CN2592280Y - Cone-diffusion cyclone separator - Google Patents
Cone-diffusion cyclone separator Download PDFInfo
- Publication number
- CN2592280Y CN2592280Y CN 02288300 CN02288300U CN2592280Y CN 2592280 Y CN2592280 Y CN 2592280Y CN 02288300 CN02288300 CN 02288300 CN 02288300 U CN02288300 U CN 02288300U CN 2592280 Y CN2592280 Y CN 2592280Y
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- cyclone separator
- cone
- air inlet
- inlet pipe
- utility
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Abstract
The utility model relates to a cone-diffusion cyclone separator, wherein, an intake pipe of which is a scroll case type of 180 DEG and is arranged on the upper part of a conic cylinder body, an exhaust pipe is in the shape of inverted cone and is inserted into the cylinder body via the middle of the scroll case type intake pipe, and the insertion depth of the exhaust pipe is shallower and is bigger than the height of the intake pipe. The lower part of the conic cylinder body is connected with an inverted cone-shaped flue-dust retainer. The new structure of the utility model enlarges the flow area of an inlet and reduces the resistance of the inlet, the secondary carrying is not easily caused, and accordingly, the separation efficiency of solid particles is improved.
Description
Technical field:
The utility model relates to a kind of conical diffusion type cyclone separator, is used for the solid particle of separation bubble, belongs to the Thermal Power Engineering technical field.
Background technology:
In boiler, chemical industry equipment, there is Dual-Phrase Distribution of Gas olid, often needs on the technology solid particle in the air-flow is separated.With the CFBB is example, need with cyclone separator the solid particle in the flue gas stream be separated at boiler furnace outlet, again solid particle is returned lower furnace portion, finishes the interior circulation of stove of solid particle, to improve efficiency of combustion and desulfuration efficiency.The cylindrical shell and the outlet section of existing cyclone separator are cylindrical, influence the solid particle separating effect owing to the air-flow secondary carries, and the resistance of outlet section is also bigger than normal.In these general cylindrical tube cyclone separators, some air-flow enters the bottom ash bucket with particle, produces inside vortex when air-flow upwards flows to blast pipe again, and the particle secondary that has separated is carried, and taken away by exit flow, influence the solid particle separative efficiency.
The utility model content:
The purpose of this utility model is at the deficiencies in the prior art, and a kind of conical diffusion type cyclone separator of new structure is provided, to improve the resistance of solid particle separative efficiency and reduction blast pipe.
For realizing such purpose, cyclone separator of the present utility model comprises air inlet pipe, blast pipe, separator cylindrical shell and flue-dust retainer, air inlet pipe is 180 ° of scroll casing types, be installed in the top of divergent-cone wall, blast pipe is a back taper, inserts in the cylindrical shell in the middle of the scroll casing type air inlet pipe, and its insertion depth is more shallow, but greater than the height of air inlet pipe, the bottom of divergent-cone wall connects the back taper flue-dust retainer.
180 ° of scroll casing type air inlet pipe sectional dimensions of the present utility model are determined by inlet velocity, back taper blast pipe and bottom flue-dust retainer, and selecting for use by the requirement of efficient separate solid particles of the cone angle of conic tube and cyclone separator each several part physical dimension determined.
When conical diffusion type cyclone separator of the present utility model is worked, after dust-contained airflow enters cylindrical shell from 180 ° of scroll casing type inlets, be subjected to centrifugal action rotation and descend, then along conical wall decline, the gas major part that has purified is discharged from blast pipe by the isolated particle of centrifugal force.Because the divergent-cone wall lower diameter increases, the inside vortex intensity that the fraction air-flow produces when upwards flowing to blast pipe a little less than, and apart from cylinder inboard wall apart from increase, be difficult for causing secondary to carry, thereby improve the solid particle separative efficiency.
Conical diffusion type cyclone separator of the present utility model can reach the purpose of efficient low-resistance, adopt the scroll casing type inlet to be easy to increase the inlet flow area, inlet volute shape annular space makes inlet air flow nearer apart from cylinder inboard wall, reduced the settling height of particle, helped the separation of particle to inwall.Scroll casing type inlet also can reduce the mutual interference mutually of inlet air flow and inside vortex air-flow, reduces entrance friction.Adopt the blast pipe of back taper, insertion depth is more shallow, can reduce the resistance of outlet section.
The drawing explanation and the specific embodiment:
Fig. 1 is the schematic top plan view of the utility model structure.
Fig. 2 is the front elevational schematic of the utility model structure.
Shown in Figure 2 as Fig. 1, cyclone separator of the present utility model comprises air inlet pipe 1, blast pipe 3, separator cylindrical shell 2 and flue-dust retainer 4, air inlet pipe 1 is 180 ° of scroll casing types, be installed in the top of divergent-cone wall 2, blast pipe 3 is a back taper, inserts in the cylindrical shell 2 in the middle of scroll casing type air inlet pipe 1, and its insertion depth is more shallow, but greater than the height of air inlet pipe 1, the bottom of divergent-cone wall 2 connects back taper flue-dust retainer 4.
