CN106865862A - A kind of hot water heat-exchange system of tubular type UHT heat recovery rates high - Google Patents
A kind of hot water heat-exchange system of tubular type UHT heat recovery rates high Download PDFInfo
- Publication number
- CN106865862A CN106865862A CN201710195389.3A CN201710195389A CN106865862A CN 106865862 A CN106865862 A CN 106865862A CN 201710195389 A CN201710195389 A CN 201710195389A CN 106865862 A CN106865862 A CN 106865862A
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- heat
- section
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- hot
- water
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 109
- 238000011084 recovery Methods 0.000 title claims abstract description 47
- 238000007872 degassing Methods 0.000 claims abstract description 29
- 238000001816 cooling Methods 0.000 claims abstract description 27
- 230000008676 import Effects 0.000 claims abstract description 5
- 230000001954 sterilising effect Effects 0.000 claims description 17
- 238000004659 sterilization and disinfection Methods 0.000 claims description 17
- 230000001105 regulatory effect Effects 0.000 claims description 4
- 241000894006 Bacteria Species 0.000 claims 1
- 238000005303 weighing Methods 0.000 claims 1
- 238000005516 engineering process Methods 0.000 description 3
- 239000000796 flavoring agent Substances 0.000 description 3
- 235000019634 flavors Nutrition 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 2
- 239000000498 cooling water Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 235000013361 beverage Nutrition 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000013021 overheating Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000004781 supercooling Methods 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/20—Treatment of water, waste water, or sewage by degassing, i.e. liberation of dissolved gases
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Apparatus For Disinfection Or Sterilisation (AREA)
Abstract
The present invention relates to a kind of hot water heat-exchange system of tubular type UHT heat recovery rates high, include compensator, product pump, degassing stages, warming-up section, sterilisating section, heat-recovery section, tower water cooling section and frozen water cooling section successively from import to outlet in all-product line, hot water line includes heat-recovery section hot water circuit part and sterilized hot water circuit part, and heat-recovery section hot water circuit part includes cooling hot-water cylinder, cools down heat-exchanger pump, flow through the heat-recovery section, flow through the warming-up section, flow through the degassing stages, finally return cooling hot-water cylinder successively；Sterilized hot water circuit part includes sterilized hot-water cylinder, sterilized heat-exchanger pump, steam segment, flows through the sterilisating section, finally returns sterilized hot-water cylinder successively.By rational hot water and the flow-rate ratio of product, heat recovery rate higher can be reached.
Description
【Technical field】
The present invention relates to beverage production technology field, and in particular to a kind of hot water heat exchange system of tubular type UHT heat recovery rates high
System.
【Background technology】
The hot water heat-exchange system of current tubular type UHT, as shown in Fig. 2 being wrapped successively from import to outlet in all-product line
Include compensator 1, product pump 2, degassing stages 3, sterilisating section 5, heat-recovery section 6, tower water cooling section 7 and frozen water cooling section 8；Hot water line
In successively include hot-water cylinder 9, heat-exchanger pump 10, flow through heat-recovery section 6, steam segment 13, flow through sterilisating section 5, flow through degassing stages 3, most
After return hot-water cylinder 9.Hot water after being heated using steam carries out heating sterilization to product, is cooled to filling temperature.It is section
The consumption of steam and cooling water is saved, heat-recovery section 6 is set, the heat of the product of high temperature after sterilization is reclaimed as far as possible.At present
Hot water heat exchange mode be：Hot water is transported out from hot-water cylinder 9, is introduced into heat-recovery section 6, after carrying out recuperation of heat to product, then
It is heated into steam segment 13 more slightly higher than product sterilization temperature, enters back into sterilisating section 5 and product is warming up to sterilization temperature, then enter
Enter degassing stages 3 and product heat exchange, while product is heated up, hot water temperature reduces, and is back to hot-water cylinder 9, so circulation is carried out
Heat exchange.This mode heat recovery rate is not high, if to improve heat recovery rate, the heat exchange area required for sterilisating section 5 increases,
Make product being increased by high-temperature time in sterilisating section 5, be unfavorable for keeping the local flavor of product.
【The content of the invention】
To solve the above problems, heat recovery rate can be improved it is an object of the invention to provide one kind, and reduce sterilisating section
The hot water heat-exchange system of the tubular type UHT heat recovery rates high of required heat exchange area.
