CN206253028U - A kind of high efficient gas and liquid mixing apparatus - Google Patents
A kind of high efficient gas and liquid mixing apparatus Download PDFInfo
- Publication number
- CN206253028U CN206253028U CN201621242704.0U CN201621242704U CN206253028U CN 206253028 U CN206253028 U CN 206253028U CN 201621242704 U CN201621242704 U CN 201621242704U CN 206253028 U CN206253028 U CN 206253028U
- Authority
- CN
- China
- Prior art keywords
- water
- vapour
- liquid
- gas
- contacting column
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Abstract
The utility model discloses a kind of high efficient gas and liquid mixing apparatus, including vapour-liquid contacting column, the component that adds water, aerating component and fluidic module;First manual valve and pressure gauge are provided with the top top outer of the vapour-liquid contacting column, liquid level gauge and lower liquid level gauge are installed in the inside of the vapour-liquid contacting column;The fluidic module includes magnetizer, high-pressure pump and ejector, one end of the magnetizer connects with the circulating outlet of vapour-liquid contacting column, the other end of magnetizer is connected with one end of high-pressure pump, the other end of the high-pressure pump is connected by circulating water inlet with ejector, the ejector has a fluid conduit, and the port of export of the fluid conduit is located at the top of vapour-liquid contacting column.The utility model is efficiently mixed by high-pressure pump and ejector using circulation manufacture, air inlet of intermittently intaking inside mixing column, it is ensured that melting concn is high and has high concentration mixing water deposit at any time.
Description
Technical field
The utility model is related to gas-liquid mixed to prepare and applied technical field, specifically, is related specifically to a kind of efficient
Gas-liquid mixed equipment.
Background technology
High-oxygen water refers to water of each liter of oxygen content in water more than or equal to 35 milligrams.High-oxygen water be it is internationally recognized more
Meet the senior drinking water of human health demand, Japan wait some developed countries that all high-oxygen water is regarded as " 2l centuries are most preferable
Drinking water ".After high-oxygen water is drunk, oxygen is set directly to be transported to whole body by blood through the absorption of stomach and small intestine.
High-concentration ozone water meets bleaching, fresh-keeping, anti-corrosion and the food life for being mainly used in the food such as Water soaking products, dry fruit
The sterilizing of product equipment, container.Due to being converted into water and oxygen after ozone water decomposition, without any pollution and side effect, thus
Have been widely used in the food industry.
The purposes of high efficient gas and liquid mixing is needed in addition with carbonated water, air-flotation process etc..
Typically using modes such as traditional stirring, jet, gas-liquid mixing pump, aerations, there is energy consumption in traditional gas-liquid mixed technology
Greatly, the low shortcoming of mixing efficiency.
Utility model content
The purpose of this utility model is for deficiency of the prior art, there is provided a kind of high efficient gas and liquid mixing apparatus, with
Solve problems of the prior art.
The technical problem that the utility model is solved can be realized using following technical scheme:
A kind of high efficient gas and liquid mixing apparatus, including vapour-liquid contacting column and the vapour-liquid contacting column connection add water component and
Aerating component and the fluidic module in the vapour-liquid contacting column;
First manual valve and pressure gauge are provided with the top top outer of the vapour-liquid contacting column, in the vapour-liquid contacting column
Inside liquid level gauge and lower liquid level gauge are installed;
The component that adds water includes the storage tank for storing water source, and the port of export of storage tank is connected successively by inlet pipeline
Water pump and entering water electromagnetic valve are connected to, and are connected with vapour-liquid contacting column;The aerating component includes the gas storage for storing gas source
Case, the port of export of expansion box is connected with air inlet electromagnetic valve by air inlet pipeline, and is connected with vapour-liquid contacting column;
The fluidic module includes magnetizer, high-pressure pump and ejector, one end and the vapour-liquid contacting column of the magnetizer
Circulating outlet is connected, and the other end of magnetizer is connected with one end of high-pressure pump, and the other end of the high-pressure pump passes through recirculated water
Entrance is connected with ejector, and the ejector has fluid conduit, and the port of export of the fluid conduit is located at vapour-liquid contacting column
Top;
The vapour-liquid contacting column also has outlet pipeline, and water solenoid valve, second are sequentially provided with the outlet pipeline
Hand-operated valve and delivery port.
Further, the magnetizer is in cylinder, and insertion pipeline is provided with the centre of cylinder, is set in cylinder edge
There is the magnetic field for applying active force to hydrone when current pass through.
Further, the gas source includes oxygen and ozone, and gas source is manufactured by oxygenerator and ozone generator, or
Directly stored by gas cylinder.
Further, the water source includes running water, purified water or chemical solvent, and water source passes through tap water pipe line, water purification
Device or tank body are provided.
Further, the solution concentration surveymeter for monitoring water quality situation is provided with the delivery port.
Further, the flows match of the flow of the ejector and water pump, the water source in vapour-liquid contacting column enters incidence
In stream device, the gas end of gas-liquid mixed top of tower is extended to by the fluid conduit gas circuit connection of ejector.
Compared with prior art, the beneficial effects of the utility model are as follows:
The utility model is using circulation manufacture, air inlet of intermittently intaking, by high-pressure pump and ejector in mixing
Tower inside efficiently mixing, it is ensured that melting concn is high and has high concentration mixing water deposit at any time.
Brief description of the drawings
Fig. 1 is the structural representation of high efficient gas and liquid mixing apparatus described in the utility model.
Label declaration in figure:Gas source 1, air inlet electromagnetic valve 2, vapour-liquid contacting column 3, magnetizer 4, high-pressure pump 5, ejector 6,
Upper liquid level gauge 7, lower liquid level gauge 8, water source 9, water pump 10, entering water electromagnetic valve 11, first manual valve 12, pressure gauge 13, water outlet electromagnetism
Valve 14, the second hand-operated valve 15, delivery port 16.
Specific embodiment
For technological means, creation characteristic, reached purpose and effect for realizing the utility model are easy to understand, below
With reference to specific embodiment, the utility model is expanded on further.
Referring to Fig. 1, a kind of high efficient gas and liquid mixing apparatus described in the utility model, including vapour-liquid contacting column 3 and the gas
Add water component and aerating component and the fluidic module in the vapour-liquid contacting column of liquid mixing column connection;
First manual valve 12 and pressure gauge 13 are provided with the top top outer of the vapour-liquid contacting column, it is mixed in the gas-liquid
The inside for closing tower is provided with liquid level gauge 7 and lower liquid level gauge 8;
The component that adds water includes the storage tank for storing water source 9, and the port of export of storage tank passes through inlet pipeline successively
Water pump 10 and entering water electromagnetic valve 11 are connected with, and are connected with vapour-liquid contacting column;The aerating component is included for storing gas source 1
Expansion box, the port of export of expansion box is connected with air inlet electromagnetic valve 2 by air inlet pipeline, and is connected with vapour-liquid contacting column;
The fluidic module includes magnetizer 4, high-pressure pump 5 and ejector 6, one end of the magnetizer and vapour-liquid contacting column
Circulating outlet connection, the other end of magnetizer be connected with one end of high-pressure pump, and the other end of the high-pressure pump passes through to circulate
Water inlet is connected with ejector, and the ejector has fluid conduit, and the port of export of the fluid conduit is located at gas-liquid mixed
The top of tower;
The vapour-liquid contacting column also has outlet pipeline, and water solenoid valve 14, the are sequentially provided with the outlet pipeline
Two hand-operated valves 15 and delivery port 16.
The magnetizer is in cylinder, and insertion pipeline is provided with the centre of cylinder, is provided with current in cylinder edge
By when to hydrone apply active force magnetic field.
The gas source includes oxygen and ozone, and gas source is manufactured by oxygenerator and ozone generator, or by gas cylinder
Directly store.The water source includes running water, purified water or chemical solvent, and water source passes through tap water pipe line, water purifier or tank body
There is provided.
The solution concentration surveymeter for monitoring water quality situation is provided with the delivery port.The flow of the ejector with
The flows match of water pump, the water source in vapour-liquid contacting column enters in ejector, is prolonged by the fluid conduit gas circuit connection of ejector
Extend the gas end of gas-liquid mixed top of tower.
The course of work of the present utility model is as follows:
1) water source is added, water pump and entering water electromagnetic valve is opened, is added water into vapour-liquid contacting column until the upper liquid level gauge of triggering, is
System control stops water inlet.
2) source of the gas is added, air inlet electromagnetic valve (2) is opened, gas is added, until pressure is increased in pressure gauge display tank body
0.2MPa or designated value, stop air inlet flow.
3) molten gas is circulated, high-pressure pump is opened, extracting water from vapour-liquid contacting column middle part transmits to ejector, and ejector sprays water
To the top of air and liquid mixer, realize that gas mixes with the current of circulation, concentration of ordinary dissolution is continuously increased by constantly circulation.
4) discharge water, open water solenoid valve, until the lower liquid level gauge of triggering, the mixture length since water inlet again.
General principle of the present utility model and principal character and advantage of the present utility model has been shown and described above.One's own profession
The technical staff of industry it should be appreciated that the utility model is not restricted to the described embodiments, described in above-described embodiment and specification
Simply illustrate principle of the present utility model, on the premise of the utility model spirit and scope are not departed from, the utility model is also
Various changes and modifications are had, these changes and improvements are both fallen within the range of claimed the utility model.The utility model
Claimed scope is by appending claims and its equivalent thereof.
Claims (6)
1. a kind of high efficient gas and liquid mixing apparatus, it is characterised in that:Including adding that vapour-liquid contacting column and the vapour-liquid contacting column are connected
Water assembly and aerating component and the fluidic module in the vapour-liquid contacting column;
First manual valve and pressure gauge are provided with the top top outer of the vapour-liquid contacting column, in the vapour-liquid contacting column
Portion is provided with liquid level gauge and lower liquid level gauge;
The component that adds water includes the storage tank for storing water source, and the port of export of storage tank is connected with turn by inlet pipeline
Water pump and entering water electromagnetic valve, and connected with vapour-liquid contacting column;The aerating component includes the expansion box for storing gas source, storage
The port of export of gas tank is connected with air inlet electromagnetic valve by air inlet pipeline, and is connected with vapour-liquid contacting column;
The fluidic module includes magnetizer, high-pressure pump and ejector, one end of the magnetizer and the circulation of vapour-liquid contacting column
Delivery port is connected, and the other end of magnetizer is connected with one end of high-pressure pump, and the other end of the high-pressure pump is by circulating water inlet
It is connected with ejector, the ejector has a fluid conduit, and the port of export of the fluid conduit is located at the top of vapour-liquid contacting column
Portion;
The vapour-liquid contacting column also has outlet pipeline, and water solenoid valve, second manual is sequentially provided with the outlet pipeline
Valve and delivery port.
2. high efficient gas and liquid mixing apparatus according to claim 1, it is characterised in that:The magnetizer is in cylinder, in circle
The centre of cylinder is provided with insertion pipeline, and the magnetic field for applying active force to hydrone when current pass through is provided with cylinder edge.
3. high efficient gas and liquid mixing apparatus according to claim 1, it is characterised in that:The gas source includes oxygen and smelly
Oxygen, gas source is manufactured by oxygenerator and ozone generator, or is directly stored by gas cylinder.
4. high efficient gas and liquid mixing apparatus according to claim 1, it is characterised in that:The water source includes running water, purification
Water or chemical solvent, water source are provided by tap water pipe line, water purifier or tank body.
5. high efficient gas and liquid mixing apparatus according to claim 1, it is characterised in that:It is provided with for supervising on the delivery port
Control the solution concentration surveymeter of water quality situation.
