CN2738579Y - Energy-saving high-temp. instance liquid sterilizing machine - Google Patents
Energy-saving high-temp. instance liquid sterilizing machine Download PDFInfo
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- CN2738579Y CN2738579Y CN 200420061688 CN200420061688U CN2738579Y CN 2738579 Y CN2738579 Y CN 2738579Y CN 200420061688 CN200420061688 CN 200420061688 CN 200420061688 U CN200420061688 U CN 200420061688U CN 2738579 Y CN2738579 Y CN 2738579Y
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Abstract
The utility model discloses an energy-saving high-temperature instance liquid sterilizing machine adapted for the beverage factory and the brewery, comprising a pre-heat cooling heat exchanger composed of a pre-heat fluid passage and a cooling fluid passage and a sterilizing heat exchanger composed of a steam passage and a sterilizing fluid passage. The energy-saving high-temperature instance liquid sterilizing machine is characterized in that the pre-heat fluid passage contains an internal bladder used for pre-heating the liquid to be sterilized; the cooling fluid passage is arranged in the internal bladder; the sterilizing fluid passage is arranged in the steam passage. The energy-saving high-temperature instance liquid sterilizing machine has simple structure, quick sterilizing and good sterilizing effect, coal saving, water-saving, save electricity and labor saving.
Description
Affiliated technical field
The utility model relates to a kind of liquid high-temperature sterilization equipment, especially a kind of equipment that is suitable for beverage, liquid flavouring sterilization.
Background technology
The method that present most middle-size and small-size Soft Drinks Plants, brewery etc. all adopt steam to dash and boil is sterilized, and this method not only wastes energy, and the fluid product water content that is sterilized is increased, and influences the quality of its product, and its cool time is also longer.Notification number is that the Chinese patent of CN2054980U discloses a kind of sterilizer, and its structure is to adopt two spiral heat exchangers, and one is played preheating and cooling liquid, and another plays the high-temperature sterilization effect.There is following shortcoming in this sterilizer: 1, its complex structure is difficult for processing; 2, because liquid subject to sterilization is not complete ordering flowing in the sterilization heat exchanger, and have the problem of flow blind angle, its sterilization effect is undesirable; 3, be not easy to working service.
Technology contents of the present utility model
Problem to be solved in the utility model be to provide a kind of simple in structure, sterilization effect is desirable, UTILIZATION OF VESIDUAL HEAT IN efficient height, the instantaneous sterilization of liquids machine of energy-saving high-temperature being convenient to safeguard.
The utility model adopts following technical scheme, comprise the preheating cooling heat exchanger of forming by preheated liquid passage and cooling liquid passage, the sterilization heat exchanger of forming by steam channel and sterilized liquid passage, described preheated liquid passage comprises first inlet and first outlet, described sterilized liquid passage comprises second inlet and second outlet, described cooling liquid passage comprises the 3rd inlet and the 3rd outlet, described steam channel comprises steam inlet and condensation-water drain, described first outlet and second inlet communicate, described second outlet and the 3rd inlet communicate, described preheated liquid passage comprises the inner bag that is used for preheating liquid subject to sterilization, described cooling liquid passage is located in the inner bag, and described sterilized liquid passage is located in the steam channel.
As improvement of the present utility model, described sterilized liquid passage is a helix tube.
The another kind of improvement is that described cooling liquid passage is a helix tube.The above-mentioned passage scheme that is modified into spiral tube structure can improve heat transfer efficiency.
Further improvement is, first inlet of described preheated liquid passage is positioned at the lower end of described preheated liquid passage, and described first outlet is positioned at the upper end of described preheated liquid passage.
Further improvement is, described second inlet is positioned at the lower end of described sterilized liquid passage, and described second outlet is positioned at the upper end of described sterilized liquid passage.
Further improvement is again, and described the 3rd inlet is positioned at the upper end of described cooling liquid passage, and described the 3rd outlet is positioned at the lower end of described cooling liquid passage.
Also have a kind of improvement, described steam inlet is positioned at the upper end of described steam channel, and described condensation-water drain is positioned at the lower end of described steam channel.Steam and liquid reverse flow subject to sterilization have guaranteed bactericidal effect.
Above-mentioned four kinds of improvement purposes about inlet, exit position heat up and the cooling in order of sterilization back before being to utilize thermal convection principle that liquid heats up to make liquid subject to sterilization can be implemented in sterilization in order.
The another kind of improvement is, described steam channel comprises the steam chest that several are set up in parallel, outer side edges between the adjacent steam chest is provided with air passing hole, the air passing hole of the steam chest at place, steam inlet is located at the relative side in steam inlet, and two the adjacent mistake steam vents that are communicated with adjacent upper and lower steam chest keep larger distance to be crisscross arranged as far as possible.Can guarantee that like this steam channel has long circulation distance.
Improving again is that described steam channel is a helix tube.
Employing the utlity model has following advantage:
1, simple in structure, be convenient to processing, its working service is convenient.
2, bactericidal effect ideal.Liquid subject to sterilization has all been realized flowing in order in intensification sterilization and cooling procedure in closed conduct, and no flow blind angle exists in the runner, has guaranteed bactericidal effect.
3, set up a storage liquid container that is positioned over eminence, can realize not having the production of pump gravity flow.
4, sterilization is rapid,, is sterilized fluid temperature and can rises to 60-110 degree centigrade, and be cooled to below 25 degrees centigrade in second at 8-15.
5, remarkable in economical benefits.The utility model is not only economized coal, power saving, also reduce manpower, save cooling water, calculate by one ton of fluid product of sterilization, economize coal 40-80 kilogram, 0.5 ton of water-saving than the old-fashioned method of boiling of dashing, power saving 4 degree, economize 0.7 man day of labour, every cost saving adds up to about 15 yuan, produces can reducing expenses about 100,000 yuan in producer's year of 5000-10000 ton per year.
Below in conjunction with embodiment the utility model is described in further detail.
Marginal data
Fig. 1 is a kind of example structure principle schematic of the utility model.
Fig. 2 is an inner-tube structure principle schematic of the present utility model.
Fig. 3 is a kind of sterilization heat exchanger principle schematic of the present utility model.
The specific embodiment
As Fig. 1, shown in Figure 2, a kind of embodiment of the utility model comprises the preheating cooling heat exchanger of being made up of preheated liquid passage 1 and cooling liquid passage 23, the sterilization heat exchanger of forming by steam channel 4 and sterilized liquid passage 56, described preheated liquid passage 1 comprises 7 and first outlet 8 of first inlet, described sterilized liquid passage 5 comprises 14 and second outlet 9 of second inlet, described cooling liquid passage 2 comprises the 10 and the 3rd outlet 11 of the 3rd inlet, described steam channel 4 comprises steam inlet 12 and condensation-water drain 13, described first outlet, 8 and second inlet 14 communicates, described second outlet the 9 and the 3rd inlet 10 communicates, described preheated liquid passage 1 comprises the inner bag 15 that is used for preheating liquid subject to sterilization, described cooling liquid passage 2 is located in the inner bag 15, and described sterilized liquid passage 5 is located in the steam channel 4.
As Fig. 1, shown in Figure 3, the described sterilized liquid passage 5 that is improved to of the present utility model is helix tube.
As shown in Figure 2, the another kind of improvement of the present utility model is that described cooling liquid passage 2 is helix tube.Above-mentioned spiral tube structure can improve heat transfer efficiency.
As shown in Figure 1, 2, 3, the utility model further is improved to, and described first inlet 7 is positioned at the lower end of described preheated liquid passage 1, and described first outlet 8 is positioned at the upper end of described preheated liquid passage 1.
Further be improved to, described second inlet 14 is positioned at the lower end of described sterilized liquid passage 5, and described second outlet 9 is positioned at the upper end of described sterilized liquid passage 5.
