CN109297285A - A kind of cloth wind structure of low temperature eddy flow turntable material desiccation machine - Google Patents
A kind of cloth wind structure of low temperature eddy flow turntable material desiccation machine Download PDFInfo
- Publication number
- CN109297285A CN109297285A CN201811298947.XA CN201811298947A CN109297285A CN 109297285 A CN109297285 A CN 109297285A CN 201811298947 A CN201811298947 A CN 201811298947A CN 109297285 A CN109297285 A CN 109297285A
- Authority
- CN
- China
- Prior art keywords
- charging tray
- cloth
- desiccation
- wind
- big
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
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
- F26B11/18—Machines or apparatus for drying solid materials or objects with movement which is non-progressive on or in moving dishes, trays, pans, or other mainly-open receptacles
-
- 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
- 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
- F26B25/14—Chambers, containers, receptacles of simple construction
- F26B25/18—Chambers, containers, receptacles of simple construction mainly open, e.g. dish, tray, pan, rack
Abstract
A kind of cloth wind structure of low temperature eddy flow turntable material desiccation machine, including desiccation room and heat pump, it is staggered big charging tray and small charging tray in desiccation room along central axis, big charging tray and small charging tray and central axis rotate synchronously, it is characterized by: cloth solar or lunar halo is respectively set in the position above corresponding big charging tray and small charging tray on the inner wall of desiccation room；Cloth solar or lunar halo is connected to the air outlet of heat pump；Air distribution mechanism is set on cloth solar or lunar halo, downward cloth air port is set on air distribution mechanism.Hot wind directly purges wet stock via wind-distributing pipe by the indoor cloth solar or lunar halo of desiccation, and the demand control of accurate hot wind air quantity and wind speed can be carried out according to humidity；Hot wind enters between next group of big charging tray and small charging tray after carrying out heat exchange with this layer of wet stock, then from the gap location of the through hole of big charging tray or small charging tray and desiccation room side wall.
Description
Technical field
The present invention relates to low-temperature material desiccation field, specially a kind of cloth wind knot of low temperature eddy flow turntable material desiccation machine
Structure.
Background technique
Need the scene of hot-air seasoning more and more currently on the market, such as tobacco drying, grain heat-drying, medicinal material drying, fruit
The processing flows such as vegetable drying, the minimizing of the wastes such as sludge and innocent treatment procedure etc..Material desiccation machine is drying operation
Capital equipment, and the hot air circulating system in desiccation machine then be improve drying efficiency, it is energy saving, guarantee product quality pass
Key.
In existing drying technique, at this stage through the method frequently with low temperature desiccation, low temperature desiccation has generallyd use " box net
Band machine " carries out, main by the way of overall cloth wind or even distributing wind, but generally existing following in actual production process
The problem of:
1, production efficiency is low: since material is laid on mesh belt in desiccation room, hot wind can only dried material surface, in order to
Guarantee desiccation effect, needs that material internal moisture is waited to migrate to surface, process is slow, and the production cycle of drying process is caused to prolong
It is long, production efficiency is reduced, and deleterious effect is also generated to desiccation quality and cost.
2, energy consumption is big: the indoor hot wind wind direction of desiccation is single and fixed, is unfavorable for surface of material and comes into full contact with hot wind
To distribute moisture, desiccation effect is poor, and heat utilization efficiency is low, in order to guarantee desiccation effect, needs to increase hot wind air quantity, leads to the energy
Consumption is big.
For this reason, it may be necessary to develop a kind of cloth wind structure of novel low temperature desiccation machine, subtract on the basis of improving drying efficiency
Few energy consumption.
Summary of the invention
In view of this, the object of the present invention is to provide a kind of cloth wind structures of low temperature eddy flow turntable material desiccation machine, by being directed to
The subregion of material turntable accurately purges hot run test and to the closed-type double action crank press circulation pattern recycled in reheating, can both make vertical turn
The wind speed and air quantity of hot wind in disk meet different needs, and can make full use of the waste heat of hot run test, reduce energy consumption, improve
The thermal efficiency, entire cloth wind system design is simple, with strong points, energy-efficient.
