CN209564807U - A kind of gas separation system - Google Patents
A kind of gas separation system Download PDFInfo
- Publication number
- CN209564807U CN209564807U CN201821996499.6U CN201821996499U CN209564807U CN 209564807 U CN209564807 U CN 209564807U CN 201821996499 U CN201821996499 U CN 201821996499U CN 209564807 U CN209564807 U CN 209564807U
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- China
- Prior art keywords
- gas
- air
- pipe
- separate pot
- solenoid valve
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/151—Reduction of greenhouse gas [GHG] emissions, e.g. CO2
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- Gas Separation By Absorption (AREA)
Abstract
The utility model relates to a kind of gas separation systems comprising an air pump, the air pump are equipped with air intake, and the first solenoid valve is equipped between the air intake and the air pump；One gas separate pot, the gas separate pot is provided with carbon dioxide molecule sieve, first pipe and second pipe are connected separately between the air pump and the gas separate pot, the first pipe is equipped with second solenoid valve, the second pipe is equipped with third solenoid valve, one end of the gas separate pot is equipped with Waste gas outlet, and the gas separate pot is additionally provided with heating device, the tank body of the gas separate pot and the heating device heat transfer；One air accumulator, the air accumulator are connected with the second pipe, and the 4th solenoid valve is equipped between the air accumulator and the second pipe.The system of the utility model extracts the process of carbon dioxide, and not only simple and practical property is again strong, and raw material materials facilitate, and not can cause environmental pollution.
Description
Technical field
The utility model relates to gas purification fields, more particularly to a kind of gas separation system.
Background technique
The pH value of carbon acid solution is weakly acidic 5 or so, has sterilizing function, and the PH of pH value and the skin hair of people
It is worth close, more has affinity than common water；Concentration is obvious in 1000ppm carbonate spring convalescent effect, has stronger decontamination to clean
With the ability for repairing damaged skin hair, the ability for having expansion and softening blood vessel, promoting metabolism, improve microcirculation；It is existing
The method that carbonic acid is prepared in technology is usually to be passed through carbon dioxide to water and pressurizeed and cooled down again, increase carbon dioxide in water
In meltage and reduce the activity of carbonic acid, wherein preparing the most important raw material of carbonic acid is exactly carbon dioxide, and generally produce two
The common means of carbonoxide are lime burning rock, to produce cement raw material and carbon dioxide, but its prepare carbon dioxide at
This is excessively high, and the process produced can generate pollution to ambient enviroment.
Summary of the invention
The purpose of this utility model is to provide a kind of gas separation systems, to solve mentioned above in the background art ask
Topic.
To achieve the above objectives, the present invention adopts the following technical solutions: a kind of gas separation system comprising a gas
Pump, the air pump are equipped with air intake, and the first solenoid valve is equipped between the air intake and the air pump；One gas separate pot, institute
It states gas separate pot and is provided with carbon dioxide molecule sieve, the first pipe is connected separately between the air pump and the gas separate pot
Road and second pipe, the first pipe are equipped with second solenoid valve, and the second pipe is equipped with third solenoid valve, the gas point
It is equipped with Waste gas outlet from tank, the gas separate pot is additionally provided with heating device, and the tank body of the gas separate pot adds with described
Thermal heat transfer；One air accumulator, the air accumulator are connected with the second pipe, the air accumulator and the second pipe
Between be equipped with the 4th solenoid valve.
Further, the Waste gas outlet is circumscribed with the 5th solenoid valve and air exhauster, the air exhauster and the gas
Knockout drum is connected, and the 5th solenoid valve is between the air exhauster and the gas separate pot.
Further, the heating device is heating sheet, and the heating device is laid on the tank body of the gas separate pot
Outer surface.
Further, the air pump is reciprocating air pump.
Further, the air accumulator is equipped with carbon dioxide exhaust outlet.
Further, the air accumulator is equipped with the second baroceptor.
Further, the gas separate pot is equipped with the first baroceptor.
Further, the air intake is connected with the second pipe.
