CN208512221U - A kind of Oxygen Purge System - Google Patents
A kind of Oxygen Purge System Download PDFInfo
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- CN208512221U CN208512221U CN201820841180.XU CN201820841180U CN208512221U CN 208512221 U CN208512221 U CN 208512221U CN 201820841180 U CN201820841180 U CN 201820841180U CN 208512221 U CN208512221 U CN 208512221U
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- oxygen
- tank
- heat exchange
- drainer
- condensation
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Abstract
The utility model discloses a kind of Oxygen Purge Systems, belong to oxygen purification technical field.Including oxygen input tube, drainer, water collect tank, oxygen output tube and heat exchange tank, the oxygen input tube is connected to the drainer, uniformly coiling has condenser coil on the condensation tank wall, the water collect tank is arranged in the condensation pot bottom and is connected to drainer, the pot bottom that catchments is equipped with discharge outlet, the discharge outlet is equipped with control valve, described oxygen output tube one end is connected to the water collect tank, the other end passes through the heat exchange tank and stretches out from the heat exchange tank, the oxygen output tube is located at the coiled coil on the heat exchange top tank structure of the part in the heat exchange tank and extends, the heat exchange tank is equipped with air inlet and exhaust outlet, the exhaust outlet is equipped with filter.The utility model, by the oxygen heating after condensation purification, to be conducive to the use of follow-up equipment, technique, improves energy utilization rate, reduces energy consumption using high hot exhaust gas.
Description
Technical field
The utility model relates to a kind of Oxygen Purge Systems, belong to oxygen purification technical field.
Background technique
Electrolysis water is a kind of current very mature hydrogen manufacturing oxygen technique, and process is simple, hydrogen and oxygen after electrolysis
Incendivity releases heat after mixing, can be used as the heat source of heater and the heat source of industrial Metal Cutting and welding, and environmental protection
It is pollution-free；When electrolysis water, hydrogen and oxygen generate on two electrodes respectively, because it can be collected respectively storage by it.
In electrolysis, steam is inevitably mixed into oxygen and hydrogen, existing method of purification is usually by oxygen
Gas cooling makes moisture condensation therein complete the separation with oxygen at liquid, but this mode also reduces oxygen simultaneously
Temperature exports the oxygen after purification to being not achieved when in air feed equipment preferably using temperature, and temperature is low to lead to equipment
Operational efficiency reduces.
Utility model content
Technical problem to be solved by the utility model is to provide a kind of Oxygen Purge Systems, it solves current
Oxygen reduces the problem of influencing subsequent use by temperature after condensation purification.
Technical problem to be solved in the utility model takes following technical scheme to realize:
A kind of Oxygen Purge System, including oxygen input tube, drainer, water collect tank, oxygen output tube and heat exchange tank, it is described
Oxygen input tube is connected to the drainer, and uniformly coiling has condenser coil, the water collect tank setting on the condensation tank wall
It is connected in the condensation pot bottom and with drainer, for the pot bottom that catchments equipped with discharge outlet, the discharge outlet is equipped with control
Valve, described oxygen output tube one end are connected to the water collect tank, and the other end passes through the heat exchange tank and stretches out from the heat exchange tank,
The oxygen output tube is located at the coiled coil on the heat exchange top tank structure of the part in the heat exchange tank and extends, the heat exchange tank
It is equipped with air inlet and exhaust outlet, the exhaust outlet is equipped with filter.
Make steam liquefaction and oxygen by the oxygen containing steam by condensing in drainer by using above-mentioned technical proposal
Gas is separated and is flowed into water collect tank and stores, and when oxygen circulates in oxygen output tube, is passed through into heat exchange tank and to be generated in factory
High hot exhaust gas, high hot exhaust gas is the oxygen heating in oxygen output tube, thus temperature when improving oxygen gas supply, to there is utilization
The use of follow-up equipment, technique improves its working efficiency, and filter can filter out the solid particle in tail gas, avoids its richness
Collection blocks tank body on heat exchange top tank structure.
