CN109673885A - A kind of method of full embrane method inspissated juice - Google Patents
A kind of method of full embrane method inspissated juice Download PDFInfo
- Publication number
- CN109673885A CN109673885A CN201910012053.8A CN201910012053A CN109673885A CN 109673885 A CN109673885 A CN 109673885A CN 201910012053 A CN201910012053 A CN 201910012053A CN 109673885 A CN109673885 A CN 109673885A
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- China
- Prior art keywords
- membrane
- juice
- ultrafiltration
- present
- inspissated juice
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Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L2/00—Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
- A23L2/02—Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation containing fruit or vegetable juices
- A23L2/08—Concentrating or drying of juices
- A23L2/082—Concentrating or drying of juices by membrane processes
- A23L2/087—Concentrating or drying of juices by membrane processes by ultrafiltration, microfiltration
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L2/00—Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
- A23L2/42—Preservation of non-alcoholic beverages
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- Engineering & Computer Science (AREA)
- Health & Medical Sciences (AREA)
- Nutrition Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Water Supply & Treatment (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The invention discloses a kind of methods of full embrane method inspissated juice, belong to inspissated juice method field.There are energy consumption high-tech for the existing inspissated juice method of the present invention.The method of the present invention: Step 1: Fresh Juice coarse filtration is handled;Step 2: then obtaining dialyzate and concentrate by ultrafiltration membrance filter, concentrate is collected;Step 3: the dialyzate heating that step 2 obtains, temperature is constant, then membrane distillation;Step 4: repetitive operation step 3 until volume becomes the 4/5 ~ 9/10 of feed volume, that is, completes concentration.The method of the present invention is not necessarily to add a little more heats to equipment, can reduce the heat that method of evaporating loses in the process.The method of the present invention greatly reduces fruit juice water content, can remove 99.999% bacterium, and the taste of juice of preparation is good.The present invention is easily operated automatically, and occupied area is small, can effectively remove bacterium, and low energy consumption, using waste heat of plant.
Description
Technical field
The invention belongs to inspissated juice method fields, and in particular to a kind of method of full embrane method inspissated juice.
Background technique
With the quickening of agricultural industrialization process and continuing to optimize for agricultural cultivation structure, inspissated juice product is increasingly
By consumers, while also causing China's orchard worker's extensive concern, there is good development prospect.Currently, concentration of juices work
Skill substantially there are two types of;One kind is multiple-effect evaporation technique, and one kind is filtration-reverse osmosis integrated membrane process technique.Since inspissated juice is
Drink directly affects consumer health, needs sterilization unit using evaporation technology, meanwhile, to guarantee as far as possible in evaporation process low
Temperature prevents nutriment in inspissated juice to be lost, therefore generally uses high pressure low temperature sterilization method, to containers demand height.Evaporation
A large amount of thermal energy are needed, therefore, this kind of method energy consumption is generally higher.
Filtration-reverse osmosis integrated membrane process, on the one hand, can effectively be gone using the ultra filtration unit in filtration-reverse osmosis technique
Except substances such as suspended particulate, bacterium, viruses, while retaining nutritional ingredient.Reverse osmosis process can effective inspissated juice, however,
Reverse osmosis process needs higher operating pressure, consumes energy still higher.
Summary of the invention
The present invention solves the problems, such as existing inspissated juice method, and there are energy consumption high-tech;And provide full embrane method inspissated juice
Method.
Fresh Juice successively passes through coarse filtration unit in the method for the present invention and ultra filtration unit removes oil removal and bacterium, then passes through
The concentration of membrane distillation system is crossed, realizes low temperature inspissated juice purpose.
To solve the above problems, the method for full embrane method inspissated juice carries out in the steps below in the present invention:
Step 1: Fresh Juice coarse filtration is handled;
Step 2: then obtaining dialyzate and concentrate by ultrafiltration membrance filter, concentrate is collected;
Step 3: the dialyzate heating that step 2 obtains, temperature is constant, then membrane distillation;
Step 4: repetitive operation step 3 is until volume becomes the 4/5 ~ 9/10 of feed volume, and complete concentration.
