CN204107101U - A kind of gas-liquid-solid three-phase separation precipitator - Google Patents
A kind of gas-liquid-solid three-phase separation precipitator Download PDFInfo
- Publication number
- CN204107101U CN204107101U CN201420415852.2U CN201420415852U CN204107101U CN 204107101 U CN204107101 U CN 204107101U CN 201420415852 U CN201420415852 U CN 201420415852U CN 204107101 U CN204107101 U CN 204107101U
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- Prior art keywords
- air guiding
- swash plate
- solid
- cylindrical shell
- gas
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- Expired - Lifetime
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- 239000007787 solid Substances 0.000 title claims abstract description 27
- 238000005191 phase separation Methods 0.000 title claims abstract description 20
- 239000012716 precipitator Substances 0.000 title claims abstract description 18
- 238000012856 packing Methods 0.000 claims abstract description 8
- 230000008021 deposition Effects 0.000 abstract description 3
- 238000005265 energy consumption Methods 0.000 abstract description 3
- 238000012423 maintenance Methods 0.000 abstract description 3
- 230000005484 gravity Effects 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 238000009360 aquaculture Methods 0.000 description 1
- 244000144974 aquaculture Species 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- NHDHVHZZCFYRSB-UHFFFAOYSA-N pyriproxyfen Chemical compound C=1C=CC=NC=1OC(C)COC(C=C1)=CC=C1OC1=CC=CC=C1 NHDHVHZZCFYRSB-UHFFFAOYSA-N 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Landscapes
- Separating Particles In Gases By Inertia (AREA)
Abstract
The utility model discloses a kind of gas-liquid-solid three-phase separation precipitator, comprise cylindrical shell, lower mud slot is offered at cylindrical shell side lower, slip swash plate is arranged on inner barrel obliquely, one end that slip swash plate is lower is arranged on the following of lower mud slot, also Air guiding flap is provided with in cylindrical shell, the incline direction of Air guiding flap is contrary with the incline direction of slip swash plate, one end of Air guiding flap is connected with the sidewall of cylindrical shell, narrow orifice is formed between the other end of Air guiding flap and slip swash plate, the sidewall that cylindrical shell is connected with Air guiding flap offers exhaust outlet, inclined tube filter packing is provided with above slip swash plate and Air guiding flap.Gas-liquid-solid three-phase separation precipitator of the present utility model, compact conformation, gas-liquid-solid three-phase separative efficiency is high, and it is high that equipment cuts solid rate, structure is simple, and cost is low, and configuration is ingenious, the not deposition of whole cylinder body bottom, energy consumption is low, can significantly reduce maintenance work and operating cost.
Description
Technical field
The utility model relates to three phase separator, particularly relates to a kind of gas-liquid-solid three-phase separation precipitator.
Background technology
Three phase separator is mainly used in the three phase separation of gas, solid, liquid, belongs to separation equipment, and it is widely used in the biological treatment of the high concentrated organic wastewaters such as food, chemical industry, aquaculture, and is applied to the process of sanitary sewage gradually.Three phase separator can realize the three phase separation of gas, liquid, solid effectively, to ensure biochemical treatment standard water discharge.Of a great variety, the configurations of three phase separator in prior art, but all there is separative efficiency and cut the shortcomings such as solid rate is low.
Therefore, need to provide a kind of gas-liquid-solid three-phase separation precipitator to solve the problem.
Utility model content
In order to solve this problem, the utility model discloses a kind of gas-liquid-solid three-phase separation precipitator, described gas-liquid-solid three-phase separation precipitator comprises cylindrical shell, lower mud slot is offered at described cylindrical shell side lower, slip swash plate is arranged on described inner barrel obliquely, one end that described slip swash plate is lower is arranged on the following of described lower mud slot, described Air guiding flap is also provided with in described cylindrical shell, the incline direction of described Air guiding flap is contrary with the incline direction of described slip swash plate, one end of described Air guiding flap is connected with the sidewall of described cylindrical shell, narrow orifice is formed between the other end of described Air guiding flap and described slip swash plate, the sidewall that described cylindrical shell is connected with described Air guiding flap offers exhaust outlet, inclined tube filter packing is provided with above described slip swash plate and described Air guiding flap.
Preferably, described lower mud slot is strip.
Preferably, above described inclined tube filter packing, overflow weir notch is also provided with.
Gas-liquid-solid three-phase separation precipitator of the present utility model has the following advantages:
1, compact conformation, reduces production volume;
2, gas-liquid-solid three-phase separative efficiency is high, and it is high that equipment cuts solid rate, and effluent quality is good;
3, structure is simple, without special tectonic requirement, significantly can reduce cost;
4, configuration is ingenious, the not deposition of whole cylinder body bottom;
5, energy consumption is low, and spoil disposal, by gravity, can significantly reduce maintenance work and operating cost.
In utility model content part, introduce the concept of a series of reduced form, this will further describe in detailed description of the invention part.The utility model content part does not also mean that the key feature and essential features that will attempt to limit technical scheme required for protection, does not more mean that the protection domain attempting to determine technical scheme required for protection.
Below in conjunction with accompanying drawing, describe advantage of the present utility model and feature in detail.
Accompanying drawing explanation
Fig. 1 is the schematic diagram of the gas-liquid-solid three-phase separation precipitator according to the utility model embodiment.
Detailed description of the invention
In the following description, give a large amount of concrete details to provide to understand more thoroughly the utility model.But, it will be apparent to one skilled in the art that the utility model can be implemented without the need to these details one or more.In other example, in order to avoid obscuring with the utility model, technical characteristics more well known in the art are not described.
In order to thoroughly understand the utility model, by following description, detailed structure is proposed.Obviously, execution of the present utility model is not limited to the specific details that those skilled in the art has the knack of.Preferred embodiment of the present utility model is described in detail as follows, but except these are described in detail, the utility model can also have other embodiments.
Below in conjunction with accompanying drawing, embodiment of the present utility model is described in detail.
With reference to figure 1, show the gas-liquid-solid three-phase separation precipitator according to the utility model embodiment.Gas-liquid-solid three-phase separation precipitator of the present utility model comprises cylindrical shell 1, offers lower mud slot 2 at cylindrical shell 1 side lower, and it is inner that slip swash plate 4 is arranged on cylindrical shell 1 obliquely, and one end that slip swash plate 4 is lower is arranged on the following of lower mud slot 2.In cylindrical shell 1, be also provided with Air guiding flap 3, the incline direction of Air guiding flap 3 is contrary with the incline direction of slip swash plate 4.One end of Air guiding flap 3 is connected with the sidewall of cylindrical shell 1, is formed with narrow orifice 8 between its other end and slip swash plate 4.The sidewall that cylindrical shell 1 is connected with Air guiding flap 3 offers exhaust outlet 5.Inclined tube filter packing 6 is provided with above slip swash plate 4 with Air guiding flap 3.
Above-mentioned lower mud slot 2 can be strip.Overflow weir notch 7 can also be provided with above above-mentioned inclined tube filter packing 6.
The workflow of gas-liquid-solid three-phase separation precipitator of the present utility model is as follows:
The strip lower mud slot 2 that waste water mixed liquor is formed by cylindrical shell 1 and slip swash plate 4 enters, and under natural sedimentation effect, the bubble of light specific gravity rises, and rises and overflowed by exhaust outlet 5 along Air guiding flap 3 lower along face; Mud in mixed liquor is because of than great, and precipitation is glided along slip swash plate 4 and discharged by strip lower mud slot 2 downwards; Through gas mud be separated compared with clean water under hydraulic pressure effect by narrow orifice 8 between slip swash plate 4 and Air guiding flap 3 to upper reaches, and through inclined tube filter packing 6 cement isolated by filtration further, water purification up to standard after treatment overflows into overflow weir notch 7 and discharges after rising to overflow liquid level.
Gas-liquid-solid three-phase separation precipitator of the present utility model has the following advantages:
1, compact conformation, reduces production volume;
2, gas-liquid-solid three-phase separative efficiency is high, and it is high that equipment cuts solid rate, and effluent quality is good;
3, structure is simple, without special tectonic requirement, significantly can reduce cost;
4, configuration is ingenious, the not deposition of whole cylinder body bottom;
5, energy consumption is low, and spoil disposal, by gravity, can significantly reduce maintenance work and operating cost.
The utility model is illustrated by above-described embodiment, but should be understood that, above-described embodiment just for the object of illustrating and illustrate, and is not intended to the utility model to be limited in described scope of embodiments.In addition it will be understood by those skilled in the art that; the utility model is not limited to above-described embodiment; more kinds of variants and modifications can also be made, within these variants and modifications all drop on the utility model scope required for protection according to instruction of the present utility model.Protection domain of the present utility model defined by the appended claims and equivalent scope thereof.
Claims (3)
1. a gas-liquid-solid three-phase separation precipitator, it is characterized in that, described gas-liquid-solid three-phase separation precipitator comprises cylindrical shell, lower mud slot is offered at described cylindrical shell side lower, slip swash plate is arranged on described inner barrel obliquely, one end that described slip swash plate is lower is arranged on the following of described lower mud slot, also Air guiding flap is provided with in described cylindrical shell, the incline direction of described Air guiding flap is contrary with the incline direction of described slip swash plate, one end of described Air guiding flap is connected with the sidewall of described cylindrical shell, narrow orifice is formed between the other end of described Air guiding flap and described slip swash plate, the sidewall that described cylindrical shell is connected with described Air guiding flap offers exhaust outlet, inclined tube filter packing is provided with above described slip swash plate and described Air guiding flap.
2. according to gas-liquid-solid three-phase separation precipitator according to claim 1, it is characterized in that, described lower mud slot is strip.
3. according to gas-liquid-solid three-phase separation precipitator according to claim 1, it is characterized in that, above described inclined tube filter packing, be also provided with overflow weir notch.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420415852.2U CN204107101U (en) | 2014-07-28 | 2014-07-28 | A kind of gas-liquid-solid three-phase separation precipitator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420415852.2U CN204107101U (en) | 2014-07-28 | 2014-07-28 | A kind of gas-liquid-solid three-phase separation precipitator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204107101U true CN204107101U (en) | 2015-01-21 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420415852.2U Expired - Lifetime CN204107101U (en) | 2014-07-28 | 2014-07-28 | A kind of gas-liquid-solid three-phase separation precipitator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204107101U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106800333A (en) * | 2016-12-26 | 2017-06-06 | 甘肃银光化学工业集团有限公司 | A kind of three-phase separating device for up-flow anaerobic reactor |
| CN113274806A (en) * | 2021-04-14 | 2021-08-20 | 成都润封电碳有限公司 | Gas-liquid-solid two-stage three-phase separation device and method for waste gas of solidification tank |
-
2014
- 2014-07-28 CN CN201420415852.2U patent/CN204107101U/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106800333A (en) * | 2016-12-26 | 2017-06-06 | 甘肃银光化学工业集团有限公司 | A kind of three-phase separating device for up-flow anaerobic reactor |
| CN113274806A (en) * | 2021-04-14 | 2021-08-20 | 成都润封电碳有限公司 | Gas-liquid-solid two-stage three-phase separation device and method for waste gas of solidification tank |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| 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: 20150121 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 | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20231129 Granted publication date: 20150121 Pledgee: Pudong Shanghai Development Bank Limited by Share Ltd. Wuhan branch Pledgor: WUHAN FUND ENVIRONMENT PROTECTION Co.,Ltd. Registration number: 2018990000703 |