CN101723291A - Low-temperature aseptic system and process for filling plastic bottled drink - Google Patents
Low-temperature aseptic system and process for filling plastic bottled drink Download PDFInfo
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- CN101723291A CN101723291A CN201010113755A CN201010113755A CN101723291A CN 101723291 A CN101723291 A CN 101723291A CN 201010113755 A CN201010113755 A CN 201010113755A CN 201010113755 A CN201010113755 A CN 201010113755A CN 101723291 A CN101723291 A CN 101723291A
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- heat exchange
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- 238000000034 method Methods 0.000 title claims abstract description 18
- 238000011049 filling Methods 0.000 title abstract description 12
- 239000000463 material Substances 0.000 claims abstract description 113
- 230000001954 sterilising effect Effects 0.000 claims abstract description 79
- 238000004659 sterilization and disinfection Methods 0.000 claims abstract description 78
- 238000010438 heat treatment Methods 0.000 claims abstract description 21
- 235000015203 fruit juice Nutrition 0.000 claims abstract description 5
- 241001122767 Theaceae Species 0.000 claims abstract 2
- 235000013361 beverage Nutrition 0.000 claims description 18
- 230000002411 adverse Effects 0.000 claims description 13
- 238000005516 engineering process Methods 0.000 claims description 11
- 230000008676 import Effects 0.000 claims description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 6
- 238000005485 electric heating Methods 0.000 claims description 5
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims description 3
- 239000002994 raw material Substances 0.000 claims description 3
- 238000012859 sterile filling Methods 0.000 claims description 3
- 238000003756 stirring Methods 0.000 claims description 3
- 238000004140 cleaning Methods 0.000 claims description 2
- 239000003814 drug Substances 0.000 claims description 2
- 235000014347 soups Nutrition 0.000 abstract description 5
- 239000000796 flavoring agent Substances 0.000 abstract description 4
- 235000019634 flavors Nutrition 0.000 abstract description 4
- 238000005265 energy consumption Methods 0.000 abstract description 2
- 235000013305 food Nutrition 0.000 abstract description 2
- 238000012423 maintenance Methods 0.000 abstract description 2
- 230000003647 oxidation Effects 0.000 abstract description 2
- 238000007254 oxidation reaction Methods 0.000 abstract description 2
- 235000012041 food component Nutrition 0.000 abstract 1
- 235000013616 tea Nutrition 0.000 description 6
- 244000269722 Thea sinensis Species 0.000 description 5
- 235000013399 edible fruits Nutrition 0.000 description 3
- 235000016709 nutrition Nutrition 0.000 description 3
- 230000006378 damage Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000002372 labelling Methods 0.000 description 2
- 241000196324 Embryophyta Species 0.000 description 1
- 230000000844 anti-bacterial effect Effects 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000005429 filling process Methods 0.000 description 1
- 235000009569 green tea Nutrition 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 230000035764 nutrition Effects 0.000 description 1
- 238000002791 soaking Methods 0.000 description 1
- 230000001052 transient effect Effects 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
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- Filling Of Jars Or Cans And Processes For Cleaning And Sealing Jars (AREA)
- Devices For Dispensing Beverages (AREA)
Abstract
The invention discloses a low-temperature aseptic system and a low-temperature aseptic process for filling plastic bottled drink, and belongs to the technical field of food processing. The system and the process are technically characterized in that: the heating sterilization adopts a countercurrent instantaneous heating sterilization device, and the device comprises a countercurrent heat exchange pipeline and an instantaneous heating sterilization pipeline; and a material is heated and sterilized in the instantaneous heating sterilization pipeline, the heated and sterilized material performs heat exchange and temperature reduction in the countercurrent heat exchange pipeline, the heating sterilization temperature is between 150 and 155 DEG C, the time is between 8 and 12 seconds, and the outlet temperature is between 25 and 30 DEG C. A countercurrent heat exchange structure and a countercurrent heat exchange process are adopted, so the system and the process have less heat loss and short heating time, avoid the high-temperature oxidation of the drink, effectively maintain nutritional components of finished products, and reduce the energy consumption. The system and the process adopt normal-temperature filling, have low filling temperature, effectively overcome the 'cooked soup taste' caused by high-temperature filling, and maintain the original flavor of tea and fruit juice. The system has the advantages of simple structure, steady operation and convenient maintenance.