It further limits, ultrafiltration membrane described in step 2 is polyvinylidene fluoride (PVDF) ultrafiltration membrane, polyacrylonitrile ultrafiltration film, polyether sulfone
Ultrafiltration membrane or ceramic super-filtering film, molecular weight cut off 100,000 ~ 200,000;The kit form of ultrafiltration membrane is hollow-fibre membrane
Component, rolled membrane module, tubular membrane component or plate film assembly.
It further limits, temperature is constant at 40-80 DEG C in step 3.
Further limit, membrane distillation is carried out using following forms in step 3: direct contact membrane distillation, absorbing film steam
It evaporates, vacuum membrane distillation or gap field orientation.
It further limits, membrane module form is taken in plate type membrane assembly, or use during membrane distillation in step 3
Hollow fiber formula membrane module, or using there is the Kynoar of surface super hydrophobic performance, in polyacrylonitrile polymeric membrane it is a kind of,
Or using the ceramic membrane with ultra-hydrophobicity.
In inventive film distillation process, material liquid is by the feed side of the membrane module of hydrophobic property, and moisture is with vapor shape
Formula penetrates film, surveys and condenses in infiltration, constantly recycles, to reach concentration purpose.
The method of the present invention makes 5 ~ 10 times of concentration of juices;The energy consumption in evaporation and crystal process is reduced, is easily operated automatically,
Occupied area is small, and low energy consumption, and handling are simple.
The method of the present invention is mild due to operating condition, it is not necessary that equipment plus crosses the more heat of point, can reduce evaporation
The heat that method is lost in the process.Solar energy confession can also be used in the exhaust-heat heating that upstream factory can be used in process of the present invention
Heat, operating condition is mild, is a kind of environmentally protective novel concentration technology.
The present invention is complete, and embrane method inspissated juice can effectively remove suspended matter and bacterium, greatly reduce fruit juice water content, energy
Enough the bacterium of removal 99.999%, the taste of juice of preparation are good.
Specific embodiment
Embodiment 1: the method for full embrane method inspissated juice carries out in the steps below:
Step 1: fresh squeezing grape juice is filtered processing using rough filtering device, suspended solid is filtered out;
Step 2: ultrafiltration membrane is hydrophilic polyethersulfone hollow fiber film assembly, and molecular weight cut off is then by ultrafiltration membrance filter
150,000, intake pressure 0.2MPa, water yield 10m3/ d obtains dialyzate and concentrate, discharges after concentrate processing;
Step 3: the dialyzate that step 2 obtains is heated to 50 DEG C, constant 50 DEG C of temperature, then membrane distillation;
Membrane distillation uses ultra-hydrophobic polyvinylidene fluoride membrane component, and the dialyzate of certain temperature passes through the feed side of membrane module, contact
Angle 160o, moisture penetrates film with vapor form, in infiltration survey generation condensation (cold fluid is water (0-3 DEG C)), water yield 10m3/
d;
(reach concentration purpose) Step 4: repetitive operation step 3 to volume become feed volume 7/8 until until, and complete
It extracts.
Step 3 vapor utilizes downstream vacuum pump, and after condensation, vapor becomes water, can recycle, and is concentrated
Fruit juice.The present embodiment method high degree of automation, low energy consumption, and degerming rate is up to 99.999%, by concentration of juices to fresh squeezing grape juice
It is octuple, yield can be adjusted by control membrane area, and low operation temperature not be related to high pressure.
Claims (6)
1. a kind of method of full embrane method inspissated juice, it is characterised in that the extracting method carries out in the steps below:
Step 1: Fresh Juice coarse filtration is handled;
Step 2: then obtaining dialyzate and concentrate by ultrafiltration membrance filter, concentrate is collected;
Step 3: the dialyzate heating that step 2 obtains, temperature is constant, then membrane distillation;
Step 4: repetitive operation step 3 until volume becomes the 4/5 ~ 9/10 of feed volume, that is, completes concentration.