The invention is realized by the following technical scheme:
A kind of cloth wind structure of low temperature eddy flow turntable material desiccation machine, including desiccation room and heat pump, in the desiccation room edge
Central axis is staggered big charging tray and small charging tray, and the big charging tray and small charging tray and the central axis rotate synchronously, and feature exists
In: on the inner wall of the desiccation room, cloth solar or lunar halo is respectively set in the position above corresponding big charging tray and small charging tray；The cloth solar or lunar halo
It is connected to the air outlet of the heat pump；Air distribution mechanism is set on the cloth solar or lunar halo, downward cloth wind is set on the air distribution mechanism
Mouthful；Desiccation room air outlet is arranged in the top of the desiccation room, and desiccation room air outlet is connected to the heat pump by backwind tube
Air intake vent.
Through-hole is arranged in the aniseed disk center, and the internal diameter of the through-hole is greater than the outer diameter of the central axis, the small charging tray
Outer rim and the cylinder inner wall between have gap；The hot wind exported by the wind-distributing pipe is on the big charging tray and small charging tray
Wet stock directly purged, the hot wind of lower layer's charging tray via between the gap, small charging tray and big charging tray, the through-hole shape
At access enter upper layer charging tray, hot wind eddy flow from bottom to top is formed in the desiccation room.
The central axis is located at the wind loop of the setting of the position above through-hole annular, and the inner wall of the desiccation room is located at described
The wind deflector of position setting annular above aniseed plate edge.
The air distribution mechanism is wind-distributing pipe or distributing wind disc.
The first rake arms is arranged in the top of the big charging tray, and the second rake arms, first rake is arranged in the top of the small charging tray
One end of arm and second rake arms is fixed on the inner wall of the cylinder；Buck rake tooth in being arranged in first rake arms, it is described
Setting extends out rake teeth, the interior buck rake tooth and the thin slice for extending out rake teeth and being vertically arranged, interior buck rake tooth in second rake arms
Thrust face towards the central axis；The thrust face of rake teeth is extended out towards the inner wall of the cylinder.
First rake arms, the second rake arms are hollow structure, and first rake arms is connected to big charging tray cloth solar or lunar halo, described the
Two rake arms are connected to small charging tray cloth solar or lunar halo；First rake arms towards at big charging tray and second rake arms towards small charging tray at
It is respectively provided with cloth air port.
The reheating backwind tube that setting is connected to the air intake vent of heat pump reheater in the middle part of the desiccation room, the reheating backwind tube
Above charging tray is top charging tray, and reheating backwind tube charging tray below is lower part charging tray；The air outlet of the heat pump reheater is logical
It crosses reheating air-supply assembly and is passed through top charging tray region.
The reheating air-supply assembly include the desiccation room inner wall on correspond to and be arranged on position above each top charging tray
Reheating cloth solar or lunar halo, reheating air distribution mechanism is set on the reheating cloth solar or lunar halo；The reheating air distribution mechanism passes through reheating cloth solar or lunar halo
It is connected to the air outlet of the heat pump reheater.
The main air supply tube of reheating, the main air supply tube of reheating and the heat are set above first layer charging tray in the desiccation room
Pump the air outlet connection of reheater.
The heat pump is dehumidifying heat pump；Fan is arranged in desiccation room inside top.
The advantages and benefits of the present invention are:
The present invention is due to being arranged big charging tray cloth solar or lunar halo along desiccation chamber interior walls in the top of big charging tray, on the top edge of small charging tray
Small charging tray cloth solar or lunar halo is arranged in desiccation chamber interior walls, and big charging tray cloth solar or lunar halo and small charging tray cloth solar or lunar halo are connected to the air outlet of heat pump respectively,
Wind-distributing pipe is all set on the cloth solar or lunar halo of every grade of charging tray, and hot wind is passed through by the indoor big charging tray cloth solar or lunar halo of desiccation and small charging tray cloth solar or lunar halo
Wet stock is directly purged by wind-distributing pipe, the demand control of accurate hot wind air quantity and wind speed can be carried out according to humidity；Heat
Wind is after carrying out heat exchange with this layer of wet stock, then from the through hole of big charging tray or the gap location of small charging tray and desiccation room side wall
Into between next group of big charging tray and small charging tray.
