CN102701427A - Novel ozone gas-liquid conversion device - Google Patents
Novel ozone gas-liquid conversion device Download PDFInfo
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- CN102701427A CN102701427A CN2012102025076A CN201210202507A CN102701427A CN 102701427 A CN102701427 A CN 102701427A CN 2012102025076 A CN2012102025076 A CN 2012102025076A CN 201210202507 A CN201210202507 A CN 201210202507A CN 102701427 A CN102701427 A CN 102701427A
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- gas
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- transfer equipment
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- liquid transfer
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- Treatment Of Water By Oxidation Or Reduction (AREA)
- Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
Abstract
The invention relates to a novel ozone gas-liquid conversion device. The device comprises a base, wherein a gas-liquid conversion device body, a suction pump and a dissolved gas pump are arranged on the base; a suction pipe is connected with the suction pump; and a water supply pipe is arranged at the bottom of the gas-liquid conversion device body. The device is stable and quick, and the dissolved oxygen of an anoxic water area can be quickly improved.
Description
Technical field
The present invention relates to the environmental protection field, be specifically related to a kind of gas-liquid transfer equipment.
Background technology
In the lake, the bottom of marsh, river, inland sea or zone similarity; Deposited a large amount of organism, above-mentioned organism is produced by domestic waste water or agricultural effluent, the remains of waterplant or the planktonic organism that utilizes this organism to breed as food that land flows into.When the bottom in zones such as lake, marsh, river, inland sea is dissolved with oxygen, these organism and settling will be decomposed.Because Decomposition is with consume oxygen, will there be the anoxic waters in the bottom in lake, marsh, river, inland sea.The dissolved oxygen concentration is very low in the anoxic waters, dissolved oxygen concentration dissolved oxygen concentration in the water surface near zone in the anoxic waters.Under special circumstances, the anoxic waters will get into vicious cycle.Because the anoxic waters is often polluted, therefore, photosynthesis can not take place in this zone, and correspondingly, phycophyta can not grow.Because do not have the phycophyta growth, this zone also can not produce oxygen, and thus, makes the anoxybiotic situation worsen more.When the anoxic of bottom, will produce various harmful effects to the environment in zones such as lake, marsh, river, inland sea.For example, if lake, marsh or zone similarity are in anoxic condition, the frequent extinction of epibiota.If lake, marsh or zone similarity anoxic will produce negative pressure state so, make metal elution near dark dish, rock and bottom ooze come out, pollute thereby produce water.
Summary of the invention
Goal of the invention: the objective of the invention is in order to overcome deficiency of the prior art, a kind of rapid raising anoxic waters dissolved oxygen amount is provided, stablize, efficiently novel ozone gas-liquid transfer equipment.
Technical scheme: in order to solve the problems of the technologies described above; A kind of novel ozone gas-liquid transfer equipment of the present invention; It comprises base, on said base, is provided with the gas-liquid transfer equipment, suction pump and air dissolved pump; Be connected with suction tube with said suction pump, be provided with water-supply pipe in said gas-liquid transfer equipment bottom.
Said gas-liquid transfer equipment comprises gas-liquid separation chamber; Be provided with the gas-liquid lysing chamber at said gas-liquid separation chamber internal fixing; Be provided with through hole in said gas-liquid lysing chamber lower side, be provided with venting hole at said gas-liquid separation top of chamber, the bottom is provided with water supply hole; In said gas-liquid separation chamber, be provided with transport pipe, be provided with jet orifice one of said transport pipe.
Said gas-liquid lysing chamber is the dome chamber.
The anoxic water that the present invention will extract from the anoxic waters changes into ozone water and annotates go back to the anoxic waters; Ozone water is with its extremely active, extremely strong oxidizing power; Directly act on bed mud, changing the original anaerobism ecotope of bed mud is aerobic ecotope, rapidly pollution substances such as the organism in the bed mud, sulfide, ammonia, prussiate is degraded; Thereby reach the purpose that bed mud is cut down, fundamentally eliminating the river, to gush blackout smelly.
Beneficial effect: the present invention compared with prior art, its remarkable advantage is: the present invention is stable quick, can improve anoxic waters dissolved oxygen amount rapidly.
Description of drawings
Fig. 1 is a structural representation of the present invention;
Fig. 2 is the structural representation of the transfer equipment of gas-liquid described in the present invention.
Wherein:
1, base; 2, gas-liquid transfer equipment; 3, suction pump; 4, air dissolved pump; 5, suction tube; 6, water-supply pipe; 7, gas-liquid separation chamber; 8, gas-liquid lysing chamber; 9, through hole; 10, venting hole; 11, water supply hole; 12, transport pipe; 13, jet orifice
Embodiment
Below in conjunction with accompanying drawing and embodiment the present invention is further described.
As depicted in figs. 1 and 2; A kind of novel ozone gas-liquid transfer equipment of the present invention belongs to the environmental protection field; It comprises base 1, on said base 1, is provided with gas-liquid transfer equipment 2, suction pump 3 and air dissolved pump 4; Be connected with suction tube 5 with said suction pump 3, be provided with water-supply pipe 6 in said gas-liquid transfer equipment 2 bottoms; Said gas-liquid transfer equipment 2 comprises gas-liquid separation chamber 7; Be provided with gas-liquid lysing chamber 8 at said gas-liquid separation chamber 7 internal fixing; Be provided with through hole 9 in said gas-liquid lysing chamber 8 lower sides, be provided with venting hole 10 at said gas-liquid separation chamber 7 tops, the bottom is provided with water supply hole 11; In said gas-liquid separation chamber 7, be provided with transport pipe 12, be provided with jet orifice 13 12 1 of said transport pipes; Said gas-liquid lysing chamber 8 is the dome chamber.The present invention is stable quick, easy to use, adopts the gas-liquid transfer equipment can improve anoxic waters dissolved oxygen amount rapidly, purifies water environment.
The present invention does not relate to all identical with the prior art prior art that maybe can adopt of part and realizes.
Claims (3)
1. novel ozone gas-liquid transfer equipment; It is characterized in that: it comprises base (1); On said base (1), be provided with gas-liquid transfer equipment (2); Suction pump (3) and air dissolved pump (4) are connected with suction tube (5) with said suction pump (3), are provided with water-supply pipe (6) in said gas-liquid transfer equipment (2) bottom.
2. novel ozone gas-liquid transfer equipment according to claim 1; It is characterized in that: said gas-liquid transfer equipment (2) comprises gas-liquid separation chamber (7); Be provided with gas-liquid lysing chamber (8) at said gas-liquid separation chamber (7) internal fixing; Be provided with through hole (9) in said gas-liquid lysing chamber (8) lower side, be provided with venting hole (10) at said gas-liquid separation chamber (7) top, the bottom is provided with water supply hole (11); In said gas-liquid separation chamber (7), be provided with transport pipe (12), be provided with jet orifice (13) (12) one of said transport pipes.
3. novel ozone gas-liquid transfer equipment according to claim 1 is characterized in that: said gas-liquid lysing chamber (8) is the dome chamber.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012102025076A CN102701427A (en) | 2012-06-19 | 2012-06-19 | Novel ozone gas-liquid conversion device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012102025076A CN102701427A (en) | 2012-06-19 | 2012-06-19 | Novel ozone gas-liquid conversion device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN102701427A true CN102701427A (en) | 2012-10-03 |
Family
ID=46894567
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012102025076A Pending CN102701427A (en) | 2012-06-19 | 2012-06-19 | Novel ozone gas-liquid conversion device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102701427A (en) |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1914123A (en) * | 2004-02-03 | 2007-02-14 | 松江土建株式会社 | Gas-liquid dissolution apparatus |
-
2012
- 2012-06-19 CN CN2012102025076A patent/CN102701427A/en active Pending
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1914123A (en) * | 2004-02-03 | 2007-02-14 | 松江土建株式会社 | Gas-liquid dissolution apparatus |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20121003 |
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| WD01 | Invention patent application deemed withdrawn after publication |