CN207566889U - A kind of preparation facilities of food-grade carbon-dioxide - Google Patents
A kind of preparation facilities of food-grade carbon-dioxide Download PDFInfo
- Publication number
- CN207566889U CN207566889U CN201721666100.3U CN201721666100U CN207566889U CN 207566889 U CN207566889 U CN 207566889U CN 201721666100 U CN201721666100 U CN 201721666100U CN 207566889 U CN207566889 U CN 207566889U
- Authority
- CN
- China
- Prior art keywords
- carbon dioxide
- preparation facilities
- carbon
- food
- dioxide
- 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.)
- Expired - Fee Related
Links
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 title claims description 123
- 229910002092 carbon dioxide Inorganic materials 0.000 title claims description 61
- 239000001569 carbon dioxide Substances 0.000 title claims description 61
- 238000002360 preparation method Methods 0.000 title claims description 25
- 239000000463 material Substances 0.000 claims description 11
- 238000000746 purification Methods 0.000 claims description 11
- 238000005201 scrubbing Methods 0.000 claims description 11
- 238000001179 sorption measurement Methods 0.000 claims description 8
- 238000001514 detection method Methods 0.000 claims description 7
- 238000001035 drying Methods 0.000 claims description 7
- 239000007788 liquid Substances 0.000 claims description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 5
- 229910052799 carbon Inorganic materials 0.000 claims description 5
- 241000790917 Dioxys <bee> Species 0.000 claims description 3
- 230000008859 change Effects 0.000 claims description 3
- 238000009434 installation Methods 0.000 claims description 3
- 239000003463 adsorbent Substances 0.000 claims description 2
- 239000000945 filler Substances 0.000 claims description 2
- 238000007689 inspection Methods 0.000 claims description 2
- 239000002808 molecular sieve Substances 0.000 claims description 2
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 claims description 2
- 229960004424 carbon dioxide Drugs 0.000 description 39
- 239000007789 gas Substances 0.000 description 21
- 238000005516 engineering process Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- WQOXQRCZOLPYPM-UHFFFAOYSA-N dimethyl disulfide Chemical compound CSSC WQOXQRCZOLPYPM-UHFFFAOYSA-N 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910002090 carbon oxide Inorganic materials 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 235000019441 ethanol Nutrition 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000003507 refrigerant Substances 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000004073 vulcanization Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
Landscapes
- Carbon And Carbon Compounds (AREA)
Abstract
The utility model discloses a kind of preparation facilities of food-grade carbon-dioxide, including carbon dioxide preparation facilities, carbon dioxide detection device, carbon dioxide purification device, carbon dioxide preparation facilities includes reaction cylinder, sealed plasthetic, react cylinder cap, material reaction plate, agitating device, liquid level sensor, gas outlet, gas open-close valve, purification devices include scrubbing tower, compressor, adsorption tower, drying tower, condenser, distiller, collecting tank, carbon dioxide detection device includes carbon dioxide on-line measuring device, carbon dioxide sample tap, the sealed plasthetic is located at the reaction cylinder and covers face, the agitating device is installed on the material reaction plate above and below, the liquid level sensor is positioned on the inside of the reaction cylinder, the gas outlet connects carbon dioxide detection device and carbon dioxide purification device respectively.The utility model can be used for industrialized production, and carbon dioxide demand is industrialized for meeting.
Description
Technical field
The utility model is related to gas Preparation equipment, specially a kind of preparation facilities of food-grade carbon-dioxide.
Background technology
Carbon dioxide has higher civilian and industrial value, has a wide range of applications in multiple fields, be it is a kind of very
Valuable resource.Not only be widely used in oil exploitation, metallurgy, welding, low temperature refrigerant, machine-building, rain making, fire-fighting,
Chemical industry, papermaking, agricultural, grocery trade, health care etc., apply also for supercritical solvent, bioengineering, laser count,
The hard-core technologies such as nuclear industry field.In this all application, food-grade carbon-dioxide is most widely used, used in hard-core technology
Carbon dioxide is also as obtained from food-grade carbon-dioxide by purifying again.Therefore, food-grade dioxy is obtained on a large scale
It is very necessary to change carbon.At present, there are more carbon dioxide preparation method and purification process, but process is all excessively cumbersome, and
The waste gas recovery purifying of carbon dioxide is all directed to, efficiency is low, it is impossible to meet the food-grade carbon-dioxide demand to grow stronger day by day.
