CN111174534A - Dynamic vacuum microwave drying method for berries with shells and product - Google Patents

Dynamic vacuum microwave drying method for berries with shells and product Download PDF

Info

Publication number
CN111174534A
CN111174534A CN201811337330.4A CN201811337330A CN111174534A CN 111174534 A CN111174534 A CN 111174534A CN 201811337330 A CN201811337330 A CN 201811337330A CN 111174534 A CN111174534 A CN 111174534A
Authority
CN
China
Prior art keywords
shell
berry
drying
berries
microwave
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
CN201811337330.4A
Other languages
Chinese (zh)
Inventor
齐爱民
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.)
Qiji Technology Co ltd
Original Assignee
Qiji 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 Qiji Technology Co ltd filed Critical Qiji Technology Co ltd
Priority to CN201811337330.4A priority Critical patent/CN111174534A/en
Publication of CN111174534A publication Critical patent/CN111174534A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B3/00Drying solid materials or objects by processes involving the application of heat
    • F26B3/32Drying solid materials or objects by processes involving the application of heat by development of heat within the materials or objects to be dried, e.g. by fermentation or other microbiological action
    • F26B3/34Drying solid materials or objects by processes involving the application of heat by development of heat within the materials or objects to be dried, e.g. by fermentation or other microbiological action by using electrical effects
    • F26B3/347Electromagnetic heating, e.g. induction heating or heating using microwave energy
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23BPRESERVING, e.g. BY CANNING, MEAT, FISH, EGGS, FRUIT, VEGETABLES, EDIBLE SEEDS; CHEMICAL RIPENING OF FRUIT OR VEGETABLES; THE PRESERVED, RIPENED, OR CANNED PRODUCTS
    • A23B7/00Preservation or chemical ripening of fruit or vegetables
    • A23B7/02Dehydrating; Subsequent reconstitution
    • 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
    • A23L19/00Products from fruits or vegetables; Preparation or treatment thereof
    • A23L19/03Products from fruits or vegetables; Preparation or treatment thereof consisting of whole pieces or fragments without mashing the original pieces
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23NMACHINES OR APPARATUS FOR TREATING HARVESTED FRUIT, VEGETABLES OR FLOWER BULBS IN BULK, NOT OTHERWISE PROVIDED FOR; PEELING VEGETABLES OR FRUIT IN BULK; APPARATUS FOR PREPARING ANIMAL FEEDING- STUFFS
    • A23N12/00Machines for cleaning, blanching, drying or roasting fruits or vegetables, e.g. coffee, cocoa, nuts
    • A23N12/08Machines for cleaning, blanching, drying or roasting fruits or vegetables, e.g. coffee, cocoa, nuts for drying or roasting
    • A23N12/10Rotary roasters
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B25/00Details of general application not covered by group F26B21/00 or F26B23/00
    • F26B25/04Agitating, stirring, or scraping devices
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B5/00Drying solid materials or objects by processes not involving the application of heat
    • F26B5/04Drying solid materials or objects by processes not involving the application of heat by evaporation or sublimation of moisture under reduced pressure, e.g. in a vacuum
    • 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 provides a dynamic vacuum microwave drying method and a product of berries with shells, belonging to the technical field of fruit and vegetable dehydration processing, and the key points of the technical scheme comprise the following steps: the method comprises the following steps: pre-treating; step two: punching; step three: sterilizing; step four: containing; step five: vacuum microwave drying; step six: balancing the water content; step seven: natural fermentation makes the flavor of the dried fruit richer; step eight: packaging; the dried fruit of a developments vacuum microwave drying area shell berry of producing through this application technical scheme has preserved the product primary color well, and drying time is short, the even difficult shell that explodes of heating has remain complete shell and has preserved the fibrous shape that fruit was originally simultaneously, has improved the rehydration rate, has increased elasticity, reduces viscidity. The dried fruit has richer flavor due to natural fermentation, and in addition, due to the selective heating effect of the microwave on water, the raw materials can be quickly dried at a lower temperature, so that the method has great significance for improving the quality of finished products and reducing the loss of nutrient components.