To achieve the above object, the technical scheme taken of the present invention is：A kind of hot water heat exchange of tubular type UHT heat recovery rates high
System, includes that compensator, product pump, degassing stages, warming-up section, sterilisating section, heat are returned successively in all-product line from import to outlet
Section, tower water cooling section and frozen water cooling section are received, hot water line includes heat-recovery section hot water circuit part and sterilized hot water circuit portion
Point, heat-recovery section hot water circuit part includes cooling hot-water cylinder, cools down heat-exchanger pump, flow through the heat-recovery section, flow through institute successively
Warming-up section is stated, the degassing stages is flowed through, is finally returned cooling hot-water cylinder；Sterilized hot water circuit part includes sterilized hot water successively
Tank, sterilized heat-exchanger pump, steam segment, flow through the sterilisating section, finally return sterilized hot-water cylinder.
A kind of hot water heat-exchange system of the tubular type UHT heat recovery rates high in the present invention is further arranged to：The sterilisating section
Sterilization temperature sensor is provided with, the steam segment is provided with steam flow control valve.
A kind of hot water heat-exchange system of the tubular type UHT heat recovery rates high in the present invention is further arranged to：The degassing stages
Degassing temperature sensor is provided with, hot water flow regulating valve is provided with the hot water line at the degassing stages.
Compared with prior art, the present invention has the advantages that：A kind of heat of above-mentioned tubular type UHT heat recovery rates high
Water heat-exchange system, by rational hot water and the flow-rate ratio of product, can reach heat recovery rate higher.Heat recovery rate is higher,
It is fewer in the consumption of steam needed for steam heating segment, while also fewer in the cooling water needed for tower water cooling section.In addition, logical
The hot water flow of reasonable disposition sterilization hot water circuit part is crossed, can reduce the heat exchange area of sterilisating section, make product in sterilization
The flowing time of section is reduced, and product is shortened by high-temperature time in sterilisating section, is more beneficial for keeping the local flavor of product.
【Brief description of the drawings】
Fig. 1 is schematic diagram of the invention；
Fig. 2 is the schematic diagram of the hot water heat-exchange system of the tubular type UHT for being used at present described in background technology；
In Fig. 1：1st, compensator, 2, product pump, 3, degassing stages, 4, warming-up section, 5, sterilisating section, 6, heat-recovery section, 7, Ta Shui
Cooling section, 8, frozen water cooling section, 9, cooling hot-water cylinder, 10, cooling heat-exchanger pump, 11, sterilized hot-water cylinder, 12, sterilized heat-exchanger pump,
13rd, steam segment, 14, sterilization temperature sensor, 15, steam flow control valve, 16, degassing temperature sensor, 17, hot water flow adjusts
Section valve.
In Fig. 2：1st, compensator, 2, product pump, 3, degassing stages, 5, sterilisating section, 6, heat-recovery section, 7, tower water cooling section, 8,
Frozen water cooling section, 9, hot-water cylinder, 10, heat-exchanger pump, 13, steam segment.
【Specific embodiment】
A kind of hot water heat-exchange system of tubular type UHT heat recovery rates high of the present invention is made below by specific embodiment
It is described in further detail.
As shown in figure 1, a kind of hot water heat-exchange system of tubular type UHT heat recovery rates high, from import to going out in all-product line
Mouth includes compensator 1, product pump 2, degassing stages 3, warming-up section 4, sterilisating section 5, heat-recovery section 6, tower water cooling section 7 and frozen water successively
Cooling section 8, hot water line includes heat-recovery section hot water circuit part and sterilized hot water circuit part, heat-recovery section hot water circuit portion
Include point successively cooling hot-water cylinder 9, cooling heat-exchanger pump 10, flow through the heat-recovery section 6, flow through the warming-up section 4, flow through it is described
Degassing stages 3, finally return cooling hot-water cylinder 9；Sterilized hot water circuit part includes sterilized hot-water cylinder 11, sterilized heat-exchanger pump successively
12nd, steam segment 13, flow through the sterilisating section 5, finally return sterilized hot-water cylinder 11.In the present embodiment, it is provided with automatic control
Part processed, the sterilisating section 5 is provided with sterilization temperature sensor 14, and the steam segment 13 is provided with steam flow control valve 15.
The degassing stages 3 are provided with degassing temperature sensor 16, and hot water flow regulation is provided with the hot water line at the degassing stages 3
Valve 17.
