15, 1959
US63288A 1960-10-18 1960-10-18 Dust collector device Expired - Lifetime US3061994A (en)

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Cited By (27)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3279156A (en) * 1963-12-21 1966-10-18 Svenska Flaektfabriken Ab Gas-cleaning apparatus
US3365058A (en) * 1965-07-06 1968-01-23 Universal Oil Prod Co Particle classifying-separating apparatus
US3401506A (en) * 1967-04-27 1968-09-17 Universal Oil Prod Co Centrifugal separators
US3425192A (en) * 1966-12-12 1969-02-04 Mitchell Co John E Vacuum cleaning system
US3572015A (en) * 1967-05-31 1971-03-23 Sulzer Ag Water separator for saturated-steam generators
DE2439648A1 (en) * 1974-07-09 1976-01-29 Asizawa Tekko Kk Multi-cyclone dust suppressor with even distribution of crude gas - for cyclone units with waste gas cylinders of varying length
US3940331A (en) * 1974-11-01 1976-02-24 Rastatter Edward L Vortical cyclone cluster apparatus
US4146469A (en) * 1977-10-11 1979-03-27 Clark & Vicario Corporation Mounting of cleaners in papermaking system
EP0003594A1 (en) * 1978-02-13 1979-08-22 STEIN INDUSTRIE Société anonyme dite: Jonction device for parallel tubes of a cyclone separator
US4273565A (en) * 1978-05-05 1981-06-16 Exxon Research & Engineering Co. Cyclone support
US5690709A (en) * 1995-08-09 1997-11-25 Barnes; Peter Haddon Separation apparatus to remove particles from a gas stream
US6174339B1 (en) 1999-03-16 2001-01-16 Uop Llc Multiple separator arrangement for fluid-particle separation
US20100011961A1 (en) * 2006-07-07 2010-01-21 Edwin Poorte Fluid separating vessel
US20100139633A1 (en) * 2006-10-02 2010-06-10 Mann+Hummel Gmbh Device for Separating Particles from a Gas Stream
US20100258008A1 (en) * 2009-04-09 2010-10-14 Mao-Nan Cheng Oil mist separator
US20110259819A1 (en) * 2007-07-30 2011-10-27 Stephen Beedie Cyclone apparatus
US20120284952A1 (en) * 2011-05-11 2012-11-15 Dyson Technology Limited Surface treating appliance
US8707512B2 (en) 2011-05-11 2014-04-29 Dyson Technology Limited Surface treating appliance
US8806708B2 (en) 2011-05-11 2014-08-19 Dyson Technology Limited Surface treating appliance
US8826492B2 (en) 2011-05-11 2014-09-09 Dyson Technology Limited Surface treating appliance
US8932472B2 (en) 2011-10-25 2015-01-13 National Oilwell Varco, L.P. Separator system and related methods
US9044125B2 (en) 2011-05-11 2015-06-02 Dyson Technology Limited Surface treating appliance
US9044126B2 (en) 2011-05-11 2015-06-02 Dyson Technology Limited Surface treating appliance
US9204771B2 (en) 2011-05-11 2015-12-08 Dyson Technology Limited Surface treating appliance
US9282863B2 (en) 2011-05-11 2016-03-15 Dyson Technology Limited Surface treating appliance
US20180043292A1 (en) * 2015-03-03 2018-02-15 Shell Oil Company Swirl tube separators
US10919053B2 (en) 2016-04-05 2021-02-16 Cory M Holdings Ltd. Particulate separator

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1909184A (en) * 1930-12-08 1933-05-16 Int Precipitation Co Centrifugal separator
US2662610A (en) * 1950-08-04 1953-12-15 Oswald X Heinrich Apparatus for centrifugal separation of suspended particles
US2904130A (en) * 1956-10-24 1959-09-15 Western Precipitation Corp Construction of multiple tube cyclone dust collector

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1909184A (en) * 1930-12-08 1933-05-16 Int Precipitation Co Centrifugal separator
US2662610A (en) * 1950-08-04 1953-12-15 Oswald X Heinrich Apparatus for centrifugal separation of suspended particles
US2904130A (en) * 1956-10-24 1959-09-15 Western Precipitation Corp Construction of multiple tube cyclone dust collector