Further be improved to, described the 3rd inlet 10 is positioned at the upper end of described cooling liquid passage 2 again, and described the 3rd outlet 11 is positioned at the lower end of described cooling liquid passage 2.
Also having a kind of improvement is the upper end that described steam inlet 12 is positioned at described steam channel 4, and described condensation-water drain 13 is positioned at the lower end of described steam channel 4.
Above-mentioned improved purpose can be lowered the temperature after being to utilize thermal convection principle that liquid heats up to make liquid subject to sterilization can heat up in order before sterilization, sterilize in order.
As Fig. 1, shown in Figure 3, the steam channel 4 of sterilization heat exchanger 6 of the present utility model comprises several steam chests that is set up in parallel 16, an outer side edges is provided with air passing hole between the adjacent steam chest 16, first air passing hole 18 of steam inlet 12 place steam chests 16 is located at the relative side in steam inlet 12, crosses steam vents (such as first air passing hole 18 and second pore 17) and keeps larger distance to be crisscross arranged as far as possible for adjacent two that are communicated with adjacent upper and lower steam chest 16.This relatively simple for structure, be easy to processing, its bactericidal effect is also more satisfactory.Certainly, also steam channel can be designed to helically coiled, " bow " word and back and forth fold multiple shapes such as shape.
This practical type also can be set up the receiver that is used to store liquid subject to sterilization, the liquid outlet of the bottom of described receiver height overhead is higher than the 3rd outlet 11 height overhead of described cooling liquid passage 2, can utilize siphon principle not have the production of pump gravity flow like this.
As shown in Figure 1, the utility model can be that preheating cooling heat exchanger 3 is integral the formula structure with sterilization heat exchanger 6, also can be that both become split-type structural.
The utility model does not limit to the concrete structure of the foregoing description, and the equivalent transformation of other homogeneous structure all falls within the protection domain of the present utility model.
Claims (10)
1, the instantaneous sterilization of liquids machine of a kind of energy-saving high-temperature, comprise the preheating cooling heat exchanger of forming by preheated liquid passage and cooling liquid passage, the sterilization heat exchanger of forming by steam channel and sterilized liquid passage, described preheated liquid passage comprises first inlet and first outlet, described sterilized liquid passage comprises second inlet and second outlet, described cooling liquid passage comprises the 3rd inlet and the 3rd outlet, described steam channel comprises steam inlet and condensation-water drain, described first outlet and second inlet communicate, described second outlet and the 3rd inlet communicate, it is characterized in that: described preheated liquid passage comprises the inner bag that is used for preheating liquid subject to sterilization, described cooling liquid passage is located in the inner bag, and described sterilized liquid passage is located in the steam channel.
2, the instantaneous sterilization of liquids machine of a kind of energy-saving high-temperature according to claim 1, it is characterized in that: described sterilized liquid passage is a helix tube.
3, the instantaneous sterilization of liquids machine of a kind of energy-saving high-temperature according to claim 2, it is characterized in that: described cooling liquid passage is a helix tube.
4, the instantaneous sterilization of liquids machine of a kind of energy-saving high-temperature according to claim 3 is characterized in that: described first inlet is positioned at the lower end of described preheated liquid passage, and described first outlet is positioned at the upper end of described preheated liquid passage.
5, the instantaneous sterilization of liquids machine of a kind of energy-saving high-temperature according to claim 4 is characterized in that: described second inlet is positioned at the lower end of described sterilized liquid passage, and described second outlet is positioned at the upper end of described sterilized liquid passage.
6, the instantaneous sterilization of liquids machine of a kind of energy-saving high-temperature according to claim 5 is characterized in that: described the 3rd inlet is positioned at the upper end of described cooling liquid passage, and described the 3rd outlet is positioned at the lower end of described cooling liquid passage.