Description
Technical field
The present invention relates to a kind of filling apparatus and technology, particularly the sterile filling plastic bottle concentrates the equipment and the process of tea beverage, fruit drink, belongs to food processing technology field.
Background technology
At present, plastic bottle beverage in the prior art generally adopts high-temperature filling technology more than 85 degrees centigrade as tea beverage, fruit drink etc., and material is under the long-time condition of high temperature in the pouring process, and the mouthfeel variation is easily lost nutritional labeling; Especially green tea is afraid of that heated time is long most, very easily produces " ripe soup flavor "; Nutriment in the beverage also can be subjected to destruction in various degree simultaneously.Therefore, high-temperature filling technology can't be produced high-quality bottles of tea, fruit beverage, and high-temperature filling need be selected the plastic bottle of high temperature material for use in addition, and its cost is higher than nearly 1 times of the plastic bottle of normal temperature material, causes cost of product higher.
Hot filling manufacturing line of the prior art also need possess one in boiler except that consuming electric power, not only power consumption is big, and adopts boiler also can cause environmental pollution.Heat sterilization also has the Far-infrared Heating of employing device at present, this plant energy consumption height, and fluctuation of service, equipment damages easily, therefore causes the system operation cost height.
Summary of the invention
The system and the technology that the purpose of this invention is to provide a kind of cryogenic sterile can plastic bottle beverage make this system not only stable, are convenient to safeguard, and can effectively reduce operating cost.
Another object of the present invention provides a kind of technology of cryogenic sterile can plastic bottle beverage, to overcome in the prior art owing to adopt that high-temperature filling easily produces ripe soup flavor, mouthfeel is not good and easily lose defective such as nutritional labeling.
Above-mentioned purpose of the present invention is achieved through the following technical solutions:
A kind of cryogenic sterile bulking system of plastic bottle beverage, comprise feed proportioning system, heat sterilization device and dash a bottle bulking system, it is characterized in that: described heat sterilization device adopts adverse current transient heating bactericidal unit, and this device is made up of force (forcing) pump, normal temperature material inlet, material countercurrent heat exchange pipeline, the instantaneous heat sterilization pipeline of material and sterilization material outlet; Described material countercurrent heat exchange pipeline flows to pipe by inlet feed and sterilization material effuser is formed; The instantaneous heat sterilization pipeline of described material by thermal material flow to the pipe and be arranged on thermal material flow to the pipe in heating arrangement form; Described heating arrangement comprises electric heating tube and conduction oil; The outlet that described thermal material flows to pipe is connected with the import of sterilization material effuser, and the outlet that described inlet feed flows to pipe is connected with the import that thermal material flows to pipe.
Technical characterictic of the present invention also is: described sterilization material effuser, thermal material flow to pipe and inlet feed flows to pipe and all adopts the U-shaped coil pipe, and the sterilization material flows out pipe box and is contained in the inside that inlet feed flows to pipe.
Another technical characterictic of the present invention is: described inlet feed flows to pipe and flows to the pipe that pipe adopts identical caliber with thermal material.
The cryogenic sterile filling process of a kind of plastic bottle beverage provided by the invention is characterized in that this technology comprises the steps:
1) tea or fruit juice raw material and auxiliary material and the pure water drunk are placed material-compound tank by desired proportioning, stir, form the can material;
2) utilize high pressure pump that the can material is sent in the instantaneous heat sterilization device of adverse current, material enters the thermal material that inlet feed in the countercurrent heat exchange pipeline flows in pipe 4 and the instantaneous heat sterilization device of adverse current successively and flows to pipe 8, in thermal material flows to pipe 8 in the process of flowing by the heating arrangement heat sterilization, the heat sterilization temperature is 150～155 ℃, and the heat sterilization time is 8～12 seconds;
3) the can material after the sterilization flows into the sterilization material effuser in the countercurrent heat exchange pipeline, the can material carries out interchange of heat with can material that inlet feed flows in the pipe in sterilization material effuser, the temperature out of sterilization back can material is 25～30 ℃, and the time of control can material from the normal temperature material inlet to the sterilization material outlet is 4～6 minutes;
4) the can material after sterilization enters hundred grades and purifies bottling department, plastic bottle behind the medicine cleaning and sterilizing is sent into hundred grades purify bottling department, adopting ozone content is that 0.8～1.2mg/L Ozone Water is dashed bottle, carries out can by dashing bottle, can and the Trinitarian bottle placer of spiral cover again.