6. high efficient gas and liquid mixing apparatus according to claim 1, it is characterised in that:The flow of the ejector and water pump
Flows match, the water source in vapour-liquid contacting column enters in ejector, and gas is extended to by the fluid conduit gas circuit connection of ejector
Gas end at the top of liquid mixing column.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201621242704.0U CN206253028U (en) | 2016-11-15 | 2016-11-15 | A kind of high efficient gas and liquid mixing apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201621242704.0U CN206253028U (en) | 2016-11-15 | 2016-11-15 | A kind of high efficient gas and liquid mixing apparatus |
Publications (1)
Publication Number | Publication Date |
---|---|
CN206253028U true CN206253028U (en) | 2017-06-16 |
Family
ID=59025120
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201621242704.0U Active CN206253028U (en) | 2016-11-15 | 2016-11-15 | A kind of high efficient gas and liquid mixing apparatus |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN206253028U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111569682A (en) * | 2020-04-02 | 2020-08-25 | 南方电网科学研究院有限责任公司 | Transformer insulating oil gas dissolving system and method |
CN114159997A (en) * | 2020-12-04 | 2022-03-11 | 佛山市美的清湖净水设备有限公司 | Gas mixing tank and water purifier with same |
-
2016
- 2016-11-15 CN CN201621242704.0U patent/CN206253028U/en active Active
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111569682A (en) * | 2020-04-02 | 2020-08-25 | 南方电网科学研究院有限责任公司 | Transformer insulating oil gas dissolving system and method |
CN114159997A (en) * | 2020-12-04 | 2022-03-11 | 佛山市美的清湖净水设备有限公司 | Gas mixing tank and water purifier with same |
CN114159997B (en) * | 2020-12-04 | 2023-12-19 | 佛山市美的清湖净水设备有限公司 | Mixed gas tank and water purifier with same |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101402024B (en) | An ozone supply device | |
CN101868426B (en) | Hyperoxidation advanced oxidative treatment of water | |
CN104176708A (en) | Unpowered pressurized chlorine dioxide automatic-generation mixing sterilizing device | |
CN104326522A (en) | Multistage efficient ozone air floatation integrated device | |
CN106345326B (en) | A kind of intermittent method and device for preparing high-concentration ozone water | |
CN206253028U (en) | A kind of high efficient gas and liquid mixing apparatus | |
CN110330093A (en) | A kind of pressure air-dissolving strengthens ozone pre-oxidation capability device and its processing method | |
CN101549900B (en) | Process for producing bottled water sterilized by ozone and sterilized bottled water | |
JP2009101329A (en) | Liquid treatment apparatus | |
CN102887605A (en) | Activating and storing device of natural water | |
CN101254014A (en) | A high-density carbon dioxide sterilization treatment reactor | |
CN207493516U (en) | A kind of high-efficiency high-concentration air-dissolving apparatus | |
CN206253024U (en) | One kind i.e. system uses gas-liquid mixed equipment | |
CN109289744B (en) | Metronidazole production method, device and application for improving nitric acid utilization rate | |
CN101659474A (en) | Water treatment device of continuous flow ozone/ultraviolet/advanced oxidation | |
CN205500884U (en) | Countercurrent circuit ozone oxidation experimental apparatus | |
CN115920682A (en) | Nano ozone generating device | |
CN214990326U (en) | Multi-concentration ozone water preparation device | |
CN109081423A (en) | A kind of container-type oxidative system and method | |
CN108975529A (en) | A kind of filtering, inert gas ballast water for ship combined apparatus and method | |
CN107596935A (en) | A kind of high-efficiency high-concentration air-dissolving apparatus | |
CN202864987U (en) | Ozone dosing equipment for alkaline drinking water | |
CN209680087U (en) | A kind of metronidazole production device for improving the utilization rate of nitric acid | |
CN102060399A (en) | Ammonia nitrogen removing device assisting organic compound denitrifier in treating high concentration ammonia nitrogen wastewater | |
CN106957101A (en) | The high-efficient treatment device and handling process of a kind of water body containing microorganism |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
PP01 | Preservation of patent right |
Effective date of registration: 20200820 Granted publication date: 20170616 |
|
PP01 | Preservation of patent right | ||
PD01 | Discharge of preservation of patent |
Date of cancellation: 20230820 Granted publication date: 20170616 |
|
PD01 | Discharge of preservation of patent | ||
PP01 | Preservation of patent right |
Effective date of registration: 20230820 Granted publication date: 20170616 |
|
PP01 | Preservation of patent right |