CN101481641A - Water-bath type carbon dioxide carburettors - Google Patents
Water-bath type carbon dioxide carburettors Download PDFInfo
- Publication number
- CN101481641A CN101481641A CNA2009100291580A CN200910029158A CN101481641A CN 101481641 A CN101481641 A CN 101481641A CN A2009100291580 A CNA2009100291580 A CN A2009100291580A CN 200910029158 A CN200910029158 A CN 200910029158A CN 101481641 A CN101481641 A CN 101481641A
- Authority
- CN
- China
- Prior art keywords
- tank body
- carbon dioxide
- water
- pipe
- carbonic acid
- 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.)
- Granted
Links
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 title claims abstract description 59
- 229910002092 carbon dioxide Inorganic materials 0.000 title claims abstract description 19
- 239000001569 carbon dioxide Substances 0.000 title claims abstract description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 25
- 238000010438 heat treatment Methods 0.000 claims abstract description 4
- 235000011089 carbon dioxide Nutrition 0.000 claims description 21
- 238000003466 welding Methods 0.000 claims description 4
- JOHZPMXAZQZXHR-UHFFFAOYSA-N pipemidic acid Chemical compound N1=C2N(CC)C=C(C(O)=O)C(=O)C2=CN=C1N1CCNCC1 JOHZPMXAZQZXHR-UHFFFAOYSA-N 0.000 claims description 2
- 239000007788 liquid Substances 0.000 abstract description 10
- 235000013405 beer Nutrition 0.000 abstract description 9
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 230000000694 effects Effects 0.000 abstract description 2
- 238000007789 sealing Methods 0.000 abstract 1
- 239000006200 vaporizer Substances 0.000 abstract 1
- 238000001816 cooling Methods 0.000 description 6
- 238000005516 engineering process Methods 0.000 description 2
- 238000002309 gasification Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000013526 supercooled liquid Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
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- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
A water bath type carbon dioxide vaporizer relates to the technical field of the structure a heat exchange tank. A carbon dioxide air outlet pipe and a carbon dioxide liquid inlet pipe are respectively connected at the upper and the lower ends of the tank body, a main pipeline is vertically arranged in the tank body, the upper end of the main pipeline is a closed end, and the lower end thereof id connected with the carbon dioxide liquid inlet pipe; coil pipes are evenly arranged along the length direction of the main pipeline, one end of the coil pipe is communicated with the main pipeline, and the other end thereof is connected with the carbon dioxide air outlet pipe; the tank body is respectively provided with a water inlet and a water outlet which are communicated with an inner cavity of the tank body, wherein, the water outlet is arranged higher than the water inlet; the tank body is provided with a steam inlet and a condensed water outlet, and a steam-heating pipe is connected between the steam inlet and the condensed water outlet in the inner cavity of the tank body in a sealing way. The invention has reasonable structure, even temperature, high heat exchange benefit and obvious energy-saving effect, and is in accordance with the production requirements of beer manufacturer; the prepared beer has pure taste and sufficient air content.
Description
Technical field
The present invention relates to technical field of heat exchange, particularly a kind of structure technology of heat exchange tank.
Background technology
In beer manufacturing field, have unique mouthfeel in order to make beer, need be vaporized into an amount of pressurising of gaseous state to liquid carbon dioxide and advance in beer liquid and each procedure of production beer to use.And only provide liquid carbon dioxide in existing carbonic acid gas supplier, in order to achieve the above object, just must earlier liquid carbon dioxide be made gaseous state.Existing gasification process is directly to vaporize with steam, and as cooling off with cooling tower, minimum also can only being cooled to also consumed a large amount of energy about 30 ℃, when carbonic acid gas is used, needs to consume a large amount of steam (energy) with the vaporization liquid carbon dioxide.Generally speaking, need to use other devices make water temperature drop to the temperature that can cool off power-equipment, during need to consume certain energy, especially consume more in summer.
Summary of the invention
The object of the invention is can save steam usage quantity, energy-conservation water-bath type carbon dioxide carburettors for beer producers provides a kind of.
