CN201997266U - Device capable of improving mixing efficiency of gas and solution - Google Patents
Device capable of improving mixing efficiency of gas and solution Download PDFInfo
- Publication number
- CN201997266U CN201997266U CN 201120059522 CN201120059522U CN201997266U CN 201997266 U CN201997266 U CN 201997266U CN 201120059522 CN201120059522 CN 201120059522 CN 201120059522 U CN201120059522 U CN 201120059522U CN 201997266 U CN201997266 U CN 201997266U
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- inlet pipe
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- mixing tube
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Abstract
The utility model relates to a device capable of improving mixing efficiency of gas and solution. A liquid inlet pipe is fixedly connected with one end of a mixing pipe, a liquid outlet pipe is fixedly connected with the other end of the mixing pipe, and both the liquid inlet pipe and the liquid outlet pipe are in parallel or bend arrangement with the mixing pipe; a gas inlet pipe is connected to the mixing pipe, a gas outlet pipe is fixedly connected with the gas outlet end of the gas inlet pipe, a countercurrent preventing cover is arranged at the gas outlet end of the gas outlet pipe, the gas inlet pipe is arranged vertical to the gas outlet pipe, the gas inlet pipe is inserted into the mixing pipe, the gas outlet pipe is positioned in the mixing pipe, the gas outlet pipe is arranged vertical to the mixing pipe, and the flow direction of the gas is consistent with the flow direction of the liquid in the mixing pipe; and the liquid inlet pipe and the liquid outlet pipe have the same inside diameter, and the inside diameters of the liquid inlet pipe and the liquid outlet pipe are smaller than the inside diameter of the mixing pipe. Through the device, the mixing efficiency of the gas and the liquid is close to 100 percent; and the device is simple in structure, convenient to install and low in cost.
Description
Technical field
The utility model relates to a kind of device that improves gas and solution mixing efficiency, can solve the device that can improve the efficient pass into solution of gas in the water treatment procedure.
Background technology
In industry, often gas need be mixed with liquid in agricultural and people's the life, the product that makes new advances with production, agricultural chemicals and daily necessities, application in chemical industry and water treatment is also very extensive, running water is wherein handled, pure water production and sewage disposal all need gas is mixed the purpose that purifies water to reach with liquid, but at present directly to inflate mode efficient lower for the air pump that adopts, the gas that is charged into mostly overflows the water surface with the form of bubble and wastes, especially oxious component is carried out the sewage of oxidation processes, the oxygen or the ozone rate of dissolving in that charge in the water are lower than 10%, so processing cost height, and oxidation efficiency is lower, and the ozone that overflows the water surface simultaneously also can work the mischief to human body.
Summary of the invention
The purpose of this utility model is to overcome the deficiencies in the prior art, for efficiently dissolving in liquid, gas provides a kind of effective method, make that organic oxidation efficiency is improved in the water, production cost is reduced, so the utility model is a kind of device that can solve the efficient pass into solution of raising gas in the water treatment procedure.
The technical scheme that provides according to the utility model, the described device that improves gas and solution mixing efficiency, be included in the fixedly connected feed tube in an end of mixing tube, the other end at mixing tube is fixedly connected with drain pipe, feed tube, drain pipe can be parallel shape with mixing tube, also can sweepingly be provided with; On mixing tube, be connected with air inlet pipe, the outlet side of air inlet pipe is fixedly connected with escape pipe, and the outlet side of escape pipe is provided with the antireflux lid, and air inlet pipe and escape pipe are vertical setting, the outlet side of air inlet pipe is positioned at mixing tube, and consistent with the flow direction in the mixing tube; Described feed tube is identical with the internal diameter of drain pipe, and the internal diameter of feed tube and drain pipe is less than the internal diameter of mixing tube.
The internal diameter of described feed tube and drain pipe is 0.02 ~ 3.0 meter, and the length of feed tube and drain pipe is 0.5 ~ 200 meter.The internal diameter of described mixing tube is feed tube and drain pipe internal diameter 0.5 ~ 2.0 times, and the length of mixing tube is 0.1 ~ 10.0 meter.The section configuration of described mixing tube, feed tube or drain pipe is circle, rectangle or rhombus.