Operation principle of the invention is：Product pump 2 is used for conveying products, makes product by degassing stages 3, warming-up section 4, sterilization
Section 5, heat-recovery section 6, heat exchange is carried out with hot water, degassing homogeneous, intensification, sterilization, recuperation of heat this process is completed, through overheating back
Product after receipts is cooled to filling temperature through supercooled water again.
Hot water in cooling hot-water cylinder 9 is delivered to heat-recovery section 6, warming-up section 4, degassing stages successively through supercooling heat-exchanger pump 10
After 3 carry out heat exchange with product, hot-water cylinder is returned.
Hot water in sterilized hot-water cylinder 11 is delivered to steam segment 13 by sterilized heat-exchanger pump 12, heats product to sterilized temperature
Degree, makes hot water temperature more slightly higher than product sterilization temperature, enters back into sterilisating section 5, finally returns hot-water cylinder.
Sterilization temperature sensor 14 is controlled with steam flow control valve 15, by the detected value of sterilization temperature sensor 14,
The aperture of steam flow control valve 15 is controlled, so that sterilization temperature meets requiring.
Degassing temperature sensor 16 is controlled with hot water flow regulating valve 17, by the detected value of degassing temperature sensor 16,
The aperture of control hot water flow regulating valve 17, so that hot water temperature meets the requirement of degassing homogeneous.
By rational hot water and the flow-rate ratio of product, heat recovery rate higher can be reached, such as cooling hot water is set
The hot water of the circulatory system is 1 with product flow ratio：1, the hot water of sterilized hot water cyclesystem is 2 with the flow-rate ratio of product：1.Heat
After recovery, lower from the product temperature out of heat-recovery section 6, heat recovery rate is higher, and the consumption of steam is fewer.What is needed simultaneously is cold
But water is also fewer.In addition, by the hot water flow of reasonable disposition sterilization hot water circuit part, the heat-transfer surface of sterilisating section 5 can be made
Product reduces, and product is reduced in the flowing time of sterilisating section 5, makes product being shortened by high-temperature time in sterilisating section 5, is more beneficial for
Keep the local flavor of product.
The principle and its effect of the above embodiments only illustrative the invention, and the implementation that part uses
Example, not for the limitation present invention；It should be pointed out that for the person of ordinary skill of the art, not departing from wound of the present invention
On the premise of making design, various modifications and improvements can be made, these belong to protection scope of the present invention.
Claims (3)
1. a kind of hot water heat-exchange system of tubular type UHT heat recovery rates high, includes from import to outlet flat successively in all-product line
Weighing apparatus tank, product pump, degassing stages, warming-up section, sterilisating section, heat-recovery section, tower water cooling section and frozen water cooling section, it is characterised in that：
Hot water line includes heat-recovery section hot water circuit part and sterilized hot water circuit part, and heat-recovery section hot water circuit part is wrapped successively
Include cooling hot-water cylinder, cool down heat-exchanger pump, flow through the heat-recovery section, flow through the warming-up section, flow through the degassing stages, it is last again
Return to cooling hot-water cylinder；Sterilized hot water circuit part include successively sterilized hot-water cylinder, sterilized heat-exchanger pump, steam segment, flow through it is described
Sterilisating section, finally return sterilized hot-water cylinder.
2. a kind of hot water heat-exchange system of tubular type UHT heat recovery rates high as claimed in claim 1, it is characterised in that：It is described to kill
Bacterium section is provided with sterilization temperature sensor, and the steam segment is provided with steam flow control valve.
3. a kind of hot water heat-exchange system of tubular type UHT heat recovery rates high as claimed in claim 1 or 2, it is characterised in that：It is described
Degassing stages are provided with degassing temperature sensor, and hot water flow regulating valve is provided with the hot water line at the degassing stages.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710195389.3A CN106865862A (en) | 2017-03-29 | 2017-03-29 | A kind of hot water heat-exchange system of tubular type UHT heat recovery rates high |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710195389.3A CN106865862A (en) | 2017-03-29 | 2017-03-29 | A kind of hot water heat-exchange system of tubular type UHT heat recovery rates high |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106865862A true CN106865862A (en) | 2017-06-20 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710195389.3A Pending CN106865862A (en) | 2017-03-29 | 2017-03-29 | A kind of hot water heat-exchange system of tubular type UHT heat recovery rates high |
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| Country | Link |
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| CN (1) | CN106865862A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107279657A (en) * | 2017-06-27 | 2017-10-24 | 江苏新美星包装机械股份有限公司 | A kind of microwave sterilization method and microwave sterilization machine sterilized for liquid medium |
| CN107549574A (en) * | 2017-08-15 | 2018-01-09 | 江苏新美星包装机械股份有限公司 | A kind of UHT ultra-high temperature sterilization systems with high-temperature condensation water heat-recovering function |
| CN107684687A (en) * | 2017-08-23 | 2018-02-13 | 江苏新美星包装机械股份有限公司 | A kind of retracting device and recovery method for peracetic acid disinfectant |
| CN109332290A (en) * | 2018-11-02 | 2019-02-15 | 江苏新美星包装机械股份有限公司 | A kind of material sterilizing machine |
| CN109367911A (en) * | 2018-11-02 | 2019-02-22 | 江苏新美星包装机械股份有限公司 | The cooling device of the sterilizing of RO water and material in sterile filling line |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1101500A (en) * | 1994-08-22 | 1995-04-19 | 花俊国 | Combined super high temperature sterilizing technology |
| CN101133761A (en) * | 2007-08-14 | 2008-03-05 | 李振先 | Process flow of the full-automatic ultra-high temperature sterilization machine |
| CN201422394Y (en) * | 2009-06-08 | 2010-03-17 | 佛山市海天调味食品有限公司 | Soy sauce sterilizing and disinfecting device |
| CN203262159U (en) * | 2013-05-03 | 2013-11-06 | 广西石埠乳业有限责任公司 | Dairy product ultra high temperature sterilization system |
| CN206654814U (en) * | 2017-03-29 | 2017-11-21 | 江苏新美星包装机械股份有限公司 | A kind of hot water heat-exchange system of the high heat recovery rates of tubular type UHT |
-
2017
- 2017-03-29 CN CN201710195389.3A patent/CN106865862A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1101500A (en) * | 1994-08-22 | 1995-04-19 | 花俊国 | Combined super high temperature sterilizing technology |
| CN101133761A (en) * | 2007-08-14 | 2008-03-05 | 李振先 | Process flow of the full-automatic ultra-high temperature sterilization machine |
| CN201422394Y (en) * | 2009-06-08 | 2010-03-17 | 佛山市海天调味食品有限公司 | Soy sauce sterilizing and disinfecting device |
| CN203262159U (en) * | 2013-05-03 | 2013-11-06 | 广西石埠乳业有限责任公司 | Dairy product ultra high temperature sterilization system |
| CN206654814U (en) * | 2017-03-29 | 2017-11-21 | 江苏新美星包装机械股份有限公司 | A kind of hot water heat-exchange system of the high heat recovery rates of tubular type UHT |
Non-Patent Citations (1)
| Title |
|---|
| 朱丹丹 主编, 中国农业大学出版 * |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107279657A (en) * | 2017-06-27 | 2017-10-24 | 江苏新美星包装机械股份有限公司 | A kind of microwave sterilization method and microwave sterilization machine sterilized for liquid medium |
| WO2019001037A1 (en) * | 2017-06-27 | 2019-01-03 | 江苏新美星包装机械股份有限公司 | Microwave sterilization method for sterilizing liquid and microwave sterilization machine |
| CN107549574A (en) * | 2017-08-15 | 2018-01-09 | 江苏新美星包装机械股份有限公司 | A kind of UHT ultra-high temperature sterilization systems with high-temperature condensation water heat-recovering function |
| CN107684687A (en) * | 2017-08-23 | 2018-02-13 | 江苏新美星包装机械股份有限公司 | A kind of retracting device and recovery method for peracetic acid disinfectant |
| CN109332290A (en) * | 2018-11-02 | 2019-02-15 | 江苏新美星包装机械股份有限公司 | A kind of material sterilizing machine |
| CN109367911A (en) * | 2018-11-02 | 2019-02-22 | 江苏新美星包装机械股份有限公司 | The cooling device of the sterilizing of RO water and material in sterile filling line |
| CN109332290B (en) * | 2018-11-02 | 2023-08-04 | 江苏新美星包装机械股份有限公司 | Material sterilizing machine |
| CN109367911B (en) * | 2018-11-02 | 2023-10-27 | 江苏新美星包装机械股份有限公司 | Sterilizing and material cooling device for RO water in sterile filling line |
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| PB01 | Publication | ||
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| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20170620 |
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| RJ01 | Rejection of invention patent application after publication |