Description

Dynamic vacuum microwave drying method for berries with shells and product
Technical Field
The invention relates to the technical field of fruit and vegetable dehydration processing, in particular to a dehydration processing method and a product of berry with a shell.
Background
The resources of fruits and vegetables in China are rich, and with the increase of the demand of people for high-quality instant food, the drying technology of various fruits and vegetables such as grapes, mangoes, strawberries, blueberries, bitter gourds, mushrooms and the like is continuously improved along with the technological progress. The fruits and vegetables contain water, sugar, protein, vitamins and a plurality of essential amino acids which can not be synthesized by human bodies, and the like, are rich in mineral elements and are main sources of calcium, phosphorus, potassium, magnesium and iron of the human bodies. The fruits and vegetables also contain rich dietary fibers, and are indispensable components for balanced diet. The traditional drying methods mainly comprise natural drying, shade drying and hot air drying, but the methods generally have the technical problems of high energy consumption, low production capacity, low efficiency and difficult guarantee of product control, and are not beneficial to the further development of the fruit and vegetable drying manufacturing industry. At present, the novel fruit and vegetable drying technology comprises permeation drying, spray drying, roller drying, fluidized bed drying, far infrared drying, vacuum freeze drying, microwave drying, vacuum frying drying, CO2 puffing drying, low-temperature high-pressure puffing drying and the like, each drying mode has the advantages and disadvantages, and the most suitable drying method is adopted according to different food raw materials and product requirements.
Although the traditional drying technology has a plurality of advantages, the temperature and the heating point are often difficult to control, so that local overheating, browning, cracking of the berry with the shell and the like are caused. Influences the nutritional ingredients and value of the dried berries with shells and reduces the quality and efficacy of the product.
The above background disclosure is only for the purpose of assisting understanding of the inventive concept and technical solutions of the present invention, and does not necessarily belong to the prior art of the present patent application, and should not be used for evaluating the novelty and inventive step of the present application in the case that there is no clear evidence that the above content is disclosed at the filing date of the present patent application.
Disclosure of Invention
In order to overcome the defects of the prior art, the invention provides a dynamic vacuum microwave drying method and a product of berries with shells.
The invention solves the problems through the following technical scheme:
a dynamic vacuum microwave drying method of berry with shell comprises the following steps:
s1: pre-treating;
s2: punching: punching the surface of the berry with the shell obtained in the step S1;
s3: and (3) sterilization: sterilizing the berries with the shells obtained in the step S2 by an ultraviolet lamp;
s4: containing: placing the berries with the shells obtained in the step S3 in a material turntable containing a stirring fan, and placing the berries into a microwave rectangular resonant cavity;
s5: vacuum microwave drying: keeping a microwave rectangular resonant cavity in a vacuum state, intermittently accessing microwaves in a pulse mode through a microwave pulse system, stirring the berry with the shell at a constant speed by a stirring fan, simultaneously rotating a material turntable at a constant speed, drying the berry with the shell by microwaves until the water content of the berry with the shell is 12-25%, and discharging the water generated by the microwave drying out of equipment through a low-temperature condensation trap device;
s6, equilibrium water content: performing spot check on the water content of the berry with the shell obtained in the step S5, and if the water content is not balanced, placing the dried fruit in a sterile environment with the humidity of 30-50% for standing for 12-36 hours;
s7: and (3) natural fermentation: naturally fermenting the dried fruits obtained in the step S6 without enzyme;
s8: packaging: and (5) performing secondary drying on the dried fruit obtained in the step (S7) until the water content of the dried fruit with shell is controlled within 15%, and packaging.
Preferably, in the dynamic vacuum microwave drying method of the shelled berries, in step S1, the pretreatment comprises the following steps:
s1.1: selecting materials: selecting fresh, disease and insect pest-free and mildew-free berries with shells as raw materials;
