CN109593618A - A kind of beer and preparation method thereof using the brewing of potato full-powder juice by-product - Google Patents

A kind of beer and preparation method thereof using the brewing of potato full-powder juice by-product Download PDF

Info

Publication number
CN109593618A
CN109593618A CN201910120111.9A CN201910120111A CN109593618A CN 109593618 A CN109593618 A CN 109593618A CN 201910120111 A CN201910120111 A CN 201910120111A CN 109593618 A CN109593618 A CN 109593618A
Authority
CN
China
Prior art keywords
juice
product
powder
wort
volume
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.)
Granted
Application number
CN201910120111.9A
Other languages
Chinese (zh)
Other versions
CN109593618B (en
Inventor
申光辉
曾雨虹
赵清锋
赵欣悦
陈安均
***
刘兴艳
黎杉珊
吴贺君
罗擎英
李美良
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.)
Sichuan Agricultural University
Original Assignee
Sichuan Agricultural University
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 Sichuan Agricultural University filed Critical Sichuan Agricultural University
Priority to CN201910120111.9A priority Critical patent/CN109593618B/en
Publication of CN109593618A publication Critical patent/CN109593618A/en
Application granted granted Critical
Publication of CN109593618B publication Critical patent/CN109593618B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12CBEER; PREPARATION OF BEER BY FERMENTATION; PREPARATION OF MALT FOR MAKING BEER; PREPARATION OF HOPS FOR MAKING BEER
    • C12C5/00Other raw materials for the preparation of beer
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12CBEER; PREPARATION OF BEER BY FERMENTATION; PREPARATION OF MALT FOR MAKING BEER; PREPARATION OF HOPS FOR MAKING BEER
    • C12C12/00Processes specially adapted for making special kinds of beer

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Health & Medical Sciences (AREA)
  • Biochemistry (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Food Science & Technology (AREA)
  • General Health & Medical Sciences (AREA)
  • Genetics & Genomics (AREA)
  • Wood Science & Technology (AREA)
  • Zoology (AREA)
  • Microbiology (AREA)
  • Distillation Of Fermentation Liquor, Processing Of Alcohols, Vinegar And Beer (AREA)
  • Non-Alcoholic Beverages (AREA)

Abstract

The invention discloses a kind of beer and preparation method thereof using the brewing of potato full-powder juice by-product.Method includes the following steps: (1) obtains the full powder juice by-product of purple-colored potato;(2) enzymatic hydrolysis sterilization;(3) brewer's wort is prepared;(4) hops is added;(5) preparation of juice is mixed;(6) mixing juice low-temperature electric field processing;(7) fermentation seed liquid is prepared;(8) main fermentation;(9) post-fermentation;(10) filtration sterilization.The present invention prepares a kind of unique flavor, ester is aromatic strongly fragrant by combining using potato full-powder juice by-product with brewer's wort, fragrance is coordinated, mellow in taste is rich in purple-colored potato anthocyanidin, the new function beer that oxidation resistance is strong and cost of material is relatively low.

