CN110307707A - Drying machine for processing of aquatic products - Google Patents
Drying machine for processing of aquatic products Download PDFInfo
- Publication number
- CN110307707A CN110307707A CN201910578142.9A CN201910578142A CN110307707A CN 110307707 A CN110307707 A CN 110307707A CN 201910578142 A CN201910578142 A CN 201910578142A CN 110307707 A CN110307707 A CN 110307707A
- Authority
- CN
- China
- Prior art keywords
- box
- drying
- drying box
- cabinet
- processing
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B11/00—Machines or apparatus for drying solid materials or objects with movement which is non-progressive
- F26B11/12—Machines or apparatus for drying solid materials or objects with movement which is non-progressive in stationary drums or other mainly-closed receptacles with moving stirring devices
- F26B11/14—Machines or apparatus for drying solid materials or objects with movement which is non-progressive in stationary drums or other mainly-closed receptacles with moving stirring devices the stirring device moving in a horizontal or slightly-inclined plane
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/001—Drying-air generating units, e.g. movable, independent of drying enclosure
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/003—Supply-air or gas filters
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/004—Nozzle assemblies; Air knives; Air distributors; Blow boxes
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/02—Circulating air or gases in closed cycles, e.g. wholly within the drying enclosure
- F26B21/04—Circulating air or gases in closed cycles, e.g. wholly within the drying enclosure partly outside the drying enclosure
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/06—Controlling, e.g. regulating, parameters of gas supply
- F26B21/08—Humidity
- F26B21/086—Humidity by condensing the moisture in the drying medium, which may be recycled, e.g. using a heat pump cycle
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/06—Controlling, e.g. regulating, parameters of gas supply
- F26B21/10—Temperature; Pressure
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B25/00—Details of general application not covered by group F26B21/00 or F26B23/00
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B25/00—Details of general application not covered by group F26B21/00 or F26B23/00
- F26B25/001—Handling, e.g. loading or unloading arrangements
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B25/00—Details of general application not covered by group F26B21/00 or F26B23/00
- F26B25/04—Agitating, stirring, or scraping devices
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B25/00—Details of general application not covered by group F26B21/00 or F26B23/00
- F26B25/06—Chambers, containers, or receptacles
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B25/00—Details of general application not covered by group F26B21/00 or F26B23/00
- F26B25/06—Chambers, containers, or receptacles
- F26B25/08—Parts thereof
- F26B25/12—Walls or sides; Doors
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Drying Of Solid Materials (AREA)
Abstract
The present invention discloses a kind of drying machine for processing of aquatic products, belong to aquatic products processing equipment technical field, drying machine of the invention includes: the first drying box, for being processed for the first time to material, first drying box has feed pipe and the first material transfer pipe, second drying box, for the material redrying after being dried for the first time to the first drying box, second drying box is connected to the first material transfer pipe, also there is discharge port, heater box, for inputting the first drying box after heating air, in second drying box, wherein, first drying box is connect by downtake pipe with heater box, cryogenic gas is sent back in heater box.Drying machine Efficient Cycle of the invention is using the dry energy, and the thermal efficiency is high, heat transfer coefficient is high, and for drying process not by such environmental effects, dry materials are thorough.
Description
Technical field
The invention belongs to aquatic products processing equipment technical fields, and in particular to a kind of drying machine for processing of aquatic products.
Background technique
Aquatic products production season is strong, raw material be easy to corruption, it is necessary to take effective means to raw material carry out in time it is fresh-keeping and
Working process.Since aquatic products dried product mustn't refrigerate, from production to being not required to cold chain during consumption, and moisture content is very
Low (generally below 14%), makes transport, storage and edible more easy, at low cost, while also avoidable cold chain is too long draws
The pollution risen and quality reduce.Therefore, the dry production of aquatic products is one of important method of processing of aquatic products.In addition, in addition to
Outside the purpose of storage, many aquatic products dried products have been favored by people because it is with peculiar flavour, such as do salty gadus, do salty shark
Fish, to do salty sardine etc. be the world's much very favorite food of regional people；Various seasoneds, dried shrimps, dried scallop, dried mussel,
Dried sea-cucumber, dry abalone etc. are also to be welcome deeply by Chinese Consumer's.In recent years, the total output that fish was dried in the world every year reaches
3140000 tons.
The conventional drying process of aquatic products is exactly solar drying method, and traditional solar drying is not required to special installation, it is only necessary to will
Aquatic products are placed under sunlight and dry, and drying cost is low, are most economical drying means.Currently, outdoor daylight is dry
It is still the major way in many areas, especially Asia, the numerous developing country's fish products dryings in Africa and the Pacific region.Due to
Solar drying is completely dependent on natural environmental condition, larger by such environmental effects, is difficult to control dry products quality.
Summary of the invention
The purpose of the present invention is to provide a kind of drying machine for processing of aquatic products, Efficient Cycle utilizes the dry energy,
The thermal efficiency is high, heat transfer coefficient is high, and for drying process not by such environmental effects, dry materials are thorough.
The technical solution that the present invention is taken to achieve the above object are as follows: the drying machine for processing of aquatic products, comprising:
First drying box, for processing for the first time to material, the first drying box has feed pipe and the first material transfer pipe,
Second drying box, for the material redrying after being dried for the first time to the first drying box, the second drying box and first
The connection of material transfer pipe, also has discharge port,
Heater box, for inputting the first drying box after heating air, in the second drying box,
Wherein, the first drying box is connect by downtake pipe with heater box, cryogenic gas is sent back in heater box, first
Exhaust pipe Single port is set to the first drying box internal upper part, and another port is set to lower part, the first drying box and drying box in heater box
Between downtake pipe be equipped with the condensation that cool down to first exhaust tube interior gas, condensation includes the 4th case
Body, the 4th cabinet have the second chamber that is connected to downtake pipe, and the 4th cabinet also has the above second chamber
One chamber.
The present invention carries out redrying processing to material using redrying treatment process, compared with the prior art by material
It is dried mode for a long time under natural light, redrying technique of the present invention can guarantee dry materials effect, and
Time compared to natural drying is greatly shortened, and is done respectively to material using the first drying box and the second drying box
Dry processing avoids environment to dry impact effect, and place is dried using mechanical equipment, it can be achieved that control drying temperature
Reason, heat transfer coefficient height high to the thermal efficiency during dry materials, effective improving material dry mass shorten process time, into
One step, by downtake pipe by the connection between the first drying box and heater box, and the entry/exit gas of downtake pipe is set
The first dry lower air of the temperature inside the box is recycled in heater box by mouth position to realize, the heat of the injection in the first drying box
Gas is injected from the first dry lower box part, it is contemplated that the air quality under heated condition is lower than the lower air of relative temperature, heat
The factor that air can rise, in this way in order in the first drying box hot gas from top to bottom to the dry materials in drying box, and
It takes the vapor generated in drying process out of first drying box upwards together, air feeding will be discharged by downtake pipe and added
It is heated again in hot tank, and the nozzle of the downtake pipe in heater box is set to heating lower box part, is conducive to so colder
Gas pushes up hot gas to form gas flowing.Downtake pipe generates dry materials in the first drying box in the process
Vapor is taken out of, therefore carries out cooling treatment to the gas to circulate in downtake pipe by setting condensation, makes to vaporize water body
It liquefies and collects, guarantee that gas flows through condensation by the second chamber set in the 4th cabinet, set above second chamber
First chamber is set in order to be absorbed heat in heat transfer to first chamber to the air flowed through in second chamber, to improve first
The endothermic effect of chamber can inject coolant liquid inside first chamber to improve endothermic effect, realize and contain vapour in the gas of recycling
The water body of change liquefies, and realizes heat recovery, and effective improving material dry mass shortens process time.
Specifically, the corresponding side wall of second chamber two is separately connected downtake pipe, gas circulation, such enlargement gas are realized
Circulation in second chamber, is also advantageous for extended residence time of the gas in second chamber, improves to containing in gas
Condensate moisture effect, the 4th cabinet below second chamber has third chamber, passes through between third chamber and second chamber
Intercommunicating pore connection.Heat absorption liquid is stored in first chamber.The pump housing is additionally provided on downtake pipe, for the water generated after condensation
Body is snapped down to second chamber bottom due to gravity, is collected into third chamber by intercommunicating pore, to guarantee replacement first
Chamber indoor liquid replacement, can set folding lid on the 4th cabinet, can be the similarly for convenient for discharging the indoor water body of third chamber
Another folding lid is set on four cabinets convenient for discharge water body.
Specifically, the first drying box includes the second cabinet, the second box house passes through material baffle upper down space respectively, charging
Pipe, downtake pipe, the first material transfer pipe are connect with the first drying box upper box body respectively.It will be in the first drying box using material baffle
Portion space is divided into two parts up and down, and separated material plate surface is evenly equipped with through-hole, and after material is sent into the first drying box, material is dry
Separated impurity out or biggish water droplet directly can fall into the first drying box by the through-hole being arranged on material baffle during dry
The processing quality of drying efficiency and dried object, feed pipe and downtake pipe and the first drying box roof are improved in lower half portion
Connection, the first material transfer pipe are connected to the side wall of the second cabinet of the first drying box case above material baffle, in order to the first drying
Material transmitting in case.
Specifically, being equipped with first motor in the second lower box cabinet, first motor shaft is set to the second cabinet upper tank
In vivo, first motor shaft is around stirring blade is laid, and the blade face of stirring blade is parallel with shaft axis, stirring blade and shaft
The corresponding sides of connection have inner concave arc surface, and the other two edges evagination of stirring blade is excessive with cambered surface junction fillet.By
Setting first motor is stirred second case intracorporal material to drive the rotation of its shaft that paddle is driven to rotate in two cabinets
Processing effect, realizes the gap expanded between material, and compared to existing by the way of illumination sunning, material is during sunning
Often in static state, for gas in body surface flow effect and bad, the present invention promotes material the by the stirring to material
Stirring movement in two cabinets expands the contact between material and air, improves the drying effect of material, the rotation pair of stirring blade
Have stirring action into second case intracorporal gas, gas flow effect in the second cabinet is improved, further by paddle
Piece is connected with the rotating shaft corresponding sides setting inner concave arc surface, while the other two edges evagination of stirring blade, with cambered surface junction fillet
Excessively, on such stirring blade vertical direction, both ends are greater than in the middle part of stirring blade the Drive the result of air-flow, convenient for vertical side
The air-flow at upward stirring blade both ends concentrates the hot-fluid and unevaporated water for realizing that moisture evaporation generates in drying process to middle part
Divide partial stack between hot melt stream and dried material hot melt stream three, to improve material entirety pyrolysis rate and volatile matter production
Rate makes material reach dehydration peak value in the short time in the first drying box, keeps away material and seeks inside it in long-time dehydration process
It forms and point gradually decreases, ensure that the quality of institute's processing materials and thoroughly dried material.
