CN207429855U - A kind of New Hydrogen/oxygen separating device - Google Patents
A kind of New Hydrogen/oxygen separating device Download PDFInfo
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- CN207429855U CN207429855U CN201720566214.4U CN201720566214U CN207429855U CN 207429855 U CN207429855 U CN 207429855U CN 201720566214 U CN201720566214 U CN 201720566214U CN 207429855 U CN207429855 U CN 207429855U
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- tank body
- air inlet
- pressure difference
- tank
- separating device
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Abstract
The utility model discloses a kind of New Hydrogen/oxygen separating devices, it is characterised in that：Including tank body, air inlet is equipped in the middle part of the tank body, the air inlet is equipped with air inlet pipe, and one end of the air inlet pipe is arranged at the outside of the tank body, and the other end inserts in the tank interior；Gas outlet is equipped at the top of the tank body, bottom is equipped with liquid outlet；A back taper baffle is additionally provided in the middle part of the tank body, the center of the back taper baffle is equipped with an air passing hole, and the outer edge surface of the back taper baffle is connected with the inner wall of the tank body, and the back taper baffle plate setting is in the top of the air inlet pipe.The utility model improves gas-liquid separation efficiency, reduces equipment size, reduces occupancy of the equipment to space, that is, reduces cost.
Description
Technical field
The utility model is related to a kind of gas-liquid separation device more particularly to a kind of New Hydrogen/oxygen separating device, suitable for hydrogen
The separation of gas and moisture content and the separation of oxygen and moisture.
Background technology
With the development of national economy, the use scope of hydrogen is more and more wider, penetrates into tens industries, in the recent period in energy
Source domain is also promoted, water electrolysis hydrogen producing system with the peculiar advantage such as its raw material, purity and operation in hydrogen preparation field increasingly
Paid attention to.Water electrolysis hydrogen producing system produces hydrogen or oxygen gas using electrolysis water, and the gas that electrolytic cell comes out contains lye (pure water),
There is a small amount of liquid during subsequent gas-liquid separation.
Current technology, lye (pure water) are taken out of into hydrogen/oxygen separator with gas from water electrolyser and carry out gas and liquid
Separation, separated principle be by both self gravitation different after certain parting surface and transport disengaging height, the two
Realization is totally separated from, both in simple terms separation fully rely on equipment have in enough large spaces by both self gravitation exist
It is not added with realizing separation in the case of external force interference, so fully relies on equipment and be sufficiently separated space to realize separation, equipment volume
It is huge.
The content of the invention
The utility model aim is to provide a kind of New Hydrogen/oxygen separating device, by using the structure, improves gas-liquid point
From efficiency and disintegrate-quality, equipment volume is reduced, device space occupancy is reduced, reduces cost.
In order to achieve the above objectives, the technical solution adopted in the utility model is：A kind of New Hydrogen/oxygen separating device, including
Tank body, is equipped with air inlet in the middle part of the tank body, and the air inlet is equipped with air inlet pipe, and one end of the air inlet pipe is arranged at described
The outside of tank body, the other end insert in the tank interior；Gas outlet is equipped at the top of the tank body, bottom is equipped with liquid outlet；It is described
A back taper baffle is additionally provided in the middle part of tank body, the center of the back taper baffle is equipped with an air passing hole, the back taper baffle
Outer edge surface be connected with the inner wall of the tank body, and the back taper baffle plate setting is in the top of the air inlet pipe.
In above-mentioned technical proposal, the air inlet pipe is curved pipe, and the inlet end of the air inlet pipe is installed on the air inlet
It is interior, the inner tank wall of air inlet side described in the face of outlet side, and the air outlet pipe is set perpendicular to the inner wall of the tank body, institute
The inner wall that outlet side is stated close to the tank body is set.
In above-mentioned technical proposal, the 1/10~1/5 of a diameter of tank diameter of the air passing hole.
In above-mentioned technical proposal, a fluid infusion is additionally provided at the top of the tank body, a liquid supplementation pipe is connected in the fluid infusion,
One end of the liquid supplementation pipe is connected with the fluid infusion, the other end pass through the air passing hole, be arranged at the liquid outlet just on
Side；The tank wall is equipped with a refluxing opening, and the refluxing opening is arranged at the lower section of the air inlet pipe, and the refluxing opening leans on
The nearly tank base is set.
In above-mentioned technical proposal, two pressure difference transmitter interfaces are respectively equipped on the tank body, the pressure difference transmitter connects
Mouth is equipped with sealing cover, the respectively upper pressure difference transmitter interface of the pressure difference transmitter interface and lower pressure difference transmitter interface, institute
It states pressure difference transmitter interface to be arranged at the top of the tank body, the lower pressure difference transmitter interface is arranged at the tank base.
In above-mentioned technical proposal, the refluxing opening is arranged between the lower pressure difference transmitter interface and the air inlet.
In above-mentioned technical proposal, a nitrogen charging mouth is additionally provided on the tank body of the liquid outlet side.
In above-mentioned technical proposal, the bottom of the tank body is additionally provided with level sensing mouth.
Since above-mentioned technical proposal is used, the utility model has following advantages compared with prior art：
1., using the setting of back taper baffle, so contained by setting back taper baffle in tank body in the utility model
The hydrogen or oxygen for having moisture content enter after tank body, by the setting of back taper baffle, liquid can be prevented to move up, make liquid
Know from experience and accelerate drippage in the bottom of tank body, and oxygen or hydrogen are then kept off by air passing hole on back taper baffle by back taper
Plate, then sent out by gas outlet from oxygen, hydrogen separator, compared with the structure being freely separating by self gravitation in the past, Neng Gouti
High gas-liquid separation efficiency, meanwhile, it can also reduce the volume of equipment, reduce cost, reduce space occupancy rate；
2. by setting nitrogen inlet on babinet in the utility model, it can break up box house oxygen, hydrogen
Concentration, security when ensureing to use.
Description of the drawings
Fig. 1 is the structure diagram in the utility model embodiment one；
Fig. 2 is the top structure schematic diagram of tank interior in the utility model embodiment one.
Wherein：1st, tank body；2nd, air inlet；3rd, air inlet pipe；4th, gas outlet；5th, liquid outlet；6th, back taper baffle；7th, gas is crossed
Hole；8th, fluid infusion；9th, liquid supplementation pipe；10th, nitrogen charging mouth；11st, refluxing opening；12nd, sealing cover；13rd, upper pressure difference transmitter interface；14th, under
Pressure difference transmitter interface.
Specific embodiment
The utility model is further described with reference to the accompanying drawings and embodiments：
Embodiment one：Referring to shown in Fig. 1,2, a kind of New Hydrogen/oxygen separating device, including tank body 1,1 middle part of tank body
Equipped with air inlet 2, the air inlet 2 is equipped with air inlet pipe 3, and one end of the air inlet pipe 3 is arranged at the outside of the tank body 1,
The other end is inserted in inside the tank body 1；1 top of tank body is equipped with gas outlet 4, and bottom is equipped with liquid outlet 5；In the tank body 1
Portion is additionally provided with a back taper baffle 6, and the center of the back taper baffle 6 is equipped with an air passing hole 7, the back taper baffle 6
Outer edge surface is connected with the inner wall of the tank body 1, and the back taper baffle 6 is arranged at the top of the air inlet pipe 3.
In previous structure, oxygen or hydrogen with moisture content enter from the middle part of tank body, then using density and again
The difference of power, after certain parting surface and transport disengaging height, moisture is kept completely separate with oxygen or hydrogen realization, that is, two
Person separation fully rely on equipment in the case that have in enough large spaces by both self gravitation be not added with external force interference realize point
From so fully relying on equipment and be sufficiently separated space to realize separation, equipment volume is huge.And in the present embodiment, pass through
Back taper baffle in the middle part of tank body is set, air passing hole, if moisture content moves upwards, back taper are set at the middle part of back taper baffle
Baffle can Active liquid move upwards, make downward liquid flow, and gas can then be sent to back taper gear by air passing hole
Oxygen separator or hydrogen separator are left in the top of plate by gas outlet, and compared with previous structure, the efficiency of gas-liquid separation is more preferable,
And equipment volume smaller, cost are less expensive.
The air inlet pipe 3 is curved pipe, and the inlet end of the air inlet pipe is installed in the air inlet, outlet side face institute
The inner tank wall of air inlet side is stated, and the air outlet pipe is set perpendicular to the inner wall of the tank body, the outlet side is close to institute
The inner wall for stating tank body is set.
Wherein, by the way that air inlet pipe is arranged to curved pipe, after gas-liquid is entered together in tank body, gas-liquid can first strike
On the inner wall of tank body, the gas-liquid in inner tank wall is impinged upon, meeting speed up gas and liquid moves up, if moved down,
Since the gravity of liquid can be more than the gravity of gas, liquid can accelerate to move down, after gas landing to a certain extent, still
It can move upwards, be sent out by air passing hole from gas outlet.If gas-liquid moves upwards, gas-liquid can be struck on back taper baffle,
So liquid can be blocked, and then since gravity is big, liquid can drip downwards, and gas can rise out of air passing hole, pass through
It sends out gas outlet.If liquid also after air passing hole is risen to above back taper baffle, also can gradually land, such
Words, due to the pyramidal structure of back taper baffle, liquid can be dripped from air passing hole, effectively improve gas-liquid separation efficiency and separation matter
Amount.
The 1/10~1/5 of a diameter of tank diameter of the air passing hole.It can so ensure the face of back taper baffle
Product, ensures the blocking effect to liquid.
1 top of tank body is additionally provided with a fluid infusion 8, and a liquid supplementation pipe 9, the liquid supplementation pipe 9 are connected in the fluid infusion 8
One end be connected with the fluid infusion 8, the other end passes through the air passing hole 7, is arranged at the surface of the liquid outlet 8；It is described
1 side wall of tank body is equipped with a refluxing opening 11, and the reflux 11 is arranged at the lower section of the air inlet pipe 3, and the refluxing opening 11 leans on
Nearly 1 bottom of tank body is set.
Two pressure difference transmitter interfaces are respectively equipped on the tank body 1, the pressure difference transmitter interface is equipped with sealing cover
12, the pressure difference transmitter interface is respectively to go up pressure difference transmitter interface 13 and lower pressure difference transmitter interface 14, the upper pressure difference
Transmitter interface is arranged at the top of the tank body, and the lower pressure difference transmitter interface is arranged at the tank base.
The refluxing opening is arranged between the lower pressure difference transmitter interface and the air inlet.
Wherein, oxygen separation uses respectively and each a tank body with nitrogen separation, wherein, for the tank body of oxygen separation
On, pressure difference transmitter is connected on pressure difference transmitter interface, for the tank body of Hydrogen Separation, pressure difference transmitter interface is then direct
It is sealed with sealing cover, pressure difference transmitter need not be connected.Wherein, the pressure difference on the tank body of Hydrogen Separation can also be become
Device interface is sent to directly sealing.
A nitrogen charging mouth 10 is additionally provided on the tank body 1 of 5 side of liquid outlet.So when tank body is cleared up, first by tank
In vivo oxygen or hydrogen are blown off, ensure security.
In the bottom of tank body, level sensing mouth is additionally provided with, for detecting tank base amount of liquid.
Claims (8)
1. a kind of New Hydrogen/oxygen separating device, it is characterised in that：Including tank body, be equipped with air inlet in the middle part of the tank body, it is described into
Gas port is equipped with air inlet pipe, and one end of the air inlet pipe is arranged at the outside of the tank body, and the other end inserts in the tank interior；
Gas outlet is equipped at the top of the tank body, bottom is equipped with liquid outlet；A back taper baffle, the back taper are additionally provided in the middle part of the tank body
The center of shape baffle is equipped with an air passing hole, and the outer edge surface of the back taper baffle is connected with the inner wall of the tank body, and described
Back taper baffle plate setting is in the top of the air inlet pipe.
2. New Hydrogen according to claim 1/oxygen separating device, it is characterised in that：The air inlet pipe is curved pipe, described
The inlet end of air inlet pipe is installed in the air inlet, the inner tank wall of air inlet side described in the face of outlet side, and it is described go out
Tracheae is set perpendicular to the inner wall of the tank body, and the outlet side is set close to the inner wall of the tank body.
3. New Hydrogen according to claim 1/oxygen separating device, it is characterised in that：The air passing hole it is a diameter of described
The 1/10~1/5 of tank diameter.
4. New Hydrogen according to claim 1/oxygen separating device, it is characterised in that：A benefit is additionally provided at the top of the tank body
Liquid mouth is connected with a liquid supplementation pipe in the fluid infusion, and one end of the liquid supplementation pipe is connected with the fluid infusion, and the other end passes through institute
Air passing hole is stated, is arranged at the surface of the liquid outlet；The tank wall is equipped with a refluxing opening, and the refluxing opening is arranged at
The lower section of the air inlet pipe, and the refluxing opening is set close to the tank base.
5. New Hydrogen according to claim 4/oxygen separating device, it is characterised in that：Two are respectively equipped on the tank body
Pressure difference transmitter interface, the pressure difference transmitter interface are equipped with sealing cover, and the pressure difference transmitter interface is respectively upper pressure difference
Transmitter interface and lower pressure difference transmitter interface, the upper pressure difference transmitter interface are arranged at the top of the tank body, the pushing
Poor transmitter interface is arranged at the tank base.
6. New Hydrogen according to claim 5/oxygen separating device, it is characterised in that：The refluxing opening be arranged at it is described under
Between pressure difference transmitter interface and the air inlet.
7. New Hydrogen according to claim 1/oxygen separating device, it is characterised in that：On the tank body of the liquid outlet side
It is additionally provided with a nitrogen charging mouth.
8. New Hydrogen according to claim 1/oxygen separating device, it is characterised in that：The bottom of the tank body, is additionally provided with
Level sensing mouth.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720566214.4U CN207429855U (en) | 2017-05-19 | 2017-05-19 | A kind of New Hydrogen/oxygen separating device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720566214.4U CN207429855U (en) | 2017-05-19 | 2017-05-19 | A kind of New Hydrogen/oxygen separating device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207429855U true CN207429855U (en) | 2018-06-01 |
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ID=62395011
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| Application Number | Title | Priority Date | Filing Date |
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| CN201720566214.4U Active CN207429855U (en) | 2017-05-19 | 2017-05-19 | A kind of New Hydrogen/oxygen separating device |
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| CN (1) | CN207429855U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107019963A (en) * | 2017-05-19 | 2017-08-08 | 苏州奥尔新能源科技有限公司 | A kind of New Hydrogen/oxygen separating device |
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2017
- 2017-05-19 CN CN201720566214.4U patent/CN207429855U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107019963A (en) * | 2017-05-19 | 2017-08-08 | 苏州奥尔新能源科技有限公司 | A kind of New Hydrogen/oxygen separating device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20190911 Address after: 215000 Lou Ji Mei Lane Industrial Zone, Suzhou Industrial Park, Suzhou City, Jiangsu Province Patentee after: Suzhou Industrial Park ofit Gas Equipment Co., Ltd. Address before: 215000 West Side Office Building of No. 4 Workshop, 59 Weixin Road, Suzhou Industrial Park, Jiangsu Province Patentee before: Suzhou Creole Amperex Technology Limited |
|
| TR01 | Transfer of patent right |