s1.2: grading: manually or mechanically grading the berry with the shell, placing the berry with the shell in a mechanical conveying device during mechanical grading, and when the berry with the shell is transmitted to an image acquisition point, utilizing a bionic vision system to carry out information analysis on the image with the shell and transmitting the image with the shell to a central control system, feeding back a sorting result to the central control system, and shunting and classifying the quality of the berry with the shell;
s1.3: cleaning: and (4) washing the same-grade shelled berries to be dried obtained in the step (S1.2) by using clear water.
Preferably, in the step S3, the ultraviolet sterilization temperature is 25-35 ℃, the ultraviolet wavelength range is 271-289 nm, and the sterilization time is 10-15 min.
Preferably, in the dynamic vacuum microwave drying method for the shelled berries, in step S4, the stacked height of the shelled berries contained in the material rotating disc is not more than 8 cm.
Preferably, in the step S5, the vacuum degree in the microwave rectangular resonant cavity during drying is-0.085 Mpa, the absolute temperature is less than or equal to 60 ℃, the stirring speed of the stirring fan is 15-25 times/min, and the rotating speed of the material turntable is 50-60 r/min.
Preferably, a bionic electronic nose system and a bionic visual system are arranged in the microwave rectangular resonant cavity, the bionic electronic nose system receives volatile gas information generated in the drying process of the berry with the shell, the bionic visual system receives picture information such as color and appearance of the berry with the shell in the drying process, the gas information and the picture information are converted into digital signals, and the digital signals are transmitted to a central control system for recording and analyzing and constructing a drying evaluation model of the berry with the shell.
Preferably, the evaluation indexes in the drying evaluation model of the shelled berries comprise browning degree, odor parameters and moisture ratio MRAnd the shape parameter.
The surface color quality of the berry with the shell is measured by a CR-300 color difference meter, the average value is obtained after three times of measurement, the browning degree is evaluated by a white-turning index WI, and the formula is as follows:
Figure BDA0001861580160000031
l coordinates range from 0 (black) to 100 (white), a coordinates represent red-green, b coordinates represent yellow-blue;
moisture ratio MRIs calculated by the formula
Figure BDA0001861580160000032
In the formula MtThe water content (%) at the drying time t, MeIndicates the equilibrium water content (%), M0The initial water content (%) is shown.
Preferably, in the method for dynamically drying the berry with the shell by the vacuum microwave, the microwave pulse system dynamically adjusts the size and the pulse frequency of the microwave according to the drying evaluation model of the berry with the shell generated by the central control system, and the microwave rectangular resonant cavity dynamically adjusts the drying temperature according to the drying evaluation model of the berry with the shell generated by the central control system.
Preferably, in the dynamic vacuum microwave drying method of the berry with the shell, the temperature of the natural enzyme-free fermentation in the step S8 is 0-25 ℃, and the fermentation time is 7-15 days.
A dynamic vacuum microwave drying of dried fruit with shell berry, the invention claims a dynamic vacuum microwave drying of dried fruit with shell berry is the dried fruit produced by the whole steps of claims 1-9.
The invention has the advantages and effects that:
according to the microwave vacuum drying equipment, the dynamic rotating tray is arranged in the microwave vacuum drying equipment, so that the berry with the shell is heated uniformly in the drying process, the water content is more balanced, the problem of nonuniform heating in the dehydration process of the dried fruit is solved, and the energy utilization rate is improved. Meanwhile, the method for punching the surface of the berry with the shell ensures that the air pressure inside and outside the shell is balanced, the problem that the shell is easy to explode in the drying process of the berry with the shell is solved, the integrity of the shell is kept, the browning is not easy to occur in the storage process, and simultaneously, the drying energy consumption of each kilogram of the berry with the shell is only 3 gross money which is far lower than the energy consumption cost of other common drying technologies in the market. The dried berry with the shell produced by the dynamic vacuum microwave drying method provided by the invention can keep good color, and the complete shell can isolate the pulp from the outside, so that the pulp is cleaner and more sanitary.
The specific implementation mode is as follows:
