CN203754494U - Conical funnel type three-phase separator - Google Patents
Conical funnel type three-phase separator Download PDFInfo
- Publication number
- CN203754494U CN203754494U CN201320856706.9U CN201320856706U CN203754494U CN 203754494 U CN203754494 U CN 203754494U CN 201320856706 U CN201320856706 U CN 201320856706U CN 203754494 U CN203754494 U CN 203754494U
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- Prior art keywords
- separator
- long neck
- funnel
- conical
- superiors
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- 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.)
- Withdrawn - After Issue
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- Y02W10/12—
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- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
The utility model discloses a conical funnel type three-phase separator which comprises a separator body, wherein the separator body has three layers of conical funnel shaped structures differing in diameter and opening direction; the conical funnel shaped structures on the uppermost layer and the lowermost layer are conical structures with lower openings smaller than upper openings, and the conical funnel shaped structure in the middle is an inverted long neck funnel structure with lower opening bigger than upper opening; the upper end of the inverted long neck funnel is communicated with a gas collection chamber above, and the lower end is arranged above the lowermost layer; the neck of the long neck funnel runs through the uppermost layer; and a filling material is added in the uppermost layer. The three-phase separator disclosed by the utility model is good in separating effect, smooth to discharge gas and high in treatment efficiency.
Description
Technical field
The utility model 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 utility model provides a kind of cone bucket type triphase separator.
The technical solution adopted in the utility model 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.
The utility model triphase separator principle of work:
Undermost triphase separator: the gas that position, main body Sludge Bed district is produced, be positioned at infraoral with part put together, send into collection chamber by the inverted long neck funnel in middle layer, (feed liquid rising in main body Sludge Bed district enters the part of return-flow system, refluxing by center, cylinder is downward to reflux, enter reflux pump, enter again main body by pore formula distribution device, 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 separates again.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, improves the final clearance of COD and BOD with this.Finally enter overflow groove through the feed liquid of three phase separation, 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, is finally discharged and is utilized by top biogas pipe.
The beneficial effects of the utility model are embodied in: good separating effect, and simple to operate, machine utilization is higher.
Brief description of the drawings
Fig. 1 is the utility model one-piece construction schematic diagram.
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.
The utility model triphase separator principle of work:
Undermost triphase separator: the gas that position, main body Sludge Bed district is produced, be positioned at infraoral with part put together, send into collection chamber by the inverted long neck funnel in middle layer, (feed liquid rising in main body Sludge Bed district enters the part of return-flow system, refluxing by center, cylinder is downward to reflux, enter reflux pump, enter again main body by pore formula distribution device, 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 separates again.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, improves the final clearance of COD and BOD with this.Finally enter overflow groove through the feed liquid of three phase separation, 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, is finally discharged and is utilized by top biogas pipe.
Content described in this specification sheets embodiment is only enumerating of way of realization to inventive concept; protection domain of the present utility model should not be regarded as only limiting to the specific form that embodiment states, protection domain of the present utility model also and conceive the equivalent technologies means that can expect according to the utility model in those skilled in the art.
Claims (2)
1. 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.
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 |
|---|---|---|---|
| CN201320856706.9U CN203754494U (en) | 2013-12-23 | 2013-12-23 | Conical funnel type three-phase separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320856706.9U CN203754494U (en) | 2013-12-23 | 2013-12-23 | Conical funnel type three-phase separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203754494U true CN203754494U (en) | 2014-08-06 |
Family
ID=51249793
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320856706.9U Withdrawn - After Issue CN203754494U (en) | 2013-12-23 | 2013-12-23 | Conical funnel type three-phase separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203754494U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103755018A (en) * | 2013-12-23 | 2014-04-30 | 陈际平 | Tapered funnel type three-phase separator |
-
2013
- 2013-12-23 CN CN201320856706.9U patent/CN203754494U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103755018A (en) * | 2013-12-23 | 2014-04-30 | 陈际平 | Tapered funnel type three-phase separator |
| CN103755018B (en) * | 2013-12-23 | 2015-09-23 | 陈际平 | Cone bucket type triphase separator |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20140806 Effective date of abandoning: 20150923 |
|
| RGAV | Abandon patent right to avoid regrant |