CN207963423U - A kind of Bee Pollen continuous drier - Google Patents
A kind of Bee Pollen continuous drier Download PDFInfo
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- CN207963423U CN207963423U CN201820254273.2U CN201820254273U CN207963423U CN 207963423 U CN207963423 U CN 207963423U CN 201820254273 U CN201820254273 U CN 201820254273U CN 207963423 U CN207963423 U CN 207963423U
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Abstract
The utility model is related to bee product processing technique fields, disclose a kind of Bee Pollen continuous drier, including frame body and babinet, it is configured with Bee Pollen feed inlet and Bee Pollen discharge port respectively on babinet, it is internally provided with demarcation strip in babinet, the internal chamber of babinet is divided into upper layer chamber and lower chamber by demarcation strip, and port is collectively formed in the free end of demarcation strip and the side wall of babinet；It is arranged and dries structure for conveying the first of upper layer chamber, the Bee Pollen to be dried fallen from Bee Pollen feed inlet can be heated, and the Bee Pollen after heating is conveyed towards close to the direction of port；It is arranged and dries structure for conveying the second of lower chamber, the Bee Pollen fallen from port can be heated, and the drying Bee Pollen after heating is conveyed towards close to the direction of Bee Pollen discharge port；Heat-pump dehumidification heating structure, air inlet are connected with lower chamber, and gas outlet is connected with upper layer chamber.The Bee Pollen continuous drier has the advantages that drying efficiency is high.
Description
Technical field
The utility model is related to bee product processing technique fields, more particularly to a kind of Bee Pollen continuous drier.
Background technology
Bee Pollen derives from the Nature, and Bee Pollen is special by being added in the pollen grain or nectar that are acquired to honeybee
A kind of irregular oblate dough mixed after glandular secretion object.Bee Pollen contain development of plants whole nutritional ingredients and
Active material is the source of plant life, is referred to as " miniature nutrition library ".The Bee Pollen total output the first in the world in China, however, by
In the limitation of the conditions such as postpartum fresh-keeping, dry and storage and transportation, frequently can lead to beekeeper reduces the harvesting amount of Bee Pollen.Fresh melissa
After powder harvesting, wet basis moisture content is up to 20% to 30%, and the activity of microorganism and enzyme is very high, needs that processing is dried in time,
Otherwise Rapid Fermentation is gone bad, loss of effective components loses effect value.Therefore, in the harvest season, fresh Bee Pollen is carried out
Timely drying is the important channel for avoiding Bee Pollen quality deterioration, extending Bee Pollen shelf life.
The conventional drying method of existing Bee Pollen has：Solar drying, aeration-drying, electrothermal drying and heated kang drying etc.
Method.But these methods are usually all difficult to be effectively protected nutritional ingredient and active material in Bee Pollen, pole in drying process
Fat oxidation, color and luster fission etc. are easily led to, to cause the inferior situation of Bee Pollen after drying.In addition, current Bee Pollen
When processing is dried, the case where there are capacity usage ratio is low and high energy consumption is also tended to, this also directly results in increase drying
Process cost.
Utility model content
(1) technical problems to be solved
The purpose of this utility model is to provide a kind of Bee Pollen continuous drier, to solve in the prior art, due to nothing
Method is continuous drying to Bee Pollen progress, and drying process is difficult to realize automate；Drying operation lacks heat energy recycle system simultaneously
System, dry processing link can not optimize adjustment according to the dry period moisture content change of melissa powder material different dry so that bee
Pollen energy consumption for drying is high, and production cost rises；And lipid oxidation, color and luster fission are not only easy to happen in drying process etc., also
There are uneven drying phenomenons, to cause the inferior technical problem of Bee Pollen after drying.
(2) technical solution
In order to solve the above-mentioned technical problem, the utility model provides a kind of Bee Pollen continuous drier, including：Frame body；
Babinet is arranged on the frame body, Bee Pollen feed inlet and Bee Pollen discharge port is configured with respectively on the babinet, described
Babinet is internally provided with demarcation strip, and the internal chamber of the babinet is divided into upper layer chamber and lower chamber by the demarcation strip,
Wherein, port is collectively formed in the free end of the demarcation strip and the side wall of the babinet；It is arranged the first of the upper layer chamber
Dry structure for conveying, can heat the Bee Pollen to be dried fallen from the Bee Pollen feed inlet, and will be after heating
Bee Pollen is conveyed towards close to the direction of the port；It is arranged and dries structure for conveying the second of the lower chamber, it can will be from
The Bee Pollen that the port is fallen is heated, and by the drying Bee Pollen after heating towards close to the side of the Bee Pollen discharge port
To conveying；And heat-pump dehumidification heating structure, the air inlet of the heat-pump dehumidification heating structure are connected with the lower chamber,
The gas outlet of the heat-pump dehumidification heating structure is connected with the upper layer chamber.
