CN103876240A - Processing method for debittering concentrated cloudy lemon juice - Google Patents
Processing method for debittering concentrated cloudy lemon juice Download PDFInfo
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- CN103876240A CN103876240A CN201410085637.5A CN201410085637A CN103876240A CN 103876240 A CN103876240 A CN 103876240A CN 201410085637 A CN201410085637 A CN 201410085637A CN 103876240 A CN103876240 A CN 103876240A
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- juice
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- enzymolysis
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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
- A23L2/70—Clarifying or fining of non-alcoholic beverages; Removing unwanted matter
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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
- A23L2/70—Clarifying or fining of non-alcoholic beverages; Removing unwanted matter
- A23L2/72—Clarifying or fining of non-alcoholic beverages; Removing unwanted matter by filtration
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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
- A23L2/70—Clarifying or fining of non-alcoholic beverages; Removing unwanted matter
- A23L2/84—Clarifying or fining of non-alcoholic beverages; Removing unwanted matter using microorganisms or biological material, e.g. enzymes
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- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Microbiology (AREA)
- Molecular Biology (AREA)
- Zoology (AREA)
- Non-Alcoholic Beverages (AREA)
- Apparatuses For Bulk Treatment Of Fruits And Vegetables And Apparatuses For Preparing Feeds (AREA)
Abstract
The invention discloses a processing method for debittering concentrated cloudy lemon juice. The method comprises the following processes: (1) juicing; (2) performing pasteurization; (3) performing enzymolysis; (4) performing ultrafiltration; (5) debittering resins; (6) mixing; (7) concentrating; and (8) performing sterile cold filling, wherein the limonin removal rate of the clear juice subjected to ultrafiltration is over 95 percent, and the content of limonin in the debittered concentrated cloudy lemon juice is below 5ppm. In the enzymolysis process, the viscosity of the juice is properly reduced by determining the addition amount of pectinase, the amount of the clear juice used by the resin is guaranteed by adopting a three-stage filtering ultrafiltration system, insoluble substances in the juice are completely remained, a ratio of the enzymolysis juice subjected to ultrafiltration to the total juice amount is controlled, the limonin in the clear juice subjected to ultrafiltration is removed by adopting a debittering resin, and the several components are effectively matched with one another, so that the content of the limonin in the concentrated cloudy lemon juice is below 5ppm. According to the process for debittering the concentrated cloudy lemon juice, the debittering efficiency is improved, the service life of the resin is prolonged, the processing time is greatly reduced, the yield is improved, and the production cost is reduced.
Description
Technical field:
The present invention relates to lemon extract deep process technology field, is the processing method of the turbid juice debitterize of a kind of concentrated lemon specifically.
Background technology: lemon can make to contain in juice a large amount of bitter substances in process is squeezed the juice in processing, cause the concentrated lemon juice processing to have certain bitter taste, domestic do not have the enterprise that processes concentrated lemon juice merely, the external concentrated conventional debitterize of the turbid juice of lemon generally uses movable bed resin debitterize, enzyme preparation suppresses bitterness value method, the movable bed resin debitterized technique debitterize time is long, flesh-content to turbid juice has a certain impact, in debitterize process, can attach some pulp, and the regeneration of resin bothers, the consumption of water is large, enzyme preparation suppresses just to have covered bitter taste, in practice bitter taste is not reduced.
Summary of the invention:
The object of the invention is to overcome that movable bed resin directly carries out all restrictions of debitterize to turbid juice and processing method that the turbid juice debitterize of a kind of concentrated lemon is provided, mainly solve a debitterize difficult problem for the turbid juice of existing concentrated lemon.
In order to achieve the above object, the present invention is achieved in that
A processing method for the turbid juice debitterize of concentrated lemon, comprises following operation:
(1), squeeze the juice: the technique of squeezing the juice routinely, makes lemon juice;
(2), bar kills: lemon juice is killed through routine bar;
(3), enzymolysis: the lemon juice after bar kills is cooled to 50~55 DEG C to enter enzymatic vessel, doses pectase and stirs, and pectase addition is 10000~12000ml/10 ton tank, and enzymolysis time 15~20 minutes, makes enzymolysis juice;
(4), ultrafiltration: enzymolysis juice is filtered by three grades of ultrafiltration systems, and high pressure is 4.0~5.5Mpa, and low pressure is 0.2~1.0Mpa, and a secondary internal circulating load is 70~75m
3/ hour, three grades of internal circulating loads are 100~105 m
3/ hour, total clear juice amount is 2.8~4.0 m
3/ hour, super filtered juice amount is 88~90% of total enzymolysis juice amount;
(5), resin debitterize: adopt resin column to carry out debitterize in the clear juice of ultra filtration, resin content is 2.7~3.2 m
3/ post, super filtered juice is taking flow velocity as 3.0~4.0 m
3/ hour by resin, resin operation 17~22 hours, makes the clear juice of debitterize lemon;
(6), mix: the insoluble matter that the clear juice of lemon after debitterize and ultrafiltration are held back and the enzymolysis juice 5~10% without ultrafiltration, in the stainless cylinder of steel that is provided with agitator, stir, make the turbid juice of lemon;
(7), concentrated: by turbid lemon juice, through evaporimeter, technique concentrates routinely, and being concentrated to pol is 42-48Brix;
(8), cold-aseptic filling: the turbid juice of lemon after concentrated stirs in finished pot, carries out sterile filling;
Preferably, the turbid juice limonin of prepared concentrated lemon content <5ppm.
The invention has the beneficial effects as follows: the processing method of the turbid juice debitterize of a kind of lemon of the present invention is the much progress that turbid juice is produced debitterize technology, suitably reduce fruit juice viscosity in enzymolysis operation by the addition of determining pectase, adopt the ultrafiltration system of three-stage filtration to ensure the amount of resin clear juice used, retain the insoluble matter in juice completely, the enzymolysis juice amount that control enters ultrafiltration accounts for the ratio of total juice amount, adopt debitterize resin to remove the limonin of super filtered juice, several persons effectively coordinate, and make in the concentrated turbid juice of lemon limonin content below 5ppm.This debitterize concentrates the turbid juice technique of lemon, has improved debitterize efficiency, has extended the service life of resin, has greatly reduced the time of process, has improved output, has reduced production cost.
Brief description of the drawings
Fig. 1 is Technology Roadmap of the present invention.
Its concrete test is as follows
1,
not definite (viscosity of reduction fruit juice and reserve part pectin do not affect the separation of ultrafiltration) of pectase addition
Adopt German WEISS pectase to test, to determine the impact of Different adding amount on ultra-filtration flux.
Pectase addition accounts for the impact (testing with the turbid juice of flesh-content <2%) of enzymolysis juice ratio on super filtered juice:
2, clear juice determining through resin flow:the relatively removal effect of limonin under different flow.
(1) debitterize resin column adopts 3 m
3/ post
(2) experimental technique
1# scheme flow is 4.0 m
3/ hour;
2# scheme flow is 3.5 m
3/ hour;
3# scheme is 3.0 m
3/ hour.
(3) experimental result
(4) conclusion
I is when pectase addition reaches 10000ml/10 ton hour, and the addition that continues raising pectase is little to the contribution of super filtered juice flux, therefore, adds pectase 10000ml at 10 tons of enzymatic vessels.
Ii adopts 2# scheme, and super filtered juice limonin removal efficiency just reaches 96.74%.
III is added 10000ml pectase, super filtered juice accounts for 90% of enzymolysis juice total amount, according to the cubage of 2# scheme limonin, limonin content 4.0ppm (11.8Brix) in the concentrated turbid juice of lemon, meet <5ppm (11.8Brix) standard, and in turbid juice, limonin removal efficiency reaches 87.0%.
Detailed description of the invention:
For Comprehension and Implementation better, describe processing method of the present invention in detail below in conjunction with embodiment.
After being cleaned, raw material lemon squeezes the juice, by fresh squeeze the juice to cling to kill, be cooled to 50 DEG C to enter enzymatic vessel, add the WEISS pectase of 10000ml/10 ton to carry out enzymolysis, after enzymolysis 15 minutes, 94% enzymolysis juice enters three-level filter system and carries out ultrafiltration, ultrafiltration technology adopts the three-level filter system of Nanjing Kai meter Ke Chemical Engineering Technology Co., Ltd, to improve the transit dose of clear juice, by the pectin decomposed of enzymolysis juice, to reduce enzymolysis juice viscosity, for ensureing that the concentrated turbid juice of lemon of finished product has certain viscosity, need reserve part pectin, high pressure is 4.0Mpa, low pressure is 0.8Mpa, one secondary internal circulating load is 72 m
3/ hour, three grades of internal circulating loads are 102 m
3/ hour, total clear juice amount is 4 .0m
3/ hour, super filtered juice amount reaches 89% of enzymolysis juice total amount, be equipped with 2 debitterize resin columns, every post loads 3 m
3debitterize resin, resin adopts the LSA-600 debitterize resin of Xi'an Lanxiao Sci-Tech Co., Ltd., and 2 posts are used alternatingly, flow velocity 3.5 m
3/ hour, 20 hours running times, the limonin rate of removing of super filtered juice reaches more than 95%, the insoluble matter that clear juice after debitterize and ultrafiltration are held back and without the enzymolysis juice 6% of ultrafiltration, mix, be concentrated into pol 42-48Brix, be the concentrated turbid juice of lemon of debitterize, the turbid juice limonin of the concentrated lemon content after debitterize is below 5ppm (11.8Brix).