The present invention compared with prior art, have the following advantages and the high-lighting effect: 1. owing to adopted the countercurrent flow structure and the technology of cold and hot material, homogeneous heating not only, and thermal loss is little, greatly reduces the consumption of the energy, 2. adopts the instantaneous type of heating of adverse current, the effect that material can reach a high temperature in flow process and sterilize, time of heat is short, has avoided the high-temperature oxidation of beverage, is damaged because of long-time heating makes the nutriment in the beverage thereby effectively overcome in the prior art.3. adopt the normal temperature can, because the can temperature is low, effectively overcome because of high-temperature filling caused " ripe soup flavor ", kept the genuineness of tea, fruit juice, not only mouthfeel is good, and the loss of the nutrition of finished product is little.4. adopt conventional PET bottle and normal pressure lid to replace heat-resisting, pressure-proof PET Bottle and closure, reduced cost of product.5. device structure is simple, and is stable, and is convenient to safeguard.
Description of drawings
Fig. 1 is the process flow diagram of cryogenic sterile can plastic bottle beverage provided by the invention.
Fig. 2 is the structural principle scheme drawing of the cryogenic sterile bulking system of plastic bottle beverage provided by the invention.
Among the figure: the 1-material-compound tank; The 2-high pressure pump; 3-normal temperature material inlet; The 4-inlet feed flows to pipe; 5-sterilization material effuser; The 6-electric heating tube; The 7-heat-conducting oil pipes; The 8-thermal material flows to pipe; The 9-material outlet of sterilizing; The 10-flow control valve; The 11-flow counter; 12-trinity bottle placer.
The specific embodiment
Below in conjunction with accompanying drawing concrete structure of the present invention, principle and technological process are described further.
Fig. 1 is the flow scheme of cryogenic sterile can plastic bottle beverage provided by the invention, and this filling process mainly comprises batching, heat sterilization and dash process procedure such as bottle can that it specifically comprises the steps:
1) tea or fruit juice raw material and auxiliary material and the pure water drunk are placed material-compound tank by desired proportioning, stir, mixing time was generally 25～30 minutes, formed the can material;
2) utilize high pressure pump that the can material is sent in the instantaneous heat sterilization device of adverse current, material enters the thermal material that inlet feed in the countercurrent heat exchange pipeline flows in pipe 4 and the instantaneous heat sterilization device of adverse current successively and flows to pipe 8, in thermal material flows to pipe 8 in the process of flowing by the heating arrangement heat sterilization, heating arrangement adopts electric heating tube 6, the can material that heated conduction oil and thermal material flow in the pipe 8 carries out interchange of heat, make the can material be heated sterilization while flowing, the heat sterilization temperature is 150～155 ℃, and the heat sterilization time is 8～12 seconds;
3) the can material after the sterilization flows into the sterilization material effuser 5 in the countercurrent heat exchange pipeline, the can material flows to the can material of managing in 4 with inlet feed and carries out interchange of heat in sterilization material effuser 5, the temperature out of sterilization back can material is 25～30 ℃, and the time of control can material from normal temperature material inlet 3 to sterilization material outlet 9 is 4～6 minutes;
4) the can material after sterilization enters hundred grades and purifies bottling department, plastic bottle after the sterilization of full automaticity bottle washing machine soup soaking disinfection also is sent to hundred grades and purifies bottling department, adopting ozone content is that 0.8～1.2mg/L Ozone Water is dashed bottle, carry out can by dashing bottle, can and the Trinitarian bottle placer of spiral cover again, can produce bottled product.