Described air inlet pipe is identical with the internal diameter of escape pipe, and the diameter of air inlet pipe and escape pipe is 0.01 ~ 0.5 meter.
Compared with the prior art the utility model has the following advantages:
1, the utility model utilizes the mode that feed tube, mixing tube and drain pipe make up successively, and in mixing tube injecting gas, because feed tube and drain pipe internal diameter are less than mixing tube, when liquid enters the bigger mixing tube of internal diameter by the less feed tube of internal diameter, to produce negative pressure in the pipe, help gas and dissolve in the liquid, the mixing efficiency that makes gas and liquid is near 100%.
2, the utility model is simple in structure, and is easy for installation, and cost is lower.
3, when input has strong oxidizing property gas, can obviously improve oxidation efficiency, have purposes widely at aspects such as sewage disposal and purification of water qualitys.
4, no waste gas is discharged after the gas-liquid mixed, helps environmental protection and personal safety.
Description of drawings
Fig. 1 is an overall structure schematic diagram of the present utility model.
The specific embodiment
The utility model is described in further detail below in conjunction with concrete drawings and Examples.
As shown in the figure, the utility model mainly is made of parts such as mixing tube 1, feed tube 2, drain pipe 3, air inlet pipe 4, escape pipe 5 and antireflux lids 6.
The utility model is used to improve the device of gas and solution mixing efficiency, be included in the fixedly connected feed tube 2 in an end of mixing tube 1, be fixedly connected with drain pipe 3 in the other end of mixing tube 1, feed tube 2, drain pipe 3 all are parallel or crooked setting with mixing tube 1; On mixing tube 1, be connected with air inlet pipe 4, the outlet side of air inlet pipe 4 is fixedly connected with escape pipe 5, the outlet side of escape pipe 5 is provided with antireflux lid 6, air inlet pipe 4 is vertical setting with escape pipe 5, air inlet pipe 4 is inserted in the mixing tube 1, escape pipe 5 is positioned at mixing tube 1, and gas flow is consistent with flowing to of mixing liquid in pipe, and air inlet pipe 4 is vertical setting with mixing tube 1; Described feed tube 2 is identical with the internal diameter of drain pipe 3, and the internal diameter of feed tube 2 and drain pipe 3 is less than the internal diameter of mixing tube 1.
The internal diameter of described feed tube 2 and drain pipe 3 is 0.02 ~ 3.0 meter, and the length of feed tube 2 and drain pipe 3 is 0.5 ~ 200 meter.The internal diameter of described mixing tube 1 is 0.5 ~ 2.0 times of feed tube 2 internal diameters, and the length of mixing tube 1 is 0.1 ~ 10 meter.The section configuration of described mixing tube 1, feed tube 2 or drain pipe 3 is circle, rectangle or rhombus.
Described air inlet pipe 4 is identical with the internal diameter of escape pipe 5, and the diameter of air inlet pipe 4 and escape pipe 5 is 0.01 ~ 0.5 meter.
The liquid outlet of infusion pump is linked to each other with feed tube 2, liquid flows to mixing tube 1 by feed tube 2, while injecting gas in mixing tube 1, because the internal diameter of mixing tube 1 is greater than feed tube 2 and drain pipe 3, therefore in mixing tube 1, there is negative pressure to produce, make gas and liquid in mixing tube 1, mix the back, thereby reach gas and the well-mixed purpose of liquid by drain pipe 3 outputs.When liquid input mixing tube 1, if this moment, drain pipe 3 was closed and air inlet pipe 4 when not importing gas by mistake, flow into air inlet pipe 4 for preventing liquid, the antireflux lid 6 of escape pipe 5 will be closed because of the pressure of liquid.When liquid flow through mixing tube 1 and the gas input is arranged, the promotion that antireflux covers 6 liquid bodies and gas will be opened automatically.
The gas that feeds in the air inlet pipe 4 can be gases such as oxygen, ozone, chlorine, nitrogen and carbon dioxide.
Embodiment 1
A kind of device that improves gas and solution mixing efficiency of the present utility model uses in the tap water quality purification process, and the concrete processing step that adopts is as follows:
1, the structure of liquid-transport pipe-line: comprise water inlet pipe 2, mixing tube 1 and outlet pipe 3; Described water inlet pipe 2 is made by the pig iron, mixing tube 1 and outlet pipe 3 be by resistance to oxidation, corrosion-resistant or seal preferably PVC be that raw material is made, be shaped as circle, the internal diameter of water inlet pipe 2 and outlet pipe 3 is 0.4 meter, length is 100 meters, and the internal diameter of mixing tube 1 is 0.6 meter, and length is 1.0 meters.
2, air inlet pipe setting: air inlet pipe 4 is made for the sludge proof stainless steel, and diameter is 0.1 meter.Air inlet pipe 4 is inserted in the mixing tube, and the gas outlet of escape pipe 5 is over against delivery port, and promptly escape pipe 5 is 90 degree with air inlet pipe 4, and the tracheae in the mixing tube is parallel with flowing to of water, and there is antireflux lid 6 gas outlet of escape pipe 5.
3, being connected of water inlet pipe, mixing tube and outlet pipe: water inlet pipe 2 is connected with an end of mixing tube 1, and the other end of mixing tube 1 is connected with outlet pipe 3, and water flows along water inlet pipe 2, mixing tube 1 and outlet pipe 3 orders successively.Inflow is 300 tons/hour.
4, gas is selected: the ozone generator of being produced by the Xuzhou safe ozone devices of dragon Co., Ltd produces ozone gas source, the ozone generating amount is 1200 Grams Per Hours, the air inlet pipe 4 that ozone efferent duct and mixing tube is outer links to each other, ozone is fully mixed with water in mixing tube 1, and by outlet pipe 3 export in the water purifying tank circularly purifying after 3 hours purification of water quality finish at this point.
A kind of device that improves gas and solution mixing efficiency of the present utility model uses in sewage disposal process, and the concrete processing step that adopts is as follows:
1, the structure of liquid-transport pipe-line: comprise water inlet pipe 2, mixing tube 1 and outlet pipe 3; Described water inlet pipe 2, mixing tube 1 and outlet pipe 3 be by resistance to oxidation, corrosion-resistant or seal preferably PVC be that raw material is made, be shaped as circle, the internal diameter of water inlet pipe 2 and outlet pipe 3 is 0.3 meter, and length is 10 meters, the internal diameter of mixing tube is 0.45 meter, and length is 0.6 meter.
2, air inlet pipe setting: air inlet pipe 4 is made for the sludge proof stainless steel, and diameter is 0.05 meter.Air inlet pipe 4 is inserted in the mixing tube 1, and the gas outlet of escape pipe 5 is over against delivery port, and promptly escape pipe 5 is 90 degree with air inlet pipe 4, and the tracheae in the mixing tube 1 is parallel with flowing to of water, and there is antireflux lid 6 gas outlet of escape pipe 5.
3, being connected of water inlet pipe, mixing tube and outlet pipe: water inlet pipe 2 is connected with an end of mixing tube 1, and the other end of mixing tube 1 is connected with outlet pipe 3, and sewage flows along water inlet pipe 2, mixing tube 1 and outlet pipe 3 orders successively.Inflow is 200 tons/hour.
4, gas is selected: the ozone generator of being produced by the good chapter ozone devices Co., Ltd in Shanghai produces ozone gas source, the ozone generating amount is 800 Grams Per Hours, the air inlet pipe 4 that ozone efferent duct and mixing tube is outer links to each other, ozone is fully mixed with water in mixing tube 1, and export in the aeration tank by outlet pipe 3, directly efflux behind 60 order nylon silk cover filterings, sewage disposal is finished at this point.
A kind of device that improves gas and solution mixing efficiency of the present utility model uses in the water treatment procedure of culturing usefulness, and the concrete processing step that adopts is as follows:
1, the structure of liquid-transport pipe-line: comprise water inlet pipe 2, mixing tube 1 and outlet pipe 3; Described water inlet pipe 2, mixing tube 1 and outlet pipe 3 be by resistance to oxidation, corrosion-resistant or seal preferably PVC be that raw material is made, be shaped as circle, the internal diameter of water inlet pipe 2 and outlet pipe 3 is 0.1 meter, and length is respectively 50 meters and 100 meters, the internal diameter of mixing tube 1 is 0.15 meter, and length is 0.4 meter.
2, air inlet pipe setting: air inlet pipe 4 is made for the sludge proof stainless steel, and diameter is 0.02 meter.Air inlet pipe 4 is inserted in the mixing tube 1, and the gas outlet of escape pipe 5 is over against delivery port, and promptly escape pipe 5 is 90 degree with air inlet pipe 4, and the escape pipe 5 in the mixing tube 1 is parallel with flowing to of water, and there is an antireflux lid gas outlet of escape pipe 5.
3, being connected of water inlet pipe, mixing tube and outlet pipe: water inlet pipe 2 is connected with an end of mixing tube 1, and the other end of mixing tube 1 is connected with outlet pipe 3, and current flow along water inlet pipe 2, mixing tube 1 and outlet pipe 3 orders successively.Inflow is 65 tons/hour.
4, gas is selected: the ozone generator of being produced by the good chapter ozone devices Co., Ltd in Shanghai produces ozone gas source, the ozone generating amount is 200 Grams Per Hours, the air inlet pipe 4 that ozone efferent duct and mixing tube is outer links to each other, ozone is fully mixed with water in mixing tube 1, and export to by outlet pipe 3 and to culture in the pond, can use through 3 hours post precipitations.
A kind of device that improves gas and solution mixing efficiency of the present utility model uses in the water treatment procedure of usefulness of growing seedlings, and the concrete processing step that adopts is as follows:
1, the structure of liquid-transport pipe-line: comprise water inlet pipe 2, mixing tube 1 and outlet pipe 3; Described water inlet pipe 2, mixing tube 1 and outlet pipe 3 be by resistance to oxidation, corrosion-resistant or seal preferably PVC be that raw material is made, be shaped as circle, the internal diameter of water inlet pipe 2 and outlet pipe 3 is 0.1 meter, and length is respectively 100 meters and 50 meters, the internal diameter of mixing tube 1 is 0.15 meter, and length is 0.3 meter.
2, air inlet pipe setting: air inlet pipe 4 is made for the sludge proof stainless steel, and diameter is 0.015 meter.Air inlet pipe 4 is inserted in the mixing tube 1, and the gas outlet of escape pipe 5 is over against delivery port, and promptly escape pipe 5 is 90 degree with air inlet pipe 4, and the escape pipe 5 in the mixing tube 1 is parallel with flowing to of water, and there is antireflux lid 6 gas outlet of escape pipe 5.
3, being connected of water inlet pipe, mixing tube and outlet pipe: water inlet pipe 2 is connected with an end of mixing tube 1, and the other end of mixing tube 1 is connected with outlet pipe 3, and current flow along water inlet pipe 2, mixing tube 1 and outlet pipe 3 orders successively.Inflow is 50 tons/hour.
4, gas is selected: the ozone generator of being produced by the good chapter ozone devices Co., Ltd in Shanghai produces ozone gas source, the ozone generating amount is 150 Grams Per Hours, the air inlet pipe 4 that ozone efferent duct and mixing tube is outer links to each other, ozone is fully mixed with water in mixing tube 1, and export in the cistern by outlet pipe 3, can use through 3 hours post precipitations.
Claims (5)
1. device that can improve gas and solution mixing efficiency, be included in the fixedly connected feed tube (2) in an end of mixing tube (1), be fixedly connected with drain pipe (3) in the other end of mixing tube (1), feed tube (2), drain pipe (3) all are parallel or crooked setting with mixing tube (1); On mixing tube (1), be connected with air inlet pipe (4), the outlet side of air inlet pipe (4) is fixedly connected with escape pipe (5), the outlet side of escape pipe (5) is provided with antireflux lid (6), air inlet pipe (4) is vertical setting with escape pipe (5), air inlet pipe (4) is inserted in the mixing tube (1), escape pipe (5) is positioned at mixing tube (1), and gas flow is consistent with flowing to of mixing liquid in pipe, and air inlet pipe (4) is vertical setting with mixing tube (1); It is characterized in that: described feed tube (2) is identical with the internal diameter of drain pipe (3), and the internal diameter of feed tube (2) and drain pipe (3) is less than the internal diameter of mixing tube (1).
