CN105639350A - Machining method capable of prolonging using time of clear apple juice concentrate resin - Google Patents
Machining method capable of prolonging using time of clear apple juice concentrate resin Download PDFInfo
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- CN105639350A CN105639350A CN201610022853.4A CN201610022853A CN105639350A CN 105639350 A CN105639350 A CN 105639350A CN 201610022853 A CN201610022853 A CN 201610022853A CN 105639350 A CN105639350 A CN 105639350A
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- resin
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- series connection
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- apple juice
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- 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
-
- 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
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- Health & Medical Sciences (AREA)
- Nutrition Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Non-Alcoholic Beverages (AREA)
Abstract
The invention discloses a machining method capable of prolonging the using time of clear apple juice concentrate resin. According to the method, based on the clear apple juice concentrate production process, the resin procedure is further optimized and improved to enable color value to be increased by about 5% during clear apple juice concentrate processing and using time to be prolonged by 30 hours, energy saving and consumption reduction effects are remarkable, clear apple juice concentrate production cost is reduced greatly, and then it is ensured that an apple juice beverage can be accepted by ordinary consumers with reasonable price.
Description
Technical field
The present invention is on concentrated apple clear juice Process ba-sis, to improve product colour further, extends resin and uses the time, reduce the process modification for the purpose of consuming, belong to fruit juice production technical field.
Background technology
In recent years, agricultural product price generally goes up, the processing method of conventional concentrated apple clear juice, in order to ensure that colour reaches requirement (> 84%), heat-proof acid-resistant bacterium does not exceed standard, and resin life cycle controls at 18-24 hour, cleans costly (2000-3000 unit) every time, cause that processing cost is of a relatively high, thus concentrated apple clear juice processing cost remains high.
Summary of the invention
The present invention is on the basis of concentrated apple clear juice manufacturing technique, by resin operation is optimized further, improves, concentrated apple clear juice is made to add colour raising in man-hour about 5%, use time lengthening 30 hours, energy conservation and consumption reduction effects is notable, the production cost of concentrated apple clear juice is greatly lowered, and then guarantees that apple juice can enough in reasonable cost be accepted by vast ordinary consumer.
The technical scheme is that the further improvement done on the basis that concentrated apple clear juice is processed, it mainly improves step and when scheme is achieved in that resin absorption, two groups of resin series connection are used, first group of resin uses to 24 hours (basic absorption is saturated), first group of resin is cleaned, again by second group of resin and the 3rd group of resin series connection (advanced second group of resin), when second group of resin re-use 24 little time (basic absorption saturated), second group of resin is cleaned, again the 3rd group is connected with first group (advanced 3rd group of resin), such iterative cycles, give full play to the absorbability of resin, both ensure that the color value of resin outlet, also extend resin and use the time, reduce processing cost.
Resin absorption mode after described improvement, its feature includes:
A, resin series connection: two groups of resins series connection are used, one group of advanced saturated rear cleaning, remain two groups of series connection and use, so repeatedly;
B, resin are connected: fruit juice is through twice absorption of resin, and colour improves 4-6%;
C, resin are connected: resin uses time lengthening 30 hours, clean the frequency and reduce, reduce processing cost.
The concrete grammar of described resin series connection, resin described in step A connect first group of resin saturated time, second group of resin also unsaturation, clean first group of resin, second group of resin continues series connection and uses; Exporting colour described in step B and control more than 88%, turbidity controls at below 2.0NTU; Often organize resin described in step C and use no more than 50 hours.
One significant contribution of the present invention is in that to adopt series connection to use resin can give full play to resin absorption ability, improve colour, series connection simultaneously uses and extends the use time, reduces and cleans cost it addition, the quality of line and final products is without any adverse effect after being used by resin series connection. Other procedure of processing parameters except resin need not change, being greatly lowered of production cost.
Detailed description of the invention
Embodiment 1
1, raw material selection: rotting rate��3% after selection.
2, broken:
2-1, Fructus Mali pumilae to add pulp enzyme 80ppm, enzymolysis 1 hour when broken, and broken Task-size Controlling is at 2��5 millimeters;
2-2, while broken raw material according to raw apple pulp 80ppm ratio add pulp enzyme, pulp enzyme is diluted to the aqueous solution of 5-20% before interpolation, is applied directly in pulp by dosing pump while broken raw material;
3, extracting juice:
3-1, by the pulp after broken, squeeze through squeezer.
3-2, by squeezing after marc add water according to 1:2 ratio, carry out twice pressing.
3-3, twice squeezing juice is mixed
4, front bar kills:
4-1, by Fructus Mali pumilae squeezing juice through front bar kill (110 �� 1 DEG C) keep 30 seconds
Squeezing juice after 4-2, front bar sterilization is with being cooled to 54 �� 1 DEG C;
5, enzymolysis: by the Fructus Mali pumilae squeezing juice through boiling cooling, adding pectase, 50ml/T Amylase Hydrolysis 1 hour according to 40ml/T, temperature keeps 53 �� 1 DEG C;
6, ultrafiltration: by the Sucus Mali pumilae after enzymolysis through ultrafilter ultrafiltration, detects turbidity 0.5NTU;
7, resin absorption: by the Sucus Mali pumilae after ultrafiltration through resin absorption, resin runs 20 hours, the colour 84.7% of detection series connection outlet, turbidity 0.7NTU.
8, rear bar kills: by the Sucus Mali pumilae after resin absorption, kills (120 �� 1 DEG C) sterilization through bar later, keeps 30 seconds.
9, concentration: be 70.10% to apple clear juice evaporation and concentration to solubility solid content by concentration evaporator, detects colour 81.4%, turbidity 0.9NTU.
