CN103988902A - Milk beverage production process for recycling cooling water - Google Patents
Milk beverage production process for recycling cooling water Download PDFInfo
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- CN103988902A CN103988902A CN201410233229.XA CN201410233229A CN103988902A CN 103988902 A CN103988902 A CN 103988902A CN 201410233229 A CN201410233229 A CN 201410233229A CN 103988902 A CN103988902 A CN 103988902A
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Abstract
The invention discloses a milk beverage production process for recycling cooling water. The production process comprises a water purification technology of a front section, a milk beverage processing technology of a rear section, and a cooling water recirculating system of an auxiliary milk beverage processing technology. The water purification technology is used for filtering impurities in running water, deodorizing, decolorizing, degerming and removing ions in water to provide purified water for a boiler; the milk beverage is blended and processed by using the purified water after the water purification technology in the milk beverage processing technology; the milk beverage processing technology is cooled by using the purified water after the water purification technology in the cooling water recirculating system; one part of used cooling water is conveyed to the milk beverage processing technology; one part is conveyed to the boiler as boiler water. The used cooling water is respectively conveyed to the boiler and a chemical tank through a boiler water supply branch and a chemical tank water supply branch as boiler water and ingredient water, the utilization rate of an energy source is improved while waste of water resources is reduced, and energy consumption is reduced.
Description
technical field:
The present invention relates to drink processing technique field, particularly a kind of milk beverage production technology of cooling water cycling and reutilization.
background technology:
Along with growth in the living standard, milk beverage is subject to the general welcome of people with its high protein, high nutritive value, and apparent consumption is very huge.In the process of milk beverage, the high temperature sterilization procedure that is absolutely necessary, cooling down, finally canned afterwards.In traditional processing technology, cooling water is often drained with just going over, and better enterprise can make cooling water have a circulatory system of one's own, by cistern, cooling water can be lowered the temperature and reuses.But this mode has two shortcomings: 1, need larger cistern can make cooling water cooling naturally fully; Although 2 have reduced the consumption of water resource, still do not reduce the consumption of the energy.
summary of the invention:
Given this, be necessary to design a kind of milk beverage production technology that can reduce the cooling water cycling and reutilization of energy consumption and water resources consumption.
A milk beverage production technology for cooling water cycling and reutilization, comprises the cooling water recirculating system of the water-purifying process of leading portion, the milk beverage processing technology of back segment and auxiliary milk beverage processing technology; Wherein, water-purifying process for filter running water impurity, deodorizing, discolor, degerming ion in the water pure water to provide suitable boiler to use is provided; Milk beverage processing technology is used the pure water allotment modified milk beverage after water-purifying process; Cooling water recirculating system is used the pure water after water-purifying process to carry out water-cooled to milk beverage processing technology, and a used cooling water part is sent into milk beverage processing technology, and a part is sent into boiler as boiler feed water.
Preferably, water-purifying process comprises: water tank, filter, pure water equipment, pure water water tank; Wherein, water tank is connected with urban water supply pipeline, for subsequent technique provides running water; Running water in water tank is by being pumped into filter, water after filtration is pressed into pure water equipment and electrical conductivity is down to 10 ~ 80 μ S/cm in pure water equipment, from pure water equipment pure water out, be pumped to pure water water tank, pure water water tank is that milk beverage processing technology and cooling water recirculating system supply water.
Preferably, milk beverage processing technology comprises: material tank, material-compound tank, temporary tank, ultra high temperature sterilization equipment, pot-type equipment; Material tank is made milk beverage semi-finished product for milk powder, white sugar, stabilizing agent are dissolved in to pure water, milk beverage semi-finished product are pumped into material-compound tank fermentation, constant volume, blending, again milk beverage semi-finished product are pumped into temporary tank afterwards, finally, milk beverage semi-finished product by keep in tank pump into ultra high temperature sterilization equipment experience ultra high temperature sterilization and cooling after send into pot-type equipment, wherein ultra high temperature sterilization temperature is 125 ~ 137 ℃.
Preferably, cooling water recirculating system comprises: cooling coil, boiler, boiler water supply branch road, material tank water supply branch road; Cooling coil is arranged in ultra high temperature sterilization equipment and is used to the milk beverage after ultra high temperature sterilization to lower the temperature, the water inlet of cooling coil is connected with the feed water inlet of pure water water tank, the delivery port of cooling coil is connected with the water inlet of material tank with boiler respectively by boiler water supply branch road, material tank water supply branch road, wherein, the leaving water temperature of cooling coil is more than 55 ℃; The steam outlet of boiler is connected with ultra high temperature sterilization equipment by steam pipework.
Preferably, cooling water recirculating system also comprises purge tank, and purge tank is connected with the delivery port of cooling coil by pipeline.Purge tank is used to the equipment of every day to clean and supplies water.
Preferably, filter is tertiary filter, comprises active carbon layer, quartz sand layer and milipore filter.
Preferably, pure water equipment is reverse osmosis equipment.
The cooling water of the present invention after using sent into respectively boiler and material tank as boiler feed water and batching water by boiler water supply branch road and material tank water supply branch road, the waste that has not only reduced water resource has also improved the utilization rate of the energy simultaneously, because the leaving water temperature of cooling coil is more than 55 ℃, therefore reduced boiler and the material tank needed heat that adds originally; In order to reach this purpose, the present invention has added pure water equipment equipment to provide demineralized water for follow-up boiler feed water at water-purifying process.Further, purge tank is connected with the delivery port of cooling coil by pipeline, like this, after the dairy products processing of last batch of every day, the cooling water after using is sent into purge tank and with cleaning equipment, removed the consumption of heated wash water temperature from.
accompanying drawing explanation:
Accompanying drawing 1 is the apparatus and process figure of milk beverage production technology of the cooling water cycling and reutilization of a width better embodiment.
In figure: water tank 11, filter 12, pure water equipment 13, pure water water tank 14, material tank 21, material-compound tank 22, temporary tank 23, ultra high temperature sterilization equipment 24, pot-type equipment 25, cooling coil 31, boiler 32, boiler water supply branch road 33, material tank water supply branch road 34, steam pipework 35, purge tank 36.
the specific embodiment:
As shown in Figure 1, a kind of milk beverage production technology of cooling water cycling and reutilization, comprises the cooling water recirculating system of the water-purifying process of leading portion, the milk beverage processing technology of back segment and auxiliary milk beverage processing technology; Wherein, water-purifying process for filter running water impurity, deodorizing, discolor, degerming ion in the water pure water to provide suitable boiler to use is provided; Milk beverage processing technology is used the pure water allotment modified milk beverage after water-purifying process; Cooling water recirculating system is used the pure water after water-purifying process to carry out water-cooled to milk beverage processing technology, and a used cooling water part is sent into milk beverage processing technology, and a part is sent into boiler 32 as boiler feed water.
In the present embodiment, water-purifying process comprises: water tank 11, filter 12, pure water equipment 13, pure water water tank 14; Wherein, water tank 11 is connected with urban water supply pipeline, for subsequent technique provides running water; Running water in water tank 11 is by being pumped into filter 12, water after filtration is pressed into pure water equipment 13 and 13 li of pure water equipments, electrical conductivity is down to 10 ~ 80 μ S/cm, from pure water equipment 13 pure water out, be pumped to pure water water tank 14, pure water water tank 14 is that milk beverage processing technology and cooling water recirculating system supply water.
In the present embodiment, milk beverage processing technology comprises: material tank 21, material-compound tank 22, temporary tank 23, ultra high temperature sterilization equipment 24, pot-type equipment 25; Material tank 21 is made milk beverage semi-finished product for milk powder, white sugar, stabilizing agent are dissolved in to pure water, milk beverage semi-finished product are pumped into material-compound tank 22 fermentations, constant volume, blending, again milk beverage semi-finished product are pumped into afterwards to temporary tank 23, finally, milk beverage semi-finished product by keep in tank 23 pump into ultra high temperature sterilization equipment 24 experience ultra high temperature sterilizations and cooling after send into canned 25 equipment, wherein ultra high temperature sterilization temperature is 125 ~ 137 ℃.
In the present embodiment, cooling water recirculating system comprises: cooling coil 31, boiler 32, boiler water supply branch road 33, material tank water supply branch road 34; Cooling coil 31 is arranged in ultra high temperature sterilization equipment 24 and is used to the milk beverage after ultra high temperature sterilization to lower the temperature, the water inlet of cooling coil 31 is connected with the feed water inlet of pure water water tank 14, the delivery port of cooling coil 31 is connected with the water inlet of material tank 21 with boiler 32 respectively by boiler water supply branch road 33, material tank water supply branch road 34, wherein, the leaving water temperature of cooling coil 31 is more than 55 ℃; The steam outlet of boiler 32 is connected with ultra high temperature sterilization equipment 24 by steam pipework 35.
In the present embodiment, cooling water recirculating system also comprises purge tank 36, and purge tank 36 is connected with the delivery port of cooling coil 31 by pipeline.Purge tank 36 is used to the equipment of every day to clean and supplies water.Filter 12 is tertiary filter, comprises active carbon layer, quartz sand layer and milipore filter.Pure water equipment 13 is reverse osmosis equipment.
Claims (7)
1. a milk beverage production technology for cooling water cycling and reutilization, is characterized in that: the cooling water recirculating system that comprises the water-purifying process of leading portion, the milk beverage processing technology of back segment and auxiliary milk beverage processing technology; Wherein, water-purifying process for filter running water impurity, deodorizing, discolor, degerming ion in the water pure water to provide suitable boiler to use is provided; Milk beverage processing technology is used the pure water allotment modified milk beverage after water-purifying process; Cooling water recirculating system is used the pure water after water-purifying process to carry out water-cooled to milk beverage processing technology, and a used cooling water part is sent into milk beverage processing technology, and a part is sent into boiler as boiler feed water.