Description

A kind of beer and preparation method thereof using the brewing of potato full-powder juice by-product
Technical field
The invention belongs to food engineering development fields, and in particular to it is a kind of using potato full-powder juice by-product brewing Beer and preparation method thereof.
Background technique
Potato (Solanum tuberosum L.), Solanaceae nightshade, stem tuber can be edible, also known as potato, potato, Foreign sweet potato etc. is the fourth-largest staple food grain that China is only second to wheat, paddy and corn.Purple-colored potato also known as purple potato, unexpected rival Bell potato, black potato, potato shape are in oblong, and bud eye is smaller, and pericarp and pulp are purple.Purple-colored potato is full of nutrition, removes Outside basic nutrition ingredient contained by normal potato, it is also rich in natural water-soluble colorants anthocyanidin, including Cyanidin, petunia There is anti-oxidant, blood pressure lowering, antitumaous effect, blood pressure lowering to make for element, malvidin, delphinidin and derivative of Chinese herbaceous peony florigen etc. With, prevention diabetes, the important physiological functions activity such as antiobesity action, development prospect is wide.
With the continuous propulsion of potatoes staple food grainization strategy, potato staple food product steps into consumption market. Potato full-powder is the important source material of potato staple food products processing, and market demand is increasingly vigorous.Freeze thawing partition method prepares horse The full powder of bell potato is dried, this method can again by carrying out freeze thawing treatment to curing mashed potatoes after removing most of moisture after centrifugation Mashed potatoes drying time is saved, reduces energy consumption cost, the full flour cell breakage rate of gained is low, and the market competitiveness is strong.But the technique is centrifuged Link can generate 30%~35% juice by-product, the nutritional ingredients such as carbohydrate rich in, free amino acid, directly Run in put and will cause environmental pollution and the wasting of resources.Therefore according to juice nutritional ingredient feature, utilization is reprocessed to it, not only may be used Juice bring environmental issue is solved, and resource utilization can be improved, extends potato processing industry chain, it is additional to increase industry Value.The research of trans-utilization again of the juice by-product generated at present for the full powder new process for processing is less, mainly due to juice Bad soil raw meat flavor is denseer, and sensory-acceptance is low, and it is big to be directly processed into various liquid food difficulty, lacks more mature feasible Resource conversion technology and the high value added product for adapting to market comsupton upgrade requirement, therefore greatly limit the full powder preparation technique Wide popularization and application.
Beer is to brew through beer yeast fermenting using fructus hordei germinatus, hops, water as primary raw material and form pick-me-up. China is the big Beer Brewage state of the first in the world and country of consumption, but the kind of beer product, flavor are comparatively single, almost 90% Beer be all using fructus hordei germinatus, rice as the light beer of raw material.As consumption constantly upgrading, light beer can not expire The diversified consumption demand of foot.In recent years, with the improvement of people's living standards, consumption structure gradually upgrades, there is health care The beer beverage market tremendous growth potential of function.Current health-care beer is mostly mainly by the dark beer to fermenting-ripening The mode for adding various health material ingredients is prepared, and production cost is relatively high.And directly to the fermentation various guarantors of Liao Tianjia Health-care function ingredient will affect beer fermentation degree.
Summary of the invention
For above-mentioned deficiency in the prior art, the present invention provide it is a kind of using potato full-powder juice by-product brewing Beer and preparation method thereof can effectively solve the problems, such as existing potato full-powder juice by-product high level trans-utilization again.
To achieve the above object, the technical solution adopted by the present invention to solve the technical problems is:
A method of utilizing potato full-powder juice by-product beer brewing, comprising the following steps:
(1) collection prepares the juice by-product generated during potato full-powder;
(2) enzymatic hydrolysis sterilization
Carbohydrase and alpha amylase is added simultaneously into juice by-product, adjusting pH value is 4.0~5.0, in 60~70 DEG C, Digest 2~3h;Then boil 5~10min, filter, collect enzymolysis liquid, after enzymolysis liquid is cooled to room temperature, then at 15~25 DEG C, It is spare to collect juice for filtration sterilization under conditions of 0.2~0.5MPa;Wherein, the additional amount of carbohydrase is juice by-product volume 0.5~1%;The additional amount of alpha amylase is the 0.5~1.5% of juice by-product volume;
(3) brewer's wort is prepared
Into malt mixture, sprinkling accounts for the water of its weight 2~5%, after stirring stands 20~30min, crushes, adds Weight is 4~5 times of powder weight, and temperature is 40~45 DEG C of water, and then adjusting pH value is 4~6, saccharification, then it is cooled to 40~ After 45 DEG C, brewer's wort is collected in filtering;
(4) hops is added
Hops is added when brewer's wort boils 12~15min and 40~45min respectively, wherein the beer being added for the first time The weight of hops is the 0.005~0.009% of wort volume;The weight of second of hops being added is wort volume 0.01~0.05%;
(5) preparation mixing juice
Step (4) products therefrom is mixed with juice obtained by step (2), the pH value of adjustment mixing juice is 5.0~7.0, Pol is 10~13 ° of Bx;The volume ratio of juice obtained by step (4) products therefrom and step (2) is 3:1~1:3;
(6) mixing juice low-temperature electric field processing
Ispol is added into mixing juice, is then heated to 50-60 DEG C, then being placed in intensity is 25-50kV/cm Electric field in handle 2000-3000 μ s;
(7) fermentation seed liquid is prepared
Brewer's yeast is seeded in 10~12 ° of Bx brewer's worts, 25~30 DEG C of 20~25h of culture, then transferred in 10~12 ° In Bx brewer's wort, 10~15 DEG C of 24~36h of culture obtain seed liquor;
(8) it ferments
By seed liquor be seeded to through step (6) treated mixing juice in, after 10~22 DEG C of 8~10d of fermentation, 4000~ 8000r/min is centrifuged 5~10min, 0~4 DEG C of 5~7d of continuation fermented supernatant fluid;Wherein, the inoculum concentration of seed liquor is mixing juice The 2~10% of volume;
(9) it sterilizes
4000~8000r/min centrifugation step (8) 5~10min of products therefrom, after filter sterilization.
Further, the process of juice by-product is prepared in step (1) are as follows: steam cure 10~15min of potato slices, Then -25~-20 DEG C freezing 20~for 24 hours, then at 20~25 DEG C persistently thaw 4~5h, be then charged into filter bag, be placed in centrifuge Middle centrifugation collects centrifugation juice to get juice by-product.
Further, potato described in step (1) is purple-colored potato.
Further, the enzyme activity of carbohydrase is 1 × 10 in step (2)5U/g, additional amount are juice by-product volume 1%.
Further, the enzyme activity of alpha amylase is 1 × 10 in step (2)4U/g, additional amount are juice by-product volume 0.8%.
Further, the malt mixture in step (3) comprises the following components in parts by weight:
1~5 part of 1~5 part of burnt malt, 1~3 part of amber malt and light color Ai Er malt.
Further, malt mixture comprises the following components in parts by weight:
3 parts of 2 parts of burnt malt, 1 part of amber malt and light color Ai Er malt.
Further, the weight for the hops being added for the first time in step (4) is the 0.0075% of wort volume;Second The weight of the hops of secondary addition is the 0.0175% of wort volume.
Further, hops is one of Lyceum section, cloth orchid family or western Chu hops or a variety of.
Further, the volume ratio of step (4) products therefrom and step (2) gained juice is 1:2 in step (5).
Further, in step (6) ispol include lysine, γ-aminobutyric acid, phenylalanine, glycine, It is at least three kinds of in cysteine, proline and alanine;Lysine, γ-aminobutyric acid, phenylalanine, glycine, half Guang ammonia The additional amount of acid, proline and alanine in mixing juice is respectively 2.0g/L, 1.6g/L, 2.5g/L, 2.2g/L, 1.8g/ L, 0.8g/L and 1.9g/L.
Further, the inoculum concentration of seed liquor is the 6% of mixed juice liquid product in step (7).
The beer that the above method is made.
The invention has the benefit that
