CN203170110U - Gas phase-liquid phase-solid phase separation precipitator - Google Patents
Gas phase-liquid phase-solid phase separation precipitator Download PDFInfo
- Publication number
- CN203170110U CN203170110U CN 201320154407 CN201320154407U CN203170110U CN 203170110 U CN203170110 U CN 203170110U CN 201320154407 CN201320154407 CN 201320154407 CN 201320154407 U CN201320154407 U CN 201320154407U CN 203170110 U CN203170110 U CN 203170110U
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- Prior art keywords
- liquid
- cylindrical shell
- phase
- sewage pipe
- phase separation
- Prior art date
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- Expired - Lifetime
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- 238000005191 phase separation Methods 0.000 title claims abstract description 15
- 239000007788 liquid Substances 0.000 title claims abstract description 13
- 239000012716 precipitator Substances 0.000 title claims abstract description 12
- 239000007790 solid phase Substances 0.000 title abstract 4
- 239000010865 sewage Substances 0.000 claims abstract description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 12
- 239000007787 solid Substances 0.000 claims description 13
- 238000007599 discharging Methods 0.000 claims description 5
- 238000012856 packing Methods 0.000 claims description 5
- 239000000945 filler Substances 0.000 abstract 1
- 238000004065 wastewater treatment Methods 0.000 abstract 1
- 239000002351 wastewater Substances 0.000 description 6
- 238000005516 engineering process Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 238000009360 aquaculture Methods 0.000 description 1
- 244000144974 aquaculture Species 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
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- Physical Water Treatments (AREA)
Abstract
The utility model discloses a gas phase-liquid phase-solid phase separation precipitator comprising a cylinder body, wherein the bottom of the cylinder body is communicated with a sewage pipe with an upward water outlet; an exhaust pipe with a top part protruding out of a liquid level is arranged in the cylinder body; a filler layer is arranged below the liquid level; an annular overflow weir is arranged on the outer wall at the top of the cylinder body; a water storage tank is arranged on the outer wall of the annular overflow weir; a clear water outlet is formed in the bottom of the water storage tank; a conical sliding mud plate with a downward opening is arranged above the sewage pipe; a water outlet of the sewage pipe penetrates into the conical sliding mud plate; an inclining air-guiding plate is arranged at the side edge of the conical sliding mud plate; and a through hole communicated with the bottom of the exhaust pipe is formed in the air-guiding plate. The gas phase-liquid phase-solid phase separation precipitator has the characteristics of high efficiency of gas phase-liquid phase-solid phase separation, simple structure and low cost, and can be widely applied to the field of organic wastewater treatment.
Description
Technical field
The utility model relates to and is applied to organic waste-water treating apparatus, particularly relates to a kind of gas-liquid-solid three-phase separation precipitator.
Background technology
The biological treatment that the three phase separation settling vessel mainly is used in high concentration organic wastewaters such as food, chemical industry, aquaculture can realize gas, liquid, solid three phase separation effectively, and it plays a part very important to obtaining good effluent quality.The many methods of separating with the gas two-phase according to solid of current three phase separator arrange, not only of a great variety, volume is big, complex structure, and energy consumption height, separative efficiency is low.
The utility model content
The purpose of this utility model is in order to overcome the deficiency of above-mentioned background technology, a kind of gas-liquid-solid three-phase separation precipitator to be provided, and makes it have gas-liquid-solid three-phase separative efficiency height, simple in structure, cheap characteristics.
The gas-liquid-solid three-phase separation precipitator that the utility model provides, comprise cylindrical shell, described cylindrical shell bottom is connected with delivery port sewage pipe up, be provided with the blast pipe that the top protrudes from liquid level in the cylindrical shell, be provided with packing layer under the liquid level, the cylindrical shell top exterior walls is provided with the ring-type downflow weir, the outer wall of described ring-type downflow weir is provided with aqua storage tank, described aqua storage tank bottom is provided with the clear water delivery port, described sewage pipe top is provided with downward opening taper slip plate, the sewage pipe delivery port gos deep in the taper slip plate, and described taper slip plate side is provided with the aeroscopic plate that is obliquely installed, and described aeroscopic plate is provided with the through hole that is connected with the blast pipe bottom.
In technique scheme, described cylindrical shell bottom is the conical surface, and described conical surface bottom is provided with mud discharging mouth.
Gas-liquid-solid three-phase separation precipitator of the present utility model has following beneficial effect: the one, and gas-liquid-solid three-phase separative efficiency height, equipment gas collecting efficiency height, effluent quality is good; The 2nd, volume is little, takes up an area of to economize; The 3rd, simple in structure, cost is low; The 4th, energy consumption is low, and intensity of workers is safeguarded and operating cost by low also the reduction significantly.
Description of drawings
Fig. 1 is structural representation of the present utility model;
The specific embodiment
Below in conjunction with drawings and Examples the utility model is described in further detail, but this embodiment should not be construed as restriction of the present utility model.
Gas-liquid-solid three-phase separation precipitator of the present utility model comprises cylindrical shell 1, sewage pipe 2, blast pipe 3, packing layer 4, ring-type downflow weir 5, aqua storage tank 6, clear water delivery port 7, taper slip plate 8, aeroscopic plate 9 and mud discharging mouth 10.
Described cylindrical shell 1 bottom is connected with delivery port sewage pipe 2 up, be provided with the blast pipe 3 that the top protrudes from liquid level in the cylindrical shell 1, be provided with packing layer 4 under the liquid level, cylindrical shell 1 top exterior walls is provided with ring-type downflow weir 5, the outer wall of described ring-type downflow weir 5 is provided with aqua storage tank 6, described aqua storage tank 6 bottoms are provided with clear water delivery port 7, described sewage pipe 2 tops are provided with downward opening taper slip plate 8, sewage pipe 2 delivery ports go deep in the taper slip plate 8, described taper slip plate 8 sides are provided with the aeroscopic plate 9 that is obliquely installed, described aeroscopic plate 9 is provided with the through hole 9.1 that is connected with blast pipe 3 bottoms, and described cylindrical shell 1 bottom is the conical surface, and described conical surface bottom is provided with mud discharging mouth 10.
The workflow of described gas-liquid-solid three-phase separation precipitator is as follows: waste water enters cylindrical shell 1 by sewage pipe 2, mud in the waste water, separates with waste water downwards under tapered slip plate 8 effects than great, and be deposited in cylindrical shell 1 bottom, discharge cylindrical shell 1 by mud discharging mouth 10 subsequently.Simultaneously, the organic matter that microorganism is decomposed in the waste water produces gas, and gas gathers formation than air pocket in uphill process, and described bubble is overflowed along aeroscopic plate 9 lower edge faces risings and by blast pipe 3.The water of preliminary purification rises at the opening that passes through under the hydraulic pressure effect between aeroscopic plate 9 and the tapered slip plate 8, and through packing layer 4 further purification filterings, water up to standard after treatment enters aqua storage tank 6 by ring-type downflow weir 5 and passes through 7 discharges of clear water delivery port.
Obviously, those skilled in the art can carry out various changes and modification to the utility model and not break away from spirit and scope of the present utility model.Like this, if of the present utility model these are revised and modification belongs within the scope of the utility model claim and equivalent technologies thereof, then the utility model also is intended to comprise these changes and modification interior.
The content that is not described in detail in this specification belongs to this area professional and technical personnel's known prior art.
Claims (2)
1. gas-liquid-solid three-phase separation precipitator, comprise cylindrical shell (1), described cylindrical shell (1) bottom is connected with delivery port sewage pipe (2) up, be provided with the blast pipe (3) that the top protrudes from liquid level in the cylindrical shell (1), be provided with packing layer (4) under the liquid level, cylindrical shell (1) top exterior walls is provided with ring-type downflow weir (5), the outer wall of described ring-type downflow weir (5) is provided with aqua storage tank (6), described aqua storage tank (6) bottom is provided with clear water delivery port (7), it is characterized in that: described sewage pipe (2) top is provided with downward opening taper slip plate (8), sewage pipe (2) delivery port gos deep in the taper slip plate (8), described taper slip plate (8) side is provided with the aeroscopic plate (9) that is obliquely installed, and described aeroscopic plate (9) is provided with the through hole (9.1) that is connected with blast pipe (3) bottom.
2. gas-liquid-solid three-phase separation precipitator according to claim 1 is characterized in that: described cylindrical shell (1) bottom is the conical surface, and described conical surface bottom is provided with mud discharging mouth (10).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320154407 CN203170110U (en) | 2013-03-30 | 2013-03-30 | Gas phase-liquid phase-solid phase separation precipitator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320154407 CN203170110U (en) | 2013-03-30 | 2013-03-30 | Gas phase-liquid phase-solid phase separation precipitator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203170110U true CN203170110U (en) | 2013-09-04 |
Family
ID=49066865
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201320154407 Expired - Lifetime CN203170110U (en) | 2013-03-30 | 2013-03-30 | Gas phase-liquid phase-solid phase separation precipitator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203170110U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107030052A (en) * | 2017-06-26 | 2017-08-11 | 芜湖启泽信息技术有限公司 | A kind of cable cleaning device for Communication power industry |
| CN110433564A (en) * | 2019-08-08 | 2019-11-12 | 王再鑫 | A kind of livestock sewage disposal device |
-
2013
- 2013-03-30 CN CN 201320154407 patent/CN203170110U/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107030052A (en) * | 2017-06-26 | 2017-08-11 | 芜湖启泽信息技术有限公司 | A kind of cable cleaning device for Communication power industry |
| CN110433564A (en) * | 2019-08-08 | 2019-11-12 | 王再鑫 | A kind of livestock sewage disposal device |
| CN110433564B (en) * | 2019-08-08 | 2021-08-31 | 深圳市环水清源生态环保技术有限公司 | Livestock sewage treatment equipment |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee |
Owner name: WUHAN FUND ENVIRONMENTAL PROTECTION CO., LTD. Free format text: FORMER NAME: WUHAN FUND ENVIRONMENTAL PROTECTION ENGINEERING CO., LTD. |
|
| CP01 | Change in the name or title of a patent holder |
Address after: 430074, Hubei, Wuhan province East Lake Development Zone Venture Street East create international A2102-3 Patentee after: WUHAN FUND ENVIRONMENT PROTECTION Co.,Ltd. Address before: 430074, Hubei, Wuhan province East Lake Development Zone Venture Street East create international A2102-3 Patentee before: WUHAN FUND ENVIRONMENT PROT ENGINEERING Co.,Ltd. |
|
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Gas phase-liquid phase-solid phase separation precipitator Effective date of registration: 20140928 Granted publication date: 20130904 Pledgee: Bank of Hankou Limited by Share Ltd. Wuchang branch Pledgor: WUHAN FUND ENVIRONMENT PROTECTION Co.,Ltd. Registration number: 2014980000086 |
|
| PLDC | Enforcement, change and cancellation of contracts on pledge of patent right or utility model | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20151023 Granted publication date: 20130904 Pledgee: Bank of Hankou Limited by Share Ltd. Wuchang branch Pledgor: WUHAN FUND ENVIRONMENT PROTECTION Co.,Ltd. Registration number: 2014980000086 |
|
| PLDC | Enforcement, change and cancellation of contracts on pledge of patent right or utility model | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Gas phase-liquid phase-solid phase separation precipitator Effective date of registration: 20180817 Granted publication date: 20130904 Pledgee: Pudong Shanghai Development Bank Limited by Share Ltd. Wuhan branch Pledgor: WUHAN FUND ENVIRONMENT PROTECTION Co.,Ltd. Registration number: 2018990000703 |
|
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| CX01 | Expiry of patent term |
Granted publication date: 20130904 |
|
| CX01 | Expiry of patent term | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20231129 Granted publication date: 20130904 Pledgee: Pudong Shanghai Development Bank Limited by Share Ltd. Wuhan branch Pledgor: WUHAN FUND ENVIRONMENT PROTECTION Co.,Ltd. Registration number: 2018990000703 |
|
| PC01 | Cancellation of the registration of the contract for pledge of patent right |