CN102923815B - Cyclone separator - Google Patents
Cyclone separator Download PDFInfo
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- CN102923815B CN102923815B CN2012104783529A CN201210478352A CN102923815B CN 102923815 B CN102923815 B CN 102923815B CN 2012104783529 A CN2012104783529 A CN 2012104783529A CN 201210478352 A CN201210478352 A CN 201210478352A CN 102923815 B CN102923815 B CN 102923815B
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- drain pipe
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Abstract
The invention relates to a cyclone separator particularly used for purification treatment of industrial water, and belongs to the field of chemical industry. The cyclone separator comprises a separator casing, a liquid outlet pipe, a liquid inlet pipe and a force reversing body, wherein the separator casing comprises a separator upper body, a separator middle body and a separator lower body, and one side of the separator upper body is tangential with and connected with the liquid inlet pipe. The upper end of the separator upper body is connected with the liquid outlet pipe; the separator middle body is connected to the lower end of the separator upper body; the lower end of the separator middle body is connected to the separator lower body; a second pressure relief vent is formed at a part of the liquid inlet pipe, which is positioned on in separator upper body; and a first pressure relief vent is formed at a part of the liquid outlet pipe, which is positioned in the separator upper body. The force reversing body is arranged in the separator lower body. The cyclone separator has simple, compact and reasonable structure, can effectively separate impurities in the industrial water for surface engineering, is good in separation effect, and lowers pollution to the environment.
Description
Technical field
The present invention relates to a kind of cyclone separator, specifically, for the purified treatment of water for industrial use, belong to chemical field.
Background technology
In prior art, the Coating Pretreatment of Surface Engineering, must eliminate rust and degreasing two road techniques to metal surface, the techniques such as the overwhelming majority adopts that pickling, alkali cleaning, ultrasonic wave are washed, a large amount of water for industrial use is through participating in surface treatment, produces a large amount of to contain oxide, SS floating thing, dust to impurity.General conventional surface engineering industry water for industrial use purified treatment adopts the precipitation method to carry out, precipitation method occupation area of equipment is large, cost is high, the sedimentation time is long, the filtration method velocity ratio is very fast, but need a large amount of filtering material of waste, owing to changing filtering material, must stop lock out operation, can not continuous operation.
The water for industrial use of current domestic Surface Engineering industry is due to the small solids that contains oil and solid, and the matter anharmonic ratio, near the matter anharmonic ratio of water, is difficult to water for industrial use is carried out to effective separating treatment, and the discharge of water for industrial use has caused ill effect to environment.
Summary of the invention
The object of the invention is to overcome above-mentioned weak point, thereby a kind of cyclone separator is provided, the impurity in can the water for industrial use of release surface engineering industry, simple in structure, good separating effect,
According to technical scheme provided by the invention, cyclone separator comprises shell separator, drain pipe and feed tube, and shell separator comprises body and separator lower body in separator upper body, separator, and separator upper body one side tangentially connects feed tube.Upper end, separator upper body connects drain pipe, and in separator, body is connected to lower end, separator upper body, and in separator, the body lower end connects the separator lower body, it is characterized in that: also comprise contrary power body, the part that feed tube is arranged in the separator upper body is provided with the second vent.The part that drain pipe is arranged in the separator upper body is provided with the first vent.In the separator lower body, be provided with contrary power body.
Described feed tube outer end connects inlet.
Described drain pipe outer end connects liquid outlet.
The Rotary-table that in described separator, body diminishes gradually for diameter from top to bottom.
Described contrary power body is cone.
Described separator lower body lower end connects sewage draining exit.
Between described contrary power body and separator hypocoelom wall, leave gap.
Described liquid outlet is funnel-shaped structure.
Described inlet is funnel-shaped structure.
Compared with the prior art the present invention has the following advantages:
The present invention is simple, compact and reasonable for structure; Impurity in the water for industrial use of effects on surface engineering industry can effectively separate, good separating effect; Reduced the pollution to environment.
The accompanying drawing explanation
Fig. 1 is structural representation of the present invention.
Description of reference numerals: body, 3-separator lower body, 4-liquid outlet, 5-drain pipe, 6-the first vent, 7-feed tube, 8-inlet, 9-the second vent, the contrary power body of 10-, 11-sewage draining exit, 12-shell separator in 1-separator upper body, 2-separator.
The specific embodiment
Following the present invention is further described in connection with the embodiment in accompanying drawing:
As shown in Figure 1, the present invention mainly comprises shell separator 12, drain pipe 5, feed tube 7 and contrary power body 10.
Shell separator 12 comprises body 2 and separator lower body 3 in separator upper body 1, separator, and separator upper body 1 one sides tangentially connect feed tube 7, and the part that feed tube 7 is arranged in separator upper body 1 is provided with the second vent 9.1 upper end, separator upper body connects drain pipe 5, and the part that drain pipe 5 is arranged in separator upper body 1 is provided with the first vent 6.Described feed tube 7 outer ends connect inlet 8, and drain pipe 5 outer ends connect liquid outlet 4.The effect of the first vent 6 and the second vent 9 is the pressure that has reduced drain pipe 5 and feed tube 7 surrounding liquids, makes the impurity in liquid can sedimentation and by liquid in rotation with pressure, do not taken away.Liquid outlet 4 and inlet 8 are funnel-shaped structure.
In separator, body 2 is connected to 1 lower end, separator upper body, the Rotary-table that in separator, body 2 diminishes gradually for diameter from top to bottom.In separator, body 2 lower ends connect separator lower body 3, in separator lower body 3, are provided with contrary power body 10, leave gap between contrary power body 10 and separator lower body 3 chamber walls.Described contrary power body 10 is cone, and contrary power body 10 can realize better that contamination precipitation separates.Separator lower body 3 lower ends connect sewage draining exit 11.
The present invention forms according to centrifugal sedimentation and density difference principle design, and the water for industrial use of Surface Engineering industry tangentially enters separator upper body 1 from feed tube 7 under certain pressure, and High Rotation Speed produces centrifugal field within it.Due to the effect of the impurity in water for industrial use and water body density variation and centrifugal force, the impurity particle that density is large is centrifuged power and gets rid of to surrounding, encounters separator upper body 1 chamber wall and sinks.Because body in separator 2 is Rotary-table, the tangential velocity of rotation of impurity particle is constantly dwindled and more and more faster with 2 radiuses of body in separator, and precipitation down, until contrary power body 10 decelerations of encountering in separator lower body 3 sink to separator lower body 3 bottoms.Last impurity is discharged from sewage draining exit 11.The effect of the first vent 6 and the second vent 9 is the pressure that has reduced drain pipe 5 and feed tube 7 surrounding liquids, makes the impurity in liquid can sedimentation and by liquid in rotation with pressure, do not taken away.
This contrive equipment can effectively be removed: the small solids such as oxide, SS floating thing, dust, grit, dirt, mud, calcium carbonate, and from water system, separating and excluding.
Claims (1)
1. cyclone separator, comprise shell separator (12), drain pipe (5) and feed tube (7), shell separator (12) comprises body (2) and separator lower body (3) in separator upper body (1), separator, and separator upper body (1) one side tangentially connects feed tube (7); Upper end, separator upper body (1) connects drain pipe (5), body in separator (2) is connected to lower end, separator upper body (1), body in separator (2) lower end connects separator lower body (3), it is characterized in that: also comprise contrary power body (10), the part that feed tube (7) is arranged in separator upper body (1) is provided with the second vent (9); The part that drain pipe (5) is arranged in separator upper body (1) is provided with the first vent (6); In separator lower body (3), be provided with contrary power body (10);
Described feed tube (7) outer end connects inlet (8);
Described drain pipe (5) outer end connects liquid outlet (4);
The Rotary-table that body in described separator (2) diminishes gradually for diameter from top to bottom;
Described contrary power body (10) is cone;
Described separator lower body (3) lower end connects sewage draining exit (11);
Between described contrary power body (10) and separator lower body (3) chamber wall, leave gap;
Described liquid outlet (4) is funnel-shaped structure;
Described inlet (8) is funnel-shaped structure.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012104783529A CN102923815B (en) | 2012-11-22 | 2012-11-22 | Cyclone separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012104783529A CN102923815B (en) | 2012-11-22 | 2012-11-22 | Cyclone separator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102923815A CN102923815A (en) | 2013-02-13 |
| CN102923815B true CN102923815B (en) | 2013-11-27 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012104783529A Active CN102923815B (en) | 2012-11-22 | 2012-11-22 | Cyclone separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102923815B (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107129007A (en) * | 2017-04-21 | 2017-09-05 | 徐州工程学院 | A kind of two-stage sewage solid granulates removal device |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN87200615U (en) * | 1987-01-14 | 1988-01-27 | 化工部光明化工研究所 | Cylindrical type whirlwind separator |
| CN201006495Y (en) * | 2007-04-05 | 2008-01-16 | 中国石油化工集团公司 | Highly effective air-solid cyclone separator |
| RU2367523C1 (en) * | 2008-02-11 | 2009-09-20 | Дочернее открытое акционерное общество "Центральное конструкторское бюро нефтеаппаратуры" Открытого акционерного общества "Газпром" (ДОАО ЦКБН ОАО "Газпром") | Cyclone |
| CN102389864A (en) * | 2011-09-19 | 2012-03-28 | 黄山 | Novel bottom-flow water-flow adjustable cyclone |
| CN102764703A (en) * | 2011-05-03 | 2012-11-07 | 中国科学院理化技术研究所 | Cyclone for realizing solution cavitation and separation and separation method |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FI54436C (en) * | 1976-05-14 | 1978-12-11 | Enso Gutzeit Oy | HYDROCYCLON |
| FI58954C (en) * | 1979-08-20 | 1981-05-11 | Enso Gutzeit Oy | HYDROCYKLON |
-
2012
- 2012-11-22 CN CN2012104783529A patent/CN102923815B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN87200615U (en) * | 1987-01-14 | 1988-01-27 | 化工部光明化工研究所 | Cylindrical type whirlwind separator |
| CN201006495Y (en) * | 2007-04-05 | 2008-01-16 | 中国石油化工集团公司 | Highly effective air-solid cyclone separator |
| RU2367523C1 (en) * | 2008-02-11 | 2009-09-20 | Дочернее открытое акционерное общество "Центральное конструкторское бюро нефтеаппаратуры" Открытого акционерного общества "Газпром" (ДОАО ЦКБН ОАО "Газпром") | Cyclone |
| CN102764703A (en) * | 2011-05-03 | 2012-11-07 | 中国科学院理化技术研究所 | Cyclone for realizing solution cavitation and separation and separation method |
| CN102389864A (en) * | 2011-09-19 | 2012-03-28 | 黄山 | Novel bottom-flow water-flow adjustable cyclone |
Non-Patent Citations (2)
| Title |
|---|
| JP昭52-140060A 1977.11.22 |
| JP昭56-70854A 1981.06.13 |
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| CN102923815A (en) | 2013-02-13 |
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