1, the present invention passes through mixed according to the ratio of 3:1~1:3 using the full powder juice by-product of purple-colored potato and brewer's wort It closes, then the brewer's yeast for accounting for its volume 2~10% by being inoculated with weight thereto, after 10~22 DEG C of 8~10d of fermentation, centrifugation, After continuing 5~7d of fermented supernatant fluid under conditions of 0~4 DEG C, the beer being prepared makes full use of and remains purple Ma Ling Various nutriments and functional component in the full powder juice by-product of potato obtain one kind rich in Anthocyanins, have relatively strong The black beer new product of oxidation resistance.
2, the present invention strengthens modification technique using complex enzyme hydrolysis, Maillard reaction, and combines beer yeast fermenting technology, with Purple-colored potato full powder production juice and brewer's wort are raw material, prepare that a kind of ester is aromatic strongly fragrant, and fragrance is coordinated, mellow in taste, Without bad smell of soil taste, sensory-acceptance is good, while being rich in purple-colored potato anthocyanidin, and oxidation resistance is strong and cost of material Relatively low new function beer;It solves freeze thawing partition method and prepares juice by-product in the full powder technique of purple-colored potato again The problem of processing and utilization.
Specific embodiment
A specific embodiment of the invention is described below, in order to facilitate understanding by those skilled in the art this hair It is bright, it should be apparent that the present invention is not limited to the ranges of specific embodiment, for those skilled in the art, As long as various change is in the spirit and scope of the present invention that the attached claims limit and determine, these variations are aobvious and easy See, all are using the innovation and creation of present inventive concept in the column of protection.
Embodiment 1
A method of utilizing potato full-powder juice by-product beer brewing, comprising the following steps:
(1) the full powder juice by-product of purple-colored potato is obtained
Using the purple-colored potato of Black King Kong kind as raw material, the slice with a thickness of 2mm, steam are made into after cleaning up 10min is cured, then -20 DEG C of freezings for 24 hours, then at 25 DEG C of 4h that persistently thaw, are fitted into the filter bag of 120 mesh, then in 1500r/ It is centrifuged 10min in the centrifuge of min, collects the juice by-product generated in centrifugal process;
(2) enzymatic hydrolysis sterilization
Juice by-product is handled using the synchronous enzymatic isolation method of double enzymes, enzymatic saccharification is carried out to starch remaining in juice by-product Processing;Carbohydrase and alpha amylase is added simultaneously i.e. into juice by-product, wherein the enzyme activity of carbohydrase is 1 × 105U/g adds Enter 1.0% that amount is juice by-product volume;The enzyme activity of alpha amylase is 1 × 104U/g, additional amount are juice by-product volume 0.5%;Then adjusting enzymatic hydrolysis pH value is 4.0~5.0,65 DEG C of enzymatic hydrolysis 3h;
After enzymatic hydrolysis, enzymolysis liquid 10min enzyme deactivation is boiled, is then filtered while hot, again in 20 DEG C, the item of 0.2MPa after cooling Under part, it is spare to collect the juice being obtained by filtration for the film filtration sterilization for being 0.2 μm with aperture;
(3) brewer's wort is prepared
3 parts of Europe wheat light color Ai Er malt, 2 parts of burnt malts and 1 part of giving off a strong fragrance amber malt are uniformly mixed, wheat is then sprayed The water of bud mixture weight 2%, stands 20min after mixing evenly, to moisten wheat husk, is then mixed malt with maltcrusher Object crushes, then 45 DEG C of water of its 4 times of weight is incorporated as into powder, and adjusting its pH value with lactic acid is 5.5, is then being saccharified It is saccharified in pot, the detailed process of saccharification are as follows: 45 DEG C, 30min;60 DEG C, 60min;72 DEG C, 10min;78 DEG C, 10min;It boils Boil 5min enzyme deactivation;
After saccharification, it is cooled to rapidly 45 DEG C with cold water, is then filtered while hot with 120 mesh filter clothes, obtains malt Juice;
(4) hops is added
Brewer's wort is boiled, Lyceum section is then added when it boils 15min and 45min respectively, wherein Lyceum section first Secondary additional amount is the 0.0075% of wort volume;The secondary additional amount of Lyceum section is the 0.0175% of wort volume;
(5) preparation of juice is mixed
Juice that step (2) is prepared and the ratio for being 1:2 according to volume ratio through step (4) treated brewer's wort Mixing, adjusting its pol with malt syrup is 13 ° of Bx, then adjusting its pH value with sodium bicarbonate is 5.5;
(6) mixing juice low-temperature electric field processing
The mixture of lysine, γ-aminobutyric acid, phenylalanine and glycine, heating are added to step (5) products therefrom To 50 DEG C, it is placed in electric field strength 30kV/cm and handles 2000 μ s;
Wherein, the additive amount of lysine, γ-aminobutyric acid, phenylalanine and glycine in mixing juice is respectively 2.0g/L, 1.6g/L, 2.5g/L and 2.2g/L;
(7) fermentation seed liquid is prepared
By M20 Yeast strain of beer from inclined plane inoculating into 12 ° of Bx brewer's worts, 28 DEG C of cultures for 24 hours, then are transferred in 12 ° of Bx Brewer's wort in, 15 DEG C of culture 30h are to get seed liquor, and saccharomycete quantity is 1 × 10 in the seed liquor7A/mL;
(8) main fermentation
Using bottom yeast fermentation method, seed liquor is seeded in mixing juice, the inoculum concentration of seed liquor is mixing juice The 6% of volume, fermentation system liquid amount are 70%~80%, then 16 DEG C of main fermentation 10d;
(9) post-fermentation
After main fermentation, fermentation liquid is placed in the centrifuge of 4000r/min and is centrifuged 10min, is separated off saccharomycete Body, supernatant are transferred in closed container, and 0~4 DEG C is continued the 7d that ferments;
(10) filtration sterilization
The product that post-fermentation is obtained, which is placed in the centrifuge of 4000r/min, is centrifuged 5min, and it is thin to be separated by filtration residual yeast Born of the same parents, supernatant use 0.45 μm of micro-pore-film filtration again, obtain draft beer, then sterilize through 65 DEG C, can be obtained into bottled beer.
Embodiment 2
A method of utilizing potato full-powder juice by-product beer brewing, comprising the following steps:
(1) the full powder juice by-product of purple-colored potato is obtained
Using the purple-colored potato of Black King Kong kind as raw material, the slice with a thickness of 2mm, steam are made into after cleaning up 10min is cured, then -20 DEG C of freezings for 24 hours, then at 25 DEG C of 4h that persistently thaw, are fitted into the filter bag of 120 mesh, then in 1500r/ It is centrifuged 10min in the centrifuge of min, collects the juice by-product generated in centrifugal process;
(2) enzymatic hydrolysis sterilization
Juice by-product is handled using the synchronous enzymatic isolation method of double enzymes, enzymatic saccharification is carried out to starch remaining in juice by-product Processing;Carbohydrase and alpha amylase is added simultaneously i.e. into juice by-product, wherein the enzyme activity of carbohydrase is 1 × 105U/g adds Enter 1.5% that amount is juice by-product volume;The enzyme activity of alpha amylase is 1 × 104U/g, additional amount are juice by-product volume 1.0%;Then adjusting enzymatic hydrolysis pH value is 5.0,65 DEG C of enzymatic hydrolysis 3h;
After enzymatic hydrolysis, enzymolysis liquid 10min enzyme deactivation is boiled, is then filtered while hot, again in 15 DEG C, the item of 0.5MPa after cooling Under part, it is spare to collect the juice being obtained by filtration for the film filtration sterilization for being 0.4 μm with aperture;
(3) brewer's wort is prepared
3 parts of Europe wheat light color Ai Er malt, 2 parts of burnt malts and 1 part of giving off a strong fragrance amber malt are uniformly mixed, wheat is then sprayed The water of bud mixture weight 2%, stands 20min after mixing evenly, to moisten wheat husk, is then mixed malt with maltcrusher Object crushes, then 45 DEG C of water of its 4 times of weight is incorporated as into powder, and adjusting its pH value with lactic acid is 6.0, is then being saccharified It is saccharified in pot, the detailed process of saccharification are as follows: 45 DEG C, 30min;60 DEG C, 60min;72 DEG C, 10min;78 DEG C, 10min;It boils Boil 5min enzyme deactivation;
After saccharification, it is cooled to rapidly 45 DEG C with cold water, is then filtered while hot with 120 mesh filter clothes, obtains malt Juice;
(4) hops is added
Brewer's wort is boiled, cloth orchid family and Lyceum section are then separately added into when it boils 15min and 45min, wherein cloth The additional amount of orchid family is the 0.005% of wort volume;The additional amount of Lyceum section is the 0.01% of wort volume;
(5) preparation of juice is mixed
Juice that step (2) is prepared and the ratio for being 3:1 according to volume ratio through step (4) treated brewer's wort Mixing, adjusting its pol with malt syrup is 13 ° of Bx, then adjusting its pH value with sodium bicarbonate is 6;
(6) mixing juice low-temperature electric field processing
The mixture of lysine, γ-aminobutyric acid, phenylalanine and glycine, heating are added to step (5) products therefrom To 60 DEG C, it is placed in electric field strength 25kV/cm and handles 2500 μ s;
Wherein, the additive amount of lysine, γ-aminobutyric acid, phenylalanine and glycine in mixing juice is respectively 2.0g/L, 1.6g/L, 2.5g/L and 2.2g/L;
(7) seed liquor is prepared
By M21 Yeast strain of beer from inclined plane inoculating into 12 ° of Bx brewer's worts, 28 DEG C of cultures for 24 hours, then are transferred in 12 ° of Bx Brewer's wort in, 15 DEG C of culture 30h are to get seed liquor, and saccharomycete quantity is 1 × 10 in the seed liquor7A/mL;
(8) main fermentation
Using bottom yeast fermentation method, seed liquor is seeded in mixing juice, the inoculum concentration of seed liquor is mixing juice The 2% of volume, fermentation system liquid amount are 70%~80%, then 16 DEG C of main fermentation 9d;
(9) post-fermentation
After main fermentation, fermentation liquid is placed in the centrifuge of 4000r/min and is centrifuged 10min, is separated off saccharomycete Body, supernatant are transferred in closed container, and 0~4 DEG C is continued the 7d that ferments;
(10) filtration sterilization
The product that post-fermentation is obtained, which is placed in the centrifuge of 4000r/min, is centrifuged 5min, and it is thin to be separated by filtration residual yeast Born of the same parents, supernatant use 0.45 μm of micro-pore-film filtration again, obtain draft beer, then sterilize through 65 DEG C, can be obtained into bottled beer.
Embodiment 3
A method of utilizing potato full-powder juice by-product beer brewing, comprising the following steps:
(1) the full powder juice by-product of purple-colored potato is obtained
Using the purple-colored potato of Black King Kong kind as raw material, the slice with a thickness of 2mm, steam are made into after cleaning up 10min is cured, then -20 DEG C of freezings for 24 hours, then at 25 DEG C of 4h that persistently thaw, are fitted into the filter bag of 120 mesh, then in 1500r/ It is centrifuged 10min in the centrifuge of min, collects the juice by-product generated in centrifugal process;
(2) enzymatic hydrolysis sterilization
Juice by-product is handled using the synchronous enzymatic isolation method of double enzymes, enzymatic saccharification is carried out to starch remaining in juice by-product Processing;Carbohydrase and alpha amylase is added simultaneously i.e. into juice by-product, wherein the enzyme activity of carbohydrase is 1 × 105U/g adds Enter 0.8% that amount is juice by-product volume;The enzyme activity of alpha amylase is 1 × 104U/g, additional amount are juice by-product volume 0.5%;Then adjusting enzymatic hydrolysis pH value is 4.0,65 DEG C of enzymatic hydrolysis 3h;
After enzymatic hydrolysis, enzymolysis liquid 10min enzyme deactivation is boiled, is then filtered while hot, again in 20 DEG C, the item of 0.2MPa after cooling Under part, it is spare to collect the juice being obtained by filtration for the film filtration sterilization for being 0.2 μm with aperture;
(3) brewer's wort is prepared
3 parts of Europe wheat light color Ai Er malt, 2 parts of burnt malts and 1 part of giving off a strong fragrance amber malt are uniformly mixed, wheat is then sprayed The water of bud mixture weight 2%, stands 20min after mixing evenly, to moisten wheat husk, is then mixed malt with maltcrusher Object crushes, then 45 DEG C of water of its 4 times of weight is incorporated as into powder, and adjusting its pH value with lactic acid is 5.5, is then being saccharified It is saccharified in pot, the detailed process of saccharification are as follows: 45 DEG C, 30min;60 DEG C, 60min;72 DEG C, 10min;78 DEG C, 10min;It boils Boil 5min enzyme deactivation;
After saccharification, it is cooled to rapidly 45 DEG C with cold water, is then filtered while hot with 120 mesh filter clothes, obtains malt Juice;
(4) hops is added
Brewer's wort is boiled, cloth orchid family is then added when it boils 15min and 45min respectively, wherein Blanc section first Secondary additional amount is the 0.009% of wort volume;The secondary additional amount of Blanc section is the 0.05% of wort volume;
(5) preparation of juice is mixed
Juice that step (2) is prepared and the ratio for being 2:1 according to volume ratio through step (4) treated brewer's wort Mixing, adjusting its pol with malt syrup is 13 ° of Bx, then adjusting its pH value with sodium bicarbonate is 5.0;
(6) mixing juice low-temperature electric field processing
The mixture of lysine, γ-aminobutyric acid, phenylalanine and glycine, heating are added to step (5) products therefrom To 60 DEG C, it is placed in electric field strength 50kV/cm and handles 3000 μ s;
Wherein, the additive amount of lysine, γ-aminobutyric acid, phenylalanine and glycine in mixing juice is respectively 2.0g/L, 1.6g/L, 2.5g/L and 2.2g/L;
(7) seed liquor is prepared
By M36 Yeast strain of beer from inclined plane inoculating into 12 ° of Bx brewer's worts, 28 DEG C of cultures for 24 hours, then are transferred in 12 ° of Bx Brewer's wort in, 15 DEG C of culture 30h are to get seed liquor, and saccharomycete quantity is 1 × 10 in the seed liquor7A/mL;
(8) main fermentation
Using bottom yeast fermentation method, seed liquor is seeded in mixing juice, the inoculum concentration of seed liquor is mixing juice The 4% of volume, fermentation system liquid amount are 70%~80%, then 16 DEG C of main fermentation 8d;
(9) post-fermentation
After main fermentation, fermentation liquid is placed in the centrifuge of 4000r/min and is centrifuged 10min, is separated off saccharomycete Body, supernatant are transferred in closed container, and 0~4 DEG C is continued the 7d that ferments;
(10) filtration sterilization
The product that post-fermentation is obtained, which is placed in the centrifuge of 4000r/min, is centrifuged 5min, and it is thin to be separated by filtration residual yeast Born of the same parents, supernatant use 0.45 μm of micro-pore-film filtration again, obtain draft beer, then sterilize through 65 DEG C, can be obtained into bottled beer.
Embodiment 4
A method of utilizing potato full-powder juice by-product beer brewing, comprising the following steps:
(1) the full powder juice by-product of purple-colored potato is obtained
Using the purple-colored potato of Black King Kong kind as raw material, the slice with a thickness of 2mm, steam are made into after cleaning up 10min is cured, then -20 DEG C of freezings for 24 hours, then at 25 DEG C of 4h that persistently thaw, are fitted into the filter bag of 120 mesh, then in 1500r/ It is centrifuged 10min in the centrifuge of min, collects the juice by-product generated in centrifugal process;
(2) enzymatic hydrolysis sterilization
Juice by-product is handled using the synchronous enzymatic isolation method of double enzymes, enzymatic saccharification is carried out to starch remaining in juice by-product Processing;Carbohydrase and alpha amylase is added simultaneously i.e. into juice by-product, wherein the enzyme activity of carbohydrase is 1 × 105U/g adds Enter 0.8% that amount is juice by-product volume;The enzyme activity of alpha amylase is 1 × 104U/g, additional amount are juice by-product volume 0.5%;Then adjusting enzymatic hydrolysis pH value is 4.0,65 DEG C of enzymatic hydrolysis 3h;
After enzymatic hydrolysis, enzymolysis liquid 10min enzyme deactivation is boiled, is then filtered while hot, again in 20 DEG C, the item of 0.2MPa after cooling Under part, it is spare to collect the juice being obtained by filtration for the film filtration sterilization for being 0.2 μm with aperture;
(3) brewer's wort is prepared
3 parts of Europe wheat light color Ai Er malt, 2 parts of burnt malts and 1 part of giving off a strong fragrance amber malt are uniformly mixed, wheat is then sprayed The water of bud mixture weight 2%, stands 20min after mixing evenly, to moisten wheat husk, is then mixed malt with maltcrusher Object crushes, then 45 DEG C of water of its 4 times of weight is incorporated as into powder, and adjusting its pH value with lactic acid is 5.5, is then being saccharified It is saccharified in pot, the detailed process of saccharification are as follows: 45 DEG C, 30min;60 DEG C, 60min;72 DEG C, 10min;78 DEG C, 10min;It boils Boil 5min enzyme deactivation;
After saccharification, it is cooled to rapidly 45 DEG C with cold water, is then filtered while hot with 120 mesh filter clothes, obtains malt Juice;
(4) hops is added
Brewer's wort is boiled, Lyceum section is then added when it boils 15min and 45min respectively, wherein Lyceum section first Secondary additional amount is the 0.006% of wort volume;The secondary additional amount of Lyceum section is the 0.02% of wort volume;
(5) preparation of juice is mixed
Juice that step (2) is prepared and the ratio for being 1:3 according to volume ratio through step (4) treated brewer's wort Mixing, adjusting its pol with malt syrup is 13 ° of Bx, then adjusting its pH value with sodium bicarbonate is 6.5;
(6) mixing juice low-temperature electric field processing
