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 methodInfo
- 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
Links
- 239000000428 dust Substances 0.000 title abstract 10
- 239000007788 liquid Substances 0.000 title abstract 2
- 239000002245 particle Substances 0.000 title abstract 2
- 239000007789 gas Substances 0.000 title 1
- 230000007935 neutral effect Effects 0.000 abstract 4
- 239000012717 electrostatic precipitator Substances 0.000 abstract 1
- 239000010419 fine particle Substances 0.000 abstract 1
- 239000012530 fluid Substances 0.000 abstract 1
- 238000000926 separation method Methods 0.000 abstract 1
- 238000005507 spraying Methods 0.000 abstract 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract 1
Classifications
-
- 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
- B04C5/04—Tangential inlets
-
- 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
-
- 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
- B04C3/00—Apparatus 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
-
- 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
- B04C5/14—Construction of the underflow ducting; Apex constructions; Discharge arrangements ; discharge through sidewall provided with a few slits or perforations
- B04C5/18—Construction of the underflow ducting; Apex constructions; Discharge arrangements ; discharge through sidewall provided with a few slits or perforations with auxiliary fluid assisting discharge
-
- 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
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.
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)
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 |
-
1964
- 1964-04-27 GB GB1742864A patent/GB992386A/en not_active Expired
- 1964-05-13 NL NL6405283A patent/NL6405283A/xx unknown
- 1964-05-13 BE BE647892A patent/BE647892A/xx unknown
Cited By (2)
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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