Specifically, the second lower box cabinet is communicated with collector tube, collector tube and the liquids recovery being set to outside the second cabinet
Case connection, material be put into the second cabinet may leach portion of water plus may also generate in the drying process it is more
Moisture, by the through-hole on material baffle, the moisture separated from material concentrates on the second lower box and is carried out by collector tube
Centralized collection to liquid recovery tank is focused on, and the water body for preventing the second lower box from collecting largely vaporizes the dry institute of exacerbation
Use energy consumption.
Specifically, the second drying box includes third cabinet, third cabinet top is connected separately with the first material transfer pipe, the second electricity
Machine and second exhaust pipe, the second machine shaft and setting are in the intracorporal stirring axis connection of third case, third lower box side wall
It is connected with the second appendix.Second exhaust pipe is connected with the pump housing.The discharge port of third cabinet is equipped with valve, and material is dry first
Rapid draing is carried out in case, the material quick dehydration in a short time handled through the first drying box effectively reduces inside material
Nutritional ingredient loss, it is dry that material after the drying process of the first drying box, by material transfer pipe is delivered to second by material
It carries out being dried for second in case, equally material is stirred by the way of stirring in the second drying box, is taken
Agitating shaft be common agitating shaft, material carries out the drying of long period in the second drying box, is thoroughly dried to material,
The mixing speed of agitating shaft should not too fast and agitating shaft select that material should be ceramic material or 304 stainless steels, material are dry second
It carries out gradually decreasing its cylinder water content under continuous rolling stirring action in dry case, the second gas transmission is set in third cabinet side
Pipe makes it travel up to second exhaust pipe discharge gas to input gas, realizes the intracorporal gas flowing of third case, avoids big
Amount vapor largely stops in third cabinet.
Specifically, the first drying box includes the second cabinet, the tank wall of the second cabinet includes inner and outer wall, inner wall and outer wall
Between be equipped with thermal insulation board, inner wall surface is evenly distributed with rectangular-shaped invagination groove body.Rectangle invagination groove body is set on inner wall, and gas is along inner wall
It needs to reduce air-flow by each groove body along the flowing velocity of inner wall and increase the friendship of the heat between gas and inner wall in flow process
It changes, the second box interior temperature is kept to be in stable state, thermal insulation board is further set to completely cut off the heat between inner wall and outer wall
Amount exchange, is further ensured that the heat insulation effect of inner wall.
Specifically, heater box is connected to the first drying box, the second drying box respectively by the first appendix, the first appendix
Entry/exit gas tube orifice be set to the first drying box, the second drying box, heater box top half.For realizing will in heater box plus
Air after heat, which inputs in each drying box, carries out heating operation to material.
Specifically, being equipped with electric boiling plate in heater box, electric boiling plate is controlled by controller, and first is equipped in the first drier
Temperature detector, is equipped with second temperature detector in the second drier, controller by connecting line respectively with the first temperature detection
Device, the connection of second temperature detector.Using the first temperature detector, second temperature detector respectively to the first drying box and second
Drying box internal temperature is monitored, when temperature is lower, controller control electric hot plate increase air heating temperature, the present invention in
Signified controller is computer terminal.
Specifically, heater box bottom opening is arranged, sealed using the filter plate that may filter that gas, by heater box
Bottom opening is situated so as to air and enters in heater box heated, and the gaseous mass after heating is lighter, floats
It will not flow out from heater box bottom in heater top, the air entered in heater box can be filtered by this filter plate
Processing filters out the impurity in air, improves the hygienic quality to dry materials.
Compared with prior art, the invention has the benefit that the present invention using redrying treatment process to material into
The processing of row redrying, is dried mode for material compared with the prior art for a long time under natural light, and the present invention is used
Redrying technique can guarantee dry materials effect, and greatly shortened compared to the time of natural drying, using the
One drying box and the second drying box are respectively dried material, it can be achieved that control drying temperature, avoid environment to dry
Dry impact effect, and be dried using mechanical equipment, heat transfer coefficient high to the thermal efficiency during dry materials
Height, effective improving material dry mass shorten process time.
Detailed description of the invention
In order to more clearly explain the embodiment of the invention or the technical proposal in the existing technology, to embodiment or will show below
There is attached drawing needed in technical description to be briefly described, it should be apparent that, the accompanying drawings in the following description is only this
Some embodiments of invention for those of ordinary skill in the art without creative efforts, can be with
It obtains other drawings based on these drawings.
Fig. 1 is schematic diagram of the present invention for the drying machine of processing of aquatic products；
Fig. 2 is heater box schematic internal view of the present invention；
Fig. 3 is the schematic internal view of the first drying box of the invention；
Fig. 4 is the schematic diagram of first motor and its stirring blade of the invention；
Fig. 5 is the partial schematic diagram of the second cabinet wall of the invention；
Fig. 6 is its tank wall partial sectional view of the second cabinet of the invention；
Fig. 7 is the second drying box schematic internal view of the invention；
Fig. 8 is condensation schematic internal view of the present invention.
Description of symbols: the first drier of 10-；11- the first material transfer pipe；12- downtake pipe；The second cabinet of 13-；
14- material baffle；15- stirring blade；16- first motor；17- feed pipe；18- inner wall；181- invagination groove body；19- outer wall；191-
Thermal insulation board；20- liquid recovery tank；21- collector tube；30- condensation；The 4th cabinet of 31-；32- first chamber；The second chamber of 33-
Room；34- third chamber；35- intercommunicating pore；40- heater box；The first appendix of 41-；The first cabinet of 42-；43- filter plate；50- control
Device processed；51- connecting line；The first temperature detector of 52-；53- electric boiling plate；54- second temperature detector；The second drier of 60-；
61- valve；62- third cabinet；63- agitating shaft；The second appendix of 64-；The second motor of 65-；66- second exhaust pipe；70- pump
Body.
Specific embodiment
Following will be combined with the drawings in the embodiments of the present invention, and technical solution in the embodiment of the present invention carries out clear, complete
Site preparation description, it is clear that described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments.It is based on
Embodiment in the present invention, it is obtained by those of ordinary skill in the art without making creative efforts every other
Embodiment shall fall within the protection scope of the present invention.
Embodiment 1:
Referring to the drying machine shown in Fig. 1-8, for processing of aquatic products, comprising:
First drying box 10, for processing for the first time to material, the first drying box 10 has feed pipe 17 and the first material transfer pipe
11,
Second drying box 60, for the material redrying to the first drying box 10 after dry for the first time, the second drying box 60
It is connected to the first material transfer pipe 11, also there is discharge port,
Heater box 40, for inputting the first drying box 10 after heating air, in the second drying box 60,
Wherein, the first drying box 10 is connect by downtake pipe 12 with heater box 40, sends cryogenic gas back to heater box
In 40,12 Single port of downtake pipe be set to 10 internal upper part of the first drying box, another port be set to heater box 40 in lower part, first
Downtake pipe 12 between drying box 10 and drying box 40 is equipped with the condensation group to cool down to 12 internal gas of downtake pipe
Part 30, condensation 30 include the 4th cabinet 31, and the 4th cabinet 31 has the second chamber 33 being connected to downtake pipe 12, the
Four cabinets 31 also have the first chamber 32 for being set to 33 top of second chamber.
The present invention carries out redrying processing to material using redrying treatment process, compared with the prior art by material
It is dried mode for a long time under natural light, redrying technique of the present invention can guarantee dry materials effect, and
Time compared to natural drying is greatly shortened, using the first drying box 10 and the second drying box 60 respectively to material into
Row is dried, it can be achieved that control drying temperature, avoids environment to dry impact effect, and done using mechanical equipment
Dry processing, heat transfer coefficient height high to the thermal efficiency during dry materials, when effective improving material dry mass, shortening are processed
Between, further, by downtake pipe 12 by the connection between the first drying box 10 and heater box 40, and first exhaust is set
The lower air of temperature in first drying box 10 is recycled in heater box 40 by the entry/exit port position of pipe 12 to realize, and first
The hot gas of injection in drying box 10 is injected from 10 lower part of the first drying box, it is contemplated that the air quality under heated condition is lower than
The lower air of relative temperature, the factor that hot-air can rise, in this way in order to which hot gas is from top to bottom in the first drying box 10
To the dry materials in drying box 10 out of, and the vapor generated in drying process is taken to the first drying box 10 upwards together, leads to
Crossing downtake pipe 12 will be heated again in discharge air feeding heater box 40, and the downtake pipe 12 in heater box 40
Nozzle be set to 40 lower part of heater box, be conducive in this way cooler gas hot gas is pushed up to be formed gas flowing.First row
Tracheae 12 takes the vapor generated during dry materials in the first drying box 10 out of, therefore by setting condensation 30 to the
The gas to circulate in one exhaust pipe 12 carries out cooling treatment, makes vaporization water body fluid and collects, passes through what is set in the 4th cabinet 31
Second chamber 33 guarantees that gas flows through condensation 30, first chamber 32 is arranged above second chamber 33 in order to heat transfer
To first chamber 32, absorb heat to the air flowed through in second chamber 33, it can to improve the endothermic effect of first chamber 32
Coolant liquid is injected inside first chamber 32 to improve endothermic effect, realizes the water body liquefaction containing vaporization in the gas of recycling,
Realize heat recovery, effective improving material dry mass shortens process time.
