CN108041582A - A kind of production technology of dragon fruit ferment powder - Google Patents

A kind of production technology of dragon fruit ferment powder Download PDF

Info

Publication number
CN108041582A
CN108041582A CN201711310858.8A CN201711310858A CN108041582A CN 108041582 A CN108041582 A CN 108041582A CN 201711310858 A CN201711310858 A CN 201711310858A CN 108041582 A CN108041582 A CN 108041582A
Authority
CN
China
Prior art keywords
product
fermentation
dragon fruit
powder
obtains
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.)
Pending
Application number
CN201711310858.8A
Other languages
Chinese (zh)
Inventor
黄永良
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.)
Guizhou Delong Food Technology Co Ltd
Original Assignee
Guizhou Delong Food Technology 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 Guizhou Delong Food Technology Co Ltd filed Critical Guizhou Delong Food Technology Co Ltd
Priority to CN201711310858.8A priority Critical patent/CN108041582A/en
Publication of CN108041582A publication Critical patent/CN108041582A/en
Pending legal-status Critical Current

Links

Classifications

    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, 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
    • A23L33/00Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23VINDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
    • A23V2002/00Food compositions, function of food ingredients or processes for food or foodstuffs

Abstract

The invention discloses a kind of production technologies of dragon fruit ferment powder;The dragon fruit ferment is made of with following raw materials, dragon fruit, lemon and white granulated sugar.The production technology of the dragon fruit ferment powder includes:Dragon fruit and lemon after cleaning, drain, peeling, is cut into block, and white granulated sugar, flue fruit and lemon are stacked by layer, lower tank amount is no more than fermenter volume 80%, is then inoculated with saccharomyces cerevisiae, sealed fermenting, then 25 DEG C 30 DEG C of fermentation temperature, fermentation time 5 10 days carry out secondary fermentation and submerged fermentation, allotment, filtering are filling, sterilizing to get.The dragon fruit ferment powder color and luster that present invention process extracts is scarlet, and taste good is sour-sweet moderate, and amino acid content is high, has stronger anti-oxidant, improves the immunity of the human body, promotes digestion, improves the functions such as sleep.For natural red colouring matter in dragon fruit easily by oxidation stain, the dragon fruit ferment color and luster of this technique productions is scarlet, by color and luster regression time lengthening 1 year in dragon fruit ferment or more.

Description

A kind of production technology of dragon fruit ferment powder
Technical field
The present invention relates to a kind of production technology of dragon fruit ferment powder, particularly a kind of dragon fruit ferment powders in good taste Production technology.
Background technology
Dragon fruit is the king in fruit, and original producton location is in Central America.The ferment prepared with dragon fruit, there is very high nutritive value. Appropriateness drinks and can help weight reducing, and long-term consumption has Constipation, hypoglycemic, reducing blood lipid, weight-reducing, whitening spot-removing and other effects, except this it It is outer also to have the effects that release heavy metal poisoning, Green Tea Extract, and long-time service is without any side effects.
At present, dragon fruit ferment powder is usually after dragon fruit is cleaned, and drying is crushed to get the mouthfeel so obtained is also Not good enough, easy oxidation stain, the holding time is short, generally 3-6 months.
The content of the invention
The purpose of the present invention is to provide the production technology of dragon fruit ferment powder.The dragon fruit ferment that present invention process obtains Color and luster is scarlet, brews rear taste good, sour-sweet moderate, have it is stronger anti-oxidant, improve the immunity of the human body, promote digestion, change The functions such as kind sleep.The dragon fruit ferment for adding probiotics also has adjusting intestinal flora, promotes the functions such as digestion.
What the present invention was realized in.A kind of production technology of dragon fruit ferment powder, comprises the following steps;
A. full maturity is chosen, pulp is in peony or claret-colored red heart dragon fruit, after cleaning, drains, obtains A product;
B.A product are removed the peel, and are cut into the block that the length of side is 1-2mm, are obtained B product;
C. yellow lemon is chosen, after cleaning, drains, obtains C product;
D.C product are removed the peel, and are cut into the block that the length of side is 1-2mm, are obtained D product;
E. the order of white granulated sugar, B product and D product is pressed from top to bottom, white granulated sugar, B product and D product is stacked by layer, lower tank amount is not More than fermenter volume 80%, E product are obtained;
Saccharomyces cerevisiae is inoculated on f.E product, the 0.1%-0.2% of inoculum concentration E product weight obtains F product;
G.F product sealed fermentings, 25 DEG C -30 DEG C of fermentation temperature, fermentation time 5-10 days, midway stirring 1-2 times or from bottom Juice is taken to carry out leaching Slag treatment to upper strata slag 2 times, obtains G product;
H. G product are crossed into 60-80 mesh filter screens, zymotic fluid and pomace separation, collects zymotic fluid, obtain H product;
I.H product are transferred in another clean fermentation tank and carry out second of fermentation, and when fermenting for the second time, the canned liquid that ferments is fermentation More than the 90% of tank volume, strictly anaerobic standing for fermentation, 25 DEG C -30 DEG C of fermentation temperature, fermentation time 5-10 days treat zymotic fluid face Static, when bubble-free generates, fermentation ends obtain I product;
J. the high fermentation liquid in i product is collected liquid, obtains J product using after 300 mesh filter-cloth filterings;
K.J product import clean fermentation tank, and the canned liquid that ferments is more than the 90% of fermenter volume, 20 DEG C -25 of fermentation temperature DEG C, stringent static anaerobic fermentation carries out profound fermentation, and fermentation time 1 month to 12 months obtains K product;
L.K product are imported in concentration tank, and concentration condition is:45 DEG C of thickening temperature, vacuum degree 0.09MPa are concentrated to stoste 75%-85% obtains L product;
The strainer filtering of m.L product 300-400 mesh collects filtrate, obtains M product;
The maltodextrin of M product weight 8%-20% and the vitamin C of M product weight 0%-0.5% are added in n.M product, is stirred evenly, Obtain N product;
O. uniform filtration, homogeneous 1-2 times filter the strainer used and control in 300-400 mesh, obtain O product;
P.O product sterilize carry out degerming by the way of filtration sterilization or high temperature sterilization;The degerming is filtration sterilization temperature It spends for room temperature, sterilization mode uses ultra high temperature short time sterilization or microwave disinfection, 135 DEG C of -140 DEG C of processing of ultra high temperature short time sterilization 5s-8s, ultra high temperature short time sterilization speed needs and spray drying speeds match;Microwave pipe-line sterilizes 60 DEG C of 2-5 points of -65 DEG C of processing Clock;Obtain P product;
Q. it is spray-dried:140 DEG C -160 DEG C of inlet air temperature is controlled, 85 DEG C -95 DEG C of leaving air temp goes out powder moisture requirement and exists Less than 5%, the requirement of powder ambient humidity is received less than 30%, is received powder with food-grade packaging bag, is obtained Q product;
R. by Q product, white sand, Icing Sugar, xylo-oligosaccharide, D-sorbite, hawthorn powder, blueberry powder, the weight for mixing probiotic powder Than for 50-80:15-40:5-15:3-10:0-20:0-5:0-5:0-5 is by Q product white sand, Icing Sugar, xylo-oligosaccharide, D-sorbite, mountain Short, bristly hair or beard powder, blueberry powder and mixing probiotic powder mixing, pack to get.
In the production technology of foregoing dragon fruit ferment powder, the mixing probiotic powder is bifidobacterium longum, acidophilus breast Bacillus, lactobacillus plantarum or Lactobacillus rhamnosus.
In the production technology of foregoing dragon fruit ferment powder, in step e, the matter of the dragon fruit, lemon and white granulated sugar Measuring ratio is:70-85:8-13:10-16.
In the production technology of foregoing dragon fruit ferment powder, the mass ratio of the dragon fruit, lemon and white granulated sugar is: 75-80:9-12:12-14.
In the production technology of foregoing dragon fruit ferment powder, the mass ratio of the dragon fruit, lemon and white granulated sugar is: 78:10:13.
Experimental example sensory evaluation
Evaluation object:The dragon fruit ferment (being extracted by embodiment 1) of present invention process extraction.
Evaluation method:7 company personnel are asked at random, dragon fruit ferment is observed and tasted, each index is carried out Scoring, is evaluated with ten point system, finally calculates the comprehensive grading that ensemble average point is dragon fruit ferment.
Evaluation index:Color and luster, bad smell, fragrance, tart flavour, sweet taste, bitter taste and whole mouthfeel.
Dragon fruit ferment Analyses Methods for Sensory Evaluation Results
Note:Fraction is higher to represent that color and luster, fragrance and whole mouthfeel are better;Sour-sweet more taste is moderate, and bitter taste is lighter, and turbidity is got over It is low.
Compared with the prior art, the dragon fruit ferment powder color and luster that present invention process obtains is scarlet, brews rear taste good, acid In comfortable, have it is stronger anti-oxidant, improve the immunity of the human body, promote digestion, improve sleep etc. functions.Add the fire of probiotics Imperial fruit ferment, which also has, adjusts intestinal flora, promotes the functions such as digestion.
Specific embodiment
Embodiment 1.
A kind of production technology of dragon fruit ferment powder, the dragon fruit ferment are made of with following raw materials, dragon fruit 780g, lemon 100g and white granulated sugar 130g.
The production technology of the dragon fruit ferment powder, comprises the following steps;
A. full maturity is chosen, pulp is in peony or claret-colored red heart dragon fruit, after cleaning, drains, obtains A product;
B.A product are removed the peel, and are cut into the block that the length of side is 1-2mm, are obtained B product;
C. yellow lemon is chosen, after cleaning, drains, obtains C product;
D.C product are removed the peel, and are cut into the block that the length of side is 1-2mm, are obtained D product;
E. the order of white granulated sugar, B product and D product is pressed from top to bottom, white granulated sugar, B product and D product is stacked by layer, lower tank amount is not More than fermenter volume 80%, E product are obtained;
Saccharomyces cerevisiae is inoculated on f.E product, the 0.1%-0.2% of inoculum concentration E product weight obtains F product;
G.F product sealed fermentings, 25 DEG C -30 DEG C of fermentation temperature, fermentation time 5-10 days, midway stirring 1-2 times or from bottom Juice is taken to carry out leaching Slag treatment to upper strata slag 2 times, obtains G product;
H. G product are crossed into 60-80 mesh filter screens, zymotic fluid and pomace separation, collects zymotic fluid, obtain H product;
I.H product are transferred in another clean fermentation tank and carry out second of fermentation, and when fermenting for the second time, the canned liquid that ferments is fermentation The 95% of tank volume, strictly anaerobic standing for fermentation, 25 DEG C -30 DEG C of fermentation temperature, fermentation time 5-10 days treat that zymotic fluid face is quiet Only, when bubble-free generates, fermentation ends obtain I product;
J. the high fermentation liquid in i product is collected liquid, obtains J product using after 300 mesh filter-cloth filterings;
K.J product import clean fermentation tank, and the canned liquid that ferments is the 95% of fermenter volume, 20 DEG C -25 DEG C of fermentation temperature, sternly The static anaerobic fermentation of lattice, carries out profound fermentation, and fermentation time 6 months obtains K product;
L.K product are imported in concentration tank, and concentration condition is:45 DEG C of thickening temperature, vacuum degree 0.09MPa are concentrated to stoste 80%, obtain L product;
The strainer filtering of m.L product 300-400 mesh collects filtrate, obtains M product;
The maltodextrin of M product weight 15% and the vitamin C of M product weight 0.25% are added in n.M product, stirs evenly, obtains N product;
O. uniform filtration, homogeneous 2 times filter the strainer used and control in 300-400 mesh, obtain O product;
P.O product sterilize carry out degerming by the way of filtration sterilization or high temperature sterilization;The degerming is filtration sterilization temperature It spends for room temperature, sterilization mode uses ultra high temperature short time sterilization or microwave disinfection, 135 DEG C of -140 DEG C of processing of ultra high temperature short time sterilization 5s-8s, ultra high temperature short time sterilization speed needs and spray drying speeds match;Microwave pipe-line sterilizes 60 DEG C of 2-5 points of -65 DEG C of processing Clock;Obtain P product;
Q. it is spray-dried:140 DEG C -160 DEG C of inlet air temperature is controlled, 85 DEG C -95 DEG C of leaving air temp goes out powder moisture requirement and exists Less than 5%, the requirement of powder ambient humidity is received less than 30%, is received powder with food-grade packaging bag, is obtained Q product;
R. by Q product, white sand, Icing Sugar, xylo-oligosaccharide, D-sorbite, hawthorn powder, blueberry powder, the weight for mixing probiotic powder Than for 65:23:10:7:10:2.5:2.5:2.5 by Q product white sand, Icing Sugar, xylo-oligosaccharide, D-sorbite, hawthorn powder, blueberry powder and Mix probiotic powder mixing, pack to get;The mixing probiotic powder is bifidobacterium longum.
Embodiment 2.
A kind of production technology of dragon fruit ferment powder, the dragon fruit ferment are made of with following raw materials, dragon fruit 800g, lemon 120g and white granulated sugar 140g.
The production technology of the dragon fruit ferment powder, comprises the following steps;
A. full maturity is chosen, pulp is in peony or claret-colored red heart dragon fruit, after cleaning, drains, obtains A product;
B.A product are removed the peel, and are cut into the block that the length of side is 1-2mm, are obtained B product;
C. yellow lemon is chosen, after cleaning, drains, obtains C product;
D.C product are removed the peel, and are cut into the block that the length of side is 1-2mm, are obtained D product;
E. the order of white granulated sugar, B product and D product is pressed from top to bottom, white granulated sugar, B product and D product is stacked by layer, lower tank amount is not More than fermenter volume 80%, E product are obtained;
It is inoculated with saccharomyces cerevisiae on f.E product, the 0.2% of inoculum concentration E product weight, obtain F product;
G.F product sealed fermentings, 25 DEG C -30 DEG C of fermentation temperature, fermentation time 10 days, midway stir 2 times or take juice from bottom Leaching Slag treatment is carried out to upper strata slag 2 times, obtain G product;
H. G product are crossed into 60-80 mesh filter screens, zymotic fluid and pomace separation, collects zymotic fluid, obtain H product;
I.H product are transferred in another clean fermentation tank and carry out second of fermentation, and when fermenting for the second time, the canned liquid that ferments is fermentation The 98% of tank volume, strictly anaerobic standing for fermentation, 25 DEG C -30 DEG C of fermentation temperature, fermentation time 10 days treat that zymotic fluid face is static, When bubble-free generates, fermentation ends obtain I product;
J. the high fermentation liquid in i product is collected liquid, obtains J product using after 300 mesh filter-cloth filterings;
K.J product import clean fermentation tank, and the canned liquid that ferments is the 98% of fermenter volume, 20 DEG C -25 DEG C of fermentation temperature, sternly The static anaerobic fermentation of lattice, carries out profound fermentation, and fermentation time 12 months obtains K product;
L.K product are imported in concentration tank, and concentration condition is:45 DEG C of thickening temperature, vacuum degree 0.09MPa are concentrated to stoste 85%, obtain L product;
The strainer filtering of m.L product 300-400 mesh collects filtrate, obtains M product;
The maltodextrin of M product weight 20% and the vitamin C of M product weight 0.5% are added in n.M product, stirs evenly, obtains N product;
O. uniform filtration, homogeneous 2 times filter the strainer used and control in 300-400 mesh, obtain O product;
P.O product sterilize carry out degerming by the way of filtration sterilization or high temperature sterilization;The degerming is filtration sterilization temperature It spends for room temperature, sterilization mode uses ultra high temperature short time sterilization or microwave disinfection, 135 DEG C of -140 DEG C of processing of ultra high temperature short time sterilization 5s-8s, ultra high temperature short time sterilization speed needs and spray drying speeds match;Microwave pipe-line sterilizes 60 DEG C -65 DEG C and handles 5 points Clock;Obtain P product;
Q. it is spray-dried:140 DEG C -160 DEG C of inlet air temperature is controlled, 85 DEG C -95 DEG C of leaving air temp goes out powder moisture requirement and exists Less than 5%, the requirement of powder ambient humidity is received less than 30%, is received powder with food-grade packaging bag, is obtained Q product;
R. it is 80 by the weight ratio of Q product, white sand, Icing Sugar, xylo-oligosaccharide:15:5:3 by Q product white sand, Icing Sugar, xylo-oligosaccharide, D-sorbite mixing, pack to get;The mixing probiotic powder is lactobacillus acidophilus.
Embodiment 3.
A kind of production technology of dragon fruit ferment powder, the dragon fruit ferment are made of with following raw materials, dragon fruit 750g, lemon 90g and white granulated sugar 120g.
The production technology of the dragon fruit ferment powder, comprises the following steps;
A. full maturity is chosen, pulp is in peony or claret-colored red heart dragon fruit, after cleaning, drains, obtains A product;
B.A product are removed the peel, and are cut into the block that the length of side is 1-2mm, are obtained B product;
C. yellow lemon is chosen, after cleaning, drains, obtains C product;
D.C product are removed the peel, and are cut into the block that the length of side is 1-2mm, are obtained D product;
E. the order of white granulated sugar, B product and D product is pressed from top to bottom, white granulated sugar, B product and D product is stacked by layer, lower tank amount is not More than fermenter volume 80%, E product are obtained;
Saccharomyces cerevisiae is inoculated on f.E product, the 0.1%-0.2% of inoculum concentration E product weight obtains F product;
G.F product sealed fermentings, 25 DEG C -30 DEG C of fermentation temperature, fermentation time 5-10 days, midway stirring 1-2 times or from bottom Juice is taken to carry out leaching Slag treatment to upper strata slag 2 times, obtains G product;
H. G product are crossed into 60-80 mesh filter screens, zymotic fluid and pomace separation, collects zymotic fluid, obtain H product;
I.H product are transferred in another clean fermentation tank and carry out second of fermentation, and when fermenting for the second time, the canned liquid that ferments is fermentation The 91% of tank volume, strictly anaerobic standing for fermentation, 25 DEG C -30 DEG C of fermentation temperature, fermentation time 5-10 days treat that zymotic fluid face is quiet Only, when bubble-free generates, fermentation ends obtain I product;
J. the high fermentation liquid in i product is collected liquid, obtains J product using after 300 mesh filter-cloth filterings;
K.J product import clean fermentation tank, and the canned liquid that ferments is the 91% of fermenter volume, 20 DEG C -25 DEG C of fermentation temperature, sternly The static anaerobic fermentation of lattice, carries out profound fermentation, and fermentation time 1 month obtains K product;
L.K product are imported in concentration tank, and concentration condition is:45 DEG C of thickening temperature, vacuum degree 0.09MPa are concentrated to stoste 75%, obtain L product;
The strainer filtering of m.L product 300-400 mesh collects filtrate, obtains M product;
The maltodextrin of M product weight 8% is added in n.M product, stirs evenly, obtains N product;
O. uniform filtration, homogeneous 1 time filter the strainer used and control in 300-400 mesh, obtain O product;
P.O product sterilize carry out degerming by the way of filtration sterilization or high temperature sterilization;The degerming is filtration sterilization temperature It spends for room temperature, sterilization mode uses ultra high temperature short time sterilization or microwave disinfection, 135 DEG C of -140 DEG C of processing of ultra high temperature short time sterilization 5s-8s, ultra high temperature short time sterilization speed needs and spray drying speeds match;Microwave pipe-line sterilizes 60 DEG C -65 DEG C and handles 2 points Clock;Obtain P product;
Q. it is spray-dried:140 DEG C -160 DEG C of inlet air temperature is controlled, 85 DEG C -95 DEG C of leaving air temp goes out powder moisture requirement and exists Less than 5%, the requirement of powder ambient humidity is received less than 30%, is received powder with food-grade packaging bag, is obtained Q product;
R. by Q product, white sand, Icing Sugar, xylo-oligosaccharide, D-sorbite, hawthorn powder, blueberry powder, the weight for mixing probiotic powder Than for 50:40:15:10:20:5:5:5 by Q product white sand, Icing Sugar, xylo-oligosaccharide, D-sorbite, hawthorn powder, blueberry powder and mixing Probiotic powder mixing, pack to get;The mixing probiotic powder is Lactobacillus rhamnosus.

Claims (5)

1. a kind of production technology of dragon fruit ferment powder, it is characterised in that:Comprise the following steps;
A. full maturity is chosen, pulp is in peony or claret-colored red heart dragon fruit, after cleaning, drains, obtains A product;
B.A product are removed the peel, and are cut into the block that the length of side is 1-2mm, are obtained B product;
C. yellow lemon is chosen, after cleaning, drains, obtains C product;
D.C product are removed the peel, and are cut into the block that the length of side is 1-2mm, are obtained D product;
E. the order of white granulated sugar, B product and D product is pressed from top to bottom, white granulated sugar, B product and D product is stacked by layer, lower tank amount is no more than Fermenter volume 80% obtains E product;
Saccharomyces cerevisiae is inoculated on f.E product, the 0.1%-0.2% of inoculum concentration E product weight obtains F product;
G.F product sealed fermentings, 25 DEG C -30 DEG C of fermentation temperature, fermentation time 5-10 days, midway stir 1-2 times or take juice from bottom Leaching Slag treatment is carried out to upper strata slag 2 times, obtain G product;
H. G product are crossed into 60-80 mesh filter screens, zymotic fluid and pomace separation, collects zymotic fluid, obtain H product;
I.H product are transferred in another clean fermentation tank and carry out second of fermentation, and when fermenting for the second time, the canned liquid that ferments holds for fermentation tank Long-pending more than 90%, strictly anaerobic standing for fermentation, 25 DEG C -30 DEG C of fermentation temperature, fermentation time 5-10 days treat that zymotic fluid face is quiet Only, when bubble-free generates, fermentation ends obtain I product;
J. the high fermentation liquid in i product is collected liquid, obtains J product using after 300 mesh filter-cloth filterings;
K.J product import clean fermentation tank, and the canned liquid that ferments is more than the 90% of fermenter volume, 20 DEG C -25 DEG C of fermentation temperature, sternly The static anaerobic fermentation of lattice, carries out profound fermentation, and fermentation time 1 month to 12 months obtains K product;
L.K product are imported in concentration tank, and concentration condition is:45 DEG C, vacuum degree 0.09MPa of thickening temperature is concentrated to the 75%- of stoste 85%, obtain L product;
The strainer filtering of m.L product 300-400 mesh collects filtrate, obtains M product;
The maltodextrin of M product weight 8%-20% and the vitamin C of M product weight 0%-0.5% are added in n.M product, stirs evenly, obtains N product;
O. uniform filtration, homogeneous 1-2 times filter the strainer used and control in 300-400 mesh, obtain O product;
P.O product sterilize carry out degerming by the way of filtration sterilization or high temperature sterilization;The degerming is that filtration sterilization temperature is Room temperature, sterilization mode use ultra high temperature short time sterilization or microwave disinfection, and 135 DEG C -140 DEG C of ultra high temperature short time sterilization handles 5s-8s, Ultra high temperature short time sterilization speed needs and spray drying speeds match;Microwave pipe-line is sterilized 60 DEG C -65 DEG C and is handled 2-5 minutes;Obtain P Product;
Q. it is spray-dried:Control 140 DEG C -160 DEG C of inlet air temperature, 85 DEG C -95 DEG C of leaving air temp, go out powder moisture requirement 5% with Under, the requirement of powder ambient humidity is received less than 30%, is received powder with food-grade packaging bag, is obtained Q product;
R. it is by the weight ratio of Q product, white sand, Icing Sugar, xylo-oligosaccharide, D-sorbite, hawthorn powder, blueberry powder, mixing probiotic powder 50-80:15-40:5-15:3-10:0-20:0-5:0-5:0-5 is by Q product white sand, Icing Sugar, xylo-oligosaccharide, D-sorbite, hawthorn Powder, blueberry powder and mixing probiotic powder mixing, pack to get.
2. the production technology of dragon fruit ferment powder as described in claim 1, it is characterised in that:The mixing probiotic powder is Bifidobacterium longum, lactobacillus acidophilus, lactobacillus plantarum or Lactobacillus rhamnosus.
3. the production technology of dragon fruit ferment powder as described in claim 1, it is characterised in that:In step e, the flue The mass ratio of fruit, lemon and white granulated sugar is:70-85:8-13:10-16.
4. the production technology of dragon fruit ferment powder as claimed in claim 3, it is characterised in that:The dragon fruit, lemon and The mass ratio of white granulated sugar is:75-80:9-12:12-14.
5. the production technology of dragon fruit ferment powder as claimed in claim 4, it is characterised in that:The dragon fruit, lemon and The mass ratio of white granulated sugar is:78:10:13.
CN201711310858.8A 2017-12-11 2017-12-11 A kind of production technology of dragon fruit ferment powder Pending CN108041582A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201711310858.8A CN108041582A (en) 2017-12-11 2017-12-11 A kind of production technology of dragon fruit ferment powder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201711310858.8A CN108041582A (en) 2017-12-11 2017-12-11 A kind of production technology of dragon fruit ferment powder

Publications (1)

Publication Number Publication Date
CN108041582A true CN108041582A (en) 2018-05-18

Family

ID=62124051

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201711310858.8A Pending CN108041582A (en) 2017-12-11 2017-12-11 A kind of production technology of dragon fruit ferment powder

Country Status (1)

Country Link
CN (1) CN108041582A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110432490A (en) * 2019-09-25 2019-11-12 贵州钏泰农业科技发展有限公司贞丰分公司 A kind of production method of dragon fruit ferment
CN112220038A (en) * 2020-08-31 2021-01-15 海南满家福健康科技有限公司 Production process of noni dry powder
CN112220039A (en) * 2020-08-31 2021-01-15 海南满家福健康科技有限公司 Noni fruit enzyme production method

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104664405A (en) * 2014-09-04 2015-06-03 杭州隽艺生物技术有限公司 Fat-reducing and weight-losing fruit enzyme powder and preparation method thereof
CN105495622A (en) * 2015-12-24 2016-04-20 广西良樱农业科技有限公司 Pitaya enzyme making method
CN105661245A (en) * 2016-01-29 2016-06-15 江苏微康生物科技有限公司 Probiotic type fruit and vegetable enzyme solid drink
CN106174172A (en) * 2016-07-01 2016-12-07 广西平果宝裕生态农业开发有限公司 Sour-sweet Hylocereus undatus ferment and preparation method thereof
CN106173773A (en) * 2016-07-06 2016-12-07 慧谷生命科技湖北有限公司 A kind of ferment probiotic bacteria solid beverage and preparation method thereof
CN106973994A (en) * 2017-04-14 2017-07-25 广西宁明百事康生物工程有限公司 The preparation method of passion fruit enzyme yogurt rich in vitamin
CN107114546A (en) * 2017-04-19 2017-09-01 句容金坤农业科技有限公司 A kind of preparation method of red heart dragon fruit ferment pressed candy

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104664405A (en) * 2014-09-04 2015-06-03 杭州隽艺生物技术有限公司 Fat-reducing and weight-losing fruit enzyme powder and preparation method thereof
CN105495622A (en) * 2015-12-24 2016-04-20 广西良樱农业科技有限公司 Pitaya enzyme making method
CN105661245A (en) * 2016-01-29 2016-06-15 江苏微康生物科技有限公司 Probiotic type fruit and vegetable enzyme solid drink
CN106174172A (en) * 2016-07-01 2016-12-07 广西平果宝裕生态农业开发有限公司 Sour-sweet Hylocereus undatus ferment and preparation method thereof
CN106173773A (en) * 2016-07-06 2016-12-07 慧谷生命科技湖北有限公司 A kind of ferment probiotic bacteria solid beverage and preparation method thereof
CN106973994A (en) * 2017-04-14 2017-07-25 广西宁明百事康生物工程有限公司 The preparation method of passion fruit enzyme yogurt rich in vitamin
CN107114546A (en) * 2017-04-19 2017-09-01 句容金坤农业科技有限公司 A kind of preparation method of red heart dragon fruit ferment pressed candy

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110432490A (en) * 2019-09-25 2019-11-12 贵州钏泰农业科技发展有限公司贞丰分公司 A kind of production method of dragon fruit ferment
CN112220038A (en) * 2020-08-31 2021-01-15 海南满家福健康科技有限公司 Production process of noni dry powder
CN112220039A (en) * 2020-08-31 2021-01-15 海南满家福健康科技有限公司 Noni fruit enzyme production method

Similar Documents

Publication Publication Date Title
CN104232422B (en) A kind of brewing method of blueberry fruit wine
CN104509907A (en) Composite plant ferment vinegar beverage and preparation method thereof
CN105410546B (en) Composite plant beverage rich in anthocyanidin and preparation method thereof
CN107981342A (en) A kind of production technology of dragon fruit ferment in good taste
CN105475763B (en) Mulberries blueberry plant beverage rich in anthocyanidin and preparation method thereof
CN101285023B (en) Red raspberry health wine and brewing process thereof
CN104489669A (en) Plant enzyme probiotic powder and preparation method thereof
CN105455128A (en) Rosa roxburghii enzyme and preparation method thereof
CN106616165A (en) Rose probiotic ferment beverage and production method thereof
CN106235308A (en) A kind of Bulbus Allii ferment and preparation method thereof
CN101955867B (en) Chrysanthemum dry red wine
CN108041582A (en) A kind of production technology of dragon fruit ferment powder
CN110042032A (en) A kind of preparation process of compound fruit wine
CN106165742A (en) The production equipment of ferment local-flavor tea concentrated solution and manufacture method
CN109042997A (en) A kind of health protection tea and preparation method thereof adjusting intestinal microecology
CN108112847A (en) A kind of preparation method of mulberry juice
CN102783692A (en) Innovative astringency removal technique for olive juice and innovative bitter removal technique for citrus juice
CN109730281A (en) Fermented tea emblic jelly and preparation method thereof
CN109998001A (en) A kind of preparation and its production technology of the collagen peptide drink of the ferment containing dragon fruit
CN108728307A (en) A kind of cherry health fruit and preparation method thereof
CN104026235A (en) Cranberry collagen polypeptide Ca yoghurt
CN107232472A (en) A kind of cherry instant beverage
CN107853699A (en) A kind of production method of dragon fruit ferment
CN106010866A (en) Snow pear and green tea fermented tea wine and preparation method thereof
CN110537700A (en) Preparation method of roxburgh rose fruit enzyme and lucid ganoderma fruit enzyme

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
RJ01 Rejection of invention patent application after publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20180518