the present invention is further illustrated by the following examples.
Example 1:
a dynamic vacuum microwave drying method for longan comprises the following steps:
s1: pre-treating;
s1.1: selecting materials: selecting fresh longan fruit bodies without diseases, insect pests and mildew as raw materials;
s1.2: grading: artificially classifying the longan into three grades of top grade, middle grade and bottom grade;
s1.3: cleaning: washing the same-grade longan with clear water at 25 ℃;
s2: punching: drilling a small hole with the diameter of 1mm on each surface of the longan obtained in the step S1;
s3: and (3) sterilization: sterilizing longan obtained in step S2 with ultraviolet lamp at 25 deg.C and wavelength of 280nm for 10 min;
s4: containing: placing the longans obtained in the step S3 in a material rotating disc containing a stirring fan, and placing the material rotating disc in a microwave rectangular resonant cavity, wherein the stacking height of the longans placed in the material rotating disc is 8 cm;
s5: vacuum microwave drying: a bionic electronic nose system and a bionic visual system are arranged in the microwave rectangular resonant cavity, the bionic electronic nose system receives odor information of alkenes, esters and alcohols generated in the drying process of the longan, the bionic visual system receives picture information of colors, shapes and the like in the drying process of the longan, the gas information and the picture information are converted into digital signals and transmitted to a central control system for recording and analyzing, and a longan drying evaluation model is constructed.
The evaluation indexes in the longan drying evaluation model comprise browning degree, odor parameters and water content ratio MRAnd the shape parameter.
The longan surface color quality is measured by a CR-300 color difference meter, the average value is obtained by measuring three times, the browning degree is evaluated by a white-turning index WI, and the formula is as follows:
Figure BDA0001861580160000041
l coordinates range from 0 (black) to 100 (white), a coordinates represent red-green, b coordinates represent yellow-blue;
moisture ratio MRIs calculated by the formula
Figure BDA0001861580160000042
In the formula MtThe water content (%) at the drying time t, MeIndicates the equilibrium water content (%), M0The initial water content (%) is shown.
Keeping the vacuum state in the microwave rectangular resonant cavity at-0.085 Mpa, dynamically adjusting the microwave size and pulse frequency in a pulse mode by a microwave pulse system according to a longan drying evaluation model generated by a central control system, intermittently accessing microwaves, and dynamically adjusting the drying temperature. Stirring longan at a constant speed of 15 times/min by a stirring fan, simultaneously rotating a material turntable at a constant speed of 50r/min, drying longan until the water content is 25%, and discharging the water generated by microwave drying out from the equipment through a low-temperature condensation trap device.
S6: balancing water content: performing spot check on the water content of the dried longan obtained in the step S5, keeping the dried longan at an unbalanced water content, and standing the dried longan in a sterile environment with the humidity of 30% for 18 hours;
s7: and (3) natural fermentation: naturally fermenting the dried longan obtained in the step S6 at 15 ℃ for 7 days without enzyme;
s8: packaging: and (4) performing secondary drying on the dried fruits obtained in the step (S7) until the moisture content of the dried longan is controlled within 15%, and packaging.
A dynamic vacuum microwave dried longan was produced through the steps S1-S7.
In order to explain the beneficial effects of the invention in detail, the experimental results are further provided.
Fresh longans with the same quality, the same production area and the same quality are randomly divided into four groups, and are respectively dehydrated and dried by three common berry drying methods with shells and the method of one embodiment of the invention, wherein the main conditions of the three common fruit and vegetable drying methods are shown in the following table.
Figure BDA0001861580160000051
The relevant physicochemical properties of the dried longan finished products produced in the four different processing procedures were detected and recorded, as shown in the following table.
Figure BDA0001861580160000052
Figure BDA0001861580160000061
While the preferred embodiments of the present invention have been described in detail, it is to be understood that the invention is not limited thereto, and that various equivalent modifications and substitutions may be made by those skilled in the art without departing from the spirit of the present invention and are intended to be included within the scope of the present application.