2. the milk beverage production technology of cooling water cycling and reutilization as claimed in claim 1, is characterized in that: water-purifying process comprises: water tank, filter, pure water equipment, pure water water tank; Water tank is connected with urban water supply pipeline, for subsequent technique provides running water; Running water in water tank is by being pumped into filter, water after filtration is pressed into pure water equipment and electrical conductivity is down to 10 ~ 80 μ S/cm in pure water equipment, from pure water equipment pure water out, be pumped to pure water water tank, pure water water tank is that milk beverage processing technology and cooling water recirculating system supply water.
3. as the milk beverage production technology of claim 1 or cooling water cycling and reutilization claimed in claim 2, it is characterized in that: milk beverage processing technology comprises: material tank, material-compound tank, temporary tank, ultra high temperature sterilization equipment, pot-type equipment; Material tank is made milk beverage semi-finished product for milk powder, white sugar, stabilizing agent are dissolved in to pure water, milk beverage semi-finished product are pumped into material-compound tank fermentation, constant volume, blending, again milk beverage semi-finished product are pumped into temporary tank afterwards, finally, milk beverage semi-finished product by keep in tank pump into ultra high temperature sterilization equipment experience ultra high temperature sterilization and cooling after send into pot-type equipment.
4. the milk beverage production technology of cooling water cycling and reutilization as claimed in claim 3, is characterized in that: cooling water recirculating system comprises: cooling coil, boiler, boiler water supply branch road, material tank water supply branch road; Wherein, cooling coil is arranged in ultra high temperature sterilization equipment and is used to the milk beverage after ultra high temperature sterilization to lower the temperature, the water inlet of cooling coil is connected with the feed water inlet of pure water water tank, the delivery port of cooling coil is connected with the water inlet of material tank with boiler respectively by boiler water supply branch road, material tank water supply branch road, and the steam outlet of boiler is connected with ultra high temperature sterilization equipment by steam pipework.
5. the milk beverage production technology of cooling water cycling and reutilization as claimed in claim 4, is characterized in that: cooling water recirculating system also comprises purge tank, and purge tank is connected with the delivery port of cooling coil by pipeline.
6. the milk beverage production technology of cooling water cycling and reutilization as claimed in claim 2, is characterized in that: filter is tertiary filter, comprises active carbon layer, quartz sand layer and milipore filter.
7. the milk beverage production technology of cooling water cycling and reutilization as claimed in claim 2, is characterized in that: pure water equipment is reverse osmosis equipment.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410233229.XA CN103988902B (en) | 2014-05-29 | 2014-05-29 | The milk beverage production technology of cooling water cycling and reutilization |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410233229.XA CN103988902B (en) | 2014-05-29 | 2014-05-29 | The milk beverage production technology of cooling water cycling and reutilization |
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| Publication Number | Publication Date |
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| CN103988902A true CN103988902A (en) | 2014-08-20 |
| CN103988902B CN103988902B (en) | 2015-11-18 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201410233229.XA Expired - Fee Related CN103988902B (en) | 2014-05-29 | 2014-05-29 | The milk beverage production technology of cooling water cycling and reutilization |
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Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101182088A (en) * | 2007-11-19 | 2008-05-21 | 广西工院糖业科技有限责任公司 | Novel technique for quality-preservation treatment of sugar plant circulation cooling water |
| CN201481813U (en) * | 2009-08-06 | 2010-05-26 | 成都锦华药业有限责任公司 | Cooling water circulating and using device |
| CN202232780U (en) * | 2011-09-26 | 2012-05-30 | 江苏春晖乳业有限公司 | Full-line production and processing apparatus for milk production line |
| CN202785845U (en) * | 2012-09-22 | 2013-03-13 | 黑龙江集贤亿丰油脂有限公司 | Processing device of cooling water in oil processing extraction workshop |
-
2014
- 2014-05-29 CN CN201410233229.XA patent/CN103988902B/en not_active Expired - Fee Related
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101182088A (en) * | 2007-11-19 | 2008-05-21 | 广西工院糖业科技有限责任公司 | Novel technique for quality-preservation treatment of sugar plant circulation cooling water |
| CN201481813U (en) * | 2009-08-06 | 2010-05-26 | 成都锦华药业有限责任公司 | Cooling water circulating and using device |
| CN202232780U (en) * | 2011-09-26 | 2012-05-30 | 江苏春晖乳业有限公司 | Full-line production and processing apparatus for milk production line |
| CN202785845U (en) * | 2012-09-22 | 2013-03-13 | 黑龙江集贤亿丰油脂有限公司 | Processing device of cooling water in oil processing extraction workshop |
Non-Patent Citations (2)
| Title |
|---|
| 李维国等: "关于冷却水二次利用的探讨", 《中国乳品工业》, vol. 20, no. 01, 28 February 1992 (1992-02-28), pages 33 - 34 * |
| 陈德放等: "乳制品加工废水的综合利用", 《上海环境科学》, vol. 8, no. 04, 30 April 1989 (1989-04-30), pages 7 - 36 * |
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| CN103988902B (en) | 2015-11-18 |
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