Fig. 2 is the structural principle scheme drawing of the cryogenic sterile bulking system of plastic bottle beverage provided by the invention, this system comprises feed proportioning system, heat sterilization device and dash a bottle bulking system, promptly mainly by material-compound tank 1, the instantaneous heat sterilization device of adverse current, control cock 10, flow counter and trinity bottle placer 12 are formed, described heat sterilization device adopts the instantaneous heat sterilization device of adverse current, and the instantaneous heat sterilization device of this adverse current comprises high pressure pump 2, normal temperature material inlet 3, material countercurrent heat exchange pipeline, the instantaneous heat sterilization pipeline of material and sterilization material outlet 9; Described material countercurrent heat exchange pipeline flows to pipe 4 by inlet feed and sterilization material effuser 5 is formed; The instantaneous heat sterilization pipeline of described material by thermal material flow to the pipe 8 and be arranged on thermal material flow to the pipe in heating arrangement form; Described heating arrangement comprises electric heating tube 6 and heat-conducting oil pipes 7.The outlet that thermal material flows to pipe 8 is connected with the import of sterilization material effuser 5, and the outlet that described inlet feed flows to pipe 4 is connected with the import that thermal material flows to pipe 8.
Inlet feed in the instantaneous heat sterilization device of adverse current of the present invention flows to pipe 4, sterilization material effuser 5 and thermal material and flows to pipe 8 and all adopt the U-shaped coil pipe, and sterilization material effuser 5 is sleeved on the inside that inlet feed flows to pipe 4.Inlet feed flows to caliber and the tube side that pipe 4, sterilization material effuser 5 and thermal material flow to pipe 8 should carry out concrete design according to the time of heat and the heat sterilization temperature of material.
For the ease of processing and maintenance, inlet feed flows to pipe 4 and flows to the pipe that pipe 8 can adopt identical caliber with thermal material.
Claims (4)
1. the cryogenic sterile bulking system of a plastic bottle beverage, comprise feed proportioning system, heat sterilization device and dash a bottle bulking system, it is characterized in that: described heat sterilization device adopts the instantaneous heat sterilization device of adverse current, and this device is made up of high pressure pump (2), normal temperature material inlet (3), material countercurrent heat exchange pipeline, the instantaneous heat sterilization pipeline of material and sterilization material outlet (1); Described material countercurrent heat exchange pipeline flows to pipe (4) by inlet feed and sterilization material effuser (5) is formed; The instantaneous heat sterilization pipeline of described material flow to pipe (8) by thermal material and be arranged on thermal material flow to the pipe in heating arrangement form; Described heating arrangement comprises electric heating tube (6) and heat-conducting oil pipes (7); The outlet that described thermal material flows to pipe (8) is connected with the import of sterilization material effuser (5), and the outlet that described inlet feed flows to pipe (4) is connected with the import that thermal material flows to pipe (8).
2. according to the cryogenic sterile bulking system of the described a kind of plastic bottle beverage of claim 1, it is characterized in that: described sterilization material effuser (5), thermal material flow to pipe (8) and inlet feed and flow to pipe (5) and all adopt the U-shaped coil pipe, and sterilization material effuser (5) is sleeved on the inside that inlet feed flows to pipe (4).
3. according to the cryogenic sterile bulking system of claim 1 or 2 described a kind of plastic bottle beverages, it is characterized in that: described inlet feed flows to pipe (4) and flows to the pipe that pipe (8) adopts identical caliber with thermal material.
4. one kind is adopted the cryogenic sterile filling process of the plastic bottle beverage of system according to claim 1, it is characterized in that this technology comprises the steps:
1) tea or fruit juice raw material and auxiliary material and the pure water drunk are placed material-compound tank by desired proportioning, stir, form the can material;
2) utilize high pressure pump that the can material is sent in the instantaneous heat sterilization device of adverse current, material enters the thermal material that inlet feed in the countercurrent heat exchange pipeline flows in pipe 4 and the instantaneous heat sterilization device of adverse current successively and flows to pipe 8, in thermal material flows to pipe 8 in the process of flowing by the heating arrangement heat sterilization, the heat sterilization temperature is 150～155 ℃, and the heat sterilization time is 8～12 seconds;
3) the can material after the sterilization flows into the sterilization material effuser in the countercurrent heat exchange pipeline, the can material carries out interchange of heat with can material that inlet feed flows in the pipe in sterilization material effuser, the temperature out of sterilization back can material is 25～30 ℃, and the time of control can material from the normal temperature material inlet to the sterilization material outlet is 4～6 minutes;
4) the can material after sterilization enters hundred grades and purifies bottling department, plastic bottle behind the medicine cleaning and sterilizing is sent into hundred grades purify bottling department, adopting ozone content is that 0.8～1.2mg/L Ozone Water is dashed bottle, carries out can by dashing bottle, can and the Trinitarian bottle placer of spiral cover again.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010101137554A CN101723291B (en) | 2010-02-09 | 2010-02-09 | Low-temperature aseptic system and process for filling plastic bottled drink |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010101137554A CN101723291B (en) | 2010-02-09 | 2010-02-09 | Low-temperature aseptic system and process for filling plastic bottled drink |
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| Publication Number | Publication Date |
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| CN101723291A true CN101723291A (en) | 2010-06-09 |
| CN101723291B CN101723291B (en) | 2011-11-09 |
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| CN2010101137554A Active CN101723291B (en) | 2010-02-09 | 2010-02-09 | Low-temperature aseptic system and process for filling plastic bottled drink |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102210475A (en) * | 2011-01-28 | 2011-10-12 | 上海海洋大学 | Energy-saving device for sterilizing beverages |
| CN102530812A (en) * | 2010-12-10 | 2012-07-04 | 克朗斯股份公司 | Method and device for aseptic filling |
| CN104030219A (en) * | 2014-06-30 | 2014-09-10 | 广西健美乐食品有限公司 | Bamboo juice filling machine |
| WO2018023974A1 (en) * | 2016-08-05 | 2018-02-08 | 江苏新美星包装机械股份有限公司 | Sterile-water temperature adjustment device and system |
| CN109439547A (en) * | 2018-11-22 | 2019-03-08 | 英诺维尔智能科技（苏州）有限公司 | A kind of full-automatic sterile method for implanting of large capacity reagent |
| CN111345420A (en) * | 2020-04-26 | 2020-06-30 | 万政豪 | Low-temperature aseptic filling method for plant and dried fruit beverage |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB810215A (en) * | 1955-02-16 | 1959-03-11 | Baltzar Jacobsson | An improved method for the production of pasteurized beverages, and apparatus for carrying out this method |
| CN2781803Y (en) * | 2005-01-27 | 2006-05-24 | 李卫国 | Ultrahigh temp instantaneous sterilizing appts. for soy |
| JP5136740B2 (en) * | 2006-07-26 | 2013-02-06 | 東洋製罐株式会社 | Method for producing containerized beverage |
-
2010
- 2010-02-09 CN CN2010101137554A patent/CN101723291B/en active Active
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102530812A (en) * | 2010-12-10 | 2012-07-04 | 克朗斯股份公司 | Method and device for aseptic filling |
| CN102530812B (en) * | 2010-12-10 | 2014-05-07 | 克朗斯股份公司 | Method and device for aseptic filling |
| CN102210475A (en) * | 2011-01-28 | 2011-10-12 | 上海海洋大学 | Energy-saving device for sterilizing beverages |
| CN104030219A (en) * | 2014-06-30 | 2014-09-10 | 广西健美乐食品有限公司 | Bamboo juice filling machine |
| WO2018023974A1 (en) * | 2016-08-05 | 2018-02-08 | 江苏新美星包装机械股份有限公司 | Sterile-water temperature adjustment device and system |
| CN109439547A (en) * | 2018-11-22 | 2019-03-08 | 英诺维尔智能科技（苏州）有限公司 | A kind of full-automatic sterile method for implanting of large capacity reagent |
| CN111345420A (en) * | 2020-04-26 | 2020-06-30 | 万政豪 | Low-temperature aseptic filling method for plant and dried fruit beverage |
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| Publication number | Publication date |
|---|---|
| CN101723291B (en) | 2011-11-09 |
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Effective date of registration: 20240524 Address after: Room 1202-3-3, No. 128 Fengqi Road, Software Park Phase III, Xiamen Torch High tech Zone, Xiamen, Fujian Province, 361000 (Address for legal document delivery) Patentee after: Xiamen Vitality Shen Biotechnology Co.,Ltd. Country or region after: China Address before: No. 2, Xianping Road, Xiandian Industrial Park, Wuyi New District, Mount Wuyi City, Fujian Province, 354305 Patentee before: Wan Zhenghao Country or region before: China |
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