Utility model content
The technical issues of the utility model solves is to provide a kind of preparation facilities of food-grade carbon-dioxide, to solve
The shortcomings that in above-mentioned background technology.
The technical issues of the utility model solves is realized using following technical scheme：A kind of food-grade carbon-dioxide
Preparation facilities, including carbon dioxide preparation facilities, carbon dioxide detection device, carbon dioxide purification device, prepared by carbon dioxide
Device is opened including reaction cylinder, sealed plasthetic, reaction cylinder cap, material reaction plate, agitating device, liquid level sensor, gas outlet, gas
Valve is closed, purification devices include scrubbing tower, compressor, adsorption tower, drying tower, condenser, distiller, collecting tank, carbon dioxide inspection
It surveys device and includes carbon dioxide on-line measuring device, carbon dioxide sample tap, the sealed plasthetic is located at the reaction cylinder and covers
Face, the agitating device are installed on the material reaction plate above and below, and the liquid level sensor is positioned over the reaction cylinder
Inside, the gas outlet connect carbon dioxide detection device and carbon dioxide purification device respectively.
In the utility model, the sealed plasthetic and the reaction cylinder cap can be moved up and down along the reaction inside wall of cylinder.
In the utility model, the material reaction plate and the agitating device can move up and down.
In the utility model, there are two the gas open-close valves for the gas outlet installation.
In the utility model, a gas open-close valve connects the scrubbing tower, and the scrubbing tower uses horizontal filler.
In the utility model, the erection sequence of carbon dioxide purification device is the scrubbing tower, the compressor, the suction
Attached tower, the drying tower, the condenser, the distiller, the collecting tank.
In the utility model, the adsorption tower is respectively using high efficiency active carbon and efficient molecular sieve as adsorbent.
In the utility model, the condenser installs an exhaust outlet, and condenser gas outlet position connects the dioxy
Change carbon on-line measuring device and a carbon dioxide sample tap.
In the utility model, the gas outlet of the condenser connects the distiller and the collecting tank respectively.
In the utility model, the condenser installs a heat exchanger, and heat exchanger connects the reaction cylinder.
The beneficial effects of the utility model：The preparation efficiency of food-grade carbon-dioxide is improved, improves the preparation of carbon dioxide
Purity industrializes carbon dioxide demand for meeting.
Description of the drawings
Fig. 1 is the external structure schematic diagram of the utility model preparation facilities；
Fig. 2 is the utility model external structure schematic diagram.
In figure：Reaction cylinder -1；Sealed plasthetic -2；React cylinder cap -3；Material reaction plate -4；Agitating device -5；Level sensing
Device -6；Gas outlet -7；Gas open-close valve -8, scrubbing tower -9；Compressor -10；Adsorption tower -11；Drying tower -12；Condenser -13；
Distiller -14；Collecting tank -15, carbon dioxide on-line measuring device -16；Carbon dioxide sample tap -17；Heat exchanger -18；Branch
Strut -19；Hand-operated wheel -20；Stainless acid-resisting steel wire -21.
Specific embodiment
In order to make technological means of the utility model；Creation characteristic；Reached purpose is easy to understand with effect, under
Face combines and is specifically illustrating, and the utility model is expanded on further.
Embodiment：As depicted in figs. 1 and 2, a kind of preparation facilities of food-grade carbon-dioxide is prepared including carbon dioxide and is filled
It puts, carbon dioxide detection device, carbon dioxide purification device, carbon dioxide preparation facilities includes reaction cylinder 1, sealed plasthetic 2, anti-
Cylinder cap 3, material reaction plate 4, agitating device 5, liquid level sensor 6, gas outlet 7, gas open-close valve 8 are answered, purification devices include washing
Wash tower 9, compressor 10, adsorption tower 11, drying tower 12, condenser 13, distiller 14, collecting tank 15, carbon dioxide detection device
Including carbon dioxide on-line measuring device 16, carbon dioxide sample tap 17, the sealed plasthetic 2 is located on the reaction cylinder cap 3
Face, the agitating device 5 are installed on the material reaction plate 4 above and below, and the liquid level sensor 6 is positioned over the reaction
1 inside of cylinder, the gas outlet 7 connects carbon dioxide detection device and carbon dioxide purification device respectively.