Wherein, the first drying structure for conveying includes being arranged in the lower surface of the roof of the babinet and can be to described
Bee Pollen to be dried carries out the first heating plate of first segment heating.
Wherein, the first drying structure for conveying further includes the front side wall and/or rear wall for being separately positioned on the babinet
On the first main drive roll and the first driven voller and both ends be respectively sleeved at first main drive roll and described first driven
The outside of roller and the first conveyer belt that can transport Bee Pollen to be dried are equipped with the first driving electricity on first main drive roll
Machine, first conveyer belt are arranged in the lower section of first heating plate.
Wherein, the second drying structure for conveying includes being arranged in the lower surface of the demarcation strip and capable of adding to first segment
Bee Pollen after heat carries out the second heating plate of second segment heating.
Wherein, the second drying structure for conveying further includes the front side wall and/or rear wall for being separately positioned on the babinet
On the second main drive roll and the second driven voller and both ends be respectively sleeved at second main drive roll and described second driven
The outside of roller and the second conveyer belt that can transport the Bee Pollen after first segment heating, are equipped with the on second main drive roll
Two driving motors, second conveyer belt are arranged in the lower section of second heating plate.
Wherein, the Bee Pollen continuous drier further includes Bee Pollen after capable of heating first segment from described first
Conveyer belt imported into the first stock guide on second conveyer belt, and first stock guide is arranged by first level plate in institute
State the inside of upper layer chamber, wherein the plane where first stock guide is cut with what the Bee Pollen after first segment heating discharged
Line direction is parallel.
Wherein, the Bee Pollen continuous drier further includes being arranged in the lower section of the babinet and capable of accepting described dry
The finished bin of dry Bee Pollen, the finished bin are connected by ready-packaged joint with the Bee Pollen discharge port of the babinet.
Wherein, the Bee Pollen continuous drier further includes that can import dry Bee Pollen from second conveyer belt
To the second stock guide in the finished bin, second stock guide is arranged by the second level board in the lower chamber
Portion, wherein the plane where second stock guide is parallel with the dry tangential direction of Bee Pollen discharging.
Wherein, the heat-pump dehumidification heating structure includes the evaporator, wind turbine and condenser being sequentially communicated, wherein institute
The air inlet for stating evaporator is connected by first pipe with the lower chamber, and the gas outlet of the condenser passes through the second pipe
Road is connected with the upper layer chamber.
Wherein, the Bee Pollen continuous drier further includes vacuum pump and gas bomb, wherein the vacuum pump passes through
One pressure pipeline is connected with the internal chamber of the babinet, and the gas bomb passes through in second pressure pipeline and the babinet
Portion's chamber is connected.
Wherein, the Bee Pollen continuous drier further includes the raw material cabin being arranged on the babinet, the raw material cabin
It is embedded the storehouse ontology in the Bee Pollen feed inlet including lower end, the first opening is configured in the upper end of the storehouse ontology,
The lower end of the storehouse ontology is configured with the second opening, wherein the lower end of the storehouse ontology is configured to interior receipts structure.
Wherein, the lid for closing first opening can be covered by being equipped in the upper end of the storehouse ontology, in the lid
Between be partly configured with transparent observing area.
Wherein, it is configured with annular groove in the top edge of first opening, sealing is embedded in the annular groove
Item.
Wherein, it is configured with downward opening regulating tank on the interior inclined-plane for receiving structure, is equipped in the regulating tank
The striker plate that can be slided up and down along the length direction of the regulating tank.
Wherein, the fastener of the striker plate can be fixed by being equipped on the regulating tank.
(3) advantageous effect
Bee Pollen continuous drier provided by the utility model has the following advantages that compared with prior art：
When Bee Pollen to be dried is dried, start heat-pump dehumidification heating structure, the heat-pump dehumidification heating structure energy
Enough that Bee Pollen to be dried is dehumidified and heated, specifically, which can be effectively reduced babinet
The humidity of inner cavity chamber, simultaneously, additionally it is possible to the latent heat and sensible heat in dry waste gas are recycled, to which energy utilization greatly improved
Rate.However, since heat-pump dehumidification heating structure belongs to middle low temperature drying, the early stage of drying heating is slow, thus, to accelerate to increase to wait doing
The drying temperature of dry Bee Pollen can be added the Bee Pollen fallen from Bee Pollen feed inlet by the first drying structure for conveying
Heat, and the Bee Pollen after heating is conveyed towards close to the direction of port, meanwhile, it will be from port by the second drying structure for conveying
The Bee Pollen fallen is heated, and the drying Bee Pollen after heating is conveyed towards close to the direction of Bee Pollen discharge port.In this way,
The application realizes the continuous drying of Bee Pollen by using the mode that belt material conveys, to be dried to greatly increase
The drying efficiency of Bee Pollen.In addition it is also necessary to which explanation, entire dry during Bee Pollen to be dried is dried
Process is in closed loop drying system, is conducive to retain volatile ingredient in Bee Pollen, improves the product quality of Bee Pollen；Heat transfer is situated between
Matter is usually inert gas, to significantly reduce Bee Pollen bioactive substance oxidative degradation degree；In Bee Pollen
In the storage in later stage, the storage medium of finished bin is inert gas, will greatly reduce oxygen, microorganism and humidity etc.
Factor is adversely affected caused by its product quality.
Finally, realize that thin layer is dry by the cooperation of the striker plate of raw material cabin and conveyer belt to adjust the thickness of dried material
Dry, belt drying is also effectively increased drying area, and rate of drying can be improved, and shortens drying time.Material is in belt conveying process
In automatic turning can occur, effectively overcome the uneven drying of material, be conducive to improve dry products quality.The invention belongs to
In the novel dried equipment that a kind of conduction, radiation, convection current and thin layer drying are combined, it is applicable not only to Bee Pollen drying, is also fitted
Close the dry processing of other heat sensitive materials.
Description of the drawings
Fig. 1 is the overall structure diagram of the Bee Pollen continuous drier of embodiments herein；
Fig. 2 is the overall structure diagram of the raw material cabin in Fig. 1；
Fig. 3 is the partial enlargement structural representation of the I in Fig. 2；
Fig. 4 is the overall structure diagram of the finished bin in Fig. 1.
In figure, 30：Frame body；1：Babinet；11：Bee Pollen feed inlet；12：Bee Pollen discharge port；2：Demarcation strip；1a：Upper layer
Chamber；1b：Lower chamber；3：First drying structure for conveying；31：First heating plate；32：First main drive roll；33：First is driven
Roller；34：First conveyer belt；4：Second structure for conveying；41：Second heating plate；42：Second main drive roll；43：Second driven voller；
44：Second conveyer belt；5：Heat-pump dehumidification heating structure；51：Condenser；52：Wind turbine；53：Evaporator；6：First stock guide；7：
Finished bin；8：Second stock guide；9：Vacuum pump；10：Gas bomb；20：Raw material cabin；21：Storehouse ontology；22：Lid；23：Sealing strip；
24：Regulating tank；25：Striker plate.
Specific implementation mode
With reference to the accompanying drawings and examples, specific embodiment of the present utility model is described in further detail.Below
Example is not intended to limit the scope of the present invention for illustrating the utility model.
In the description of the present invention, it should be noted that unless otherwise clearly defined and limited, term " is pacified
Dress ", " connected ", " connection " shall be understood in a broad sense, for example, it may be being fixedly connected, may be a detachable connection, or integrally
Connection；It can be mechanical connection, can also be electrical connection；Can be directly connected, can also indirectly connected through an intermediary,
It can be the connection inside two elements.For the ordinary skill in the art, it can understand above-mentioned art with concrete condition
The concrete meaning of language in the present invention.
Embodiment 1：
As shown in Figure 1, schematically showing that the Bee Pollen continuous drier includes frame body 30, babinet 1, separates in figure
Plate 2, first dries structure for conveying 3, second and dries structure for conveying 4 and heat-pump dehumidification heating structure 5.
In embodiments herein, babinet 1 be arranged on frame body 30, be configured with respectively on the babinet 1 Bee Pollen into
Material mouth 11 and Bee Pollen discharge port 12 are internally provided with demarcation strip 2 in the babinet 1, and the demarcation strip 2 is by the internal chamber of babinet 1
It is divided into upper layer chamber 1a and lower chamber 1b, wherein port is collectively formed with the side wall of babinet 1 in the free end of the demarcation strip 2.
It should be noted that it is by the free end of demarcation strip 2, the front side wall of babinet 1, rear wall and the common structure of right side wall to be somebody's turn to do " port "
It makes.
In addition, it should also be noted that, the demarcation strip 2 needs to have certain rigidity, so as to play support and peace
The effect of dress the second heating plate 41 as described below.
The first drying structure for conveying 3 is arranged in the chamber 1a of upper layer, can be waited for what is fallen from Bee Pollen feed inlet 11
Dry Bee Pollen is heated, and the Bee Pollen after heating is conveyed towards close to the direction of port.
The second drying structure for conveying 4 is arranged in lower chamber 1b, can be added the Bee Pollen fallen from port
Heat, and the drying Bee Pollen after heating is conveyed towards close to the direction of Bee Pollen discharge port 12.
The air inlet of heat-pump dehumidification heating structure 5 is connected with lower chamber 1b, the outlet of the heat-pump dehumidification heating structure 5
Mouth is connected with upper layer chamber 1a.Specifically, when Bee Pollen to be dried is dried, start heat-pump dehumidification heating structure 5,
The heat-pump dehumidification heating structure 5 can be dehumidified and heated to Bee Pollen to be dried, specifically, the heat-pump dehumidification heating structure
5 can be effectively reduced the humidity of the inner cavity chamber of babinet 1, simultaneously, additionally it is possible to the latent heat and sensible heat in dry waste gas are recycled,
To which capacity usage ratio greatly improved.However, since heat-pump dehumidification heating structure 5 belongs to middle low temperature drying, the early stage of drying liter
It is warm slow, thus, to accelerate to increase the drying temperature of Bee Pollen to be dried, can dry structure for conveying 3 by first will be from Bee Pollen
The Bee Pollen that feed inlet 11 is fallen is heated, and the Bee Pollen after heating is conveyed towards close to the direction of port, meanwhile, pass through
The second drying structure for conveying 4 heats the Bee Pollen fallen from port, and by the drying Bee Pollen after heating towards close
The direction of Bee Pollen discharge port 12 conveys.In this way, the application realizes Bee Pollen by using the mode that belt material conveys
It is continuous drying, to greatly increase the heating rate of Bee Pollen to be dried.In addition it is also necessary to explanation, to be dried
During Bee Pollen is dried, heat transfer medium is usually inert gas (being, for example, nitrogen, helium, argon gas or neon etc.),
To significantly reduce Bee Pollen bioactive substance oxidative degradation degree, in the storage in Bee Pollen later stage,
The storage medium of finished bin 7 as described below is inert gas, will greatly reduce the factors pair such as oxygen, microorganism and humidity
Adverse effect caused by its product quality.
Above-mentioned heat transfer medium is alternatively carbon dioxide.
In addition it is also necessary to explanation, the application are applicable not only to the drying of Bee Pollen, meanwhile, it also is adapted for other temperature-sensitives
Property particulate matter drying and dehydrating processing.
As shown in Figure 1, schematically showing that the first drying structure for conveying 3 includes being arranged on the top of the babinet 1 in figure
The lower surface of wall and the first heating plate 31 that first segment heating can be carried out to Bee Pollen to be dried.Specifically, by this first
Heating plate 31 heats Bee Pollen to be dried, can so as to rapidly improve the temperature of Bee Pollen to be dried
It is dehydrated as early as possible.
To advanced optimize the first drying structure for conveying 3 in above-mentioned technical proposal, based on the above technical solution,
The first drying structure for conveying 3 further includes the front side wall for being separately positioned on the babinet 1 and/or the first main drive roll on rear wall
32 and first driven voller 33 and both ends be respectively sleeved at the outside of the first main drive roll 32 and the first driven voller 33 and can transport
First conveyer belt 34 of defeated Bee Pollen to be dried is equipped with the first driving motor, the first conveyer belt 34 on the first main drive roll 32
It is arranged in the lower section of the first heating plate 31.Specifically, first main drive roll 32 is promoted to carry out week by first driving motor
To rotation, by the rotation of first main drive roll 32, to drive the rotation of the first conveyer belt 34 further to pass through
The rotation of first conveyer belt 34 drives the rotation of the first driven voller 33, in this way, working as Bee Pollen to be dried from Bee Pollen feed inlet 11
After falling on first conveyer belt 34, it will be conveyed towards the direction of port (not shown) while being heated.
In addition, by making first conveyer belt 34 be arranged in the lower section of first heating plate 31, waited for so as to increase
The heating surface area of dry Bee Pollen, improves the drying efficiency of Bee Pollen to be dried.
As shown in Figure 1, in the ratio more preferably in technical solution of the application, which includes setting
Set the second heating plate that the Bee Pollen in the lower surface of the demarcation strip 2 and after capable of being heated to first segment carries out second segment heating
41.Specifically, which can do the Bee Pollen after first segment heats and further heat, so as into
Improve to one step the drying efficiency of Bee Pollen.It should be noted that during being heated to Bee Pollen, difference can be passed through
Different heating temperatures is set to the first heating plate 31 and the second heating plate 41, to reach to Bee Pollen in different drying stages
Carry out the purpose of different degrees of heating.
In a specific embodiment, first heating plate 31 and the second heating plate 41 can be carbon fiber electrothermal plate.
To advanced optimize the second drying structure for conveying 4 in above-mentioned technical proposal, based on the above technical solution,
The second drying structure for conveying 4 further includes the front side wall for being separately positioned on the babinet 1 and/or the second main drive roll on rear wall
42 and second driven voller 43 and both ends be respectively sleeved at the outside of the second main drive roll 42 and the second driven voller 43 and can transport
Second conveyer belt 44 of the Bee Pollen after the heating of defeated first segment, is equipped with the second driving motor on the second main drive roll 42, and second
Conveyer belt 44 is arranged in the lower section of the second heating plate 44.It should be noted that by second conveyer belt 44 setting in the second heating
The benefit of the lower section of plate 41 is identical as the benefit that the first conveyer belt 34 is arranged in the lower section of first heating plate 31, to save a piece
For the sake of width, it is not detailed herein.
In addition it is also necessary to explanation, the rotation of the rotation direction of first main drive roll 32 and the second main drive roll 42
Direction on the contrary, in this way it can be ensured that after being heated to first segment melissa carry out second segment heating after, can be accurately and timely
Dry Bee Pollen is transported at Bee Pollen discharge port 12, further, facilitates and the drying Bee Pollen is collected into finished bin 7
In, to complete the drying operation of Bee Pollen.