Claims (2)
1. a processing method for the turbid juice debitterize of concentrated lemon, is characterized in that comprising following operation:
(1), squeeze the juice: the technique of squeezing the juice routinely, makes lemon juice;
(2), bar kills: lemon juice is killed through routine bar;
(3), enzymolysis: the lemon juice after bar kills is cooled to 50~55 DEG C to enter enzymatic vessel, doses pectase and stirs, and pectase addition is 10000~12000ml/10 ton tank, and enzymolysis time 15~20 minutes, makes enzymolysis juice;
(4), ultrafiltration: enzymolysis juice is filtered by three grades of ultrafiltration systems, and high pressure is 4.0~5.5Mpa, and low pressure is 0.2~1.0Mpa, and a secondary internal circulating load is 70~75m
3/ hour, three grades of internal circulating loads are 100~105 m
3/ hour, total clear juice amount is 2.8~4.0 m
3/ hour, super filtered juice amount is 88~90% of total enzymolysis juice amount;
(5), resin debitterize: adopt resin column to carry out debitterize in the clear juice of ultra filtration, resin content is 2.7~3.2 m
3/ post, super filtered juice is taking flow velocity as 3.0~4.0 m
3/ hour by resin, resin operation 17~22 hours, makes the clear juice of debitterize lemon;
(6), mix: the insoluble matter that the clear juice of lemon after debitterize and ultrafiltration are held back and the enzymolysis juice 5~10% without ultrafiltration, in the stainless cylinder of steel that is provided with agitator, stir, make the turbid juice of lemon;
(7), concentrated: by turbid lemon juice, through evaporimeter, technique concentrates routinely, and being concentrated to pol is 42-48Brix;
(8), cold-aseptic filling: the turbid juice of lemon after concentrated stirs in finished pot, carries out sterile filling.
2. the processing method of the turbid juice debitterize of a kind of concentrated lemon according to claim 1, is characterized in that the turbid juice limonin of prepared concentrated lemon content <5ppm.
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Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106721867A (en) * | 2015-11-24 | 2017-05-31 | 宜兴恒盛农业发展有限公司 | Ultrafiltration system is digested in a kind of cranberry juice production |
CN106805060A (en) * | 2017-01-10 | 2017-06-09 | 陕西蜂产品工程技术研究中心 | A kind of lemon juice bee product |
CN107897611A (en) * | 2017-12-19 | 2018-04-13 | 山东鲁菱果汁有限公司 | A kind of concentration peach juice in good taste and preparation method |
CN108065151A (en) * | 2017-12-14 | 2018-05-25 | 统企业(中国)投资有限公司昆山研究开发中心 | The processing method of the turbid juice of full fruit lemon |
CN111202193A (en) * | 2020-01-21 | 2020-05-29 | 重庆汇达柠檬科技集团有限公司 | Production method of limonin-rich nano lipid plasmid lemon juice |
CN111357892A (en) * | 2020-03-21 | 2020-07-03 | 重庆天邦食品有限公司 | Processing technology of concentrated orange juice |
CN116035155A (en) * | 2022-12-20 | 2023-05-02 | 合浦果香园食品有限公司 | Production method for debitterizing turbid shaddock juice |
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CN1688212A (en) * | 2002-09-04 | 2005-10-26 | 热带产品公司 | Juice processing incorporating resin treatment |
CN101632743A (en) * | 2009-07-30 | 2010-01-27 | 重庆长龙实业(集团)有限公司 | Method for extracting limonin substances |
CN101849690A (en) * | 2010-03-31 | 2010-10-06 | 西安银能科技发展有限责任公司 | Aspermous orange environment-friendly processing method |
CN102669767A (en) * | 2012-06-05 | 2012-09-19 | 谢振文 | Method for processing a plurality of types of lemon juice integrally |
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Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106721867A (en) * | 2015-11-24 | 2017-05-31 | 宜兴恒盛农业发展有限公司 | Ultrafiltration system is digested in a kind of cranberry juice production |
CN106805060A (en) * | 2017-01-10 | 2017-06-09 | 陕西蜂产品工程技术研究中心 | A kind of lemon juice bee product |
CN108065151A (en) * | 2017-12-14 | 2018-05-25 | 统企业(中国)投资有限公司昆山研究开发中心 | The processing method of the turbid juice of full fruit lemon |
CN108065151B (en) * | 2017-12-14 | 2021-09-17 | 统一企业(中国)投资有限公司昆山研究开发中心 | Processing method of whole-fruit lemon cloudy juice |
CN107897611A (en) * | 2017-12-19 | 2018-04-13 | 山东鲁菱果汁有限公司 | A kind of concentration peach juice in good taste and preparation method |
CN111202193A (en) * | 2020-01-21 | 2020-05-29 | 重庆汇达柠檬科技集团有限公司 | Production method of limonin-rich nano lipid plasmid lemon juice |
CN111357892A (en) * | 2020-03-21 | 2020-07-03 | 重庆天邦食品有限公司 | Processing technology of concentrated orange juice |
CN116035155A (en) * | 2022-12-20 | 2023-05-02 | 合浦果香园食品有限公司 | Production method for debitterizing turbid shaddock juice |
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Application publication date: 20140625 |