10, fill stores: the Sucus Mali pumilae after concentration is cooled to 25 DEG C, filters through sheet frame cardboard filter, by aseptic filler fill, and 0-5 DEG C of storage after fill.
Embodiment 2
1, raw material selection: rotting rate��3% after selection.
2, broken:
2-1, Fructus Mali pumilae to add pulp enzyme 80ppm, enzymolysis 1 hour when broken, and broken Task-size Controlling is at 2��5 millimeters;
2-2, while broken raw material according to raw apple pulp 80ppm ratio add pulp enzyme, pulp enzyme is diluted to the aqueous solution of 5-20% before interpolation, is applied directly in pulp by dosing pump while broken raw material;
3, extracting juice:
3-1, by the pulp after broken, squeeze through squeezer.
3-2, by squeezing after marc add water according to 1:2 ratio, carry out twice pressing.
3-3, twice squeezing juice is mixed
4, front bar kills:
4-1, by Fructus Mali pumilae squeezing juice through front bar kill (110 �� 1 DEG C) keep 30 seconds
Squeezing juice after 4-2, front bar sterilization is with being cooled to 54 �� 1 DEG C;
5, enzymolysis: by the Fructus Mali pumilae squeezing juice through boiling cooling, adding pectase, 50ml/T Amylase Hydrolysis 1 hour according to 40ml/T, temperature keeps 53 �� 1 DEG C;
6, ultrafiltration: by the Sucus Mali pumilae after enzymolysis through ultrafilter ultrafiltration, detects turbidity 0.6NTU;
7, resin absorption:
7-1, by the Sucus Mali pumilae after ultrafiltration through the 1st group of resin absorption;
7-2, by the Sucus Mali pumilae after the 1st group of resin absorption through the 2nd group of resin absorption, the 1st group of resin runs 20 hours, the colour 89.5% of detection series connection outlet, and turbidity 0.8NTU cleans the 1st group of resin, connects second group with the 3rd group of resin, be continuing with;
7-3, second group of resin run 50 hours time, the colour 89.0% of detection series connection outlet, turbidity 0.7NTU.
8, rear bar kills: by the Sucus Mali pumilae after resin absorption, kills (120 �� 1 DEG C) sterilization through bar later, keeps 30 seconds.
9, concentration: be 70.16% to apple clear juice evaporation and concentration to solubility solid content by concentration evaporator, detects colour 85.3%, turbidity 0.8NTU.
10, fill stores: the Sucus Mali pumilae after concentration is cooled to 25 DEG C, filters through sheet frame cardboard filter, by aseptic filler fill, and 0-5 DEG C of storage after fill.
Being seen by two above example, connecting through resin, the indexs such as the product colour after concentration improves 4%, turbidity are satisfied by requirement, and the cleaning frequency of resin extends 30 hours, reduce resin and clean cost.
The embodiment that the present invention enumerates is intended to further illustrate process, and the scope of the present invention is not constituted any restriction, reach improve product colour and all can reach the effect improving product colour, reduction cleaning cost of the present invention via the method described in claims of the present invention 1-9 by the embodiment of the present invention.
Claims (5)
1. one kind extends the processing method that concentrated apple clear juice resin uses the time, it is characterised in that during resin absorption, two groups of resin series connection is used, and makes concentrated apple clear juice add colour raising in man-hour about 5%, uses time lengthening 30 hours.
2. according to claim 1, its feature includes:
A, resin series connection: two groups of resins series connection are used, one group of advanced saturated rear cleaning, remain two groups of series connection and use, so repeatedly;
B, resin are connected: fruit juice is through twice absorption of resin, and colour improves 4-6%;
C, resin are connected: resin uses time lengthening 30 hours, clean the frequency and reduce, reduce processing cost.
3. according to claim 2, resin described in step A connect first group of resin saturated time, second group of resin also unsaturation, clean first group of resin, second group of resin continues series connection and uses.
4. according to claim 2, exporting colour and control more than 88% described in step B, turbidity controls at below 2.0NTU.
5. according to claim 2, often organize resin described in step C and use no more than 50 hours.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610022853.4A CN105639350A (en) | 2016-01-14 | 2016-01-14 | Machining method capable of prolonging using time of clear apple juice concentrate resin |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610022853.4A CN105639350A (en) | 2016-01-14 | 2016-01-14 | Machining method capable of prolonging using time of clear apple juice concentrate resin |
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| CN105639350A true CN105639350A (en) | 2016-06-08 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610022853.4A Pending CN105639350A (en) | 2016-01-14 | 2016-01-14 | Machining method capable of prolonging using time of clear apple juice concentrate resin |
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Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101229207A (en) * | 2008-01-30 | 2008-07-30 | 南开大学 | Decolor refined technology of notoginseng total saponin duolite method |
| CN202226866U (en) * | 2011-09-20 | 2012-05-23 | 山东福田药业有限公司 | Wood sugar hydrolysate decoloring system device |
-
2016
- 2016-01-14 CN CN201610022853.4A patent/CN105639350A/en active Pending
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101229207A (en) * | 2008-01-30 | 2008-07-30 | 南开大学 | Decolor refined technology of notoginseng total saponin duolite method |
| CN202226866U (en) * | 2011-09-20 | 2012-05-23 | 山东福田药业有限公司 | Wood sugar hydrolysate decoloring system device |
Non-Patent Citations (3)
| Title |
|---|
| 杜连启主编: "《甘薯综合加工技术》", 28 February 2014, 中国轻工业出版社 * |
| 王思新: "树脂吸附法提高苹果浓缩清汁色值和透光率研究", 《果蔬学报》 * |
| 王玉亭主编: "《生物反应及制药单元操作技术》", 30 September 2014, 中国轻工业出版社 * |
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Application publication date: 20160608 |
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