The utility model has the following beneficial effects: the system of the utility model is sieved in absorption air by carbon dioxide molecule
Carbon dioxide utilizes heating carbon dioxide molecule sieve separation carbon dioxide, entire separation process not only simple and practical property but also strong, raw material
Materials are convenient, and not can cause environmental pollution.
Detailed description of the invention
The utility model is described in further detail for attached drawing, but the embodiment in attached drawing is not constituted to any of the utility model
Limitation.
Fig. 1 is the structural schematic diagram that an embodiment of the present invention provides.
Specific embodiment
As shown in fig. 1, a kind of gas separation system that an embodiment of the present invention provides comprising air pump 1, gas
Knockout drum 2 and air accumulator 3.First pipe 4 and second pipe are connected separately between the air pump 1 and the gas separate pot 2
5, the air pump 1 is reciprocating air pump, and the air pump 1 is equipped with air intake 11, is equipped between the air intake 11 and the air pump 1
First solenoid valve 12, and the air intake 11 is connected with the first pipe 4.The gas separate pot 2 is provided with titanium dioxide
Carbon molecular sieve by easily disengaging carbon dioxide strong to carbon dioxide adsorption ability, heated using carbon dioxide molecule sieve and can follow
The characteristics of ring uses fills full carbon dioxide molecule sieve in the gas separate pot 2, is being passed through the gas separate pot 2
Carbon dioxide can be absorbed when air.Since carbon dioxide molecule sieve is common chemical materials, therefore the utility model is not
Its ingredient and principle are repeated.The first pipe 4 is equipped with second solenoid valve 41, and the second pipe 5 is equipped with third electricity
Magnet valve 51.
As shown in fig. 1, the gas separate pot 2 is equipped with Waste gas outlet 21, and the Waste gas outlet 21 is circumscribed with the
Five solenoid valves 211 and air exhauster 212, the air exhauster 212 are connected with the gas separate pot 2, the 5th solenoid valve 211
Between the air exhauster 212 and the gas separate pot 2.The gas separate pot 2 is additionally provided with heating device 22, described to add
Thermal 22 is heating sheet, and the heating device 22 is laid on the outer surface of the tank body of the gas separate pot 2, the heating dress
It sets 22 and conducts heat to the carbon dioxide molecule sieve by heating the outer surface of the tank body of the gas separate pot 2.
The gas separate pot 2 is equipped with the first baroceptor 23, and first baroceptor 23 is for detecting the gas separation
Air pressure in tank 2 can stop when detecting the air pressure in the gas separate pot 2 close to upper limit value toward the gas point
From gas transmission in tank 2, avoid air pressure in the gas separate pot 2 excessive.The air accumulator 3 is connected with the second pipe 5, institute
It states and is equipped with the 4th solenoid valve 31 between air accumulator 3 and the second pipe 5.The air accumulator 3 is equipped with carbon dioxide exhaust outlet 32,
The carbon dioxide exhaust outlet 32 is used to export the carbon dioxide after separation.The air accumulator 3 is equipped with the second baroceptor 33,
Second baroceptor 33 is used to detect air pressure in the air accumulator 3, when detecting that the air pressure in the air accumulator 3 connects
When nearly upper limit value, the gas transmission in the air accumulator 3 can be stopped, avoiding air pressure is excessive from exploding.
As shown in fig. 1, in the actual operation process, the switch for first opening first solenoid valve 12, starts the gas
Pump 1 is drawn air into the air pump 1, closes first solenoid valve 12, is opened the switch of third solenoid valve 51, is utilized air pump
Air is pressed into the gas separate pot 2 by 1, is turned off the switch of the third solenoid valve 51 and the switch of the air pump 1, is allowed institute
The carbon dioxide in carbon dioxide molecule sieve absorption air is stated, waits for a period of time and the carbon dioxide molecule is allowed to sieve adsorption saturation
Afterwards, the 5th solenoid valve 211 is opened, takes remaining gas in the gas separate pot 2, Zhi Houguan away using air exhauster 212
The 5th solenoid valve 211 is closed, the switch of the heating device 22 is opened, the heating device 22 conducts heat to described two
Carbon molecular sieve is aoxidized, the carbon dioxide of the carbon dioxide molecule sieve release absorption then opens 41 He of second solenoid valve
4th solenoid valve 31 starts the air pump 1, will be described in the carbon dioxide indentation in the gas separate pot 2 using air pump 1
In air accumulator 3, until the air accumulator 3 turns off the second solenoid valve 41 and the 4th solenoid valve 31 after filling gas,
The separation to Carbon Dioxide in Air can be completed.
Each technical characteristic of embodiment described above can be combined arbitrarily, for simplicity of description, not to above-mentioned reality
It applies all possible combination of each technical characteristic in example to be all described, as long as however, the combination of these technical characteristics is not deposited
In contradiction, all should be considered as described in this specification.
Above-described embodiments merely represent several embodiments of the utility model, the description thereof is more specific and detailed,
But it cannot be understood as the limitations to utility model patent range.It should be pointed out that for the common skill of this field
For art personnel, without departing from the concept of the premise utility, various modifications and improvements can be made, these are belonged to
The protection scope of the utility model.Therefore, the scope of protection shall be subject to the appended claims for the utility model patent.
Claims (8)
1. a kind of gas separation system characterized by comprising
One air pump, the air pump are equipped with air intake, and the first solenoid valve is equipped between the air intake and the air pump；
One gas separate pot, the gas separate pot are provided with carbon dioxide molecule sieve, the air pump and the gas separate pot
Between be connected separately with first pipe and second pipe, the first pipe is equipped with second solenoid valve, and the second pipe is equipped with
Third solenoid valve, the gas separate pot are equipped with Waste gas outlet, and the gas separate pot is additionally provided with heating device, the gas
The tank body of knockout drum and the heating device heat transfer；
One air accumulator, the air accumulator are connected with the second pipe, are equipped between the air accumulator and the second pipe
4th solenoid valve.
2. gas separation system according to claim 1, it is characterised in that: the Waste gas outlet is circumscribed with the 5th electromagnetism
Valve and air exhauster, the air exhauster are connected with the gas separate pot, and the 5th solenoid valve is located at the air exhauster and institute
It states between gas separate pot.
3. gas separation system according to claim 2, it is characterised in that: the heating device is heating sheet, described to add
Thermal is laid on the outer surface of the tank body of the gas separate pot.
4. gas separation system according to claim 1, it is characterised in that: the air pump is reciprocating air pump.
5. gas separation system according to claim 1, it is characterised in that: the air accumulator is vented equipped with carbon dioxide
Mouthful.
6. gas separation system according to claim 5, it is characterised in that: the air accumulator is equipped with the second air pressure sensing
Device.
7. gas separation system according to claim 1, it is characterised in that: the gas separate pot is equipped with the first air pressure transmission
Sensor.
8. gas separation system according to claim 1, it is characterised in that: the air intake is connected with the first pipe
It is logical.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821996499.6U CN209564807U (en) | 2018-11-29 | 2018-11-29 | A kind of gas separation system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821996499.6U CN209564807U (en) | 2018-11-29 | 2018-11-29 | A kind of gas separation system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209564807U true CN209564807U (en) | 2019-11-01 |
Family
ID=68321657
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821996499.6U Active CN209564807U (en) | 2018-11-29 | 2018-11-29 | A kind of gas separation system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209564807U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114405237A (en) * | 2022-03-02 | 2022-04-29 | 深圳市安驰环保科技有限公司 | Combined absorption carbon dioxide capture and compression treatment system and process |
-
2018
- 2018-11-29 CN CN201821996499.6U patent/CN209564807U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114405237A (en) * | 2022-03-02 | 2022-04-29 | 深圳市安驰环保科技有限公司 | Combined absorption carbon dioxide capture and compression treatment system and process |
| CN114405237B (en) * | 2022-03-02 | 2022-12-23 | 深圳市安驰环保科技有限公司 | Combined absorption carbon dioxide capture and compression treatment system and process |
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