Claims (10)

1. A dynamic vacuum microwave drying method of berries with shells is characterized by comprising the following steps:
s1: pre-treating;
s2: punching: punching the surface of the berry with the shell obtained in the step S1;
s3: and (3) sterilization: sterilizing the berries with the shells obtained in the step S2 by an ultraviolet lamp;
s4: containing: placing the berries with the shells obtained in the step S3 in a material turntable containing a stirring fan, and placing the berries into a microwave rectangular resonant cavity;
s5: vacuum microwave drying: keeping a microwave rectangular resonant cavity in a vacuum state, intermittently accessing microwaves in a pulse mode through a microwave pulse system, stirring the berry with the shell at a constant speed by a stirring fan, simultaneously rotating a material turntable at a constant speed, drying the berry with the shell by microwaves until the water content of the berry with the shell is 12-25%, and discharging the water generated by the microwave drying out of equipment through a low-temperature condensation trap device;
s6, equilibrium water content: performing spot check on the water content of the berry with the shell obtained in the step S5, and if the water content is not balanced, placing the dried fruit in a sterile environment with the humidity of 30-50% for standing for 12-36 hours;
s7: and (3) natural fermentation: naturally fermenting the dried fruits obtained in the step S6 without enzyme;
s8: packaging: and (5) performing secondary drying on the dried fruit obtained in the step (S7) until the water content of the dried fruit with shell is controlled within 15%, and packaging.
2. The dynamic vacuum microwave drying method of shelled berries in accordance with claim 1, wherein the pre-treatment in step S1 comprises the steps of:
s1.1: selecting materials: selecting fresh, disease and insect pest-free and mildew-free berries with shells as raw materials;
s1.2: grading: manually or mechanically grading the berry with the shell, placing the berry with the shell in a mechanical conveying device during mechanical grading, and when the berry with the shell is transmitted to an image acquisition point, utilizing a bionic vision system to carry out information analysis on the image with the shell and transmitting the image with the shell to a central control system, feeding back a sorting result to the central control system, and shunting and classifying the quality of the berry with the shell;
s1.3: cleaning: and (4) washing the same-grade shelled berries to be dried obtained in the step (S1.2) by using clear water.
3. The dynamic vacuum microwave drying method of shelled berries according to claim 1, wherein the ultraviolet sterilization temperature in step S3 is 25-35 ℃, the ultraviolet wavelength range is 271-289 nm, and the sterilization time is 10-15 min.
4. The dynamic vacuum microwave drying method of shelled berries, as claimed in claim 1, wherein in step S4, the height of the stack of shelled berries held in the material carousel does not exceed 8 cm.
5. The dynamic vacuum microwave drying method of berry with shell as claimed in claim 1, wherein in step S5, the vacuum degree inside the microwave rectangular resonant cavity is-0.085 Mpa, the absolute temperature is less than or equal to 60 ℃, the stirring speed of the stirring fan is 15-25 times/min, and the rotation speed of the material turntable is 50-60 r/min.
6. The dynamic vacuum microwave drying method for berry with shell as claimed in claim 1, wherein a bionic electronic nose system and a bionic vision system are arranged in the microwave rectangular resonant cavity, the bionic electronic nose system receives volatile gas information generated during the drying process of berry with shell, the bionic vision system receives picture information such as color and shape during the drying process of berry with shell, and converts the gas information and the picture information into digital signals to be transmitted to a central control system for recording and analyzing and constructing a drying evaluation model of berry with shell.
7. The dynamic vacuum microwave drying method of a shelled berry according to claim 6, wherein the evaluation indexes in the drying evaluation model of the shelled berry include browning degree, odor parameters, moisture ratio MRAnd the shape parameter;
the surface color quality of the berry with the shell is measured by a CR-300 color difference meter, the average value is obtained after three times of measurement, the browning degree is evaluated by a white-turning index WI, and the formula is as follows:
Figure FDA0001861580150000021
l coordinates range from 0 (black) to 100 (white), a coordinates represent red-green, b coordinates represent yellow-blue;
moisture ratio MRIs calculated by the formula
Figure FDA0001861580150000022
In the formula MtIndicating the drying time tWater content (%), MeIndicates the equilibrium water content (%), M0The initial water content (%) is shown.
8. The method of claim 1, wherein the microwave pulsing system dynamically adjusts the microwave frequency and the microwave intensity according to a dryness evaluation model of the berry with shell generated by the central control system, and the microwave rectangular resonant cavity dynamically adjusts the drying temperature according to the dryness evaluation model of the berry with shell generated by the central control system.
9. The dynamic vacuum microwave drying process of a shelled berry according to claim 1, wherein the temperature of the natural enzyme-free fermentation in step S8 is 0-25 degrees and the fermentation time is 7-15 days.
10. A dynamic vacuum microwave drying of dried fruit with shell berries, characterized in that a dynamic vacuum microwave drying of dried fruit with shell berries is a dried fruit produced by all the steps of claims 1-9.
CN201811337330.4A 2018-11-12 2018-11-12 Dynamic vacuum microwave drying method for berries with shells and product Pending CN111174534A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201811337330.4A CN111174534A (en) 2018-11-12 2018-11-12 Dynamic vacuum microwave drying method for berries with shells and product

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201811337330.4A CN111174534A (en) 2018-11-12 2018-11-12 Dynamic vacuum microwave drying method for berries with shells and product

Publications (1)

Publication Number Publication Date
CN111174534A true CN111174534A (en) 2020-05-19

Family

ID=70624113

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201811337330.4A Pending CN111174534A (en) 2018-11-12 2018-11-12 Dynamic vacuum microwave drying method for berries with shells and product

Country Status (1)