The mixture of lysine, γ-aminobutyric acid, phenylalanine and glycine, heating are added to step (5) products therefrom To 55 DEG C, it is placed in electric field strength 25kV/cm and handles 2000 μ s;
Wherein, the additive amount of lysine, γ-aminobutyric acid, phenylalanine and glycine in mixing juice is respectively 2.0g/L, 1.6g/L, 2.5g/L and 2.2g/L;
(7) seed liquor is prepared
By M47 Yeast strain of beer from inclined plane inoculating into 12 ° of Bx brewer's worts, 28 DEG C of cultures for 24 hours, then are transferred in 12 ° of Bx Brewer's wort in, 15 DEG C of culture 30h are to get seed liquor, and saccharomycete quantity is 1 × 10 in the seed liquor7A/mL;
(8) main fermentation
Using bottom yeast fermentation method, seed liquor is seeded in mixing juice, the inoculum concentration of seed liquor is mixing juice The 10% of volume, fermentation system liquid amount are 70%~80%, then 16 DEG C of main fermentation 8d;
(9) post-fermentation
After main fermentation, fermentation liquid is placed in the centrifuge of 4000r/min and is centrifuged 10min, is separated off saccharomycete Body, supernatant are transferred in closed container, and 0~4 DEG C is continued the 7d that ferments;
(10) filtration sterilization
The product that post-fermentation is obtained, which is placed in the centrifuge of 4000r/min, is centrifuged 5min, and it is thin to be separated by filtration residual yeast Born of the same parents, supernatant use 0.45 μm of micro-pore-film filtration again, obtain draft beer, then sterilize through 65 DEG C, can be obtained into bottled beer.
Embodiment 5
A method of utilizing potato full-powder juice by-product beer brewing, comprising the following steps:
(1) the full powder juice by-product of purple-colored potato is obtained
Using the purple-colored potato of Black King Kong kind as raw material, the slice with a thickness of 2mm, steam are made into after cleaning up 10min is cured, then -20 DEG C of freezings for 24 hours, then at 25 DEG C of 4h that persistently thaw, are fitted into the filter bag of 120 mesh, then in 1500r/ It is centrifuged 10min in the centrifuge of min, collects the juice by-product generated in centrifugal process;
(2) enzymatic hydrolysis sterilization
Juice by-product is handled using the synchronous enzymatic isolation method of double enzymes, enzymatic saccharification is carried out to starch remaining in juice by-product Processing;Carbohydrase and alpha amylase is added simultaneously i.e. into juice by-product, wherein the enzyme activity of carbohydrase is 1 × 105U/g adds Enter 0.8% that amount is juice by-product volume;The enzyme activity of alpha amylase is 1 × 104U/g, additional amount are juice by-product volume 0.5%;Then adjusting enzymatic hydrolysis pH value is 4.0,65 DEG C of enzymatic hydrolysis 3h;
After enzymatic hydrolysis, enzymolysis liquid 10min enzyme deactivation is boiled, is then filtered while hot, again in 20 DEG C, the item of 0.2MPa after cooling Under part, it is spare to collect the juice being obtained by filtration for the film filtration sterilization for being 0.2 μm with aperture;
(3) brewer's wort is prepared
3 parts of Europe wheat light color Ai Er malt, 2 parts of burnt malts and 1 part of giving off a strong fragrance amber malt are uniformly mixed, wheat is then sprayed The water of bud mixture weight 2%, stands 20min after mixing evenly, to moisten wheat husk, is then mixed malt with maltcrusher Object crushes, then 45 DEG C of water of its 4 times of weight is incorporated as into powder, and adjusting its pH value with lactic acid is 5.5, is then being saccharified It is saccharified in pot, the detailed process of saccharification are as follows: 45 DEG C, 30min;60 DEG C, 60min;72 DEG C, 10min;78 DEG C, 10min;It boils Boil 5min enzyme deactivation;
After saccharification, it is cooled to rapidly 45 DEG C with cold water, is then filtered while hot with 120 mesh filter clothes, obtains malt Juice;
(4) preparation of juice is mixed
The juice and brewer's wort that step (2) is prepared are mixed according to the ratio that volume ratio is 1:1, with malt syrup tune Saving its pol is 13 ° of Bx, then adjusting its pH value with sodium bicarbonate is 5.0;
(5) seed liquor is prepared
By M44 Yeast strain of beer from inclined plane inoculating into 12 ° of Bx brewer's worts, 28 DEG C of cultures for 24 hours, then are transferred in 12 ° of Bx Brewer's wort in, 15 DEG C of culture 30h are to get seed liquor, and saccharomycete quantity is 1 × 10 in the seed liquor7A/mL;
(6) mixing juice low-temperature electric field processing
The mixture of lysine, γ-aminobutyric acid, phenylalanine and glycine, heating are added to step (5) products therefrom To 50 DEG C, it is placed in electric field strength 25kV/cm and handles 2000 μ s;
Wherein, the additive amount of lysine, γ-aminobutyric acid, phenylalanine and glycine in mixing juice is respectively 2.0g/L, 1.6g/L, 2.5g/L and 2.2g/L;
(7) main fermentation
Using bottom yeast fermentation method, seed liquor is seeded in mixing juice, the inoculum concentration of seed liquor is mixing juice The 8% of volume, fermentation system liquid amount are 70%~80%, then 16 DEG C of main fermentation 8d;
(8) post-fermentation
After main fermentation, fermentation liquid is placed in the centrifuge of 4000r/min and is centrifuged 10min, is separated off saccharomycete Body, supernatant are transferred in closed container, and 0~4 DEG C is continued the 7d that ferments;
(9) filtration sterilization
The product that post-fermentation is obtained, which is placed in the centrifuge of 4000r/min, is centrifuged 5min, and it is thin to be separated by filtration residual yeast Born of the same parents, supernatant use 0.45 μm of micro-pore-film filtration again, obtain draft beer, then sterilize through 65 DEG C, can be obtained into bottled beer.
Embodiment 6
A method of utilizing potato full-powder juice by-product beer brewing, comprising the following steps:
(1) the full powder juice by-product of purple-colored potato is obtained
Using the purple-colored potato of Black King Kong kind as raw material, the slice with a thickness of 2mm, steam are made into after cleaning up 10min is cured, then -20 DEG C of freezings for 24 hours, then at 25 DEG C of 4h that persistently thaw, are fitted into the filter bag of 120 mesh, then in 1500r/ It is centrifuged 10min in the centrifuge of min, collects the juice by-product generated in centrifugal process;
(2) enzymatic hydrolysis sterilization
Juice by-product is handled using the synchronous enzymatic isolation method of double enzymes, enzymatic saccharification is carried out to starch remaining in juice by-product Processing;Carbohydrase and alpha amylase is added simultaneously i.e. into juice by-product, wherein the enzyme activity of carbohydrase is 1 × 105U/g adds Enter 0.8% that amount is juice by-product volume;The enzyme activity of alpha amylase is 1 × 104U/g, additional amount are juice by-product volume 0.5%;Then adjusting enzymatic hydrolysis pH value is 4.0,65 DEG C of enzymatic hydrolysis 3h;
After enzymatic hydrolysis, enzymolysis liquid 10min enzyme deactivation is boiled, is then filtered while hot, again in 20 DEG C, the item of 0.2MPa after cooling Under part, it is spare to collect the juice being obtained by filtration for the film filtration sterilization for being 0.2 μm with aperture;
(3) brewer's wort is prepared
3 parts of Europe wheat light color Ai Er malt, 2 parts of burnt malts and 1 part of giving off a strong fragrance amber malt are uniformly mixed, wheat is then sprayed The water of bud mixture weight 2%, stands 20min after mixing evenly, to moisten wheat husk, is then mixed malt with maltcrusher Object crushes, then 45 DEG C of water of its 4 times of weight is incorporated as into powder, and adjusting its pH value with lactic acid is 5.5, is then being saccharified It is saccharified in pot, the detailed process of saccharification are as follows: 45 DEG C, 30min;60 DEG C, 60min;72 DEG C, 10min;78 DEG C, 10min;It boils Boil 5min enzyme deactivation;
After saccharification, it is cooled to rapidly 45 DEG C with cold water, is then filtered while hot with 120 mesh filter clothes, obtains malt Juice;
(4) preparation of juice is mixed
The juice and brewer's wort that step (2) is prepared are mixed according to the ratio that volume ratio is 1:1, with malt syrup tune Saving its pol is 13 ° of Bx, then adjusting its pH value with sodium bicarbonate is 5.0;
(5) seed liquor is prepared
By M44 Yeast strain of beer from inclined plane inoculating into 12 ° of Bx brewer's worts, 28 DEG C of cultures for 24 hours, then are transferred in 12 ° of Bx Brewer's wort in, 15 DEG C of culture 30h are to get seed liquor, and saccharomycete quantity is 1 × 10 in the seed liquor7A/mL;
(6) mixing juice low-temperature electric field processing
To step (5) products therefrom addition lysine, γ-aminobutyric acid, phenylalanine, glycine, cysteine and dried meat The mixture of propylhomoserin is heated to 50 DEG C, is placed in electric field strength 25kV/cm and handles 2000 μ s;
Wherein, lysine, γ-aminobutyric acid, phenylalanine, glycine, cysteine and proline are in mixing juice Additive amount be respectively 2.0g/L, 1.6g/L, 2.5g/L, 2.2g/L, 1.8g/L and 0.8g/L;
(7) main fermentation
Using bottom yeast fermentation method, seed liquor is seeded in mixing juice, the inoculum concentration of seed liquor is mixing juice The 8% of volume, fermentation system liquid amount are 70%~80%, then 16 DEG C of main fermentation 8d;
(8) post-fermentation
After main fermentation, fermentation liquid is placed in the centrifuge of 4000r/min and is centrifuged 10min, is separated off saccharomycete Body, supernatant are transferred in closed container, and 0~4 DEG C is continued the 7d that ferments;
(9) filtration sterilization
The product that post-fermentation is obtained, which is placed in the centrifuge of 4000r/min, is centrifuged 5min, and it is thin to be separated by filtration residual yeast Born of the same parents, supernatant use 0.45 μm of micro-pore-film filtration again, obtain draft beer, then sterilize through 65 DEG C, can be obtained into bottled beer.
Embodiment 7
A method of utilizing potato full-powder juice by-product beer brewing, comprising the following steps:
(1) the full powder juice by-product of purple-colored potato is obtained
Using the purple-colored potato of Black King Kong kind as raw material, the slice with a thickness of 2mm, steam are made into after cleaning up 10min is cured, then -20 DEG C of freezings for 24 hours, then at 25 DEG C of 4h that persistently thaw, are fitted into the filter bag of 120 mesh, then in 1500r/ It is centrifuged 10min in the centrifuge of min, collects the juice by-product generated in centrifugal process;
(2) enzymatic hydrolysis sterilization
Juice by-product is handled using the synchronous enzymatic isolation method of double enzymes, enzymatic saccharification is carried out to starch remaining in juice by-product Processing;Carbohydrase and alpha amylase is added simultaneously i.e. into juice by-product, wherein the enzyme activity of carbohydrase is 1 × 105U/g adds Enter 0.8% that amount is juice by-product volume;The enzyme activity of alpha amylase is 1 × 104U/g, additional amount are juice by-product volume 0.5%;Then adjusting enzymatic hydrolysis pH value is 4.0,65 DEG C of enzymatic hydrolysis 3h;
After enzymatic hydrolysis, enzymolysis liquid 10min enzyme deactivation is boiled, is then filtered while hot, again in 20 DEG C, the item of 0.2MPa after cooling Under part, it is spare to collect the juice being obtained by filtration for the film filtration sterilization for being 0.2 μm with aperture;
(3) brewer's wort is prepared
3 parts of Europe wheat light color Ai Er malt, 2 parts of burnt malts and 1 part of giving off a strong fragrance amber malt are uniformly mixed, wheat is then sprayed The water of bud mixture weight 2%, stands 20min after mixing evenly, to moisten wheat husk, is then mixed malt with maltcrusher Object crushes, then 45 DEG C of water of its 4 times of weight is incorporated as into powder, and adjusting its pH value with lactic acid is 5.5, is then being saccharified It is saccharified in pot, the detailed process of saccharification are as follows: 45 DEG C, 30min;60 DEG C, 60min;72 DEG C, 10min;78 DEG C, 10min;It boils Boil 5min enzyme deactivation;
After saccharification, it is cooled to rapidly 45 DEG C with cold water, is then filtered while hot with 120 mesh filter clothes, obtains malt Juice;
(4) preparation of juice is mixed
The juice and brewer's wort that step (2) is prepared are mixed according to the ratio that volume ratio is 1:1, with malt syrup tune Saving its pol is 13 ° of Bx, then adjusting its pH value with sodium bicarbonate is 5.0;
(5) seed liquor is prepared
By M44 Yeast strain of beer from inclined plane inoculating into 12 ° of Bx brewer's worts, 28 DEG C of cultures for 24 hours, then are transferred in 12 ° of Bx Brewer's wort in, 15 DEG C of culture 30h are to get seed liquor, and saccharomycete quantity is 1 × 10 in the seed liquor7A/mL;
(6) mixing juice low-temperature electric field processing
The mixture of lysine, γ-aminobutyric acid, phenylalanine and glycine, heating are added to step (5) products therefrom To 50 DEG C, it is placed in electric field strength 25kV/cm and handles 2000 μ s;
Wherein, lysine, γ-aminobutyric acid, phenylalanine, glycine, proline and alanine are in mixing juice Additive amount is respectively 2.0g/L, 1.6g/L, 2.5g/L, 2.2g/L, 0.8g/L and 1.9g/L;
(7) main fermentation
Using bottom yeast fermentation method, seed liquor is seeded in mixing juice, the inoculum concentration of seed liquor is mixing juice The 8% of volume, fermentation system liquid amount are 70%~80%, then 16 DEG C of main fermentation 8d;
(8) post-fermentation
After main fermentation, fermentation liquid is placed in the centrifuge of 4000r/min and is centrifuged 10min, is separated off saccharomycete Body, supernatant are transferred in closed container, and 0~4 DEG C is continued the 7d that ferments;
(9) filtration sterilization
The product that post-fermentation is obtained, which is placed in the centrifuge of 4000r/min, is centrifuged 5min, and it is thin to be separated by filtration residual yeast Born of the same parents, supernatant use 0.45 μm of micro-pore-film filtration again, obtain draft beer, then sterilize through 65 DEG C, can be obtained into bottled beer.
Comparative example 1
Juice direct fermentation will be digested obtained by step (2), other steps are by the sterilizing gained of embodiment 1 at bottled beer.
Comparative example 2
Omit step (6) mixing juice low-temperature electric field processing, will directly be mixed obtained by step (5) by embodiment 1 juice into Row fermentation, sterilizing gained is at bottled beer.
Embodiment 6
1, beer sense organ overall merit
Group is evaluated by 10 subjective appreciation compositions of personnel through professional training, rating standard is shown in Table 1, set of factors U ={ color u1, fragrance u2, foam u3, mouthfeel u4 };Comment gathers V={ I grade of v1, II grades of v2, III level v3, IV grade v4 };Weight sets K={ 0.20k1,0.25k2,0.20k3,0.35k4 }, methods of marking: I grade is assigned 90 points, and II grades are assigned 80 points, and III level assigns 70 points, IV Grade assigns 60 points).Sense organ comprehensive evaluation result is shown in Table 2.
1 purple-colored potato beer subjective appreciation classification standard of table
As shown in Table 2, comparative example 1 and comparative example 2 have apparent juice smell of soil taste, embodiment 1~implementation Beer sample ester perfume (or spice) and fragrance prepared by example 5 are strong, and smell is coordinated, without apparent juice smell of soil taste, in addition, foaming properties It is superior to beer sample prepared by comparative example with mouthfeel, comprehensive score > 80 divides, wherein 1 comprehensive score highest of embodiment It is 90.8 points.
2 beer sense organ comprehensive evaluation result of table
2, beer sample physical and chemical index is analyzed
The beer physical and chemical index that Examples 1 to 5 is prepared is detected according to GB/T4928-2008 " beer analysis method ", Testing result is shown in Table 3;Wherein alcoholic strength presses spectrophotometer method (the second method) referring to density bottle method (the first method), coloration, total acid Agent method (the first method) as indicated.Other index determinings of beer: reduced sugar uses DNS colorimetric method, and pol is using hand-held saccharometer Measurement, pH are directly measured using acidometer.
3 beer physical and chemical index of table
Note: same column different alphabetical (a, b, c) indicates significant difference (P < 0.05)
Implement from the data in table 3, it can be seen that the beer indices that 1~embodiment of embodiment 5 is prepared are substantially better than comparison Example 1 and comparative example 2, the beer properties that embodiment 1 is prepared are substantially better than embodiment 2~5.
3, Antioxidant Indexes measure
The beer and the black beer of commercially available Hubertus that embodiment 1 is prepared carry out detection comparison, and the result is shown in tables 4;Its In, anthocyanidin content shows poor method using pH;Total phenol content uses Folin-Ciocalteu method;Total reducing power uses iron cyaniding Potassium method is indicated with Vc equivalent concentration;Total antioxidant capacity uses ABTS method, is as a result indicated with ABTS free radical scavenging activity;DPPH Free radical scavenging ability uses spectrophotometry, is as a result indicated with Vc equivalent concentration.
4 Antioxidant Indexes testing result of table
As shown in Table 4,0.768~1.574mg/mL of anthocyanidin content in the beer sample prepared by the present invention, total phenol contain 171.98~312.82 μ g/mL are measured, and the black beer of commercially available Hubertus is free of anthocyanidin, total phenol content is relatively low, in addition, using purple The total reducing power of beer sample, the DPPH Scavenging activity of color potato fruit preparation are much higher than the black beer of commercially available Hubertus, and ABTS is clear Except rate is suitable with commercial product;It is indicated above that the black beer antioxidant component content of this technology preparation is high, comprehensive anti-oxidant energy Power is better than commercial product.

Claims (10)

1. a kind of method using potato full-powder juice by-product beer brewing, which comprises the following steps:
(1) collection prepares the juice by-product generated during potato full-powder;
(2) enzymatic hydrolysis sterilization
Carbohydrase and alpha amylase is added simultaneously into juice by-product, adjusting pH value is 4.0~5.0, in 60~70 DEG C, enzymatic hydrolysis 2 ~3h;Then boil 5~10min, filter, collect enzymolysis liquid, after enzymolysis liquid is cooled to room temperature, then at 15~25 DEG C, 0.2~ It is spare to collect juice for filtration sterilization under conditions of 0.5MPa;Wherein, the additional amount of carbohydrase is the 0.5 of juice by-product volume ~1%;The additional amount of alpha amylase is the 0.5~1.5% of juice by-product volume;
(3) brewer's wort is prepared
Into malt mixture, sprinkling accounts for the water of its weight 2~5%, after stirring stands 20~30min, crushes, adds weight It is 4~5 times of powder weight, the water that temperature is 40~45 DEG C, then adjusting pH value is 4~6, saccharification, then is cooled to 40~45 DEG C Afterwards, it filters, collects brewer's wort;
(4) hops is added
Hops is added when brewer's wort boils 12~15min and 40~45min respectively, wherein the hops being added for the first time Weight be wort volume 0.005~0.009%;The weight of second of hops being added is the 0.01 of wort volume ~0.05%;
(5) preparation mixing juice
Step (4) products therefrom is mixed with juice obtained by step (2), the pH value of adjustment mixing juice is 5.0~7.0, pol For 10~13 ° of Bx;The volume ratio of juice obtained by step (4) products therefrom and step (2) is 3:1~1:3;
(6) mixing juice low-temperature electric field processing
Ispol is added into mixing juice, is then heated to 50-60 DEG C, then is placed in the electricity that intensity is 25-50kV/cm 2000-3000 μ s is handled in;
(7) fermentation seed liquid is prepared
Brewer's yeast is seeded in 10~12 ° of Bx brewer's worts, 25~30 DEG C of 20~25h of culture, then transferred in 10~12 ° of Bx wheats In bud juice, 10~15 DEG C of 24~36h of culture obtain seed liquor;
(8) it ferments
By seed liquor be seeded to through step (6) treated mixing juice in, after 10~22 DEG C of 8~10d of fermentation, 4000~ 8000r/min is centrifuged 5~10min, 0~4 DEG C of 5~7d of continuation fermented supernatant fluid;Wherein, the inoculum concentration of seed liquor is mixing juice The 2~10% of volume;
(9) it sterilizes
4000~8000r/min centrifugation step (8) 5~10min of products therefrom, after filter sterilization.
2. the method according to claim 1 using potato full-powder juice by-product beer brewing, which is characterized in that step Suddenly the process of juice by-product is prepared in (1) are as follows: steam cure 10~15min of potato slices, then -25~-20 DEG C of freezings 20~for 24 hours, persistently thaw 4~5h then at 20~25 DEG C, is then charged into filter bag, is placed in a centrifuge centrifugation, collects centrifugate Liquid is to get juice by-product.
3. the method according to claim 1 using potato full-powder juice by-product beer brewing, which is characterized in that step Suddenly the enzyme activity of carbohydrase described in (2) is 1 × 105U/g, additional amount are the 1% of juice by-product volume.
4. the method according to claim 1 using potato full-powder juice by-product beer brewing, which is characterized in that step Suddenly the enzyme activity of alpha amylase described in (2) is 1 × 104U/g, additional amount are the 0.8% of juice by-product volume.
5. the method according to claim 1 using potato full-powder juice by-product beer brewing, which is characterized in that step Suddenly the malt mixture in (3) comprises the following components in parts by weight:
1~5 part of 1~5 part of burnt malt, 1~3 part of amber malt and light color Ai Er malt.
6. the method according to claim 1 using potato full-powder juice by-product beer brewing, which is characterized in that step Suddenly the weight for the hops being added for the first time described in (4) is the 0.0075% of wort volume;Second of hops being added Weight be wort volume 0.0175%.
7. the method according to claim 1 or 6 using potato full-powder juice by-product beer brewing, feature exist In the hops is one of Lyceum section, cloth orchid family or western Chu hops or a variety of.
8. the method according to claim 1 using potato full-powder juice by-product beer brewing, which is characterized in that step Suddenly ispol described in (6) includes lysine, γ-aminobutyric acid, phenylalanine, glycine, cysteine, proline With it is at least three kinds of in alanine;
The lysine, γ-aminobutyric acid, phenylalanine, glycine, cysteine, proline and alanine are in mixing juice In additional amount be respectively 2.0g/L, 1.6g/L, 2.5g/L, 2.2g/L, 1.8g/L, 0.8g/L and 1.9g/L.
9. the method according to claim 1 using potato full-powder juice by-product beer brewing, which is characterized in that step Suddenly the inoculum concentration of seed liquor described in (7) is the 6% of mixed juice liquid product.
10. the beer that any one of claim 1~9 the method is made.
CN201910120111.9A 2019-02-18 2019-02-18 Beer brewed by using potato whole powder juice byproduct and preparation method thereof Active CN109593618B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201910120111.9A CN109593618B (en) 2019-02-18 2019-02-18 Beer brewed by using potato whole powder juice byproduct and preparation method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201910120111.9A CN109593618B (en) 2019-02-18 2019-02-18 Beer brewed by using potato whole powder juice byproduct and preparation method thereof

Publications (2)

Publication Number Publication Date
CN109593618A true CN109593618A (en) 2019-04-09
CN109593618B CN109593618B (en) 2022-08-05

Family

ID=65967475

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201910120111.9A Active CN109593618B (en) 2019-02-18 2019-02-18 Beer brewed by using potato whole powder juice byproduct and preparation method thereof

Country Status (1)

Country Link
CN (1) CN109593618B (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110878241A (en) * 2019-12-27 2020-03-13 青岛啤酒股份有限公司 Wine-fragrance IPA beer and preparation method thereof
CN112500950A (en) * 2020-11-18 2021-03-16 西昌学院 Potato beer production line
CN113717804A (en) * 2021-09-03 2021-11-30 深圳市绿航星际太空科技研究院 Solid acid beer capable of adjusting emotion and preparation method thereof

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB977387A (en) * 1960-09-20 1964-12-09 Apv Co Ltd Improvements in the processing of wort
CN1147550A (en) * 1996-08-20 1997-04-16 吉林省银瀑啤酒厂(集团) Prodn technology of whole-malt dark beer
CA2189268A1 (en) * 1996-10-30 1998-04-30 Stephen J. Davids Process for producing from a potatoe wort an alcoholic beverage having essentially the characteristics of barley beer
CN102960796A (en) * 2012-11-18 2013-03-13 杨学青 Fermentation and preparation method for producing juice in starch from black potato
CN103710188A (en) * 2014-01-09 2014-04-09 青岛万里江食品有限公司 Method for preparing health-care purple sweet potato beer
CN106107335A (en) * 2016-06-17 2016-11-16 四川农业大学 Potato starch processing juice lactic acid beverage and preparation method thereof
CN106350333A (en) * 2016-08-25 2017-01-25 南宁邝氏兄弟酒类生产有限公司 Production technology for raw stock black beer
CN109090436A (en) * 2018-09-07 2018-12-28 四川农业大学 A kind of deodorant flavouring method of potato processing juice

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB977387A (en) * 1960-09-20 1964-12-09 Apv Co Ltd Improvements in the processing of wort
CN1147550A (en) * 1996-08-20 1997-04-16 吉林省银瀑啤酒厂(集团) Prodn technology of whole-malt dark beer
CA2189268A1 (en) * 1996-10-30 1998-04-30 Stephen J. Davids Process for producing from a potatoe wort an alcoholic beverage having essentially the characteristics of barley beer
CN102960796A (en) * 2012-11-18 2013-03-13 杨学青 Fermentation and preparation method for producing juice in starch from black potato
CN103710188A (en) * 2014-01-09 2014-04-09 青岛万里江食品有限公司 Method for preparing health-care purple sweet potato beer
CN106107335A (en) * 2016-06-17 2016-11-16 四川农业大学 Potato starch processing juice lactic acid beverage and preparation method thereof
CN106350333A (en) * 2016-08-25 2017-01-25 南宁邝氏兄弟酒类生产有限公司 Production technology for raw stock black beer
CN109090436A (en) * 2018-09-07 2018-12-28 四川农业大学 A kind of deodorant flavouring method of potato processing juice

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
张彬等: "添加马铃薯辅料酿制高氨基酸营养啤酒的研究", 《酿酒》 *
贺小贤等: "全麦黑啤酒的研制", 《山西食品工业》 *

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110878241A (en) * 2019-12-27 2020-03-13 青岛啤酒股份有限公司 Wine-fragrance IPA beer and preparation method thereof
CN112500950A (en) * 2020-11-18 2021-03-16 西昌学院 Potato beer production line
CN113717804A (en) * 2021-09-03 2021-11-30 深圳市绿航星际太空科技研究院 Solid acid beer capable of adjusting emotion and preparation method thereof

Also Published As

Publication number Publication date
CN109593618B (en) 2022-08-05

Similar Documents

Publication Publication Date Title
CN101892141B (en) Method for preparing sweet red jujube wine
CN105851751B (en) A kind of compound small berries fermented health drink and preparation method thereof
CN101921686B (en) Method for producing dry date wine
CN105349348B (en) A kind of dendrobium candidum liquor made from sorghum and its production technology
CN109439489A (en) A kind of preparation method of Pitaya wine
CN109593618A (en) A kind of beer and preparation method thereof using the brewing of potato full-powder juice by-product
CN106754172A (en) A kind of production technology of fruit flavoured type spirit
CN101245302A (en) Method for preparing alcoholic beverage using incubated wild ginseng root
KR100843358B1 (en) Method for preparing of lycium chinense liquor
CN105112226B (en) A kind of preparation method of highland barley original plasm wine
CN108441367A (en) A kind of Chinese chestnut beer brewage process
CN108624444A (en) A kind of brewing method of nutrition and health care Yangtao wine
CN105400656B (en) A kind of brewing method of yellow rice wine
CN107603812B (en) Brewing method of compound-flavor health-care highland barley wine
CN107937185B (en) Production method of dendrobium officinale beer
CN113186061A (en) Preparation method of rice wine
CN109294807A (en) A kind of preparation method of Sugarless type black rice wine
CN105733915A (en) Fermentation method of waxberry rice vinegar
CN108753558A (en) A kind of preparation method of red yeast rice Olive vinegar
CN107828598A (en) A kind of purple potato black garlic wine and preparation method thereof
CN107868743A (en) The yellow rice wine and its brew method of a kind of liquid state fermentation
CN114617242B (en) Processing technology of black pickled vegetables and products thereof
CN103125822B (en) Preparing method of brown rice function red rice health care wine
CN110050919A (en) A kind of preparation method of walnut dregs rhizoma polygonati mixed fermentation drink
CN109852515A (en) A kind of preparation method of compound fruit and vegetable fermented wine

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant