CN103141564B - Vacuum freezing puff-drying processing method of hawthorn - Google Patents

Vacuum freezing puff-drying processing method of hawthorn Download PDF

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CN103141564B
CN103141564B CN201310102229.1A CN201310102229A CN103141564B CN 103141564 B CN103141564 B CN 103141564B CN 201310102229 A CN201310102229 A CN 201310102229A CN 103141564 B CN103141564 B CN 103141564B
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hawthorn
bulking tank
temperature
heating plate
type heat
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CN103141564A (en
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张克林
孙曙光
冀利
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SHANDONG ZHANHUA HAOHUA JUICE CO Ltd
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SHANDONG ZHANHUA HAOHUA JUICE CO Ltd
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P60/00Technologies relating to agriculture, livestock or agroalimentary industries
    • Y02P60/80Food processing, e.g. use of renewable energies or variable speed drives in handling, conveying or stacking
    • Y02P60/85Food storage or conservation, e.g. cooling or drying

Abstract

The invention discloses a vacuum freezing puff-drying processing method of hawthorn, and belongs to dry-processing of hawthorn. The method comprises the following steps: (1) pre-treating raw material: carrying out picking, cleaning and kernel penetrating treatment on fresh hawthorn; soaking the treated hawthorn in a sugar solution with 40% of sugar content for 12h, then taking the hawthorn out for sprinkling, removing the sugar solution on the surface of the hawthorn, and draining off water; (3) spreading the dry hawthorn to form a single layer uniformly distributed on a material tray, putting the hawthorn into an instant freezer, quickly freezing the hawthorn at -40 DEG C for 4-6 hours to ensure that water in the hawthorn is completely frozen; and (4)carrying out vacuum freezing puff-drying with a vacuum freezing puff-dryer. The processing method can maintain the original biological activity and nutritious components of hawthorn food to the maximum extent and improve the mouthfeel, and has the characteristics of good crispness, intact outer appearance, good mouthfeel, prolonged shelf life, no need of any additive and antiseptic, relatively low drying energy consumption, improved production efficiency, and the like.

Description

The vacuum refrigeration explosion puffing drying processing method of a kind of hawthorn
Technical field
The present invention relates to the drying of a kind of hawthorn, the vacuum refrigeration explosion puffing drying processing method of especially a kind of hawthorn.
Background technology
Hawthorn has important medical value, since ancient times, just becomes the good medicine of spleen benefiting and stimulating the appetite, relieving dyspepsia, phlegm reduction of blood circulation promoting.Hawthorn is containing materials such as carbohydrate, protein, fat, vitamin C, carrotene, starch, malic acid, citric acid, calcium and iron.In addition, in hawthorn, contain organic acid as chlorogenic acid, caffeic acid and tannin, the acid anhydride of tanning, epicatechol, choline, acetylcholine, Sitosterolum etc.Hawthorn energy prevention and cure of cardiovascular disease, has hemangiectasis, cardiac stimulant, increase CF, improves heart vigor, stimulating central nervous system system, reduces blood pressure and cholesterol, softening blood vessel and diuresis and sedation; Prevent and treat artery sclerosis, anti-aging, anticancer effect.Crataegolic acid also has cardiotonic, also helpful to senile heart disease.Its energy appetite-stimulating indigestion-relieving, offsets carnivorous stagnant effect better especially, in a lot of digestant medicines, has all adopted hawthorn; Hawthorn has the effect activating blood circulation and dispersing blood clots, and contributes to remove local extravasated blood state, and traumatic injury is had to auxiliary curative effect; Hawthorn has contraction to uterus, has the effect expediting the emergence of just before giving birth time, and can promote uterine involution in postpartum pregnant woman; The generation of free radical is blocked and reduced to the substances such as the flavonoids that hawthorn is contained and vitamin C, carrotene, can strengthen the immunity of body, has anti-aging, anticancer effect.In hawthorn, having relievings asthma reduces phlegm, the composition of anti-bacteria, treatment abdominal pain diarrhea.
Vacuum Freeze Drying Technology for Food is a complex art interdisciplinary, relates to multidisciplinary, multi-field.The progress of food freeze drying technology depends on the development of cross discipline.Vacuum Freezing & Drying Technology can to greatest extent, maximum duration keep its look, taste, shape and nutritional labeling.
Now when hawthorn is dried, vacuum freeze drying normally, and only through the final products hawthorn of vacuum freeze drying, can produce appearance fold, the phenomenon that structure is collapsed, product hardness is large, have a strong impact on the sensory evaluation of product, and mouthfeel is poor, the hawthorn shelf-life is short, and energy consumption for drying is high.At present, the solution also not had.
Summary of the invention
Technical assignment of the present invention is that the vacuum refrigeration explosion puffing drying processing method of a kind of hawthorn is provided for above-mentioned deficiency of the prior art, the vacuum refrigeration explosion puffing drying processing method of this kind of hawthorn has can keep the original biologically active of haw food and nutritional labeling to greatest extent, and improve mouthfeel, there is good crisp brittleness, profile is complete, mouthfeel is good, improved the added value of hawthorn, extend the shelf life, without any additive and anticorrisive agent, energy consumption for drying is lower, the thermal efficiency is higher, improved production efficiency, and effectively reduced the feature of hawthorn production cost.
The technical solution adopted for the present invention to solve the technical problems is: it comprises the following steps: (1) pretreatment of raw material: fresh hawthorn is processed through pick, cleaning, saturating core;
(2) hawthorn of handling well be impregnated in the liquid glucose of sugar content 40% after 12h, take out spray, remove hawthorn surface liquid glucose, control is dry;
(3) the dry hawthorn of control is spread out into individual layer, be uniformly distributed on material tray, put into instant freezer, at-40 ℃, carry out quick-frozen 4-6h, guarantee moisture fully charge in hawthorn;
(4) by vacuum refrigeration swelling drier, carry out vacuum refrigeration explosion puffing drying:
Through the good hawthorn of quick-frozen, together with one of material tray, put into Bulking tank, be placed on the bracket of heating plate, make material tray consistent with levels heating plate distance; Temperature of charge probe is inserted in hawthorn, to monitor the variations in temperature of hawthorn; Close Bulking tank door, sealing Bulking tank; The state of hawthorn can be learnt by the peep hole on Bulking tank door;
Open refrigeration unit, open magnetic valve on condenser tube and the second operated pneumatic valve between cold-trap and Bulking tank, refrigeration unit provides low-temperature receiver by condenser tube to cold-trap and Bulking tank, and the temperature in cold-trap is down to-50 ℃;
Open vacuum unit, open the first operated pneumatic valve between vacuum unit and cold-trap, vacuum unit vacuumizes Bulking tank and cold-trap simultaneously, extracts non-condensable gas; Maintain below Bulking tank internal pressure 100pa, start vacuum freeze drying process;
ON cycle water pot, open the water pump with frequency-converter device and the magnetic valve that are connected with lower plate type heat exchanger, to in lower plate type heat exchanger, pass into steam, cold water in circulation water pot is carried out to heat exchange, condensed water after heat exchange is discharged to lower plate type heat exchanger, cold water in circulation water pot heats up the heating plate in Bulking tank after lower plate type heat exchanger heating, temperature of heating plate is learnt by the temperature of heating plate probe contacting with heating plate, make temperature of heating plate rise to design temperature 65-70 ℃, while surpassing design temperature, the flow velocity that can change by adjusting the frequency converter of water pump hot water makes hot water remain on design temperature, if the temperature adjustment of hot water exceeds the control range of frequency converter, can close the magnetic valve and the water pump that are connected with lower plate type heat exchanger, make it to be cooled to design temperature, with this, keep the temperature of heating plate in design temperature,
Along with the carrying out of vacuum freeze drying, the temperature of hawthorn progressively rises, and until hawthorn temperature, during to 20-25 ℃, closes the second operated pneumatic valve, closes refrigeration unit;
The magnetic valve that unlatching is connected with aseptic air filter, injects the aseptic compressed air of steam and impurity after filtration to Bulking tank, makes Bulking tank pressure recover normal pressure; Until hawthorn temperature, during to 60-65 ℃, open the second operated pneumatic valve, make cold-trap and Bulking tank UNICOM, utilize pressure differential between two tanks to carry out expanded and humidity discharging and solidify; 7-8 time so repeatedly, begin to cool down process; Close the magnetic valve and the water pump that are connected with lower plate type heat exchanger, open the band frequency-converter device water pump and the magnetic valve that are connected with upper plate type heat exchanger, to in upper plate type heat exchanger, pass into frozen water, carry out after heat exchange with the hot water in circulation water pot, discharge the warm water after upper board-like exchanger heat exchange; Hot water in circulation water pot makes the cooling of heating plate in Bulking tank after upper plate type heat exchanger is cooling, is cooled to room temperature, and closing device is opened Bulking tank, minute grade packaged, obtains the crisp complete haw products of vacuum refrigeration explosion puffing drying.
Described vacuum refrigeration swelling drier comprises cold-trap, refrigeration unit, vacuum unit, Bulking tank, plate type heat exchanger and circulation water pot, the two ends of described cold-trap are connected with Bulking tank with vacuum unit respectively, described refrigeration unit is connected with cold-trap by condenser tube, described Bulking tank upper and lower is respectively arranged with water inlet pipe and outlet pipe, between the water inlet pipe of described Bulking tank outside and outlet pipe, be provided with circulation water pot, between described circulation water pot and water inlet pipe, be arranged in parallel, lower two plate type heat exchangers, described is upper, between lower two plate type heat exchangers and circulation water pot, be respectively arranged with water pump, one end of described Bulking tank is provided with Bulking tank door, in Bulking tank, be provided with material tray, the bottom of described Bulking tank is provided with aseptic air filter, between described cold-trap and vacuum unit and Bulking tank, be respectively arranged with the first operated pneumatic valve and the second operated pneumatic valve, between described refrigeration unit and condenser tube, between Bulking tank and aseptic air filter and the two ends of two plate type heat exchangers are respectively arranged with magnetic valve, in described Bulking tank, be provided with heating plate, described heating plate comprises Transverse Heated plate and longitudinal heating plate, described Transverse Heated plate longitudinally heating plate evenly arranges, on longitudinal heating plate of described every two Transverse Heated plate both sides, be symmetrically arranged with respectively bracket, described material tray is separately positioned on bracket, the upper and lower of described Transverse Heated plate is connected with water inlet pipe and outlet pipe respectively, in described Bulking tank, be provided with temperature of heating plate probe and temperature of charge probe, described temperature of heating plate probe and temperature of charge probe contact with Transverse Heated plate and material tray respectively, on described Bulking tank door, be provided with peep hole.
The first described operated pneumatic valve, the second operated pneumatic valve and magnetic valve are connected with control system respectively, and the opening and closing of the first operated pneumatic valve, the second operated pneumatic valve and magnetic valve are all controlled automatically by control system.
The vacuum refrigeration explosion puffing drying processing method of a kind of hawthorn of the present invention compared to the prior art, there is following outstanding beneficial effect: the hawthorn of producing through vacuum refrigeration swelling drier, in color and local flavor, nutritional labeling, can compare favourably with the product quality of vacuum freeze drying, the hawthorn of process explosion puffing drying is because raw material inside has produced porous, spongiform structure simultaneously, compare product with vacuum freeze drying product and have good crisp brittleness, profile is complete, mouthfeel is crisp, has improved the added value of hawthorn; Nutritious, hawthorn vacuum refrigeration explosion puffing drying product is without the technique such as broken, to squeeze the juice, concentrate, the shape, the color and luster that have not only retained hawthorn, also possessed intrinsic low in calories, the low fat feature of hawthorn, retains to greatest extent more nutritional labeling in hawthorn; Energy consumption for drying is lower, owing to having taked the measures such as circulating cooling and circulating hot water heating, the thermal efficiency is higher, can consume the energy consumption well below vacuum freeze drying, this has greatly improved production efficiency in actual production, and has effectively reduced hawthorn production cost; Environmental protection, in process, water consumption is few, and the discarded object of generation is few, meets environmental requirement, and processing byproduct is further processing and utilization also, pollutes few; Hawthorn long shelf-life, the water content of expanded hawthorn is generally below 5%, is unfavorable for growth of microorganism breeding, can long preservation; Overcome the shortcoming that contains grease in lower temperature vacuum frying product, be difficult for causing the features such as bad quality variation that wait spoiled by rancid oil or fat.
Accompanying drawing explanation
Accompanying drawing 1 is the main TV structure schematic diagram of the vacuum refrigeration swelling drier that uses in the vacuum refrigeration explosion puffing drying processing method of a kind of hawthorn;
Accompanying drawing 2 is that Bulking tank and the heating plate of the vacuum refrigeration swelling drier that uses in the vacuum refrigeration explosion puffing drying processing method of a kind of hawthorn amplifies plan structure schematic diagram;
Accompanying drawing 3 is Bulking tank enlarged left views of the vacuum refrigeration swelling drier that uses in the vacuum refrigeration explosion puffing drying processing method of a kind of hawthorn;
Accompanying drawing 4 is material tray enlarged left views of the vacuum refrigeration swelling drier that uses in the vacuum refrigeration explosion puffing drying processing method of a kind of hawthorn;
Description of reference numerals: 1, vacuum unit, 2, the first operated pneumatic valve, 3, cold-trap, 4, magnetic valve, 5, refrigeration unit, 6, condenser tube, 7, the second operated pneumatic valve, 8, aseptic air filter, 9, peep hole, 10, bracket, 11, Bulking tank, 12, material tray, 13, outlet pipe, 14, Bulking tank door, 15, temperature of heating plate probe, 16, temperature of charge probe, 17, heating plate, 18, water inlet pipe, 19, lower plate type heat exchanger, 20, circulation water pot, 21, upper plate type heat exchanger, 22, water pump, 23, Transverse Heated plate, 24, longitudinal heating plate.
The specific embodiment
Vacuum refrigeration explosion puffing drying processing method with reference to Figure of description 1 to 4 pairs of a kind of hawthorn of the present invention of accompanying drawing is described in detail below.
The vacuum refrigeration explosion puffing drying processing method of a kind of hawthorn of the present invention, it comprises the following steps: (1) pretreatment of raw material: fresh hawthorn is processed through pick, cleaning, saturating core;
(2) hawthorn of handling well be impregnated in the liquid glucose of sugar content 40% after 12h, take out spray, remove hawthorn surface liquid glucose, control is dry;
(3) the dry hawthorn of control is spread out into individual layer, be uniformly distributed on material tray 12, put into instant freezer, at-40 ℃, carry out quick-frozen 4-6h, guarantee moisture fully charge in hawthorn;
(4) by vacuum refrigeration swelling drier, carry out vacuum refrigeration explosion puffing drying:
Through the good hawthorn of quick-frozen, together with 12 1 of material trays, put into Bulking tank 11, be placed on the bracket 10 of heating plate 17, make material tray 12 consistent with levels heating plate distance; Temperature of charge probe 16 is inserted in hawthorn, to monitor the variations in temperature of hawthorn; Close Bulking tank door 14, sealing Bulking tank 11; The state of hawthorn can be learnt by the peep hole 9 on Bulking tank door 14;
Open refrigeration unit 5, open magnetic valve 4 on condenser tube 6 and the second operated pneumatic valve 7 between cold-trap 3 and Bulking tank 11, refrigeration unit 5 provides low-temperature receiver by 6 pairs of cold-traps 3 of condenser tube and Bulking tank 11, and the temperature in cold-trap 3 is down to-50 ℃;
Open vacuum unit 1, open the first operated pneumatic valve 2 between vacuum unit 1 and cold-trap 3,1 pair of Bulking tank 11 of vacuum unit and cold-trap 3 vacuumize simultaneously, extract non-condensable gas; Maintain below Bulking tank 11 internal pressure 100pa, start vacuum freeze drying process;
ON cycle water pot 20, open the water pump 22 with frequency-converter device and the magnetic valve 4 that are connected with lower plate type heat exchanger 19, to in lower plate type heat exchanger 19, pass into steam, cold water in circulation water pot 20 is carried out to heat exchange, condensed water after heat exchange is discharged to lower plate type heat exchanger 19, cold water in circulation water pot 20 heats up the heating plate 17 in Bulking tank 11 after lower plate type heat exchanger 19 heating, heating plate 17 temperature are learnt by the temperature of heating plate probe 15 contacting with heating plate 17, make heating plate 17 temperature rise to design temperature 65-70 ℃, while surpassing design temperature, the flow velocity that can change by adjusting the frequency converter of water pump 22 hot water makes hot water remain on design temperature, if the temperature adjustment of hot water exceeds the control range of frequency converter, can close the magnetic valve and the water pump that are connected with lower plate type heat exchanger 19, make it to be cooled to design temperature, with this, keep the temperature of heating plate 17 in design temperature,
Along with the carrying out of vacuum freeze drying, the temperature of hawthorn progressively rises, and until hawthorn temperature, during to 20-25 ℃, closes the second operated pneumatic valve 7, closes refrigeration unit 5;
The magnetic valve that unlatching is connected with aseptic air filter 8, injects the aseptic compressed air of steam and impurity after filtration to Bulking tank 11, makes Bulking tank 11 pressure recover normal pressures; Until hawthorn temperature, during to 60-65 ℃, open the second operated pneumatic valve 7, make cold-trap 3 and Bulking tank 11 UNICOMs, utilize pressure differential between two tanks to carry out expanded and humidity discharging and solidify; 7-8 time so repeatedly, begin to cool down process; Close the magnetic valve and the water pump that are connected with lower plate type heat exchanger 19, open the band frequency-converter device water pump and the magnetic valve that are connected with upper plate type heat exchanger 21, to in upper plate type heat exchanger 21, pass into frozen water, carry out after heat exchange with the hot water in circulation water pot 20, discharge the warm water after upper plate type heat exchanger 21 heat exchanges; Hot water in circulation water pot 20 makes 17 coolings of heating plate in Bulking tank 11 after upper plate type heat exchanger 21 is cooling, is cooled to room temperature, and closing device, opens Bulking tank 11, minute grade packaged, obtains the crisp complete haw products of vacuum refrigeration explosion puffing drying.
Described vacuum refrigeration swelling drier comprises cold-trap 3, refrigeration unit 5, vacuum unit 1, Bulking tank 11, plate type heat exchanger and circulation water pot 20, the two ends of described cold-trap 3 are connected with Bulking tank 11 with vacuum unit 1 respectively, described refrigeration unit 5 is connected with cold-trap 3 by condenser tube 6, described Bulking tank 11 upper and lowers are respectively arranged with water inlet pipe 18 and outlet pipe 13, between the water inlet pipe 18 of described Bulking tank 11 outsides and outlet pipe 13, be provided with circulation water pot 20, between described circulation water pot 20 and water inlet pipe 18, be arranged in parallel, lower two plate type heat exchangers, described is upper, between lower two plate type heat exchangers and circulation water pot 20, be respectively arranged with water pump 22, one end of described Bulking tank 11 is provided with Bulking tank door 14, in Bulking tank 11, be provided with material tray 12, the bottom of described Bulking tank 11 is provided with aseptic air filter 8, between described cold-trap 3 and vacuum unit 1 and Bulking tank 11, be respectively arranged with the first operated pneumatic valve 2 and the second operated pneumatic valve 7, between described refrigeration unit 5 and condenser tube 6, between Bulking tank 11 and the aseptic air filter 8 and two ends of two plate type heat exchangers are respectively arranged with magnetic valve 4, in described Bulking tank 11, be provided with heating plate 17, described heating plate 17 comprises Transverse Heated plate 23 and longitudinal heating plate 24, described Transverse Heated plate 23 longitudinally heating plate 24 evenly arranges, on longitudinal heating plate 24 of described every two Transverse Heated plate 23 both sides, be symmetrically arranged with respectively bracket 10, described material tray 12 is separately positioned on bracket 10, the upper and lower of described Transverse Heated plate 23 is connected with water inlet pipe 18 and outlet pipe 13 respectively, the interior heat drying mode of Bulking tank 11 is the interior logical hot water heating of built-in heating plate 17, thereby by plate type heat exchanger, pass into steam and to heating plate 17, provide hot water to the cool water heating in circulation water pot 20, form airtight loop, Bulking tank 11 pressurizations adopt the filtrated air through filtering to realize.Therefore adopt heating plate plate type heating mode, strengthened and be subject to thermocontact area, improved the efficiency of heating surface, the temperature fluctuation in whole Bulking tank 11 is little, be also more convenient for controlling, and hot water can recycle, more energy-saving and cost-reducing; In described Bulking tank 11, be provided with temperature of heating plate probe 15 and temperature of charge probe 16, described temperature of heating plate probe 15 and temperature of charge probe 16 contact with Transverse Heated plate 23 and material tray 12 respectively, be convenient to detect the temperature of heating plate 17 and material tray 12 interior materials, on described Bulking tank door 14, be provided with peep hole 9, be convenient to observe the state of the material in Bulking tank 11.
Described the first operated pneumatic valve 2, the second operated pneumatic valve 7 are connected with control system respectively with magnetic valve 4, and the opening and closing of the first operated pneumatic valve 2, the second operated pneumatic valve 7 and magnetic valve 4 are all controlled automatically by control system.
Except the technical characterictic described in description, be the known technology of those skilled in the art.

Claims (2)

1. a vacuum refrigeration explosion puffing drying processing method for hawthorn, is characterized in that: comprise the following steps: (1) pretreatment of raw material: fresh hawthorn is processed through pick, cleaning, saturating core;
(2) hawthorn of handling well be impregnated in the liquid glucose of sugar content 40% after 12h, take out spray, remove hawthorn surface liquid glucose, control is dry;
(3) the dry hawthorn of control is spread out into individual layer, be uniformly distributed on material tray, put into instant freezer, at-40 ℃, carry out quick-frozen 4-6h, guarantee moisture fully charge in hawthorn;
(4) by vacuum refrigeration swelling drier, carry out vacuum refrigeration explosion puffing drying:
Through the good hawthorn of quick-frozen, together with one of material tray, put into Bulking tank, be placed on the bracket of heating plate, make material tray consistent with levels heating plate distance; Temperature of charge probe is inserted in hawthorn, to monitor the variations in temperature of hawthorn; Close Bulking tank door, sealing Bulking tank; The state of hawthorn can be learnt by the peep hole on Bulking tank door;
Open refrigeration unit, open magnetic valve on condenser tube and the second operated pneumatic valve between cold-trap and Bulking tank, refrigeration unit provides low-temperature receiver by condenser tube to cold-trap and Bulking tank, and the temperature in cold-trap is down to-50 ℃;
Open vacuum unit, open the first operated pneumatic valve between vacuum unit and cold-trap, vacuum unit vacuumizes Bulking tank and cold-trap simultaneously, extracts non-condensable gas; Maintain below Bulking tank internal pressure 100pa, start vacuum freeze drying process;
ON cycle water pot, open the water pump with frequency-converter device and the magnetic valve that are connected with lower plate type heat exchanger, to in lower plate type heat exchanger, pass into steam, cold water in circulation water pot is carried out to heat exchange, condensed water after heat exchange is discharged to lower plate type heat exchanger, cold water in circulation water pot heats up the heating plate in Bulking tank after lower plate type heat exchanger heating, temperature of heating plate is learnt by the temperature of heating plate probe contacting with heating plate, make temperature of heating plate rise to design temperature 65-70 ℃, while surpassing design temperature, the flow velocity that can change by adjusting the frequency converter of water pump hot water makes hot water remain on design temperature, if the temperature adjustment of hot water exceeds the control range of frequency converter, can close the magnetic valve and the water pump that are connected with lower plate type heat exchanger, make it to be cooled to design temperature, with this, keep the temperature of heating plate in design temperature,
Along with the carrying out of vacuum freeze drying, the temperature of hawthorn progressively rises, and until hawthorn temperature, during to 20-25 ℃, closes the second operated pneumatic valve, closes refrigeration unit;
The magnetic valve that unlatching is connected with aseptic air filter, injects the aseptic compressed air of steam and impurity after filtration to Bulking tank, makes Bulking tank pressure recover normal pressure; Until hawthorn temperature, during to 60-65 ℃, open the second operated pneumatic valve, make cold-trap and Bulking tank UNICOM, utilize pressure differential between two tanks to carry out expanded and humidity discharging and solidify; 7-8 time so repeatedly, begin to cool down process; Close the magnetic valve and the water pump that are connected with lower plate type heat exchanger, open the band frequency-converter device water pump and the magnetic valve that are connected with upper plate type heat exchanger, to in upper plate type heat exchanger, pass into frozen water, carry out after heat exchange with the hot water in circulation water pot, discharge the warm water after upper board-like exchanger heat exchange; Hot water in circulation water pot makes the cooling of heating plate in Bulking tank after upper plate type heat exchanger is cooling, is cooled to room temperature, and closing device is opened Bulking tank, minute grade packaged, obtains the crisp complete haw products of vacuum refrigeration explosion puffing drying;
Described vacuum refrigeration swelling drier comprises cold-trap, refrigeration unit, vacuum unit, Bulking tank, plate type heat exchanger and circulation water pot, the two ends of described cold-trap are connected with Bulking tank with vacuum unit respectively, described refrigeration unit is connected with cold-trap by condenser tube, described Bulking tank upper and lower is respectively arranged with water inlet pipe and outlet pipe, between the water inlet pipe of described Bulking tank outside and outlet pipe, be provided with circulation water pot, between described circulation water pot and water inlet pipe, be arranged in parallel, lower two plate type heat exchangers, described is upper, between lower two plate type heat exchangers and circulation water pot, be respectively arranged with water pump, one end of described Bulking tank is provided with Bulking tank door, in Bulking tank, be provided with material tray, the bottom of described Bulking tank is provided with aseptic air filter, between described cold-trap and vacuum unit and Bulking tank, be respectively arranged with the first operated pneumatic valve and the second operated pneumatic valve, between described refrigeration unit and condenser tube, between Bulking tank and aseptic air filter and the two ends of two plate type heat exchangers are respectively arranged with magnetic valve, in described Bulking tank, be provided with heating plate, described heating plate comprises Transverse Heated plate and longitudinal heating plate, described Transverse Heated plate longitudinally heating plate evenly arranges, on longitudinal heating plate of described every two Transverse Heated plate both sides, be symmetrically arranged with respectively bracket, described material tray is separately positioned on bracket, the upper and lower of described Transverse Heated plate is connected with water inlet pipe and outlet pipe respectively, in described Bulking tank, be provided with temperature of heating plate probe and temperature of charge probe, described temperature of heating plate probe and temperature of charge probe contact with Transverse Heated plate and material tray respectively, on described Bulking tank door, be provided with peep hole.
2. the vacuum refrigeration explosion puffing drying processing method of a kind of hawthorn according to claim 1, it is characterized in that: the first described operated pneumatic valve, the second operated pneumatic valve and magnetic valve are connected with control system respectively, the opening and closing of the first operated pneumatic valve, the second operated pneumatic valve and magnetic valve are all controlled automatically by control system.
CN201310102229.1A 2013-03-27 2013-03-27 Vacuum freezing puff-drying processing method of hawthorn Expired - Fee Related CN103141564B (en)

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CN103636754A (en) * 2013-11-25 2014-03-19 张俊辉 Haw processing method
CN105806044A (en) * 2016-03-31 2016-07-27 王飞 Universal drying equipment and method for extracting concentrates
CN107616538A (en) * 2017-11-03 2018-01-23 宁夏杞芽食品科技有限公司 A kind of expanded reduction apparatus of fructus lycii

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