2. extracting method according to claim 1, it is characterised in that ultrafiltration membrane described in step 2 is Kynoar ultrafiltration
Film, polyacrylonitrile ultrafiltration film, poly (ether-sulfone) ultrafiltration membrane or ceramic super-filtering film, molecular weight cut off 100,000 ~ 200,000.
3. extracting method according to claim 2, it is characterised in that the kit form of ultrafiltration membrane is hollow fiber film assembly, volume
Formula membrane module, tubular membrane component or plate film assembly.
4. extracting method according to claim 1, it is characterised in that temperature is constant at 40-80 DEG C in step 3.
5. according to claim 1 or 3 extracting methods, it is characterised in that membrane distillation is carried out using following forms in step 3:
Direct contact membrane distillation absorbs membrane distillation, vacuum membrane distillation or gap field orientation.
6. extracting method according to claim 4, it is characterised in that membrane module form is taken during membrane distillation in step 3
Plate type membrane assembly, perhaps using hollow fiber form membrane module or using have surface super hydrophobic performance Kynoar,
It is a kind of in polyacrylonitrile polymeric membrane, or using the ceramic membrane with ultra-hydrophobicity.
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CN201910012053.8A CN109673885A (en) | 2019-01-07 | 2019-01-07 | A kind of method of full embrane method inspissated juice |
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CN201910012053.8A CN109673885A (en) | 2019-01-07 | 2019-01-07 | A kind of method of full embrane method inspissated juice |
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CN109673885A true CN109673885A (en) | 2019-04-26 |
Family
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CN201910012053.8A Pending CN109673885A (en) | 2019-01-07 | 2019-01-07 | A kind of method of full embrane method inspissated juice |
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Citations (6)
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---|---|---|---|---|
CN101941937A (en) * | 2010-08-20 | 2011-01-12 | 英杰华纳(厦门)生物工程有限公司 | Method for concentrating 5-hydroxytrophan |
CN103537191A (en) * | 2013-10-24 | 2014-01-29 | 哈尔滨工业大学 | Method for concentrating glucose by using membrane distillation |
CN104211245A (en) * | 2013-06-03 | 2014-12-17 | 洁海瑞泉膜技术(北京)有限公司 | Treatment method of membrane-process concentrated solution of garbage leachate |
CN107549531A (en) * | 2017-09-08 | 2018-01-09 | 安徽阜南常晖食品有限公司 | A kind of processing method for concentrating pineapple juice |
US20180118585A1 (en) * | 2015-04-23 | 2018-05-03 | Aquatech International, Llc | Method and Apparatus for Advanced Vacuum Membrane Distillation |
CN108479406A (en) * | 2018-06-19 | 2018-09-04 | 北京电子科技职业学院 | A kind of positive infiltration-membrane distillation coupling concentration of juices device and method for concentration |
-
2019
- 2019-01-07 CN CN201910012053.8A patent/CN109673885A/en active Pending
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101941937A (en) * | 2010-08-20 | 2011-01-12 | 英杰华纳(厦门)生物工程有限公司 | Method for concentrating 5-hydroxytrophan |
CN104211245A (en) * | 2013-06-03 | 2014-12-17 | 洁海瑞泉膜技术(北京)有限公司 | Treatment method of membrane-process concentrated solution of garbage leachate |
CN103537191A (en) * | 2013-10-24 | 2014-01-29 | 哈尔滨工业大学 | Method for concentrating glucose by using membrane distillation |
US20180118585A1 (en) * | 2015-04-23 | 2018-05-03 | Aquatech International, Llc | Method and Apparatus for Advanced Vacuum Membrane Distillation |
CN107549531A (en) * | 2017-09-08 | 2018-01-09 | 安徽阜南常晖食品有限公司 | A kind of processing method for concentrating pineapple juice |
CN108479406A (en) * | 2018-06-19 | 2018-09-04 | 北京电子科技职业学院 | A kind of positive infiltration-membrane distillation coupling concentration of juices device and method for concentration |
Non-Patent Citations (2)
Title |
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周柏青: "《全膜水处理技术》", 31 January 2006, 中国电力出版社 * |
张增志,等: "《中国战略性新兴产业.新材料,环境工程材料》", 30 November 2018, 中国铁道出版社 * |
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