As shown in Figure 1, in a preferred embodiment, which further includes can be by first segment
Bee Pollen after heating imported into the first stock guide 6 on the second conveyer belt 44 from the first conveyer belt 34, and the first stock guide 6 passes through
First level plate is arranged in the inside of upper layer chamber 1a, wherein the plane where the first stock guide 6 and the bee after first segment heating
The tangential direction of pollen discharging is parallel.Specifically, the setting of first stock guide 6, it can be ensured that after first segment heats
Bee Pollen is accurately smoothly fallen on the second conveyer belt 44, avoids falling on the bottom wall of babinet 1, causes waste Bee Pollen
Situation.
As shown in Figure 1 and Figure 4, it further includes being arranged in case that the Bee Pollen continuous drier is also schematically shown in figure
The lower section of body 1 and the finished bin 7 that can accept dry Bee Pollen, the finished bin 7 are gone out by the Bee Pollen of ready-packaged joint and babinet 1
Material mouth 12 is connected.It should be noted that butterfly valve is equipped in the finished bin 7, so as to ensure the sealing in the finished bin 7
Property, simultaneously as during Bee Pollen is dried, the butterfly valve in finished bin 7 is always the state in opening, because
And the inert gas injected into babinet 1 by gas bomb 10 as described below also can some be injected into finished bin 7,
After having collected dry Bee Pollen in finished bin 7, by closing butterfly valve, the sealing storage to dry Bee Pollen can be realized,
In this way, during term storage after dry Bee Pollen carries out, the factors pair such as oxygen, microorganism and humidity will be greatly reduced
Adverse effect caused by its product quality.
As shown in Figure 1, it further includes that can will dry bee to also schematically show the Bee Pollen continuous drier in figure
Pollen imported into finished bin 7 the second stock guide 8 from the second conveyer belt 44, and the second stock guide 8 is arranged by the second level board
In the inside of lower chamber 1b, wherein the plane where the second stock guide 8 is equal with the dry tangential direction of Bee Pollen discharging
Row.Specifically, pass through the setting of second stock guide 8, it can be ensured that the drying Bee Pollen after second segment heats is accurately steady
Ground is transported at Bee Pollen discharge port 12, is avoided dry Bee Pollen from falling on the bottom wall of babinet 1, is caused the feelings of waste Bee Pollen
Condition.
In a specific embodiment, stainless steel 304 L materials can be used in first stock guide 6 and the second stock guide 8
It is fabricated, thickness can be 2 millimeters to 3 millimeters, and food is installed on the inclined surface of first stock guide 6 and the second stock guide 8
The thickness of grade layer of silica gel, the food grade silicone layer is 3 millimeters to 6 millimeters.
In one embodiment, heat-pump dehumidification heating structure 5 includes the evaporator 53 being sequentially communicated, wind turbine 52 and condensation
Device 51, wherein the air inlet of evaporator 53 is connected by first pipe with lower chamber 1b, and the gas outlet of condenser 51 passes through
Second pipe is connected with upper layer chamber 1a.In this way it can be ensured that the internal chamber of babinet 1 and heat-pump dehumidification heating structure 5
Inside forms Closed Cycle access, meanwhile, it can play the role of dehumidifying to the internal chamber of babinet 1 and being heated.
As shown in Figure 1, the Bee Pollen continuous drier further includes vacuum pump 9 and gas bomb 10, wherein vacuum pump 9 is logical
It crosses first pressure pipeline with the internal chamber of babinet 1 to be connected, the inner chamber that gas bomb 10 passes through second pressure pipeline and babinet 1
Room is connected.It should be noted that before Bee Pollen to be dried is dried, it can be by starting vacuum pump 9, to babinet 1
Internal chamber carries out vacuumizing operation, when the vacuum of the pressure sensor (not shown) monitoring in the internal chamber of babinet 1
When pressure reaches 4kPa, the solenoid valve being arranged on the first pressure pipeline is closed, and vacuum pump 9 stops operation.At this point, setting exists
Solenoid valve on second pressure pipeline is opened, and gas bomb 10 inputs inert gas into the internal chamber of babinet 1, when babinet 1
When the pressure of internal chamber reaches standard atmospheric pressure, pressure sensor sends a signal to automatic controller (not shown), electricity
Magnet valve is closed immediately.At this point, starting the first driving motor, simultaneously so that first heating plate 31 is begun to warm up, and wind turbine 52 starts
Work.
As depicted in figs. 1 and 2, schematically show that the Bee Pollen continuous drier further includes being arranged in babinet in figure
Raw material cabin 20 on 1, raw material cabin 20 are embedded the storehouse ontology 21 in Bee Pollen feed inlet 11 including lower end, and in storehouse, ontology 21 is upper
End is configured with the first opening, and in storehouse, the lower end of ontology is configured with the second opening, wherein the lower end of storehouse ontology 21 is configured to interior receipts knot
Structure.Specifically, by the way that the lower end of storehouse ontology 21 is configured to interior receipts structure, so as to accelerate the conveying of Bee Pollen to be dried,
During avoiding Bee Pollen to be dried from being conveyed towards the direction of Bee Pollen feed inlet 11 along the inside of storehouse ontology 21, knot arch occurs
Situation.
In one embodiment, the lid 22 for closing the first opening can be covered by being equipped in the upper end of the storehouse ontology 21, in lid
22 middle section is configured with transparent observing area.It should be noted that the setting of the lid 22, enables to the interior of storehouse ontology 21
Portion is in relatively closed environment, avoids extraneous air, dust or moisture etc. from entering the inside of storehouse ontology 21, further
Ground, it is ensured that the quality of the Bee Pollen to be dried in storehouse ontology 21 is free from the influence of the external environment.In addition, the transparent observing area
The case where being arranged, the material position height for observing Bee Pollen to be dried and blanking can be facilitated, at the same time it can also according to the change of material position
Change, add Bee Pollen to be dried to the inside of storehouse ontology 21 in real time, to realize the continuous work dried to Bee Pollen to be dried
Industry.
In one embodiment, it is configured with annular groove (not shown) in the top edge of first opening, in the ring
Sealing strip 23 is embedded in connected in star.Specifically, by adding the sealing strip 23, so as to greatly improve lid 22 and storehouse
Leakproofness between ontology 21.
As shown in Figures 2 and 3, also schematically shown in figure this it is interior receive structure inclined-plane on be configured with it is opening down
Regulating tank 24, being equipped in the regulating tank 24 can be along the striker plate 25 that the length direction of regulating tank 24 slides up and down.
It should be noted that since the moisture content of Bee Pollen to be dried is not quite similar, it, can to improve the drying efficiency of Bee Pollen to be dried
Achieve the purpose that adjust the thickness of Bee Pollen to be dried by the cooperation of striker plate 25 and first conveyer belt 34, further,
Realize the thin layer drying to Bee Pollen, that is to say, that adjusting can be reached and fall to the first conveyer belt from Bee Pollen feed inlet 11
The purpose of the thickness of Bee Pollen to be dried on 34.In addition, belt thin layer drying can also effectively increase drying area, improve dry
Dry rate shortens drying time.In addition, Bee Pollen to be dried is during belt conveying, it may occur that automatic turning, so as to
With the defect of the uneven drying efficiently against Bee Pollen to be dried, advantageously improve the quality of Bee Pollen to be dried.
In another embodiment, (do not show in figure equipped with the fastener that can fix striker plate 25 on the regulating tank 24
Go out).It should be noted that the setting of the fastener, can neatly be fixed the position where the striker plate 25.It needs
Illustrate, which can be bolt, screw rod or bolt etc..
The specific work process of the Bee Pollen continuous drier is as follows：
First, the internal chamber of babinet 1 is carried out vacuumizing operation.
Secondly, inert gas is injected into the internal chamber for vacuumizing post-job babinet 1.
Next, starting heat-pump dehumidification heating structure 5, at the same time, it is defeated that Bee Pollen to be dried is transported to the first drying
Progress first segment drying in structure 3 is sent, to which Bee Pollen to be dried is carried out preliminary hydro-extraction operation.
Then, the post-job Bee Pollen of preliminary hydro-extraction is transported to progress second segment drying on the second drying structure for conveying 4,
To obtain dry Bee Pollen.
Finally, dry Bee Pollen is collected in the closed finished bin 7 rich in inert gas, drying operation is completed.Tool
Body, finished bin 7 is connect with babinet 1, opens butterfly valve.Striker plate 25 is adjusted, the thickness of Bee Pollen to be dried is adjusted to 6 millis
Bee Pollen to be dried is added in raw material cabin 20 by rice to 12 millimeters, closes lid 22.Power on, automatic controller is (in figure
It is not shown) start, the speed of service of the first conveyer belt 34 and the second conveyer belt 44 is set as 5 mm/mins to 60 millis m/min
The temperature of first heating plate 31 and second heating 41 is set as 45 degree to 65 degree, the speed of circulating current is set as 0.5 by clock
Meter per second is to 2.5 meter per seconds.Start vacuum pump 9, opens the solenoid valve being arranged on first pressure pipeline, wait for the inner chamber of babinet 1
When the vacuum pressure of pressure sensor monitoring in room reaches 4kPa, solenoid valve is closed, and vacuum pump 9 stops operation.Setting is the
Solenoid valve on two pressure pipelines is opened, and gas bomb 10 inputs inert gas into babinet 1, when the pressure in babinet 1 reaches mark
When quasi- atmospheric pressure, pressure sensor sends a signal to automatic controller, and the solenoid valve on second pressure pipeline is arranged and closes immediately
It closes.First driving motor starts, and the first heating plate 31 is begun to warm up, and wind turbine 52 starts, and compressor (not shown) starts work
Make.When first batch of Bee Pollen falls to the first stock guide 6 from the first conveyer belt 34, the transmission of photoelectric sensor (not shown)
To automatic controller, the second driving motor starts signal, and the second heating plate 41 is begun to warm up, with the rising of drying temperature, when
After monitors temperature reaches the peak of set temperature, automatic controller will be switched off the first heating plate 31 and second and add
The power supply of hot plate 41, with the propulsion of drying process, after monitors temperature reaches the minimum of set temperature, from
Movement controller will turn on the power supply of the first heating plate 31 and the second heating plate 41, to realize the accurate control of temperature in drying process
System.After all Bee Pollens on the first conveyer belt 34 fall into the first stock guide 6, photoelectric sensor, which is sent a signal to, to be automatically controlled
Device, subsequent first driving motor and the first heating plate 31 are automatically stopped work.When all Bee Pollens are fallen on the second conveyer belt 44
After second stock guide 8, photoelectric sensor sends a signal to automatic controller, then, the second driving motor, the second heating plate 41,
Compressor and wind turbine 52 are stopped, and Bee Pollen drying is completed, and closes the butterfly valve in finished bin 7, closed finished bin 7 is put
Enter freezer storage.
In conclusion when Bee Pollen to be dried is dried, start heat-pump dehumidification heating structure 5, the heat-pump dehumidification
Heating structure 5 can be dehumidified and heated to Bee Pollen to be dried, and specifically, which can be effective
Ground reduces the humidity of the inner cavity chamber of babinet 1, simultaneously, additionally it is possible to the latent heat and sensible heat in dry waste gas is recycled, to substantially
Improve capacity usage ratio.However, since heat-pump dehumidification heating structure 5 belongs to middle low temperature drying, heat up before dry slow, thus,
To accelerate the drying temperature of dry Bee Pollen to be lifted, can will be fallen from Bee Pollen feed inlet 11 by the first drying structure for conveying 3
The Bee Pollen fallen is heated, and the Bee Pollen after heating is conveyed towards close to the direction of port, meanwhile, it second is dried by this
Structure for conveying 4 heats the Bee Pollen fallen from port, and the drying Bee Pollen after heating is discharged towards close to Bee Pollen
The direction conveying of mouth 12.In this way, the application realizes the continuous drying of Bee Pollen by using the mode that belt material conveys, from
And greatly increase the drying efficiency of Bee Pollen to be dried.In addition it is also necessary to which explanation, does Bee Pollen to be dried
In dry process, heat transfer medium is usually inert gas, to significantly reduce Bee Pollen bioactive substance oxidation
Palliating degradation degree, in the storage in Bee Pollen later stage, the storage medium of finished bin is inert gas, will greatly reduce oxygen
The factors such as gas, microorganism and humidity are adversely affected caused by its product quality.
The above is only the preferred embodiment of the utility model only, is not intended to limit the utility model, all at this
Within the spirit and principle of utility model, any modification, equivalent replacement, improvement and so on should be included in the utility model
Protection domain within.
Claims (15)
1. a kind of Bee Pollen continuous drier, which is characterized in that including：
Frame body；
Babinet is arranged on the frame body, is configured with Bee Pollen feed inlet and Bee Pollen discharge port respectively on the babinet,
The babinet is internally provided with demarcation strip, and the internal chamber of the babinet is divided into upper layer chamber and lower layer's chamber by the demarcation strip
Room, wherein port is collectively formed in the free end of the demarcation strip and the side wall of the babinet；
It is arranged and dries structure for conveying the first of the upper layer chamber, can will be fallen from the Bee Pollen feed inlet to be dried
Bee Pollen is heated, and the Bee Pollen after heating is conveyed towards close to the direction of the port；
It is arranged and dries structure for conveying the second of the lower chamber, the Bee Pollen fallen from the port can be added
Heat, and the drying Bee Pollen after heating is conveyed towards close to the direction of the Bee Pollen discharge port；And
The air inlet of heat-pump dehumidification heating structure, the heat-pump dehumidification heating structure is connected with the lower chamber, the heat
The gas outlet of pump dehumidifying heating structure is connected with the upper layer chamber.
2. Bee Pollen continuous drier according to claim 1, which is characterized in that the first drying structure for conveying packet
It includes and is arranged in the lower surface of the roof of the babinet and the first of the Bee Pollen progress first segment heating to be dried can be added
Hot plate.
3. Bee Pollen continuous drier according to claim 2, which is characterized in that the first drying structure for conveying is also
Including the first main drive roll being separately positioned on the front side wall and/or rear wall of the babinet and the first driven voller and two
End is respectively sleeved at the outside of first main drive roll and first driven voller and can transport the of Bee Pollen to be dried
One conveyer belt, is equipped with the first driving motor on first main drive roll, and the first conveyer belt setting adds described first
The lower section of hot plate.
4. Bee Pollen continuous drier according to claim 3, which is characterized in that the second drying structure for conveying packet
It includes and is arranged in the lower surface of the demarcation strip and second of the Bee Pollen progress second segment heating after first segment heating can be added
Hot plate.
5. Bee Pollen continuous drier according to claim 4, which is characterized in that the second drying structure for conveying is also
Including the second main drive roll being separately positioned on the front side wall and/or rear wall of the babinet and the second driven voller and two
End is respectively sleeved at the outside of second main drive roll and second driven voller and can transport the bee after first segment heating
Second conveyer belt of pollen, is equipped with the second driving motor on second main drive roll, and second conveyer belt is arranged in institute
State the lower section of the second heating plate.
6. Bee Pollen continuous drier according to claim 5, which is characterized in that the Bee Pollen continuous drier
Further include Bee Pollen after capable of heating first segment imported into from first conveyer belt on second conveyer belt first
Stock guide, first stock guide are arranged by first level plate in the inside of the upper layer chamber, wherein first guide
The tangential direction of Bee Pollen discharging after plane where plate is heated with first segment is parallel.
7. Bee Pollen continuous drier according to claim 5, which is characterized in that the Bee Pollen continuous drier
Further include the finished bin that is arranged in the lower section of the babinet and can accept the dry Bee Pollen, the finished bin passes through fast-assembling
Connector is connected with the Bee Pollen discharge port of the babinet.
8. Bee Pollen continuous drier according to claim 7, which is characterized in that the Bee Pollen continuous drier
Further include the second stock guide that dry Bee Pollen can be imported into from second conveyer belt in the finished bin, described second
Stock guide is arranged by the second level board in the inside of the lower chamber, wherein plane where second stock guide with
The tangential direction of the dry Bee Pollen discharging is parallel.
9. Bee Pollen continuous drier according to any one of claim 1 to 8, which is characterized in that the heat pump removes
Wet heating structure includes the evaporator, wind turbine and condenser being sequentially communicated, wherein the air inlet of the evaporator passes through first
Pipeline is connected with the lower chamber, and the gas outlet of the condenser is connected by second pipe with the upper layer chamber.
10. Bee Pollen continuous drier according to claim 1, which is characterized in that the continuous drying dress of Bee Pollen
Set further includes vacuum pump and gas bomb, wherein the internal chamber phase that the vacuum pump passes through first pressure pipeline and the babinet
Connection, the gas bomb are connected by second pressure pipeline with the internal chamber of the babinet.
11. Bee Pollen continuous drier according to claim 1, which is characterized in that the continuous drying dress of Bee Pollen
It further includes the raw material cabin being arranged on the babinet to set, and the raw material cabin includes that lower end is embedded in the Bee Pollen feed inlet
Storehouse ontology, the first opening is configured in the upper end of the storehouse ontology, and the second opening is configured in the lower end of the storehouse ontology,
In, the lower end of the storehouse ontology is configured to interior receipts structure.
12. Bee Pollen continuous drier according to claim 11, which is characterized in that set in the upper end of the storehouse ontology
There is the lid that can be covered and close first opening, transparent observing area is configured in the middle section of the lid.
13. Bee Pollen continuous drier according to claim 11, which is characterized in that in the top of first opening
Edge is configured with annular groove, and sealing strip is embedded in the annular groove.
14. Bee Pollen continuous drier according to claim 11, which is characterized in that on the interior inclined-plane for receiving structure
On be configured with downward opening regulating tank, in the regulating tank be equipped with can along the length direction of the regulating tank carry out up and down
The striker plate of sliding.
15. Bee Pollen continuous drier according to claim 14, which is characterized in that be equipped with energy on the regulating tank
Enough fix the fastener of the striker plate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820254273.2U CN207963423U (en) | 2018-02-12 | 2018-02-12 | A kind of Bee Pollen continuous drier |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201820254273.2U CN207963423U (en) | 2018-02-12 | 2018-02-12 | A kind of Bee Pollen continuous drier |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2019153609A1 (en) * | 2018-02-12 | 2019-08-15 | 中国农业科学院蜜蜂研究所 | Continuous drying device for bee pollen and drying method therefor |
| CN112113407A (en) * | 2020-09-02 | 2020-12-22 | 李永 | Fodder drying equipment |
-
2018
- 2018-02-12 CN CN201820254273.2U patent/CN207963423U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2019153609A1 (en) * | 2018-02-12 | 2019-08-15 | 中国农业科学院蜜蜂研究所 | Continuous drying device for bee pollen and drying method therefor |
| US11248842B2 (en) | 2018-02-12 | 2022-02-15 | Institute Of Apicultural Research Chinese Academy Of Agricultural Sciences | Continuous drying apparatus for bee pollen and related drying method |
| CN112113407A (en) * | 2020-09-02 | 2020-12-22 | 李永 | Fodder drying equipment |
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