Application method：When the utility model is used, reaction solution is squeezed into the reaction cylinder 1, while reaction mass is put
It puts on the material reaction plate 4, shakes the hand-operated wheel 20 so that the material reaction plate 4 and the agitating device 5 decline
Into reaction solution, and the switch of the agitating device 5 is opened, reacted.At this moment the hand-operated wheel 20 is shaken, by the sealing
Plastic cement and the reaction cylinder cap 3 drop to the position that the liquid level sensor 6 is shown, in the process, the gas outlet 7 is beaten
It opens, discharges exhaust gas.The gas outlet 7 is then turned off, opens the gas open-close valve 8 for leading to the scrubbing tower 9, gas is in institute
It states in scrubbing tower 9 and removes water-solubility impurity, subsequently into removing ethyl alcohol, dimethyl disulfide, vulcanization hydrocarbon etc. one in the adsorption tower 11
A little organic substances enter back into the drying tower 12 and remove moisture, then enter the condenser 14 by compressor 10 so that big portion
Divide co 2 liquefaction, and extra exhaust gas is discharged, the purity of carbon dioxide is detected at this time, if its purity reaches food-grade two
The purity of carbonoxide, then be directly entered the collecting tank 15 collect it is spare, it is liquefied in the condenser 14 if not reaching requirement
Carbon dioxide, which enters in the distiller 15, to be distilled, and the gas after distillation is squeezed into the condenser 14 and is purified again, until
Reach required purity, you can directly collect.
The heat exchanger 18 used in the utility model is to described by the heat transfer that the condenser 14 is released
It is used in reaction cylinder 1, escapable cost.
The basic principle of the utility model and main feature and the advantages of the utility model, one's own profession has been shown and described above
The technical staff of industry is it should be appreciated that the present utility model is not limited to the above embodiments, described in above embodiments and description
Only illustrate the principle of the utility model, on the premise of not departing from the spirit and scope of the utility model, the utility model is also
Various changes and modifications are had, these various changes and improvements fall within the scope of the claimed invention, the utility model
Claimed range is defined by the appending claims and its equivalent thereof.
Claims (10)
1. a kind of preparation facilities of food-grade carbon-dioxide, including carbon dioxide preparation facilities, carbon dioxide detection device, dioxy
Change carbon sublimated device, carbon dioxide preparation facilities includes reaction cylinder (1), sealed plasthetic (2), reaction cylinder cap (3), material reaction plate
(4), agitating device (5), liquid level sensor (6), gas outlet (7), gas open-close valve (8), purification devices include scrubbing tower (9),
Compressor (10), adsorption tower (11), drying tower (12), condenser (13), distiller (14), collecting tank (15), carbon dioxide inspection
It surveys device and includes carbon dioxide on-line measuring device (16), carbon dioxide sample tap (17), it is characterized in that：The sealed plasthetic
(2) positioned at the reaction cylinder cap (3) above, the agitating device (5) is installed on the material reaction plate (4) above and below,
The liquid level sensor (6) is positioned on the inside of the reaction cylinder (1), and the gas outlet (7) connects carbon dioxide detection dress respectively
It puts and carbon dioxide purification device.
2. a kind of preparation facilities of food-grade carbon-dioxide according to claim 1, it is characterized in that：The sealed plasthetic
(2) it can be moved up and down with the reaction cylinder cap (3) along the reaction cylinder (1) inner wall.
3. a kind of preparation facilities of food-grade carbon-dioxide according to claim 1, it is characterized in that：The material reaction plate
(4) it can be moved up and down with the agitating device (5).
4. a kind of preparation facilities of food-grade carbon-dioxide according to claim 1, it is characterized in that：The gas outlet (7)
There are two the gas open-close valves (8) for installation.
5. a kind of preparation facilities of food-grade carbon-dioxide according to claim 1, it is characterized in that：One gas is opened
It closes valve (8) and connects the scrubbing tower (9), the scrubbing tower (9) uses horizontal filler.
6. a kind of preparation facilities of food-grade carbon-dioxide according to claim 1, it is characterized in that：Carbon dioxide purification fills
The erection sequence put is the scrubbing tower (9), the compressor (10), the adsorption tower (11), the drying tower (12), described
Condenser (13), the distiller (14), the collecting tank (15).
7. a kind of preparation facilities of food-grade carbon-dioxide according to claim 1, it is characterized in that：The adsorption tower (11)
Respectively using high efficiency active carbon and efficient molecular sieve as adsorbent.
8. a kind of preparation facilities of food-grade carbon-dioxide according to claim 1, it is characterized in that：The condenser (13)
One exhaust outlet is installed, condenser (13) the gas outlet position connects the carbon dioxide on-line measuring device (16) and described in one
Carbon dioxide sample tap (17).
9. a kind of preparation facilities of food-grade carbon-dioxide according to claim 1, it is characterized in that：The condenser (13)
Gas outlet connect the distiller (14) and the collecting tank (15) respectively.
10. a kind of preparation facilities of food-grade carbon-dioxide according to claim 1, it is characterized in that：The condenser
(13) one heat exchanger of installation (18), heat exchanger (18) connect the reaction cylinder (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721666100.3U CN207566889U (en) | 2017-12-05 | 2017-12-05 | A kind of preparation facilities of food-grade carbon-dioxide |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721666100.3U CN207566889U (en) | 2017-12-05 | 2017-12-05 | A kind of preparation facilities of food-grade carbon-dioxide |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207566889U true CN207566889U (en) | 2018-07-03 |
Family
ID=62689787
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721666100.3U Expired - Fee Related CN207566889U (en) | 2017-12-05 | 2017-12-05 | A kind of preparation facilities of food-grade carbon-dioxide |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207566889U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109328714A (en) * | 2018-11-20 | 2019-02-15 | 黄仙才 | A kind of agricultural greenhouse gas generating unit |
| CN114561292A (en) * | 2022-04-27 | 2022-05-31 | 天津长和生物技术有限公司 | Cell culture case with from drum-type carbon dioxide preparation facilities |
-
2017
- 2017-12-05 CN CN201721666100.3U patent/CN207566889U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109328714A (en) * | 2018-11-20 | 2019-02-15 | 黄仙才 | A kind of agricultural greenhouse gas generating unit |
| CN114561292A (en) * | 2022-04-27 | 2022-05-31 | 天津长和生物技术有限公司 | Cell culture case with from drum-type carbon dioxide preparation facilities |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN207566889U (en) | A kind of preparation facilities of food-grade carbon-dioxide | |
| CN108085249A (en) | A kind of preparation of marsh-gas of house refuse producing methane preparation system | |
| CN108102901A (en) | A kind of house refuse producing methane preparation system and preparation of marsh-gas | |
| CN103423968B (en) | A kind of neon helium separation and Extraction system and technique | |
| CN100528293C (en) | Multi-component organic-gas pressure-changing adsorption and realtime detection-control experiment device | |
| CN104556035A (en) | Preparation method and preparation device of food-grade high-purity liquid carbon dioxide | |
| CN2655143Y (en) | Vacuum drying box | |
| CN104353259A (en) | Combined rectifying column and application thereof | |
| CN203454605U (en) | Neon and helium separation and extraction system | |
| CN103223287B (en) | Purifying and recovering device of exhaust gas comprising toluene, and exhaust gas purifying and recovering method | |
| CN107854862B (en) | Experimental device integrating extraction and steam distillation separation | |
| CN113834702B (en) | Use method of negative pressure gas production box for odor evaluation | |
| CN205287992U (en) | Gas and liquid separator | |
| CN209771374U (en) | Distillation tower for purifying musk | |
| CN203329583U (en) | Chlorine hydride absorption device in polycrystalline silicon tail gas recovery system | |
| CN202575992U (en) | Carbon dioxide recovery device | |
| CN102775267B (en) | Method and system for recycling cyclohexane solvent in SBS (styrene-butadiene-styrene) production | |
| CN207478011U (en) | A kind of medicine produces dedicated vacuum decompressioning and concentrating tank | |
| CN206168395U (en) | Desorption bottle organic reagent recovery unit | |
| CN207562641U (en) | A kind of zero gas consumption compression heat regenerative drying machine | |
| CN207694274U (en) | A kind of separated body type low temp inspissator | |
| CN205386349U (en) | Jar is retrieved to bromoethane | |
| CN207294188U (en) | Rectification and purification device prepared by high-purity carbon dioxide | |
| CN211585272U (en) | A kind of dimethylacetamide intermittent recovery device | |
| CN219783847U (en) | Glacial acetic acid waste liquid recovery device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180703 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |