CN104939257B - OPC grape concentrated essence liquids and preparation method thereof - Google Patents

OPC grape concentrated essence liquids and preparation method thereof Download PDF

Info

Publication number
CN104939257B
CN104939257B CN201510342401.XA CN201510342401A CN104939257B CN 104939257 B CN104939257 B CN 104939257B CN 201510342401 A CN201510342401 A CN 201510342401A CN 104939257 B CN104939257 B CN 104939257B
Authority
CN
China
Prior art keywords
opc
grape
fermentation
concentration
concentrated essence
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN201510342401.XA
Other languages
Chinese (zh)
Other versions
CN104939257A (en
Inventor
姚秀业
姚中哲
王鹏
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Zheng Jianping
Original Assignee
LIAONING TIANCHI WINERY GROUP CO Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by LIAONING TIANCHI WINERY GROUP CO Ltd filed Critical LIAONING TIANCHI WINERY GROUP CO Ltd
Priority to CN201510342401.XA priority Critical patent/CN104939257B/en
Publication of CN104939257A publication Critical patent/CN104939257A/en
Application granted granted Critical
Publication of CN104939257B publication Critical patent/CN104939257B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

The present invention discloses a kind of OPC grapes concentrated essence liquid and preparation method thereof, it is with grape as raw material, by main techniques such as broken, biofermentation, OPC leaching, freeze concentration, vacuum outgas and heat sterilizations, OPC concentration >=15g/L is processed into, the OPC grape concentrated essence liquids rich in OPC bioactive ingredients.Can well solve the problems, such as that OPC is difficult to be leached and farthest keep the original bioactivity of OPC using the inventive method.Processing method of the present invention is not only able to keep the original natural properties of OPC, and can be by the sugar transition in grape juice into acetic acid using biofermentation, the solubility increase of OPC in an acidic solution, the leaching efficiency of its OPC is dramatically increased, product is formed flavour during the fermentation simultaneously, greatly strengthen the consumption of OPC products.Long-period drinking of said product, can remove internal free radical, enhance metabolism, and reach the purpose for improving autoimmunity and extension aging.

Description

OPC grape concentrated essence liquids and preparation method thereof
Technical field
The present invention relates to wine production technical field, a kind of auxotype OPC grape concentrated essence liquids, particularly with grape It is OPC grape concentrated essence liquids that raw material makes and preparation method thereof.
Technical background
OPC (Oligomeric Proanthocyanidins), Chinese belongs to biological flavone also known as oligomeric proanthocyanidins One kind of class, is the removing maximally effective natural of people's interior free yl generally acknowledged in the world at present.OPC is widely present in In the plants such as grape, blueberry, cherry, plum and pine bark, wherein grape pip is the important sources of OPC.OPC is generally rufous Powder, taste micro-puckery is dissolved in water and most organic solvent.
OPC can remove the free radical in human body, for human body have superpower anti-aging, anti-cancer, anti-angiocardiopathy, Radioresistance, anti-inflammatory, antibacterial etc. are acted on.Grape Skin and grape pip are rich in OPC, there are some researches show:In grape pip, OPC is low Polymers constitutes about the 80%~85% of polyphenols total amount.OPC is to find to be originated most efficient antioxidant in plant so far One of, its antioxidant effect is stronger than vitamin e 50 times, stronger than Vitamin C 20 times, with the strength for improving body immunity Effect.The product containing OPC is generally tablet and paste at present, taste bad and cost of manufacture is high;It is existing for grape pip and Grape Skin The extracting method of middle OPC has a lot, for example:It is microwave loss mechanisms, adsorption and desorption by resin method, supercritical carbon dioxide extraction method, super Sound wave extraction method, column chromatographic isolation and purification method, organic solvent extractionprocess etc..But these method extraction costs are higher, and product is edible Property it is poor, be only capable of selling in the form of tablets or capsules, lack unique local flavor.For example:Adsorption and desorption by resin method needs the time long, Treatment material quantity is low, product purity is low;Column chromatographic isolation and purification method and organic solvent extractionprocess, there is organic solvent makes Consumption is big, the power consumption of subsequent concentration process is high, production cost defect high;Microwave―assisted extraction, thermal effect short with extraction time The characteristics of rate is high, but with danger higher during microwave leakage, security is poor.
The content of the invention
The present invention seeks to solve grape in band seed, belt leather fermentation process, OPC is difficult to be leached and at utmost protects Hold the problem of the original bioactivity of OPC, there is provided a kind of OPC grapes concentrated essence liquid made as raw material with grape and its preparation side Method.
The present invention proposes following technical scheme:A kind of OPC grapes concentrated essence liquid, it is characterised in that:It is with grape as former Material, by including broken, biofermentation, OPC leaching, freeze concentration, vacuum outgas and heat sterilization technique, being processed into OPC The concentrated essence liquid of concentration >=15g/L.
The preparation method of OPC grapes concentrated essence liquid of the present invention, it is characterised in that:Preparation with grape as raw material Method is comprised the following steps:
(1) crush:Gap between broken wheel roller is adjusted to 2~5mm, with disintegrating machine by Grape fragmentation 1~2 time, Grape juice is set fully to escape, Grape Skin is in released state with seed, obtains grape juice mixture;
(2) allocate:The sugar content in grape juice mixture is adjusted to weight 15~22% with sucrose;
(3) grape juice mixture biofermentation:Biofermentation is divided into two processes of alcohol fermentation and acetic fermentation:Exist first The saccharomyces cerevisiae that weight is 0.01~0.02% is added in the grape juice mixture of allotment, is mixed under the conditions of 16~22 DEG C Row alcohol fermentation, fermentation time 10~15 days when sugar content≤12g/L, terminates fermentation;Then to inoculating active in zymotic fluid Acetic acid bacteria bacterium powder, inoculum concentration is the 0.1~0.5% of zymotic fluid weight, and acetic fermentation 5 is carried out under 16~24 DEG C and aerobic conditions ~10 days, when ethanol content < 0.5% (v/v), terminate fermentation;
(4) OPC is leached:The fermentation liquid mixture that (3rd) step is obtained is placed in be sealed at 10~20 DEG C and is placed, every 4~8h Agitation once, places 24~48h so that OPC is fully leached;
(5) freeze concentration:(4th) step OPC fermentation liquid mixtures are carried out into freeze concentration, temperature is opened when dropping to -2~-4 DEG C Beginning freezes, and when temperature is down to -6 DEG C~-9 DEG C, cooling time is 24~48 hours, and freezing rate is up to more than 85%, Fermented Condensed OPC concentration >=15g/L in liquid;
(6) filter:(5th) step OPC concentrates are maintained at a temperature of -6 DEG C to -9 DEG C and are filtered, except deicing quarrel and its Its solid impurity, makes OPC concentrate clears;
(7) cryogenic vacuum degassing:The OPC concentration filtrates that (6th) step is clarified are added in degassing tank, in temperature 10~20 DEG C, deaerate 5~10min under conditions of 0.05~0.09Mpa of vacuum, removes acetic acid, makes acetic acid≤1.0g/ in product L;
(8) heat sterilization:(7th) step product is filtered using the milipore filter that aperture is 0.25~0.45 μm, is removed Thalline in product is to be made OPC concentrated essence liquids;
(9) the OPC concentrated essence liquids product of heat sterilization is carried out into sterile filling, is sealed, in preservation under normal temperature lucifuge.
The present invention has following features compared with prior art:
Present invention employs biofermentation, the method such as acetic acid dissolution solution, freeze concentration, vacuum outgas and heat sterilization has Effect ground solve OPC not readily dissolved in immersion and bioactivity easily suffer destroy the problems such as.The product that the present invention is processed It is not only able to keep the original natural properties of OPC, also with flavour, greatly strengthen the consumption of OPC products;Take this Product, can reach the purpose for improving autoimmunity and extension aging.
During Grape fragmentation, grape pip should not be crushed excessively, in preventing grape-kernel oil from excessively residuing in product, shadow Ring product quality.Because grape pip outer wall is solid, contained OPC is difficult to infiltrate.But in an acidic solution, due to grape Seed and Grape Skin are softened, and liquid can be preferably permeated in the tissue of grape pip and Grape Skin, while in an acidic solution, The solubility of OPC increases, therefore the leaching efficiency of OPC is dramatically increased;Because additional acid flux material is unfavorable for this product local flavor Formed, therefore the present invention is by the way of alcohol fermentation and acetic fermentation, by the sugar transition in grape juice into acetic acid, while Flavour is formed in fermentation process.
During freeze concentration, the presence of solid can be conducive to ice-nucleus to produce, so that ice crystal is quickly formed, in order to reach This purpose, improves chilling rate, and the present invention can remarkably promote ice using the method with Grape Skin and seed freeze concentration, the method The quick formation of crystal.
Because OPC is easily hydrolyzed under acid and heating condition, so as to change intrinsic bioactivity, therefore the present invention The method deaerated using cryogenic vacuum removes acetic acid, meanwhile, the method can also reduce the decomposition of original aromatic substance in product.
The comparing result of the technology of the present invention and properties of product and routine techniques
Specific embodiment
The technological process of production:Grape → select → clean → drain → crush → allocate → belt leather, seed biofermentation → leaching Go out OPC → freeze concentration → filtering → cryogenic vacuum degassing → heat sterilization → sterile filling → sealing → storage.
1st, fruit is selected:The impurity such as removal is rotted, mildews, going bad, spoiled grape and carpopodium;
2nd, clean, drain:Grape is immersed in 3~4 times of clear water, is gently agitated for, kept for more than 3 minutes, bleed off filthy water, Change clear water to rinse 2~3 times, pull grape out and draining is drained;
3rd, crush:Gap between the wheel roller of disintegrating machine is adjusted to 2~3mm, using disintegrating machine by Grape fragmentation 1~2 It is secondary, grape juice is fully escaped, Grape Skin is in released state with seed, obtains grape juice mixture (containing Grape Skin and seed);
4th, allocate:With sucrose by the sugar content in grape juice mixture (containing Grape Skin and seed) adjust to weight 20~ 22%;
5th, grape juice mixture biofermentation:Biofermentation is divided into two processes of alcohol fermentation and acetic fermentation:Exist first The brewer's dried yeast that weight is 0.01~0.02% is added in the grape juice mixture of allotment, is mixed under the conditions of 20~22 DEG C Alcohol fermentation is carried out, fermentation time 12~15 days when sugar content≤12g/L, terminates fermentation;Then lived to inoculation in zymotic fluid Property acetic acid bacteria bacterium powder, inoculum concentration be ferment liquid mixture weight 0.1~0.2%, carried out under 20~24 DEG C and aerobic conditions Acetic fermentation 8~10 days, when ethanol content < 0.5% (v/v), terminates fermentation;
6th, OPC is leached:The fermentation liquid mixture that 5th step is obtained is placed in be sealed at 15~20 DEG C and is placed, the agitation one per 8h It is secondary, place 36~48h so that OPC is fully leached;
7th, freeze concentration:OPC fermentations liquid mixture (the OPC leachates i.e. with Grape Skin and seed) that 6th step is obtained enters Row freeze concentration, to improve the generation speed of ice crystal, during freeze concentration, temperature starts to freeze when dropping to -2~-4 DEG C, When temperature is down to -6 DEG C~-9 DEG C, cooling time is maintained at 36~48 hours, makes freezing rate up to more than 85%, OPC concentrates Concentration >=15g/L;
8th, filter:The OPC concentrates that 7th step is obtained are maintained at a temperature of -6 DEG C to -9 DEG C and are filtered, except deicing quarrel And other solid impurities, make OPC concentrate clears;
9th, cryogenic vacuum degassing:The concentration filtrate that 8th step is clarified is added in degassing tank, in 15~20 DEG C of temperature, very 5~10min of vacuum outgas is carried out under conditions of 0.05~0.09Mpa of reciprocal of duty cycle, acetic acid therein is removed, acetic acid is remained in making product Amount≤1.0g/L;
10th, heat sterilization:The product that the 9th step is obtained is filtered using the milipore filter that aperture is 0.25~0.45 μm, The thalline removed in product is to be made OPC concentrated essence liquids;
11st, filling, sealing, storage:The OPC concentrated essence liquids of heat sterilization are entered using brown oral liquid bottle (cillin bottle) Row sterile filling, sealing, in preservation under normal temperature lucifuge.

Claims (2)

1. a kind of preparation method of OPC grapes concentrated essence liquid, it is characterised in that:Described OPC is oligomeric proanthocyanidins, is With grape as raw material, by including broken, biofermentation, OPC leaching, freeze concentration, vacuum outgas and heat sterilization technique, The concentrated essence liquid of OPC concentration >=15g/L is processed into, the preparation method with grape as raw material is comprised the following steps:
(1) crush:Gap between broken wheel roller is adjusted to 2~5mm, with disintegrating machine by Grape fragmentation 1~2 time, makes Portugal Grape juice is fully escaped, and Grape Skin is in released state with seed, obtains grape juice mixture;
(2) allocate:The sugar content in grape juice mixture is adjusted to weight 15~22% with sucrose;
(3) grape juice mixture biofermentation:Biofermentation is divided into two processes of alcohol fermentation and acetic fermentation;First in allotment Grape juice mixture in add weight be 0.01~0.02% saccharomyces cerevisiae, be mixed carries out second under the conditions of 16~22 DEG C Alcohol fermentation, fermentation time 10~15 days when sugar content≤12g/L, terminates fermentation;Then to inoculating active acetic acid in zymotic fluid Bacterium bacterium powder, inoculum concentration is the 0.1~0.5% of zymotic fluid weight, and acetic fermentation 5~10 is carried out under 16~24 DEG C and aerobic conditions My god, when ethanol content < 0.5% (v/v), terminate fermentation;
(4) OPC is leached:The fermentation liquid mixture that (3rd) step is obtained is placed in be sealed at 10~20 DEG C and is placed, every 4~8h agitations Once, 24~48h is placed so that OPC is fully leached;
(5) freeze concentration:(4th) step OPC fermentation liquid mixtures are carried out into freeze concentration, temperature starts to freeze when dropping to -2~-4 DEG C Knot, when temperature is down to -6 DEG C~-9 DEG C, cooling time be 24~48 hours, freezing rate up to more than 85%, in Fermented Condensed liquid OPC concentration >=15g/L;
(6) filter:(5th) step OPC concentrates are maintained at a temperature of -6 DEG C to -9 DEG C and are filtered, except deicing quarrel and other are solid Body impurity, makes OPC concentrate clears;
(7) cryogenic vacuum degassing:The OPC concentration filtrates that (6th) step is clarified are added in degassing tank, in 10~20 DEG C of temperature, Deaerate 5~10min under conditions of 0.05~0.0gMpa of vacuum, removes acetic acid, makes acetic acid≤1.0g/L in product;
(8) heat sterilization:(7th) step product is filtered using the milipore filter that aperture is 0.25~0.45 μm, is removed product In thalline be to be made OPC concentrated essence liquids;
(9) the OPC concentrated essence liquids product of heat sterilization is carried out into sterile filling, is sealed, in preservation under normal temperature lucifuge.
2. the OPC grape concentrated essence liquids that preparation method is obtained according to claim 1, it is characterised in that:Described OPC is Oligomeric proanthocyanidins, are with grape as raw material, by including broken, biofermentation, OPC leaching, freeze concentration, vacuum outgas And heat sterilization technique, it is processed into the concentrated essence liquid of OPC concentration >=15g/L.
CN201510342401.XA 2015-06-13 2015-06-13 OPC grape concentrated essence liquids and preparation method thereof Active CN104939257B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510342401.XA CN104939257B (en) 2015-06-13 2015-06-13 OPC grape concentrated essence liquids and preparation method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510342401.XA CN104939257B (en) 2015-06-13 2015-06-13 OPC grape concentrated essence liquids and preparation method thereof

Publications (2)

Publication Number Publication Date
CN104939257A CN104939257A (en) 2015-09-30
CN104939257B true CN104939257B (en) 2017-06-30

Family

ID=54154779

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510342401.XA Active CN104939257B (en) 2015-06-13 2015-06-13 OPC grape concentrated essence liquids and preparation method thereof

Country Status (1)

Country Link
CN (1) CN104939257B (en)

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101165153A (en) * 2006-10-17 2008-04-23 通化通久葡萄酒有限公司 OPC grape wine
CN102433236A (en) * 2012-01-06 2012-05-02 杨琳 Method for making proanthocyanidin-rich wine and product thereof
CN103265520A (en) * 2013-05-18 2013-08-28 湖南鑫利生物科技有限公司 Method for preparing oligomeric proanthocyanidins and tannin pigment from grape seeds after winemaking

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20110206721A1 (en) * 2010-02-19 2011-08-25 Vijaya Nair Fermented soy nutritional supplements including mushroom components

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101165153A (en) * 2006-10-17 2008-04-23 通化通久葡萄酒有限公司 OPC grape wine
CN102433236A (en) * 2012-01-06 2012-05-02 杨琳 Method for making proanthocyanidin-rich wine and product thereof
CN103265520A (en) * 2013-05-18 2013-08-28 湖南鑫利生物科技有限公司 Method for preparing oligomeric proanthocyanidins and tannin pigment from grape seeds after winemaking