Country Link
CN (1) CN111174534A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111765723A (en) * 2020-07-13 2020-10-13 四川卢川中药材开发有限公司 Longan pulp drying method
RU2781965C1 (en) * 2022-01-19 2022-10-21 Федеральное государственное бюджетное образовательное учреждение высшего образования "Кузбасская государственная сельскохозяйственная академия" Method for vacuum drying of sea buckthorn

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000042406A (en) * 1998-07-31 2000-02-15 Erii Kk Production of concentrated substance
CN201615680U (en) * 2010-02-10 2010-10-27 梁宏 Stirring type microwave vacuum drier
CN101878882A (en) * 2010-04-30 2010-11-10 陆爱章 Processing method of dried lychee and dried longan
CN102715469A (en) * 2012-06-26 2012-10-10 广西名香园食品有限公司 Dried litchi processing method
CN103622022A (en) * 2013-12-12 2014-03-12 桂林千烨农产品有限公司 Method for preparing high-quality dried momordica grosvenori

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000042406A (en) * 1998-07-31 2000-02-15 Erii Kk Production of concentrated substance
CN201615680U (en) * 2010-02-10 2010-10-27 梁宏 Stirring type microwave vacuum drier
CN101878882A (en) * 2010-04-30 2010-11-10 陆爱章 Processing method of dried lychee and dried longan
CN102715469A (en) * 2012-06-26 2012-10-10 广西名香园食品有限公司 Dried litchi processing method
CN103622022A (en) * 2013-12-12 2014-03-12 桂林千烨农产品有限公司 Method for preparing high-quality dried momordica grosvenori

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
李辉: "《荔枝果肉微波真空干燥特性与动力学模型》", 《荔枝果肉微波真空干燥特性与动力学模型》 *
杨晓童: "《荔枝微波真空干燥及前处理设备研发及干制品品质调控研究》", 《荔枝微波真空干燥及前处理设备研发及干制品品质调控研究》 *
罗树灿: "《荔枝结合干燥工艺的初步研究》", 《荔枝结合干燥工艺的初步研究》 *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111765723A (en) * 2020-07-13 2020-10-13 四川卢川中药材开发有限公司 Longan pulp drying method
RU2781965C1 (en) * 2022-01-19 2022-10-21 Федеральное государственное бюджетное образовательное учреждение высшего образования "Кузбасская государственная сельскохозяйственная академия" Method for vacuum drying of sea buckthorn

Similar Documents

Publication Publication Date Title
CN101933617B (en) Puffed pleurotus eryngii chip production process and puffed pleurotus eryngii chip products
CN101301012B (en) Tea processing and producing method
CN101427757B (en) Method for producing puffing sweet potato slice and products produced thereby
CN101579031B (en) Method for preparing puffed crisp carrot cubes
EP0336571B1 (en) A method for preparing reconstitutable refried beans containing crused and whole beans
CN102907626A (en) Making method for dehydration tempeh
CN106260454A (en) A kind of processing method of instant mushroom crispy slice
CN103393096B (en) Brewing-type instant tremella and preparation method thereof
CN111174534A (en) Dynamic vacuum microwave drying method for berries with shells and product
RU1793888C (en) Method for production of tinned snack foods
CN1248405A (en) Method for producing pesticide-eating fungus floor
CN101810291B (en) Method for preparing packaged fermentative pickling wild pepper
CN111165567A (en) Dynamic vacuum microwave drying method of shiitake mushrooms and product
CN101836671A (en) Method for processing crispy fresh jujube
RU2277818C2 (en) Method for producing of canned cabbage rolls stuffed with fish
CN107712244A (en) A kind of pear cv nanguo preserved fruit(Preserved fruit)Processing method
CN113079946A (en) Edible fungus cultivation method and culture medium
KR20180086620A (en) Method for production of fermented coffee bean
KR101401543B1 (en) Manufacturing methods of dried blueberry and processed products containing dried blueberry
KR100653646B1 (en) manufacturing method of drink with fruit extracting juice mixing fermented soybeans
CN108812059A (en) A kind of method for planting almond abalone mushroom based on Internet of Things
CN103461628A (en) Method for producing coated peanuts at low temperature and variable pressure
CN113475693B (en) Nutritional fruit and vegetable crisp chips and production method thereof
CN109303305A (en) A kind of method that low-temperature bake produces milky white shelled peanut
CN109303310A (en) A kind of method that low-temperature bake produces peanut half

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
WD01 Invention patent application deemed withdrawn after publication
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20200519