The present invention includes tank body, connect carbonic acid gas escape pipe and carbonic acid gas liquid-inlet pipe respectively at the tank body upper and lower end, main pipe line vertically is set in tank body, the upper end of described main pipe line is a blind end, the lower end is connected with the carbonic acid gas liquid-inlet pipe, along the uniform coil pipe of main pipe line length direction, an end of each coil pipe is communicated with main pipe line, and the other end is communicated with the carbonic acid gas escape pipe; Water-in and the water outlet that is communicated with tank inner chamber is set respectively on tank body, and described water outlet is higher than water-in and arranges; Steam inlet and condensation-water drain are set on tank body, and steam heating tube is tightly connected between the steam inlet of tank inner chamber and condensation-water drain.
Principle of work of the present invention is: a large amount of cooling circulating waters that brew-house's power-equipment is produced enter in the tank body by water-in, carry out heat exchange with the supercooled liquid carbonic acid gas in the coil pipe, make that liquid carbon dioxide is vaporized, water in cooling, reach gasification condition.The present invention is owing to adopted coil pipe, heat exchanger time, the contact area of supercooled liquid carbonic acid gas and cooling circulating water are increased, the design of this sufficient heat exchange, can reduce tank body internal cooling circulating water temperature condition greatly, temperature is controlled at 4～10 ℃ liquid carbon dioxide is fully vaporized in actual motion, this service life of equipment is long, obviously energy-saving and cost-reducing, can effectively improve the economic benefit of applying unit.
The present invention is rational in infrastructure, and temperature is even, the heat exchange high efficiency, and energy-saving effect is obvious, meets the beer producers production requirement, and the beer taste of making is pure, the air content abundance.
Because winter, gas consumption was little, natural temperature is on the low side, and can suitably replenish steam and vaporize winter, and described vapour pipe is arranged in the inner bottom part of tank body, connects recycle pump between the upper and lower end of tank body.Can make a jar intravital water temperature reach consistent by recycle pump, be beneficial to the Rapid Thermal exchange.
In addition, the present invention also connects pneumatic ball valve in carbonic acid gas liquid-inlet pipe outer end by three formula welding ball valves, can control the flow of carbonic acid gas liquid state automatically.
The tank body top is provided with safety valve.Purpose is to prevent that the valve on the water lines from not opening.
Description of drawings
Fig. 1 is a kind of structural representation of the present invention.
Fig. 2 bows to view for Fig. 1's.
Fig. 3 is an A-A sectional drawing among Fig. 1.
Fig. 4 is a B-B sectional drawing among Fig. 1.
Embodiment
Shown in Fig. 1,2,3,4, connect carbonic acid gas escape pipe 2 and carbonic acid gas liquid-inlet pipe 3 respectively at tank body 1 upper and lower end of water-bath type carbon dioxide carburettors, connect pneumatic ball valves 5 in carbonic acid gas liquid-inlet pipe outer end by three formula welding ball valves 4.Outer end at carbonic acid gas escape pipe 2 connects electro connecting pressure gauge 7 by three formula welding ball valves 6, reaches the purpose of automatic control pneumatic ball valve.
Water-in 10 and the water outlet 11 that is communicated with tank body 1 inner chamber is set respectively on tank body 1, and water outlet 11 is higher than water-in 10 and arranges.
Inner bottom part at tank body 1 is provided with steam inlet 12 and condensation-water drain 13, and steam heating tube 14 is tightly connected between the steam inlet 12 of tank body 1 inner chamber and condensation-water drain 13.Between the upper and lower end of tank body 1, connect recycle pump 15.
At tank body 1 top safety valve 16 is set.
Claims (4)
1, water-bath type carbon dioxide carburettors, it is characterized in that comprising tank body, connect carbonic acid gas escape pipe and carbonic acid gas liquid-inlet pipe respectively at the tank body upper and lower end, main pipe line vertically is set in tank body, the upper end of described main pipe line is a blind end, and the lower end is connected with the carbonic acid gas liquid-inlet pipe, along the uniform coil pipe of main pipe line length direction, one end of each coil pipe is communicated with main pipe line, and the other end is communicated with the carbonic acid gas escape pipe; Water-in and the water outlet that is communicated with tank inner chamber is set respectively on tank body, and described water outlet is higher than water-in and arranges; Steam inlet and condensation-water drain are set on tank body, and steam heating tube is tightly connected between the steam inlet of tank inner chamber and condensation-water drain.
2,, it is characterized in that described vapour pipe is arranged in the inner bottom part of tank body, connects recycle pump between the upper and lower end of tank body according to the described water-bath type carbon dioxide carburettors of claim 1.
