CN103755018A - Tapered funnel type three-phase separator - Google Patents
Tapered funnel type three-phase separator Download PDFInfo
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- CN103755018A CN103755018A CN201310718245.3A CN201310718245A CN103755018A CN 103755018 A CN103755018 A CN 103755018A CN 201310718245 A CN201310718245 A CN 201310718245A CN 103755018 A CN103755018 A CN 103755018A
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- funnel
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Abstract
The invention discloses a tapered funnel type three-phase separator, which comprises a separator body, wherein the separator body has a three-layer tapered funnel-shaped structure; the three layers of the tapered funnel-shaped structure have different diameters and different opening directions; each of the uppermost layer and the lowermost layer is a tapered structure with a small lower opening and a large upper opening; the middle layer is a long-neck funnel structure with a large lower opening and a small upper opening; the upper end of the inverted long-neck funnel structure is communicated with a gas collection chamber above the inverted long-neck funnel structure, and the lower end of the inverted long-neck funnel structure is arranged above the lowermost layer; the neck of the long-neck funnel structure penetrates through the uppermost layer; a filler is added into the uppermost layer. The tapered funnel type three-phase separator has good separation effects, and is smooth in exhaust and high in treatment efficiency.
Description
Technical field
The present invention relates to a kind of cone bucket type triphase separator.
Background technology
Triphase separator is mainly to utilize hydraulic principle to realize effective separation of gas, solid, liquid three-phase, thereby reaches the object of Separation of Water, mud and biogas.At present triphase separator has been widely used in such as flow lifting type anaerobic reactor, anaerobism waste disposal plant anaerobic mud bed.As one of 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 variation of water flow section to cause the difference of gas-solid-liquid three-phase flow velocity, thereby realizes the object of three phase separation.Traditional triphase separator is all existing the halfway defect of separating effect in varying degrees.
Summary of the invention
For 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 of 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 the greatly upper young inverted long neck funnel structure of end opening, the upper end of inverted long neck funnel is connected with the collection chamber of its top, and lower end is arranged on undermost top, and the neck of described long neck funnel is through the superiors.
Further, in the described triphase separator of the superiors, be added with filler.
Triphase separator principle of work of the present invention:
Undermost triphase separator: the gas that position, main body Sludge Bed district is produced, be positioned at infraoral with part put together, by the inverted long neck funnel in middle layer, send into collection chamber, (feed liquid rising in main body Sludge Bed district enters the part of return-flow system, by center, refluxing, cylinder is downward to reflux, enter reflux pump, by pore formula distribution device, enter again main body, with this circular flow).
The triphase separator of the superiors: the gas, liquid, solid three-phase material in the feed liquid rising from middle layer carries out again separated.The function of packing layer is further processed the not yet processed pollutent (COD or BOD) still remaining in feed liquid by the microbial film on filler, with this, improves the final clearance of COD and BOD.Through the feed liquid of three phase separation, finally enter overflow groove, then enter upflow tube and finally discharge.The mud being trapped in separator passes back into position, Sludge Bed district through separator wall.Gas enters collection chamber, finally by top biogas pipe, is discharged and is utilized.
Beneficial effect of the present invention is embodied in: good separating effect, and 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 of three layers of different diameter different openings direction, the superiors 63 are respectively lower young large pyramidal structure suitable for reading with orlop 61, and middle layer 62 is the greatly upper young inverted long neck funnel structure of end opening, and the upper end of inverted long neck funnel is connected with the collection chamber of its top, lower end is arranged on undermost top, and the neck of described long neck funnel is through the superiors 63.
Further, in the superiors, be added with filler 64.
Triphase separator principle of work of the present invention:
Undermost triphase separator: the gas that position, main body Sludge Bed district is produced, be positioned at infraoral with part put together, by the inverted long neck funnel in middle layer, send into collection chamber, (feed liquid rising in main body Sludge Bed district enters the part of return-flow system, by center, refluxing, cylinder is downward to reflux, enter reflux pump, by pore formula distribution device, enter again main body, with this circular flow).
The triphase separator of the superiors: the gas, liquid, solid three-phase material in the feed liquid rising from middle layer carries out again separated.The function of packing layer is further processed the not yet processed pollutent (COD or BOD) still remaining in feed liquid by the microbial film on filler, with this, improves the final clearance of COD and BOD.Through the feed liquid of three phase separation, finally enter overflow groove, then enter upflow tube and finally discharge.The mud being trapped in separator passes back into position, Sludge Bed district through separator wall.Gas enters collection chamber, finally by top biogas pipe, is discharged and is utilized.
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 only limiting to the specific form that embodiment states, protection scope of the present invention also and in those skilled in the art, according to the present invention, conceive the equivalent technologies means that can expect.
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 of 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 the greatly upper young inverted long neck funnel structure of end opening, the upper end of inverted long neck funnel is connected with the collection chamber of its top, 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: in the superiors, be added with filler.
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 true CN103755018A (en) | 2014-04-30 |
| CN103755018B CN103755018B (en) | 2015-09-23 |
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| 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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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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| CN103755018B (en) | 2015-09-23 |
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