GB297446A - - Google Patents

Info

Publication number
GB297446A
GB297446A GB10754/28A GB1075428A GB297446A GB 297446 A GB297446 A GB 297446A GB 10754/28 A GB10754/28 A GB 10754/28A GB 1075428 A GB1075428 A GB 1075428A GB 297446 A GB297446 A GB 297446A
Authority
GB
United Kingdom
Prior art keywords
dust
separator
pipe
water
gases
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
GB10754/28A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
AMERICAN BLOWER Corp
Original Assignee
AMERICAN BLOWER Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by AMERICAN BLOWER Corp filed Critical AMERICAN BLOWER Corp
Publication of GB297446A publication Critical patent/GB297446A/en
Expired legal-status Critical Current

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
    • B01D45/12—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces
    • B01D45/14—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces generated by rotating vanes, discs, drums or brushes
    • 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
    • B04C5/00—Apparatus in which the axial direction of the vortex is reversed
    • B04C5/02—Construction of inlets by which the vortex flow is generated, e.g. tangential admission, the fluid flow being forced to follow a downward path by spirally wound bulkheads, or with slightly downwardly-directed tangential admission
    • 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
    • B04C5/00—Apparatus in which the axial direction of the vortex is reversed
    • B04C5/08—Vortex chamber constructions
    • B04C5/103—Bodies or members, e.g. bulkheads, guides, in the vortex chamber
    • 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

Landscapes

  • Physics & Mathematics (AREA)
  • Fluid Mechanics (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Separating Particles In Gases By Inertia (AREA)
  • Cyclones (AREA)

Abstract

297,446. American Blower Corporation, (Assignees of Morse, C. T., and Hogan, E. L.). Sept. 22, 1927, [Convention date]. Density separators.-Dust-laden gases, such as the gases from the blast furnace 1, are led to the separator 3 in which the heavy dust parrticles, are separated, while the gas with a quantity of fine dust passes through the pipe 7 to the disintegrator 8. Water is sprayed into this machine from the pipe 9 and the moistened gas passes through the pipe 10 to the separator 11. This has a closed conical casing 12 with a tangential inlet 15 anc a spiral track 16 which decreases in width from the inlet until it terminates in a point 18 at the dust outlet 17. The water and dust are deposited on the track 16 and pass downwards to the vessel 13; the clean gas passes out through the central tube 14. The heavy dust from the first separator 3 drops into the container 5 and is returned by the conveyer 6 to the furnace 1.
GB10754/28A 1927-09-22 1928-04-11 Expired GB297446A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US297446TA 1927-09-22 1927-09-22

Publications (1)

Publication Number Publication Date
GB297446A true GB297446A (en) 1929-02-07

Family

ID=31945801

Family Applications (1)

Application Number Title Priority Date Filing Date
GB10754/28A Expired GB297446A (en) 1927-09-22 1928-04-11

Country Status (3)

Country Link
BE (1) BE351051A (en)
FR (1) FR653406A (en)
GB (1) GB297446A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4357152A (en) * 1979-07-02 1982-11-02 Progressive Development, Inc. Fluid borne particulate separator

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE113599C (en) * 1952-10-15

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4357152A (en) * 1979-07-02 1982-11-02 Progressive Development, Inc. Fluid borne particulate separator

Also Published As

Publication number Publication date
FR653406A (en) 1929-03-21
BE351051A (en)

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