7, the instantaneous sterilization of liquids machine of a kind of energy-saving high-temperature according to claim 6, it is characterized in that: described steam inlet is positioned at the upper end of described steam channel, and described condensation-water drain is positioned at the lower end of described steam channel.
8, the instantaneous sterilization of liquids machine of a kind of energy-saving high-temperature according to claim 7, it is characterized in that: described steam channel comprises the steam chest that several are set up in parallel, outer side edges between the adjacent steam chest is provided with air passing hole, first air passing hole of the steam chest at place, steam inlet is located at the relative side in steam inlet, and two the adjacent mistake steam vents that are communicated with adjacent upper and lower steam chest keep larger distance to be crisscross arranged as far as possible.
9, the instantaneous sterilization of liquids machine of a kind of energy-saving high-temperature according to claim 7, it is characterized in that: described steam channel is a helix tube.
10, according to Claim 8 or the instantaneous sterilization of liquids machine of 9 described a kind of energy-saving high-temperatures, it is characterized in that: also comprise the receiver that is used to store liquid subject to sterilization, the liquid outlet of the bottom of described receiver height overhead is higher than the 3rd outlet height overhead of described cooling liquid passage.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200420061688 CN2738579Y (en) | 2004-10-13 | 2004-10-13 | Energy-saving high-temp. instance liquid sterilizing machine |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200420061688 CN2738579Y (en) | 2004-10-13 | 2004-10-13 | Energy-saving high-temp. instance liquid sterilizing machine |
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| Publication Number | Publication Date |
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| CN2738579Y true CN2738579Y (en) | 2005-11-09 |
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| CN 200420061688 Expired - Fee Related CN2738579Y (en) | 2004-10-13 | 2004-10-13 | Energy-saving high-temp. instance liquid sterilizing machine |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102726806A (en) * | 2011-11-09 | 2012-10-17 | 上海海洋大学 | Steam heating sterilization device for beverages |
| CN103910395A (en) * | 2013-01-06 | 2014-07-09 | 中石化上海工程有限公司 | Ultrahigh temperature sterilizer and its use |
| CN104663882A (en) * | 2015-03-25 | 2015-06-03 | 成都巨龙生物科技有限公司 | Multifunctional energy-saving high-temperature sterilization system |
| CN107232473A (en) * | 2017-06-05 | 2017-10-10 | 温州市伯泰机械科技有限公司 | Sterilizer |
| CN113207970A (en) * | 2021-05-10 | 2021-08-06 | 济南道丰食品有限公司 | Processing technology of compound protein beverage |
-
2004
- 2004-10-13 CN CN 200420061688 patent/CN2738579Y/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102726806A (en) * | 2011-11-09 | 2012-10-17 | 上海海洋大学 | Steam heating sterilization device for beverages |
| CN102726806B (en) * | 2011-11-09 | 2014-01-08 | 上海海洋大学 | Steam heating sterilization device for beverages |
| CN103910395A (en) * | 2013-01-06 | 2014-07-09 | 中石化上海工程有限公司 | Ultrahigh temperature sterilizer and its use |
| CN103910395B (en) * | 2013-01-06 | 2015-10-21 | 中石化上海工程有限公司 | Ultra high temperature sterilization (UHTS) device and uses thereof |
| CN104663882A (en) * | 2015-03-25 | 2015-06-03 | 成都巨龙生物科技有限公司 | Multifunctional energy-saving high-temperature sterilization system |
| CN104663882B (en) * | 2015-03-25 | 2017-11-24 | 成都巨龙生物科技股份有限公司 | A kind of multifunction energy-saving high-temperature sterilization system |
| CN107232473A (en) * | 2017-06-05 | 2017-10-10 | 温州市伯泰机械科技有限公司 | Sterilizer |
| CN113207970A (en) * | 2021-05-10 | 2021-08-06 | 济南道丰食品有限公司 | Processing technology of compound protein beverage |
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| CF01 | Termination of patent right due to non-payment of annual fee |