33 liang of second chamber corresponding side walls are separately connected downtake pipe 12, realize gas circulation, and such enlargement gas exists
Circulation in second chamber 33, is also advantageous for extended residence time of the gas in second chamber 33, improves to containing in gas
4th cabinet 31 of some condensate moisture effects, 33 lower section of second chamber has third chamber 34, third chamber 34 and the second chamber
It is connected between room 33 by intercommunicating pore 35.Heat absorption liquid is stored in first chamber 32.The pump housing is additionally provided on downtake pipe 12
70,33 bottom of second chamber is snapped down to for the water body generated after condensation due to gravity, is collected by intercommunicating pore 35
In third chamber 34, for guarantee replacement first chamber 32 in liquid replacement, folding lid can be set on the 4th cabinet 31, similarly for
Convenient for the water body in discharge third chamber 34, another folding lid can be set on the 4th cabinet 31 convenient for discharge water body.
First drying box 10 includes the second cabinet 13, passes through the upper down space respectively of material baffle 14 inside the second cabinet 13, into
Expects pipe 17, downtake pipe 12, the first material transfer pipe 11 are connect with 10 upper box body of the first drying box respectively.It will using material baffle 14
First drying box, 10 inner space is divided into two parts up and down, and 14 surface of material baffle is evenly equipped with through-hole, is sent into first in material
After drying box 10, separated impurity out or biggish water droplet can be directly by being arranged on material baffle 14 in the drying process for material
Through-hole fall into 10 lower half portion of the first drying box, improve the processing quality of drying efficiency and dried object, feed pipe 17 and the
One exhaust pipe 12 is connected to 10 roof of the first drying box, and the first material transfer pipe 11 is connected to the first drying box 10 of 14 top of material baffle
The side wall of second cabinet 13 of case, in order to the material transmitting in the first drying box 10.
First motor 16 is equipped in second cabinet, 13 lower part box, 16 shaft of first motor is set to 13 upper tank of the second cabinet
In vivo, 16 shaft of first motor is around stirring blade 15 is laid, and the blade face of stirring blade 15 is parallel with shaft axis, stirring blade
15 are connected with the rotating shaft corresponding sides with inner concave arc surface, the other two edges evagination of stirring blade 15, with cambered surface junction fillet mistake
Degree.The rotation of its shaft is driven to drive the rotation of paddle 15 to the second cabinet by the way that first motor 16 is arranged in the second cabinet 13
Material in 13 is stirred effect, realizes the gap expanded between material, compared to the existing side dried using illumination
Formula, material is often in static state during sunning, and in body surface flow effect and bad, the present invention passes through to material gas
Stirring, promote material stirring movement in the second cabinet 13, expand the contact between material and air, improve the drying of material
The rotation of effect, stirring blade 15 has stirring action to the gas entered in the second cabinet 13, improves gas in the second cabinet 13
Stirring blade 15 is further connected with the rotating shaft corresponding sides setting inner concave arc surface, while stirring blade 15 by body flow effect
In addition two edges evagination, it is excessive with cambered surface junction fillet, on such 15 vertical direction of stirring blade, band of the both ends to air-flow
Dynamic effect is greater than 15 middle part of stirring blade, concentrates realization dry to middle part convenient for the air-flow at 15 both ends of stirring blade on vertical direction
It is partially folded between the moisture evaporation hot-fluid generated and unevaporated water point hot melt stream and dried material hot melt stream three during dry
Add, to improve material entirety pyrolysis rate and volatile producibility, material is made to reach dehydration in the short time in the first drying box 10
Peak value is kept away material its internal nutritional ingredient in long-time dehydration process and is gradually decreased, ensure that the quality of institute's processing materials simultaneously
Material is thoroughly dried.
Second cabinet, 13 lower part box is communicated with collector tube 21, collector tube 21 and the liquids recovery being set to outside the second cabinet 13
Case 20 connect, material be put into the second cabinet 13 may leach portion of water plus may also generate in the drying process compared with
More moisture, by the through-hole on material baffle 14, the moisture separated from material concentrates on 13 lower part of the second cabinet by collecting
Liquid pipe 21 carries out centralized collection to liquid recovery tank 20 and is focused on, and prevents the water body of 13 collective low of the second cabinet a large amount of
Vaporization aggravates dry energy consumption used.
Second drying box 60 includes third cabinet 62, and 62 top of third cabinet is connected separately with the first material transfer pipe 11, second
Motor 65 and second exhaust pipe 66,65 shaft of the second motor are connect with the agitating shaft 63 being arranged in third cabinet 62, third case
The second appendix 64 is connected on 62 lower sides of body.Second exhaust pipe 66 is connected with the pump housing 70.The discharge port of third cabinet 62
Equipped with valve 62, material has carried out rapid draing in the first drying box 10, and the material handled through the first drying box 10 is in short-term
Interior quick dehydration, effectively reduces the loss of the nutritional ingredient inside material, material after the drying process of the first drying box 10,
Material is delivered in the second drying box 60 by material transfer pipe 11 and carries out second of drying process, it is same in the second drying box 60
Material is stirred by the way of stirring, the agitating shaft 63 taken is common agitating shaft, and material is in the second drying box 60
The interior drying for carrying out the long period, thoroughly dries material, the unsuitable too fast and agitating shaft 63 of the mixing speed of agitating shaft 63
Material is selected to should be ceramic material or 304 stainless steels, material carries out constantly rolling under stirring action in the second drying box 60
Its cylinder water content is gradually decreased, the second appendix 64, which is arranged, in 62 side of third cabinet travels up to it to input gas
Gas is discharged in second exhaust pipe 66, realizes the gas flowing in third cabinet 62, avoids a large amount of vapor in third cabinet 62
It is a large amount of to stop.
First drying box 10 includes the second cabinet 13, and the tank wall of the second cabinet 13 includes inner wall 18 and outer wall 19, inner wall 18
Thermal insulation board 191 is equipped between outer wall 19,18 surface of inner wall is evenly distributed with rectangular-shaped invagination groove body 181.Rectangle is set on the inner wall 18
Invaginate groove body 181, and gas needs to reduce air-flow along the flowing velocity of inner wall 18 by each groove body 181 along 18 flow process of inner wall
And the heat increased between gas and inner wall 18 exchanges, and keeps 13 internal temperature of the second cabinet to be in stable state, further sets
It sets thermal insulation board 191 to exchange come the heat completely cut off between inner wall 18 and outer wall 19, is further ensured that the heat insulation effect of inner wall 18.
Heater box 40 is connected to the first drying box 10, the second drying box 60 respectively by the first appendix 41, the first gas transmission
The entry/exit gas tube orifice of pipe 41 is set to the first drying box 10, the second drying box 60,40 top half of heater box.For realizing general
Air in heater box 40 after heating, which inputs in each drying box, carries out heating operation to material.
Electric boiling plate 53 is equipped in heater box 40, electric boiling plate 53 is controlled by controller 50, is equipped in the first drier 10
First temperature detector 52, the second drier 60 is interior equipped with second temperature detector 54, and controller 50 is distinguished by connecting line 51
It is connect with the first temperature detector 52, second temperature detector 54.Utilize the first temperature detector 52, second temperature detector 54
The first drying box 10 and 60 internal temperature of the second drying box are monitored respectively, when temperature is lower, controller 50 controls electricity
Hot plate 53 increases air heating temperature, and signified controller 50 is computer terminal in the present invention.
The setting of 40 bottom opening of heater box, is sealed using the filter plate 43 that may filter that gas, by heater box 40
Bottom opening is situated so as to air and enters in heater box 40 heated, and the gaseous mass after heating is lighter, on
Floating on 40 top of heater will not flow out from 40 bottom of heater box, can be to the sky entered in heater box 40 by this filter plate 43
Gas is filtered processing, filters out the impurity in air, improves the hygienic quality to dry materials.
Embodiment 2:
The present invention is used for the drying machine of processing of aquatic products in actual use: carrying out before dry materials to each components interior clear
It washes, disinfect, before being put into material, it is dry to inputting first respectively after air heating that electric boiling plate 53 is controlled by controller 50
In dry room 10 and secondary drying chamber 60, the first temperature detector 52 and second temperature detector 54 carry out temperature detection and feedback coefficient
According to in controller 50, after temperature is up to standard, operator or that material is put into first by feed pipe 17 using manipulator is dry
It being dried in dry case 10, the water body generated during dry materials is collected and fed into liquid recovery tank 20 by collector tube 21,
Vapor caused by drying is discharged from downtake pipe 12, and condensation 30 carries out condensation process, removal first to vapor
Gas is inputted into back heater box 40 after most of moisture in 12 gas of exhaust pipe and carries out heating utilization again, material is dry first
After completing drying in case 10, redrying processing will be carried out in material transmission to the second drying box 60 using the first material transfer pipe 11.
It should be noted that material is shorter than the drying time in the second drying box 60 in the drying time in the first drying box 10.In the present embodiment
Signified material is the aquatic products such as fish, shrimps, crab class, shellfish.
Embodiment 3:
Test is dried to abalone using the drying machine of embodiment 1 and the operating method of embodiment 2 in the present embodiment, as
Experimental group concurrently sets two groups of control groups, and control group 1 uses micro-wave vacuum, and used equipment is that KL-2D-4ZG microwave is true
Empty drying equipment, the industrial microwave equipment Co., Ltd of the triumphant rib in Guangzhou are produced, microwave power 2000w, vacuum degree -80KPa, right
It is dry using natural drying according to group 2, it is dried under the weather that 32 DEG C~38 DEG C of Yu Xiaji outdoor temperature.
The abalone dried is the abalone after pickling, and abalone is fish market purchase；
The dried abalone of experimental group makes its moisture content of drying base to 10% or less used time 30min after tested, and control group 1 is dried
Abalone makes its moisture content of drying base to 10% or less used time 10min, the dried abalone of control group 2 make its moisture content of drying base to 10% with
The lower used time will be 2 days~3 days.
The abalone color evaluation processed to each group is as follows: the abalone color that experimental group is processed is orange-yellow, control group 1
The abalone processed is dark yellow, and the abalone color that control group 2 is processed is canescence.
The abalone mouthfeel evaluation processed to each group is as follows: the abalone hardness that experimental group is processed is moderate, there is higher bullet
Property and chewiness；The abalone elasticity that control group 1 is processed is general；The abalone hardness that control group 2 is processed is moderate, elasticity it is general and
There is fishy smell.
The abalone processed to each group carries out Contents of Amino Acids, and measured value is taurine Tau (mass parts in this test
Number/gkg-1), taurine value is 72.78 ± 0.18 before abalone used in each group is dry, is tested after each group is dry, experimental group
Abalone content of taurine is 71.66 ± 0.34；1 abalone content of taurine of control group is 52.34 ± 0.40,2 abalone ox of control group
Sulfonic acid content is 50.18 ± 0.25.
By above-mentioned test and testing result it is found that the rate of drying of control group 1 is due to experimental group and control group 2, but in fact
The processed abalone color of group, mouthfeel are tested due to control group 1,2, and the abalone amino acid turnover rate that experimental group is processed is far below
Control group 1,2, it is seen that the abalone processed by experimental group can be completed in a short time the dry work of abalone and nutritional ingredient stream
Mistake rate is lower.
The above disclosure is only the preferred embodiments of the present invention, cannot limit the right model of the present invention with this certainly
It encloses, therefore equivalent changes made in accordance with the claims of the present invention, is still within the scope of the present invention.
Claims (10)
1. being used for the drying machine of processing of aquatic products, comprising:
First drying box, for processing for the first time to material, first drying box has feed pipe and the first material transfer pipe,
Second drying box, for the material redrying after being dried for the first time to the first drying box, second drying box and first
The connection of material transfer pipe, also has discharge port,
Heater box, for inputting the first drying box after heating air, in the second drying box,
Wherein, first drying box is connect by downtake pipe with heater box, and cryogenic gas is sent back in heater box, described
Downtake pipe Single port is set to the first drying box internal upper part, and another port is set to lower part in heater box, first drying box
Downtake pipe between drying box is equipped with the condensation to cool down to first exhaust tube interior gas, the condensation
Including the 4th cabinet, the 4th cabinet has the second chamber being connected to downtake pipe, and the 4th cabinet, which also has, to be set
First chamber above second chamber.
2. the drying machine according to claim 1 for processing of aquatic products, it is characterised in that: the second chamber two is corresponding
Side wall is separately connected downtake pipe, realizes gas circulation, and the 4th cabinet below the second chamber has third chamber, institute
It states and is connected between third chamber and second chamber by intercommunicating pore.
3. the drying machine according to claim 1 for processing of aquatic products, it is characterised in that: first drying box includes
Second cabinet, by material baffle, upper down space, the feed pipe, downtake pipe, first pass second box house respectively
Expects pipe is connect with the first drying box upper box body respectively.
4. the drying machine according to claim 3 for processing of aquatic products, it is characterised in that: the second lower box case
It is equipped with first motor in vivo, the first motor shaft is set in the second cabinet upper box body, and the first motor shaft is surround
Stirring blade is laid, the blade face of the stirring blade is parallel with shaft axis, and the stirring blade is connected with the rotating shaft corresponding sides
With inner concave arc surface, the other two edges evagination of stirring blade is excessive with cambered surface junction fillet.
5. the drying machine according to claim 3 for processing of aquatic products, it is characterised in that: the second lower box case
Body is communicated with collector tube, and the collector tube is connect with the liquid recovery tank being set to outside the second cabinet.
6. the drying machine of processing of aquatic products is used for described in -5 any claims according to claim 1, it is characterised in that: described
Second drying box includes third cabinet, and third cabinet top is connected separately with the first material transfer pipe, the second motor and second row
Tracheae, second machine shaft and setting connect in the intracorporal stirring axis connection of third case, the third lower box side wall
It is connected to the second appendix.
7. the drying machine of processing of aquatic products is used for described in -5 any claims according to claim 1, it is characterised in that: described
First drying box includes the second cabinet, and the tank wall of second cabinet includes inner and outer wall, is set between the inner wall and outer wall
There is thermal insulation board, the inner wall surface is evenly distributed with rectangular-shaped invagination groove body.
8. the drying machine of processing of aquatic products is used for described in -5 any claims according to claim 1, it is characterised in that: described
Heater box is connected to the first drying box, the second drying box respectively by the first appendix, the entry/exit tracheae of first appendix
Mouth is set to the first drying box, the second drying box, heater box top half.
9. the drying machine of processing of aquatic products is used for described in -5 any claims according to claim 1, it is characterised in that: described
Electric boiling plate is equipped in heater box, the electric boiling plate is controlled by controller, and the first temperature is equipped in first drier and is examined
Device is surveyed, second temperature detector is equipped in second drier, the controller is examined with the first temperature respectively by connecting line
Survey device, the connection of second temperature detector.
10. the drying machine of processing of aquatic products is used for described in -5 any claims according to claim 1, it is characterised in that: institute
The setting of heater box bottom opening is stated, is sealed using the filter plate that may filter that gas.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910578142.9A CN110307707B (en) | 2019-06-28 | 2019-06-28 | A desiccator for aquatic products processing |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910578142.9A CN110307707B (en) | 2019-06-28 | 2019-06-28 | A desiccator for aquatic products processing |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN110307707A true CN110307707A (en) | 2019-10-08 |
| CN110307707B CN110307707B (en) | 2020-09-01 |
Family
ID=68078082
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910578142.9A Active CN110307707B (en) | 2019-06-28 | 2019-06-28 | A desiccator for aquatic products processing |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN110307707B (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105360877A (en) * | 2015-12-09 | 2016-03-02 | 重庆蜂糖妹农业开发有限公司 | Aquatic product lens drying box |
| CN111964361A (en) * | 2020-08-28 | 2020-11-20 | 太和县美欣药业有限公司 | Freeze-drying processing equipment for traditional Chinese medicine decoction pieces |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN200986363Y (en) * | 2006-12-25 | 2007-12-05 | 郑州大学生化工程中心 | Hot vapor and air combination type pneumatic dryer |
| CN201974013U (en) * | 2011-03-04 | 2011-09-14 | 宁波大发化纤有限公司 | PET (Polyethylene Terephthalate) bottle-flake hot-air circulating and continuous-drying system |
| CN206385008U (en) * | 2016-12-26 | 2017-08-08 | 南昌航空大学 | A kind of sludge two-stage drying device |
| CN107976054A (en) * | 2017-10-12 | 2018-05-01 | 浙江工业大学 | A kind of hydroresorcinol closed cycle two-stage drying means and drying device |
| CN207797629U (en) * | 2017-10-30 | 2018-08-31 | 浙江晶华玻璃有限公司 | A kind of drying device for makeup vial |
| CN108895789A (en) * | 2018-05-22 | 2018-11-27 | 安徽过湾农业科技有限公司 | A kind of baker of selenium-rich paddy |
| CN208751207U (en) * | 2018-08-10 | 2019-04-16 | 苏州爱立方服饰有限公司 | Textile process drying unit |
-
2019
- 2019-06-28 CN CN201910578142.9A patent/CN110307707B/en active Active
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN200986363Y (en) * | 2006-12-25 | 2007-12-05 | 郑州大学生化工程中心 | Hot vapor and air combination type pneumatic dryer |
| CN201974013U (en) * | 2011-03-04 | 2011-09-14 | 宁波大发化纤有限公司 | PET (Polyethylene Terephthalate) bottle-flake hot-air circulating and continuous-drying system |
| CN206385008U (en) * | 2016-12-26 | 2017-08-08 | 南昌航空大学 | A kind of sludge two-stage drying device |
| CN107976054A (en) * | 2017-10-12 | 2018-05-01 | 浙江工业大学 | A kind of hydroresorcinol closed cycle two-stage drying means and drying device |
| CN207797629U (en) * | 2017-10-30 | 2018-08-31 | 浙江晶华玻璃有限公司 | A kind of drying device for makeup vial |
| CN108895789A (en) * | 2018-05-22 | 2018-11-27 | 安徽过湾农业科技有限公司 | A kind of baker of selenium-rich paddy |
| CN208751207U (en) * | 2018-08-10 | 2019-04-16 | 苏州爱立方服饰有限公司 | Textile process drying unit |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105360877A (en) * | 2015-12-09 | 2016-03-02 | 重庆蜂糖妹农业开发有限公司 | Aquatic product lens drying box |
| CN111964361A (en) * | 2020-08-28 | 2020-11-20 | 太和县美欣药业有限公司 | Freeze-drying processing equipment for traditional Chinese medicine decoction pieces |
| CN111964361B (en) * | 2020-08-28 | 2021-11-23 | 太和县美欣药业有限公司 | Freeze-drying processing equipment for traditional Chinese medicine decoction pieces |
Also Published As
| Publication number | Publication date |
|---|---|
| CN110307707B (en) | 2020-09-01 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN110307707A (en) | Drying machine for processing of aquatic products | |
| CN109959218A (en) | A kind of Chinese prickly ash mentions dew, furnace drying method and device | |
| CN107036428A (en) | Solar energy and air source heat pump double source joint drying system | |
| CN207936654U (en) | Heat pump drying equipment | |
| CN208154934U (en) | A kind of dryer integrating photovoltaic and air energy heat pump | |
| CN108308266A (en) | A kind of pressure differential vacuum precooling all-in-one machine | |
| CN206880024U (en) | A kind of white fungus, matrimony vine, bamboo shoot, the drying unit of apricot | |
| CN206989664U (en) | Solar energy and air source heat pump double source joint drying system | |
| CN213060776U (en) | Rose essential oil processing is with oil-water separator | |
| CN211424869U (en) | Vacuum drying machine | |
| CN110074251A (en) | The production system of soy protein concentrate | |
| CN214172712U (en) | High-efficient circulation drying device | |
| CN208720656U (en) | It is dehydrated heat recovery apparatus and roasting plant | |
| CN114518025A (en) | Hot air blowing dryer capable of circularly heating | |
| CN206959477U (en) | A kind of closed loop dehumidifying heat pump drier with outside heat exchangers | |
| CN209001025U (en) | A kind of process equipment of recycling used batteries convenient for heating | |
| CN107337707A (en) | A kind of drying enrichment facility of high efficiency extraction Fish protein | |
| CN208312939U (en) | A kind of material drying device for kitchen castoff | |
| CN208653172U (en) | A kind of drier for Chinese medicine | |
| CN206891083U (en) | A kind of high Heisui River gadfly drying plant of drying efficiency | |
| CN208414403U (en) | A kind of dewatered drying installation for fermenting | |
| CN206744488U (en) | A kind of new fresh ox bone meat powder preparation facilities | |
| CN208296493U (en) | Vehicle-mounted floating drying equipment | |
| CN205980709U (en) | But split type heat pump drying equipment of recycle used heat | |
| CN214382171U (en) | A multistage sterilization equipment of dairy products for laboratory |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |