CN105984911A - Air-water mixing jet flow foam breaker - Google Patents
Air-water mixing jet flow foam breaker Download PDFInfo
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- CN105984911A CN105984911A CN201510069383.2A CN201510069383A CN105984911A CN 105984911 A CN105984911 A CN 105984911A CN 201510069383 A CN201510069383 A CN 201510069383A CN 105984911 A CN105984911 A CN 105984911A
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- water inlet
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Abstract
The invention provides an air-water mixing jet flow foam breaker. The air-water mixing jet flow foam breaker comprises a cylindrical shell, a water inlet, a nozzle, a high pressure tuyere, a defoaming pipe, a bubble capture net and a foam inlet, the water inlet is arranged at the outer side end of the cylindrical shell, the nozzle is arranged in the cylindrical shell, the nozzle is communicated with the water inlet, the high pressure tuyere is arranged at the upper end of the cylindrical shell, the foam inlet is arranged at the lower end of the cylindrical shell, the defoaming pipe is crosswise arranged in the cylindrical shell, one end of the defoaming pipe close to the nozzle is an inlet, the other end is an outlet, and the bubble capture net is arranged at the outlet. Under action of high pressure air from the high pressure tuyere, water injected by the nozzle blows foam at the front end of the nozzle into the defoaming pipe, bubbles in the defoaming pipe are broken because of pressure sudden release and water impact and the water drops go through the bubble capture net and then are gathered along a down pipe. The air-water mixing jet flow foam breaker has the advantages of simple structure, low operation cost, ideal defoaming effects, no secondary pollution on water and operation stability.
Description
Technical field
The invention belongs to field of sewage treatment equipment, especially relate to a kind of edema due to wind pathogen mixing jet froth breaker.
Background technology
The continuous reinforcement administered along with the most in short supply of water resource and environmental pollution, people start increasingly
Pay close attention to this work of waste water control；In sewage disposal process, due to being mixed into of air, it is easy to produce
Bubble, affects the quality of sewage disposal；And mostly use interpolation to disappear in oil platform sewage treatment process
Bubble during the mode Processing for removing of bubble medicament, the froth breaking dose efficacy persistent period is short, and consumption is big,
Therefore froth breaking reagent cost is added the highest, and froth breaking medicament inherently a kind of pollutant, medicament can not be kept away
Water quality is caused secondary pollution by the meeting exempted from, and therefore, needs badly to develop and a kind of just can disappear without chemical agent
The bubble produced in scrubbing water treatment procedure, and can the defoaming treatment equipment of continuous and steady operation.
Summary of the invention
The problem to be solved in the present invention be to provide a kind of simple in construction, operating cost is low, defoaming effect is preferable,
Do not result in the secondary pollution of water quality, stable edema due to wind pathogen mixing jet froth breaker.
For solving above-mentioned technical problem, the technical solution used in the present invention is: a kind of edema due to wind pathogen mixing jet disappears
Bubble device, including cylinder, water inlet, nozzle, high pressure tuyere, froth breaking pipeline, catches and indulges in serfing the Net and foam inlet,
Described cylinder horizontally set；Described water inlet is arranged at the outside side of cylinder, and described nozzle is arranged at cylinder
Inside, this nozzle is connected with water inlet, nozzle diameter with described nozzle stretch into the cylinder degree of depth increase and
It is gradually reduced；Described high pressure tuyere is arranged at cylinder upper end, is connected with cylinder, and this high pressure tuyere is positioned at
Above nozzle water exit position；Described foam inlet is arranged at cylinder lower end, is connected with cylinder, this foam
Import is positioned at below nozzle centre position；Described froth breaking passage is horizontally set in cylinder, this froth breaking passage
Nearly nozzle one end is entrance point, and the other end is the port of export；Described catch to indulge in serfing the Net be arranged at port of export position；
Described cylinder is provided with moisture separator away from water inlet one end, and this moisture separator includes being connected
Up-hill line and downstream pip.
It is provided with baffle plate between described froth breaking channel entrance end and cylinder inboard wall.
Described froth breaking passage is class conical flask structure, entrance point gradually increase to port of export direction channel diameter
Greatly.
Described water inlet is cylindrical structure.
Owing to using technique scheme, through the water of nozzle at the work of the high-pressure blast blown out through high pressure tuyere
Under with, the foam entering cylinder inner nozzle front end is blown in froth breaking pipeline, enter the gas in froth breaking pipeline
Bubble discharges suddenly due to pressure and the impact of waterpower ruptures, and water droplet converges along downstream pip after catching and indulging in serfing the Net
Collection, gas is discharged by up-hill line, makes the present invention without chemical agent, relies on wind and water combination froth breaking structure
Just can eliminate the bubble produced in sewage disposal process, make the operation for the treatment of facility continuous-stable.
The invention has the beneficial effects as follows: have simple in construction, operating cost is low, defoaming effect is preferable, no
The secondary pollution of water quality, stable advantage can be caused.
Accompanying drawing explanation
Below with reference to accompanying drawing and combine example and be specifically described the present invention, advantages of the present invention and realization
Mode will become apparent from, and wherein content shown in accompanying drawing is only used for explanation of the present invention, and not structure
The restriction gone up in all senses of the present invention in pairs, in the accompanying drawings:
Fig. 1 is the structural representation of the present invention
In figure:
1, cylinder 2, water inlet 3, nozzle
4, high pressure tuyere 5, froth breaking pipeline 6, catch and indulge in serfing the Net
7, foam inlet 8, moisture separator 9, baffle plate
51, entrance point 52, the port of export 81, up-hill line
82, downstream pip
Detailed description of the invention
As it is shown in figure 1, one edema due to wind pathogen of the present invention mixing jet froth breaker, including cylinder 1, water inlet 2,
Nozzle 3, high pressure tuyere 4, froth breaking pipeline 5, catching and indulge in serfing the Net 6 and foam inlet 7, described cylinder 1 is horizontal
Arrange；Described water inlet 2 is arranged at the outside side of cylinder 1, and it is internal that described nozzle 3 is arranged at cylinder 1,
This nozzle 3 is connected with water inlet 2, and nozzle 3 diameter stretches into the increase of the cylinder degree of depth with described nozzle 3
And be gradually reduced；Described high pressure tuyere 4 is arranged at cylinder 1 upper end, is connected with cylinder 1, this high pressure
Tuyere 4 is positioned at above nozzle 3 water exit position；Described foam inlet 7 is arranged at cylinder 1 lower end, with cylinder
Body 1 is connected, and this foam inlet 7 is positioned at below nozzle 3 centre position；Described froth breaking passage 5 is horizontal
Being arranged in cylinder 1, this nearly nozzle 3 one end of froth breaking passage 5 is entrance point 51, and the other end is the port of export
52；Described catch to indulge in serfing the Net 6 be arranged at the port of export 52 position；Described cylinder 1 sets away from water inlet 2 one end
Being equipped with moisture separator 8, this moisture separator 8 includes up-hill line 81 and the down pipe being connected
Road 82；It is provided with baffle plate 9 between described froth breaking passage 5 entrance point 51 and cylinder 1 inwall；Described disappear
Bubble passage 5 is class conical flask structure, entrance point 51 to the port of export 52 direction channel diameter be gradually increased；
Described water inlet 2 is cylindrical structure.
The work process of this example: enter cylinder 1 from water inlet 2, through nozzle 3 injection water at warp
Under the high pressure wind action of high pressure tuyere 4 blowout, before cylinder 1 inner nozzle 3 being entered by foam inlet 7
The foam of end blows in froth breaking pipeline 5, enter the bubble in froth breaking pipeline 5 discharge suddenly due to pressure and
The impact of waterpower ruptures, and water droplet is indulged in serfing the Net after 6 along descending through catching of froth breaking pipeline 5 port of export 52
Pipeline 82 collects, and gas is discharged by up-hill line 81, makes the present invention without chemical agent, relies on wind and water
Combination froth breaking structure just can eliminate the bubble produced in sewage disposal process, makes treatment facility continuous-stable
Run.
Above embodiments of the invention are described in detail, but described content has been only the preferable of the present invention
Embodiment, it is impossible to be considered the practical range for limiting the present invention.All according to the scope of the invention made equal
Deng change and improvement etc., within all should still belonging to this patent covering scope.
Claims (4)
1. an edema due to wind pathogen mixing jet froth breaker, it is characterised in that: include cylinder, water inlet, nozzle,
High pressure tuyere, froth breaking pipeline, catch and indulge in serfing the Net and foam inlet, described cylinder horizontally set；Described water inlet
Being arranged at the outside side of cylinder, described nozzle is arranged at inner barrel, and this nozzle is connected with water inlet,
Nozzle diameter stretches into the increase of the cylinder degree of depth with described nozzle and is gradually reduced；Described high pressure tuyere is arranged at
Cylinder upper end, is connected with cylinder, and this high pressure tuyere is positioned at above nozzle water exit position；Described foam enters
Mouth is arranged at cylinder lower end, is connected with cylinder, and this foam inlet is positioned at below nozzle centre position；Institute
Stating froth breaking passage to be horizontally set in cylinder, this froth breaking passage nearly nozzle one end is entrance point, and the other end is
The port of export；Described catch to indulge in serfing the Net be arranged at port of export position；Described cylinder is provided with away from water inlet one end
Moisture separator, this moisture separator includes up-hill line and the downstream pip being connected.
Edema due to wind pathogen the most according to claim 1 mixing jet froth breaker, it is characterised in that: described froth breaking
It is provided with baffle plate between channel entrance end and cylinder inboard wall.
Edema due to wind pathogen the most according to claim 1 mixing jet froth breaker, it is characterised in that: described froth breaking
Passage is class conical flask structure, entrance point be gradually increased to port of export direction channel diameter.
Edema due to wind pathogen the most according to claim 1 mixing jet froth breaker, it is characterised in that: described water inlet
Mouth is cylindrical structure.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510069383.2A CN105984911A (en) | 2015-02-10 | 2015-02-10 | Air-water mixing jet flow foam breaker |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510069383.2A CN105984911A (en) | 2015-02-10 | 2015-02-10 | Air-water mixing jet flow foam breaker |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105984911A true CN105984911A (en) | 2016-10-05 |
Family
ID=57041650
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510069383.2A Pending CN105984911A (en) | 2015-02-10 | 2015-02-10 | Air-water mixing jet flow foam breaker |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105984911A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114471211A (en) * | 2022-01-24 | 2022-05-13 | 黑龙江中医药大学 | Preparation device and method of traditional Chinese medicine shampoo for conditioning scalp psoriasis |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20110180633A1 (en) * | 2010-01-27 | 2011-07-28 | Vaughan Co., Inc. | System Having Foam Busting Nozzle and Sub-Surface Mixing Nozzle |
| CN202689981U (en) * | 2012-08-05 | 2013-01-23 | 吉林大学 | Fluid impacting type mechanical defoamer for foam drilling |
| CN203890124U (en) * | 2014-05-25 | 2014-10-22 | 山东正清环保科技有限公司 | High dissolved oxygen plug-free defoaming jet aerator |
| CN204454679U (en) * | 2015-02-10 | 2015-07-08 | 天津翼高腾飞电解技术有限公司 | A kind of geomantic omen mixing jet froth breaker |
-
2015
- 2015-02-10 CN CN201510069383.2A patent/CN105984911A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20110180633A1 (en) * | 2010-01-27 | 2011-07-28 | Vaughan Co., Inc. | System Having Foam Busting Nozzle and Sub-Surface Mixing Nozzle |
| CN202689981U (en) * | 2012-08-05 | 2013-01-23 | 吉林大学 | Fluid impacting type mechanical defoamer for foam drilling |
| CN203890124U (en) * | 2014-05-25 | 2014-10-22 | 山东正清环保科技有限公司 | High dissolved oxygen plug-free defoaming jet aerator |
| CN204454679U (en) * | 2015-02-10 | 2015-07-08 | 天津翼高腾飞电解技术有限公司 | A kind of geomantic omen mixing jet froth breaker |
Non-Patent Citations (3)
| Title |
|---|
| 丁启圣等: "《新型实用过滤技术》", 31 January 2000, 冶金工业出版社 * |
| 朱耕青等: "《石油炼制工艺学》", 31 May 1992, 中国石化出版社 * |
| 耿瑞伦，陈星庆 主编: "《多工艺空气钻探》", 31 October 1995, 北京：地质出版社 * |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114471211A (en) * | 2022-01-24 | 2022-05-13 | 黑龙江中医药大学 | Preparation device and method of traditional Chinese medicine shampoo for conditioning scalp psoriasis |
| CN114471211B (en) * | 2022-01-24 | 2022-09-02 | 黑龙江中医药大学 | Preparation device and method of traditional Chinese medicine shampoo for conditioning scalp psoriasis |
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|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20161005 |
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| RJ01 | Rejection of invention patent application after publication |