3,, it is characterized in that connecting pneumatic ball valve by three formula welding ball valves in the outer end of carbonic acid gas liquid-inlet pipe according to the described water-bath type carbon dioxide carburettors of claim 1.
4,, it is characterized in that the tank body top is provided with safety valve according to the described water-bath type carbon dioxide carburettors of claim 1.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009100291580A CN101481641B (en) | 2009-01-06 | 2009-01-06 | Water-bath type carbon dioxide carburettors |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009100291580A CN101481641B (en) | 2009-01-06 | 2009-01-06 | Water-bath type carbon dioxide carburettors |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101481641A true CN101481641A (en) | 2009-07-15 |
| CN101481641B CN101481641B (en) | 2011-12-07 |
Family
ID=40878931
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009100291580A Expired - Fee Related CN101481641B (en) | 2009-01-06 | 2009-01-06 | Water-bath type carbon dioxide carburettors |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN101481641B (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102434777A (en) * | 2011-10-14 | 2012-05-02 | 中国空分设备有限公司 | Water bath vaporizer provided with vapor-water mixer |
| CN102829326A (en) * | 2012-09-12 | 2012-12-19 | 镇海石化建安工程有限公司 | Steam-heated water-bath type vaporizer |
| CN104266421A (en) * | 2014-09-26 | 2015-01-07 | 烟台冰轮股份有限公司 | Working medium discharge device and discharge control method used for CO2 refrigeration system |
| CN106481979A (en) * | 2016-12-20 | 2017-03-08 | 上海华林工业气体有限公司 | A kind of steam heating water bath type carburetion system with feedback control |
| CN114893717A (en) * | 2022-04-28 | 2022-08-12 | 宁波东君工程技术有限公司 | By using CO 2 Liquefaction energy-saving equipment for heat exchange from pipeline to evaporation cooling equipment and method thereof |
| CN115978446A (en) * | 2022-11-24 | 2023-04-18 | 新疆敦华绿碳技术股份有限公司 | Gas phase conversion equipment |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2310062Y (en) * | 1996-11-04 | 1999-03-10 | 中国通用石化机械工程总公司 | Vaporation for carbon dioxide purifying recovery device |
| CN2848266Y (en) * | 2005-12-28 | 2006-12-20 | 四川威龙消防设备有限公司 | Carbon dioxide inertial device |
-
2009
- 2009-01-06 CN CN2009100291580A patent/CN101481641B/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102434777A (en) * | 2011-10-14 | 2012-05-02 | 中国空分设备有限公司 | Water bath vaporizer provided with vapor-water mixer |
| CN102829326A (en) * | 2012-09-12 | 2012-12-19 | 镇海石化建安工程有限公司 | Steam-heated water-bath type vaporizer |
| CN102829326B (en) * | 2012-09-12 | 2014-07-23 | 镇海石化建安工程有限公司 | Steam-heated water-bath type vaporizer |
| CN104266421A (en) * | 2014-09-26 | 2015-01-07 | 烟台冰轮股份有限公司 | Working medium discharge device and discharge control method used for CO2 refrigeration system |
| CN106481979A (en) * | 2016-12-20 | 2017-03-08 | 上海华林工业气体有限公司 | A kind of steam heating water bath type carburetion system with feedback control |
| CN114893717A (en) * | 2022-04-28 | 2022-08-12 | 宁波东君工程技术有限公司 | By using CO 2 Liquefaction energy-saving equipment for heat exchange from pipeline to evaporation cooling equipment and method thereof |
| CN115978446A (en) * | 2022-11-24 | 2023-04-18 | 新疆敦华绿碳技术股份有限公司 | Gas phase conversion equipment |
| CN115978446B (en) * | 2022-11-24 | 2024-05-24 | 新疆敦华绿碳技术股份有限公司 | Gas phase conversion equipment |
Also Published As
| Publication number | Publication date |
|---|---|
| CN101481641B (en) | 2011-12-07 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20170527 Address after: 225600, Yangzhou City, Jiangsu province Gaoyou Heng Jing Zhen Town Temple No. 36 Patentee after: YANGZHOU RUNMING LIGHT-INDUSTRY MACHINERY CO., LTD. Address before: 225009 Yangzhou Yangzhou Light Industrial Machinery Co., Ltd., 450 Yangzi Road, Jiangsu, China Patentee before: Liu Jinzhi |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20111207 Termination date: 20180106 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |