CN103755018B - Cone bucket type triphase separator - Google Patents
Cone bucket type triphase separator Download PDFInfo
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- CN103755018B CN103755018B CN201310718245.3A CN201310718245A CN103755018B CN 103755018 B CN103755018 B CN 103755018B CN 201310718245 A CN201310718245 A CN 201310718245A CN 103755018 B CN103755018 B CN 103755018B
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- cone bucket
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- long neck
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- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
The invention discloses a kind of cone bucket type triphase separator, comprise separator body, described separator body has the cone bucket shape structure in three layers of different diameter different openings direction, the superiors and orlop are respectively lower young large pyramidal structure suitable for reading, middle layer is that end opening goes up greatly young inverted long neck funnel structure, the upper end of inverted long neck funnel is connected with the collection chamber above it, and lower end is arranged on undermost top, and the neck of described long neck funnel is through the superiors; Filler is added with in the superiors.Good separating effect of the present invention, smooth in exhaust, processing efficiency are high.
Description
Technical field
The present invention relates to a kind of cone bucket type triphase separator.
Background technology
Triphase separator mainly utilizes hydraulic principle to realize effective separation of gas, solid, liquid three-phase, thus reaches the object of Separation of Water, mud and biogas.Current triphase separator has been widely used in such as flow lifting type anaerobic reactor, anaerobic mud bed and so on anaerobism waste disposal plant.As one of the core structure of anaerobic biochemical reaction device, the separating effect of triphase separator directly determines the quality of anaerobic reaction device performance.Traditional triphase separator is generally individual layer, mainly utilizes the change of water flow section to cause the difference of gas-solid-liquid three-phase flow velocity, thus realizes the object of three phase separation.Traditional triphase separator is all also existing the halfway defect of separating effect in varying degrees.
Summary of the invention
In order to overcome separating effect that existing triphase separator exists not thoroughly, the shortcoming of complex structure etc., the invention provides a kind of cone bucket type triphase separator.
The technical solution used in the present invention is:
Cone bucket type triphase separator, comprise separator body, it is characterized in that: described separator body has the cone bucket shape structure in three layers of different diameter different openings direction, the superiors and orlop are respectively lower young large pyramidal structure suitable for reading, middle layer is that end opening goes up greatly young inverted long neck funnel structure, the upper end of inverted long neck funnel is connected with the collection chamber above it, and lower end is arranged on undermost top, and the neck of described long neck funnel is through the superiors.
Further, filler is added with in the described triphase separator of the superiors.
Triphase separator principle of work of the present invention:
Undermost triphase separator: the gas that position, main body Sludge Bed district is produced, the part be positioned within infraoral puts together, collection chamber is sent into by the inverted long neck funnel in middle layer, (feed liquid that main body Sludge Bed district rises enters the part of return-flow system, refluxed downwards by central backflow cylinder, enter reflux pump, enter main body again by Tube hole type distribution device, with this circular flow).
The triphase separator of the superiors: be again separated from the gas, liquid, solid three-phase material in the feed liquid that middle layer rises.The not yet processed pollutent (COD or BOD) still remained in feed liquid is processed by the microbial film on filler by the function of packing layer further, improves the final clearance of COD and BOD with this.Feed liquid through three phase separation finally enters overflow groove, then enters upflow tube and finally discharge.The mud be trapped in the separator passes back into position, Sludge Bed district through separator wall.Gas then enters collection chamber, is finally discharged by top biogas pipe and utilizes.
Beneficial effect of the present invention is embodied in: good separating effect, simple to operate, machine utilization is higher.
Accompanying drawing explanation
Fig. 1 is one-piece construction schematic diagram of the present invention.
Embodiment
With reference to Fig. 1, cone bucket type triphase separator, comprise separator body, described separator body has the cone bucket shape structure in three layers of different diameter different openings direction, the superiors 63 and orlop 61 are respectively lower young large pyramidal structure suitable for reading, and middle layer 62 is that end opening goes up greatly young inverted long neck funnel structure, and the upper end of inverted long neck funnel is connected with the collection chamber above it, lower end is arranged on undermost top, and the neck of described long neck funnel is through the superiors 63.
Further, filler 64 is added with in the superiors.
Triphase separator principle of work of the present invention:
Undermost triphase separator: the gas that position, main body Sludge Bed district is produced, the part be positioned within infraoral puts together, collection chamber is sent into by the inverted long neck funnel in middle layer, (feed liquid that main body Sludge Bed district rises enters the part of return-flow system, refluxed downwards by central backflow cylinder, enter reflux pump, enter main body again by Tube hole type distribution device, with this circular flow).
The triphase separator of the superiors: be again separated from the gas, liquid, solid three-phase material in the feed liquid that middle layer rises.The not yet processed pollutent (COD or BOD) still remained in feed liquid is processed by the microbial film on filler by the function of packing layer further, improves the final clearance of COD and BOD with this.Feed liquid through three phase separation finally enters overflow groove, then enters upflow tube and finally discharge.The mud be trapped in the separator passes back into position, Sludge Bed district through separator wall.Gas then enters collection chamber, is finally discharged by top biogas pipe and utilizes.
Content described in this specification sheets embodiment is only enumerating the way of realization of inventive concept; protection scope of the present invention should not be regarded as being only limitted to the specific form that embodiment is stated, protection scope of the present invention also and conceive the equivalent technologies means that can expect according to the present invention in those skilled in the art.
Claims (2)
1. bore bucket type triphase separator, comprise separator body, it is characterized in that: described separator body has the cone bucket shape structure in three layers of different diameter different openings direction, the superiors and orlop are respectively lower young large pyramidal structure suitable for reading, middle layer is that end opening goes up greatly young inverted long neck funnel structure, the upper end of inverted long neck funnel is connected with the collection chamber above it, and lower end is arranged on undermost top, and the neck of described long neck funnel is through the superiors.
2. cone bucket type triphase separator as claimed in claim 1, is characterized in that: be added with filler in the superiors.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310718245.3A CN103755018B (en) | 2013-12-23 | 2013-12-23 | Cone bucket type triphase separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310718245.3A CN103755018B (en) | 2013-12-23 | 2013-12-23 | Cone bucket type triphase separator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN103755018A CN103755018A (en) | 2014-04-30 |
| CN103755018B true CN103755018B (en) | 2015-09-23 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201310718245.3A Active CN103755018B (en) | 2013-12-23 | 2013-12-23 | Cone bucket type triphase separator |
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| CN (1) | CN103755018B (en) |
Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2006078962A2 (en) * | 2005-01-21 | 2006-07-27 | Kenneth Doyle Oglesby | Gas liquid solid compact cyclonic separator |
| CN2848324Y (en) * | 2005-12-20 | 2006-12-20 | 沈阳建筑大学 | Three phase separator device |
| CN101007680A (en) * | 2007-01-12 | 2007-08-01 | 浙江大学 | Highly effective anaerobic bioreacto |
| CN201046371Y (en) * | 2007-05-26 | 2008-04-16 | 丹东市振兴石油橡胶厂 | Oil-contaminated water purifying three-phase cyclone separator |
| CN101428876A (en) * | 2008-12-02 | 2009-05-13 | 大庆油田有限责任公司 | Uses of high-speed dish piece type three-phase centrifuge in treating ternary composite flooding water extraction |
| CN101766935A (en) * | 2009-01-06 | 2010-07-07 | 中国海洋石油总公司 | Combined type gas-liquid-solid three phase separation method and device |
| CN203079751U (en) * | 2013-02-05 | 2013-07-24 | 王利 | Internal circulation A-O biological denitrogenation reactor |
| CN103319018A (en) * | 2013-04-23 | 2013-09-25 | 江苏省环境科学研究院 | Efficient fractional three-phase separator system |
| CN203754494U (en) * | 2013-12-23 | 2014-08-06 | 陈际平 | Conical funnel type three-phase separator |
-
2013
- 2013-12-23 CN CN201310718245.3A patent/CN103755018B/en active Active
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2006078962A2 (en) * | 2005-01-21 | 2006-07-27 | Kenneth Doyle Oglesby | Gas liquid solid compact cyclonic separator |
| CN2848324Y (en) * | 2005-12-20 | 2006-12-20 | 沈阳建筑大学 | Three phase separator device |
| CN101007680A (en) * | 2007-01-12 | 2007-08-01 | 浙江大学 | Highly effective anaerobic bioreacto |
| CN201046371Y (en) * | 2007-05-26 | 2008-04-16 | 丹东市振兴石油橡胶厂 | Oil-contaminated water purifying three-phase cyclone separator |
| CN101428876A (en) * | 2008-12-02 | 2009-05-13 | 大庆油田有限责任公司 | Uses of high-speed dish piece type three-phase centrifuge in treating ternary composite flooding water extraction |
| CN101766935A (en) * | 2009-01-06 | 2010-07-07 | 中国海洋石油总公司 | Combined type gas-liquid-solid three phase separation method and device |
| CN203079751U (en) * | 2013-02-05 | 2013-07-24 | 王利 | Internal circulation A-O biological denitrogenation reactor |
| CN103319018A (en) * | 2013-04-23 | 2013-09-25 | 江苏省环境科学研究院 | Efficient fractional three-phase separator system |
| CN203754494U (en) * | 2013-12-23 | 2014-08-06 | 陈际平 | Conical funnel type three-phase separator |
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| CN103755018A (en) | 2014-04-30 |
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