Also Published As

Publication number Publication date
CN104939257A (en) 2015-09-30

Similar Documents

Publication Publication Date Title
CN105273895B (en) Betel nut flavor alcohol-free beer and preparation method thereof
CN106350418A (en) Red raspberry complex fruit wine and preparing method thereof
CN109730224A (en) Oligopeptide rose enzyme new function drink
CN103805489A (en) Processing method for star fruit vinegar
CN105286018A (en) Pear vinegar beverage capable of clearing heat and clearing internal heat and preparation method of pear vinegar beverage
CN107927786A (en) A kind of method that polyphenol is extracted from butter fruit
CN101481644B (en) Brewing process for yellow peach wine
CN104522445B (en) A kind of persimmon full-fruit puree sauce and preparation method thereof
CN106883976A (en) A kind of production method of sugar grass rose white wine
CN103589559A (en) Production method for chaenomeles speciosa icewine
KR101042576B1 (en) Manufacturing method for fermented drink using korean pear
CN108823034A (en) A kind of brewing method of honey raisin tree fruit wine
CN105936866B (en) A kind of brew method of high calcium high polyphenolic content V. amurensis wine brewing skin slag vinegar
CN112167406A (en) Preparation method of black tea fermented tea beverage
CN105566512B (en) A kind of extracting method of persimmon fruit pectin
CN104921122B (en) Resveratrol grape concentration essence and preparation method thereof
CN107118932A (en) A kind of brewing method of birchleaf pear fruit vinegar
CN104939257B (en) OPC grape concentrated essence liquids and preparation method thereof
CN111053222A (en) Production method of green plum concentrated juice
CN107475061A (en) A kind of winter jujube fruit vinegar beverage preparation method
CN107488555A (en) A kind of method for producing applejack without using antioxidant and antiseptic
CN107177452A (en) A kind of technique for brewing hydromel
CN103421636A (en) Manufacturing method of kiwi wine
CN105998750A (en) Avicennia marina fruit wine
CN107495015B (en) Processing method of shell-containing litchi full-fruit functional beverage

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant
TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20180529

Address after: 122000 2 unit 1302, Yin Xin Garden, three section of Changjiang Road, Twin Towers District, Chaoyang City, Liaoning, 1302

Patentee after: Yao Zhongzhe

Address before: 122005 1 Tianchi street, modern agricultural park, Longcheng District, Chaoyang City, Liaoning

Patentee before: LIAONING TIANCHI WINERY GROUP Co.,Ltd.

PP01 Preservation of patent right
PP01 Preservation of patent right

Effective date of registration: 20180716

Granted publication date: 20170630

PD01 Discharge of preservation of patent
PD01 Discharge of preservation of patent

Date of cancellation: 20190628

Granted publication date: 20170630

TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20190731

Address after: 122000 Modern Agricultural Park in Longcheng District, Chaoyang City, Liaoning Province

Patentee after: LIAONING TIANCHI WINERY GROUP Co.,Ltd.

Address before: 122000 Unit 1302, Building 4, Yinxin Garden, Third Section of Yangtze River Road, Shuangta District, Chaoyang City, Liaoning Province

Patentee before: Yao Zhongzhe

PP01 Preservation of patent right

Effective date of registration: 20190628

Granted publication date: 20170630

PP01 Preservation of patent right
PD01 Discharge of preservation of patent
PD01 Discharge of preservation of patent

Date of cancellation: 20220524

Granted publication date: 20170630

PP01 Preservation of patent right
PP01 Preservation of patent right

Effective date of registration: 20220524

Granted publication date: 20170630

CI03 Correction of invention patent

Correction item: preservation of patent right

Correct: Effective date of revocation of patent right preservation registration: May 24, 2022

False: The effective date of patent right preservation registration is May 24, 2022

Number: 27-01

Volume: 38

CI03 Correction of invention patent
TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20220801

Address after: 122099 Room 201, unit 1, building 37, third section of Changjiang Road, Shuangta District, Chaoyang City, Liaoning Province

Patentee after: Zheng Jianping

Address before: 122000 modern agricultural park, Longcheng District, Chaoyang City, Liaoning

Patentee before: LIAONING TIANCHI WINERY GROUP Co.,Ltd.