In separator when work, after dust-contained airflow enters cylindrical shell 2 from the inlet of 180 ° of scroll casing type air inlet pipe 1, be subjected to the centrifugal action rotation and descend, then descended along the conical wall of cylindrical shell 2 by the isolated particle of centrifugal force, and the gas major part that has purified is from blast pipe 3 discharges.Because the lower diameter of divergent-cone wall 2 increases, the inside vortex intensity that produces when the fraction air-flow upwards flows to blast pipe 3 a little less than, and apart from cylindrical shell 2 inwalls apart from increase, be difficult for causing secondary to carry, thereby improve the solid particle separative efficiency.
Claims (1)
1, a kind of conical diffusion type cyclone separator, comprise air inlet pipe (1), blast pipe (3), separator cylindrical shell (2) and flue-dust retainer (4), it is characterized in that air inlet pipe (1) is 180 ° of scroll casing types, be installed in the top of divergent-cone wall (2), blast pipe (3) is a back taper, inserts in the cylindrical shell (2) in the middle of scroll casing type air inlet pipe (1), and its insertion depth is more shallow, but greater than the height of air inlet pipe (1), the bottom of divergent-cone wall (2) connects back taper flue-dust retainer (4).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 02288300 CN2592280Y (en) | 2002-12-12 | 2002-12-12 | Cone-diffusion cyclone separator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 02288300 CN2592280Y (en) | 2002-12-12 | 2002-12-12 | Cone-diffusion cyclone separator |
Publications (1)
Publication Number | Publication Date |
---|---|
CN2592280Y true CN2592280Y (en) | 2003-12-17 |
Family
ID=33748236
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 02288300 Expired - Fee Related CN2592280Y (en) | 2002-12-12 | 2002-12-12 | Cone-diffusion cyclone separator |
Country Status (1)
Country | Link |
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CN (1) | CN2592280Y (en) |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102614721A (en) * | 2012-04-25 | 2012-08-01 | 任文建 | Booster-type air filter |
CN102773162A (en) * | 2012-08-02 | 2012-11-14 | 上海交通大学 | Method for removing fine particles and heavy metals in coal fume |
CN103286011A (en) * | 2013-05-22 | 2013-09-11 | 江苏新鹏重型机电制造有限公司 | Diffusion type cyclone dust collector |
CN103962249A (en) * | 2013-01-29 | 2014-08-06 | 昆山尚达智机械有限公司 | Cyclone separator |
CN107716130A (en) * | 2017-11-10 | 2018-02-23 | 重庆市贵金象炭黑有限责任公司 | A kind of fine powder collection device and its system |
CN109187108A (en) * | 2018-09-25 | 2019-01-11 | 泰山学院 | A kind of automatic sand-taped instrument of multistage reduction of speed formula and working method |
CN109225689A (en) * | 2018-10-24 | 2019-01-18 | 华辰天诚科技有限公司 | A kind of tubular cyclones |
CN111085049A (en) * | 2019-12-17 | 2020-05-01 | 上海交通大学 | Dust removal separation device with center bent and biased air outlet |
-
2002
- 2002-12-12 CN CN 02288300 patent/CN2592280Y/en not_active Expired - Fee Related
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102614721A (en) * | 2012-04-25 | 2012-08-01 | 任文建 | Booster-type air filter |
CN102773162A (en) * | 2012-08-02 | 2012-11-14 | 上海交通大学 | Method for removing fine particles and heavy metals in coal fume |
CN102773162B (en) * | 2012-08-02 | 2015-05-20 | 上海交通大学 | Method for removing fine particles and heavy metals in coal fume |
CN103962249A (en) * | 2013-01-29 | 2014-08-06 | 昆山尚达智机械有限公司 | Cyclone separator |
CN103286011A (en) * | 2013-05-22 | 2013-09-11 | 江苏新鹏重型机电制造有限公司 | Diffusion type cyclone dust collector |
CN107716130A (en) * | 2017-11-10 | 2018-02-23 | 重庆市贵金象炭黑有限责任公司 | A kind of fine powder collection device and its system |
CN109187108A (en) * | 2018-09-25 | 2019-01-11 | 泰山学院 | A kind of automatic sand-taped instrument of multistage reduction of speed formula and working method |
CN109225689A (en) * | 2018-10-24 | 2019-01-18 | 华辰天诚科技有限公司 | A kind of tubular cyclones |
CN109225689B (en) * | 2018-10-24 | 2023-08-22 | 华辰天诚科技有限公司 | Tubular cyclone separator |
CN111085049A (en) * | 2019-12-17 | 2020-05-01 | 上海交通大学 | Dust removal separation device with center bent and biased air outlet |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C19 | Lapse of patent right due to non-payment of the annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |