GB992386A - Method for separating particles of dust or liquid from gases and cyclone collector orprecipitator for carrying out the method - Google Patents

Method for separating particles of dust or liquid from gases and cyclone collector orprecipitator for carrying out the method

Info

Publication number
GB992386A
GB992386A GB1742864A GB1742864A GB992386A GB 992386 A GB992386 A GB 992386A GB 1742864 A GB1742864 A GB 1742864A GB 1742864 A GB1742864 A GB 1742864A GB 992386 A GB992386 A GB 992386A
Authority
GB
United Kingdom
Prior art keywords
dust
ducts
gas
chamber
duct
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
GB1742864A
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.)
Schuchtermann & Kremer Baum AG
Original Assignee
Schuchtermann & Kremer Baum AG
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 Schuchtermann & Kremer Baum AG filed Critical Schuchtermann & Kremer Baum AG
Publication of GB992386A publication Critical patent/GB992386A/en
Expired legal-status Critical Current

Links

Classifications

    • 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
    • B04C5/02Construction 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
    • B04C5/04Tangential inlets
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D45/00Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
    • B01D45/12Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04CAPPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C3/00Apparatus in which the axial direction of the vortex flow following a screw-thread type line remains unchanged ; Devices in which one of the two discharge ducts returns centrally through the vortex chamber, a reverse-flow vortex being prevented by bulkheads in the central discharge duct
    • 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
    • B04C5/14Construction of the underflow ducting; Apex constructions; Discharge arrangements ; discharge through sidewall provided with a few slits or perforations
    • B04C5/18Construction of the underflow ducting; Apex constructions; Discharge arrangements ; discharge through sidewall provided with a few slits or perforations with auxiliary fluid assisting discharge
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04CAPPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C9/00Combinations with other devices, e.g. fans, expansion chambers, diffusors, water locks
    • B04C2009/001Combinations with other devices, e.g. fans, expansion chambers, diffusors, water locks with means for electrostatic separation

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Physics & Mathematics (AREA)
  • Fluid Mechanics (AREA)
  • Separation Of Particles Using Liquids (AREA)

Abstract

992,386. Cyclone separators; electrostatic precipitators. SCHUCHTERMANN & KREMER-BAUM A.G. FUR AUFBEREITUNG. April 27, 1964 [May 14, 1963 ; Feb.14, 1964], No. 17428/64. Headings B2J and B2P. [Also in Division G3] In a cyclone for separating dust or liquid particles from a gas, Fig. 1, at least two axially spaced inlet ducts 4, 5 open out tangentially and in the same tangential direction into the cyclone turbulence chamber 1, the duct 4, which is adjacent the particle-collecting chamber 2 at one end of the turbulence chamber, feeding particle-laden gas to the turbulence chamber and the duct 5, which is adjacent a purified gas central outlet 3 at the other end of the turbulence chamber, feeding to the turbulence chamber an auxiliary gas current for the purpose of accelerating the rotation of purified gas currents so that any fine particles entrained therein are separated before discharge through the outlet 3. The auxiliary gas may be pure or particle-laden gas. A plurality of inlet ducts may be distributed at regular intervals over the periphery of the turbulence chamber at the levels of ducts 4, 5. In the dust separator shown, the kinetic energies of the dust-laden and auxiliary gas currents may be adjusted to each other in such a manner that the auxiliary gas current predominates and thus displaces into the dust-collecting chamber 2 the total current which carries with it the separated dust. Alternatively, the kinetic energies are adjusted in such a manner that in the space between the ducts 4 and 5 in the chamber 1, a neutral zone x is formed in which the axial components of motion of the two gas currents balance each other out so that the dust ejected by centrifugal action accumulates to form a rotating dust ring a from which, when saturation is reached, dust drops into the collecting chamber 2 as more dust is fed with the dust-laden gas. In order to maintain the neutral zone x between the ducts 4 and 5, the pressure ratio of the dustladen and auxiliary gas currents in the ducts is kept constant by an automatic control device shown in Fig. 2. Throttling members 14, 15 provided in the ducts 4, 5 are operated by a piston 16 controlled by pressure calibrators 17, 18 responsive to the pressures in the ducts 4, 5. The diaphragms of the calibrators engage the free ends of a balance beam 23 in opposition to springs 21, 22 which are adjustably tensioned to give the desired pressure ratio in the ducts. Baffle plates 24, 25 secured to the beam 23 control the discharge from nozzles 26, 27, of fluid supplied by a conduit 29 to the working spaces in the cylinder 28 on both sides of the piston 16. In operation, should, for example, the pressure in the duct 5 increase, the balance beam 23 rotates, from its neutral position shown, in a clockwise direction causing the baffle plate 24 to move closer to the nozzle 26 whereupon pressure increases in the left-hand working space of the cylinder and the piston 16 is displaced to the right with the result that the duct 5 is throttled to an increased extent by the member 15 with simultaneous reduced throttling action of the member 14 in the duct 4. As soon as the pressure ratio beyond the throttling members 14, 15 is restored, the balance beam 23 resumes its neutral position with the piston remaining in its new position. The separation of the dust may be improved by providing: (a) a rod-shaped discharge electrode 6 in the turbulence chamber the wall of which is earthed at 8 so as to function as a collecting electrode; (b) nozzles 9, 10 for spraying water into the rotating dust ring a and/or into the dust-laden gas current.
GB1742864A 1963-05-14 1964-04-27 Method for separating particles of dust or liquid from gases and cyclone collector orprecipitator for carrying out the method Expired GB992386A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DESC033274 1963-05-14
DESC034634 1964-02-14

Publications (1)

Publication Number Publication Date
GB992386A true GB992386A (en) 1965-05-19

Family

ID=25993080

Family Applications (1)

Application Number Title Priority Date Filing Date
GB1742864A Expired GB992386A (en) 1963-05-14 1964-04-27 Method for separating particles of dust or liquid from gases and cyclone collector orprecipitator for carrying out the method

Country Status (3)

Country Link
BE (1) BE647892A (en)
GB (1) GB992386A (en)
NL (1) NL6405283A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3851404A (en) * 1966-03-10 1974-12-03 Siemens Ag Apparatus for drying particulate matter with gaseous media
CN109432916A (en) * 2018-12-18 2019-03-08 江苏徐工工程机械研究院有限公司 Dust pelletizing system and pitch mixing station

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3851404A (en) * 1966-03-10 1974-12-03 Siemens Ag Apparatus for drying particulate matter with gaseous media
CN109432916A (en) * 2018-12-18 2019-03-08 江苏徐工工程机械研究院有限公司 Dust pelletizing system and pitch mixing station

Also Published As

Publication number Publication date
NL6405283A (en) 1964-11-16
BE647892A (en) 1964-08-31

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