2. the device that improves gas and solution mixing efficiency as claimed in claim 1 is characterized in that: the internal diameter of described feed tube (2) and drain pipe (3) is 0.02 ~ 3.0 meter, and the length of feed tube (2) and drain pipe (3) is 0.5 ~ 200 meter.
3. the device that improves gas and solution mixing efficiency as claimed in claim 1 is characterized in that: the internal diameter of described mixing tube (1) is 0.5 ~ 2.0 times of feed tube (2) internal diameter, and the length of mixing tube (1) is 0.1 ~ 10 meter.
4. the device that improves gas and solution mixing efficiency as claimed in claim 1 is characterized in that: the section configuration of described mixing tube (1), feed tube (2) or drain pipe (3) is circle, rectangle or rhombus.
5. the device that improves gas and solution mixing efficiency as claimed in claim 1 is characterized in that: described air inlet pipe (4) is identical with the internal diameter of escape pipe (5), and the diameter of air inlet pipe (4) and escape pipe (5) is 0.01 ~ 0.5 meter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201120059522 CN201997266U (en) | 2011-03-09 | 2011-03-09 | Device capable of improving mixing efficiency of gas and solution |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201120059522 CN201997266U (en) | 2011-03-09 | 2011-03-09 | Device capable of improving mixing efficiency of gas and solution |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201997266U true CN201997266U (en) | 2011-10-05 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201120059522 Expired - Fee Related CN201997266U (en) | 2011-03-09 | 2011-03-09 | Device capable of improving mixing efficiency of gas and solution |
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| CN (1) | CN201997266U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102172484A (en) * | 2011-03-09 | 2011-09-07 | 中国水产科学研究院淡水渔业研究中心 | Device capable of improving gas and solution mixing efficiency |
| CN105668663A (en) * | 2016-03-24 | 2016-06-15 | 佛山市顺德区美的饮水机制造有限公司 | Water purifying system and bubble generating device for same |
| CN109402947A (en) * | 2017-08-16 | 2019-03-01 | 青岛海尔滚筒洗衣机有限公司 | Cleaner and device for clothing processing |
| CN109395618A (en) * | 2017-08-16 | 2019-03-01 | 青岛海尔滚筒洗衣机有限公司 | Bubble generator and device for clothing processing |
-
2011
- 2011-03-09 CN CN 201120059522 patent/CN201997266U/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102172484A (en) * | 2011-03-09 | 2011-09-07 | 中国水产科学研究院淡水渔业研究中心 | Device capable of improving gas and solution mixing efficiency |
| CN105668663A (en) * | 2016-03-24 | 2016-06-15 | 佛山市顺德区美的饮水机制造有限公司 | Water purifying system and bubble generating device for same |
| CN105668663B (en) * | 2016-03-24 | 2018-12-21 | 佛山市顺德区美的饮水机制造有限公司 | Water purification system and bubble formation device for water purification system |
| CN109402947A (en) * | 2017-08-16 | 2019-03-01 | 青岛海尔滚筒洗衣机有限公司 | Cleaner and device for clothing processing |
| CN109395618A (en) * | 2017-08-16 | 2019-03-01 | 青岛海尔滚筒洗衣机有限公司 | Bubble generator and device for clothing processing |
| CN109395618B (en) * | 2017-08-16 | 2021-12-24 | 青岛海尔滚筒洗衣机有限公司 | Bubble generating device and clothes treating device |
| CN109402947B (en) * | 2017-08-16 | 2022-04-22 | 青岛海尔滚筒洗衣机有限公司 | Cleaner and clothes treatment device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20111005 Termination date: 20130309 |