Cited By (34)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3279156A (en) * 1963-12-21 1966-10-18 Svenska Flaektfabriken Ab Gas-cleaning apparatus
US3365058A (en) * 1965-07-06 1968-01-23 Universal Oil Prod Co Particle classifying-separating apparatus
US3425192A (en) * 1966-12-12 1969-02-04 Mitchell Co John E Vacuum cleaning system
US3401506A (en) * 1967-04-27 1968-09-17 Universal Oil Prod Co Centrifugal separators
US3572015A (en) * 1967-05-31 1971-03-23 Sulzer Ag Water separator for saturated-steam generators
DE2439648A1 (en) * 1974-07-09 1976-01-29 Asizawa Tekko Kk Multi-cyclone dust suppressor with even distribution of crude gas - for cyclone units with waste gas cylinders of varying length
US3940331A (en) * 1974-11-01 1976-02-24 Rastatter Edward L Vortical cyclone cluster apparatus
US3984308A (en) * 1974-11-01 1976-10-05 Rastatter Edward L Vortical cyclone cluster apparatus
US4146469A (en) * 1977-10-11 1979-03-27 Clark & Vicario Corporation Mounting of cleaners in papermaking system
FR2416733A1 (en) * 1978-02-13 1979-09-07 Stein Industrie JUNCTION DEVICE FOR TUBULAR ELEMENTS PARALLEL OF A CYCLONE SEPARATOR
EP0003594A1 (en) * 1978-02-13 1979-08-22 STEIN INDUSTRIE Société anonyme dite: Jonction device for parallel tubes of a cyclone separator
US4273565A (en) * 1978-05-05 1981-06-16 Exxon Research & Engineering Co. Cyclone support
US5690709A (en) * 1995-08-09 1997-11-25 Barnes; Peter Haddon Separation apparatus to remove particles from a gas stream
US6174339B1 (en) 1999-03-16 2001-01-16 Uop Llc Multiple separator arrangement for fluid-particle separation
US20100011961A1 (en) * 2006-07-07 2010-01-21 Edwin Poorte Fluid separating vessel
US8025706B2 (en) * 2006-07-07 2011-09-27 Shell Oil Company Fluid separating vessel
US20100139633A1 (en) * 2006-10-02 2010-06-10 Mann+Hummel Gmbh Device for Separating Particles from a Gas Stream
US7938872B2 (en) * 2006-10-02 2011-05-10 Mann + Hummel Gmbh Device for separating particles from a gas stream
US20110259819A1 (en) * 2007-07-30 2011-10-27 Stephen Beedie Cyclone apparatus
US8439206B2 (en) * 2007-07-30 2013-05-14 Merpro Tortek Limited Cyclone apparatus
US20100258008A1 (en) * 2009-04-09 2010-10-14 Mao-Nan Cheng Oil mist separator
US7931718B2 (en) * 2009-04-09 2011-04-26 San Ford Machinery Co., Ltd. Oil mist separator
US9204771B2 (en) 2011-05-11 2015-12-08 Dyson Technology Limited Surface treating appliance
US8707511B2 (en) * 2011-05-11 2014-04-29 Dyson Technology Limited Surface treating appliance
US8707512B2 (en) 2011-05-11 2014-04-29 Dyson Technology Limited Surface treating appliance
US8806708B2 (en) 2011-05-11 2014-08-19 Dyson Technology Limited Surface treating appliance
US8826492B2 (en) 2011-05-11 2014-09-09 Dyson Technology Limited Surface treating appliance
US9044125B2 (en) 2011-05-11 2015-06-02 Dyson Technology Limited Surface treating appliance
US9044126B2 (en) 2011-05-11 2015-06-02 Dyson Technology Limited Surface treating appliance
US20120284952A1 (en) * 2011-05-11 2012-11-15 Dyson Technology Limited Surface treating appliance
US9282863B2 (en) 2011-05-11 2016-03-15 Dyson Technology Limited Surface treating appliance
US8932472B2 (en) 2011-10-25 2015-01-13 National Oilwell Varco, L.P. Separator system and related methods
US20180043292A1 (en) * 2015-03-03 2018-02-15 Shell Oil Company Swirl tube separators
US10919053B2 (en) 2016-04-05 2021-02-16 Cory M Holdings Ltd. Particulate separator

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