It as preferred embodiment, is set on the condensation tank wall there are two condenser coil, two condenser coils disk respectively
It is wound on the drainer top and the bottom.
By using above-mentioned technical proposal, cooling medium is passed through into condenser coil, and make the flow direction of cooling medium with it is cold
The opposite formation adverse current of oxygen flow direction in solidifying tank, to improve condensation efficiency；If there are two condenser coils, make tank body top and the bottom temperature
It spends uniform, it is ensured that condensation efficiency.
As preferred embodiment, the oxygen input tube is connected to the upper end of the drainer.
As preferred embodiment, the control valve is diaphragm valve.
As preferred embodiment, the oxygen output tube is connected with the water collect tank top.
As preferred embodiment, insulating jacket is additionally provided on the drainer, the insulating jacket is covered in the condenser coil
On.
By using above-mentioned technical proposal, condenser coil is isolated with external environment, its temperature is avoided to increase too fast influence
Condensation effect.
The beneficial effects of the utility model are: by the oxygen containing steam by condensing in drainer, make steam liquefaction with
Oxygen separation and flowing into water collect tank stores, and when oxygen circulates in oxygen output tube, is passed through in factory and generates into heat exchange tank
High hot exhaust gas, high hot exhaust gas be oxygen output tube in oxygen heating, thus improve oxygen gas supply when temperature, thus favorably
With follow-up equipment, the use of technique, its working efficiency is improved, filter can filter out the solid particle in tail gas, avoid it
It is enriched on heat exchange top tank structure and blocks tank body；High-temperature residual heat in industrial tail gas is recycled, without providing additional heating
Equipment reheats oxygen, improves energy utilization rate, reduces energy consumption；Structure is simple, can promote the use of.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model.
In figure: oxygen input tube 1, drainer 2, water collect tank 3, oxygen output tube 4, heat exchange tank 5, condenser coil 6, discharge outlet
7, control valve 8, air inlet 9, exhaust outlet 10, filter 11, insulating jacket 12.
Specific embodiment
In order to which the technical means, creative features, achievable purpose and effectiveness to the utility model are easy to understand, tie below
Conjunction is specifically illustrating, and the utility model is further described.
As shown in Figure 1, a kind of Oxygen Purge System, including oxygen input tube 1, drainer 2, water collect tank 3, oxygen output tube
4 and heat exchange tank 5, the oxygen input tube 1 be connected to the drainer 2, on 2 outer wall of drainer uniformly coiling have condensate pans
Pipe 6, the water collect tank 3 are arranged in 2 bottom of drainer and are connected to drainer 2, and 3 bottom of water collect tank is equipped with discharge outlet
7, the discharge outlet 7 is equipped with control valve 8, and described 4 one end of oxygen output tube is connected to the water collect tank 3, and the other end passes through institute
It states heat exchange tank 5 and is stretched out from the heat exchange tank 5, the oxygen output tube 4 is located at the part in the heat exchange tank 5 in the heat exchange
Coiled coil extends on 5 inner wall of tank, and the heat exchange tank 5 is equipped with air inlet 9 and exhaust outlet 10, and the exhaust outlet 10 is equipped with
Filter 11.
Condenser coil 6 there are two setting on 2 outer wall of drainer, two condenser coils 6 are coiled in described cold respectively
Solidifying 2 top and the bottom of tank.
The oxygen input tube 1 is connected to the upper end of the drainer 2.
The control valve 8 is diaphragm valve.
The oxygen output tube 4 is connected with 3 top of water collect tank.
Insulating jacket 12 is additionally provided on the drainer 2,12 sets of the insulating jacket on the condenser coil 6.
Oxygen output tube 4 and 5 tank skin through part of heat exchange tank weld formation sealing.
Oxygen containing steam by condensing in drainer 2, is made steam liquefaction and oxygen separation cocurrent by the utility model
Enter and stored in water collect tank 3, when oxygen circulates in oxygen output tube 4, the high fever tail generated in factory is passed through into heat exchange tank 5
Gas, high hot exhaust gas is the oxygen heating in oxygen output tube 4, thus temperature when improving oxygen gas supply, to have using subsequent
The use of equipment, technique improves its working efficiency, and filter 11 can filter out the solid particle in tail gas, avoids its enrichment
Tank body is blocked on 5 inner wall of heat exchange tank；High-temperature residual heat in industrial tail gas is recycled, without providing additional heating equipment
Oxygen is reheated, energy utilization rate is improved, reduces energy consumption.
The basic principles and main features of the present invention and the advantages of the present invention have been shown and described above.Current row
The technical staff of industry it should be appreciated that the present utility model is not limited to the above embodiments, do not depart from the spirit of the present invention and
Under the premise of range, the utility model also has various changes and improvements, these changes and improvements both fall within the utility model and want
In the range of asking protection.The protection scope of the present invention is defined by the appended claims and their equivalents.
Claims (6)
1. a kind of Oxygen Purge System, it is characterised in that: including oxygen input tube, drainer, water collect tank, oxygen output tube and change
Hot tank, the oxygen input tube are connected to the drainer, and uniformly coiling has condenser coil, the collection on the condensation tank wall
Water pot, which is arranged, to be connected in the condensation pot bottom and with drainer, and the pot bottom that catchments is equipped with discharge outlet, in the discharge outlet
Equipped with control valve, described oxygen output tube one end is connected to the water collect tank, and the other end passes through the heat exchange tank and changes from described
Hot tank stretches out, and the oxygen output tube is located at the coiled coil on the heat exchange top tank structure of the part in the heat exchange tank and extends,
The heat exchange tank is equipped with air inlet and exhaust outlet, and the exhaust outlet is equipped with filter.
2. a kind of Oxygen Purge System according to claim 1, it is characterised in that: there are two being set on the condensation tank wall
Condenser coil, two condenser coils are coiled in the drainer top and the bottom respectively.
3. a kind of Oxygen Purge System according to claim 1, it is characterised in that: the oxygen input tube and the condensation
The upper end of tank is connected to.
4. a kind of Oxygen Purge System according to claim 1, it is characterised in that: the control valve is diaphragm valve.
5. a kind of Oxygen Purge System according to claim 1, it is characterised in that: the oxygen output tube catchments with described
Tank top is connected.
6. a kind of Oxygen Purge System according to claim 1, it is characterised in that: be additionally provided with heat insulation clamps on the drainer
Set, the insulating jacket cover on the condenser coil.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820841180.XU CN208512221U (en) | 2018-06-01 | 2018-06-01 | A kind of Oxygen Purge System |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820841180.XU CN208512221U (en) | 2018-06-01 | 2018-06-01 | A kind of Oxygen Purge System |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208512221U true CN208512221U (en) | 2019-02-19 |
Family
ID=65339724
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820841180.XU Active CN208512221U (en) | 2018-06-01 | 2018-06-01 | A kind of Oxygen Purge System |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208512221U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116395642A (en) * | 2023-03-24 | 2023-07-07 | 长沙莲湖乙炔有限公司 | Oxygen supply device |
-
2018
- 2018-06-01 CN CN201820841180.XU patent/CN208512221U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116395642A (en) * | 2023-03-24 | 2023-07-07 | 长沙莲湖乙炔有限公司 | Oxygen supply device |
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Legal Events
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|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20210726 Address after: 201109 building 17, 1288 Zhongchun Road, Minhang District, Shanghai Patentee after: Shanghai Xianpu Gas Technology Co.,Ltd. Address before: 201108 room 6224, building 6, No. 4299, Jindu Road, Minhang District, Shanghai Patentee before: SIMPURE TECHNOLOGY (SHANGHAI) Co.,Ltd. |