While Flow of Goods and Materials of the present invention, hot wind and this layer of wet stock that lower layer's charging tray wind-distributing pipe is passed through carry out heat exchange
Afterwards, waste heat via between gap, small charging tray and the big charging tray between small charging tray and desiccation room, the through-hole of big charging tray formed access
Into upper layer charging tray, working gas eddy flow from bottom to up is formed in desiccation room, the material desiccation on the charging tray of upper layer can be step by step
Using the waste heat of the working gas after lower layer's dried material, gas cyclone can sufficiently take away the steam of Sludge Surface, this structure
Both the contact area for having increased wet stock Yu xeothermic working gas in turn ensures wet stock drying time, so that wet stock and work
It is come into full contact with as gas, strengthens the heat transfer between xeothermic working gas and wet stock, improved the thermal efficiency, reduce simultaneously
Hot wind air quantity, has saved the energy, reduces desiccation cost.
The reheating backwind tube being connected to the air intake vent of heat pump reheater, reheating backwind tube is arranged in the present invention in the middle part of desiccation room
Above charging tray is top charging tray, and reheating backwind tube charging tray below is lower part charging tray；The air outlet of heat pump reheater is by again
Hot air-supply assembly is passed through top charging tray region.Top charging tray is passed through the reheating working gas by reheat loop heating to top
Wet feed purged, the problem too low into the working gas temperature of top charging tray is compensated with this.
Detailed description of the invention
Fig. 1 a, Fig. 1 b are overall structure and hot blast flow direction schematic diagram of the invention
Fig. 2 a, Fig. 2 b are wind-distributing pipe structural schematic diagrams on big charging tray of the invention
Fig. 3 a, Fig. 3 b are wind-distributing pipe structural schematic diagrams on small charging tray of the invention
Wherein:
1- desiccation room, 2- heat pump, 3- pressure fan, 4- air supply tube, 5- aid distributing pipe, 6- backwind tube, the big charging tray of 7-, 8- keep out the wind
The big charging tray cloth solar or lunar halo of the small charging tray of plate, 9-, 10-, the big charging tray wind-distributing pipe of 11-, 12- big charging tray cloth air port, 13- wind loop, 14- wind
Fan, the small charging tray cloth solar or lunar halo of 15-, the small charging tray wind-distributing pipe of 16-, 17- small charging tray cloth air port, 18- desiccation room air outlet, 19- reheating are returned
Air hose, the main air supply tube of 20- reheating, the main air outlet of 21- reheating, 22- reheating air supply tube, the first rake arms of 23-, buck rake tooth, 25- in 24
Second rake arms, 26- extend out rake teeth, 27- central axis, 29- wet feed entrance, 30- drier outlet, 31- through-hole, 32- heat pump reheater,
33- reheating cloth solar or lunar halo, 34- reheating wind-distributing pipe, 35- reheating cloth air port.
Specific embodiment
Below by specific embodiment, the invention will be further described, and it is not limit that following embodiment, which is descriptive,
Qualitatively, this does not limit the scope of protection of the present invention.
The principle of the present invention are as follows: be staggered big charging tray and small charging tray in desiccation room along central axis, the top of big charging tray exists
Big charging tray cloth solar or lunar halo is arranged in desiccation chamber interior walls, and small charging tray cloth solar or lunar halo, big charging tray is arranged along desiccation chamber interior walls in the top of small charging tray
Cloth solar or lunar halo and small charging tray cloth solar or lunar halo are connected to the air outlet of heat pump respectively, there is corresponding wind-distributing pipe on every grade of charging tray.By cloth wind
The hot wind of pipe output directly purges the wet stock on charging tray, the hot wind that lower layer's charging tray wind-distributing pipe is passed through and this layer of wet stock
Carry out heat exchange after, waste heat via between gap, small charging tray and the big charging tray between small charging tray and desiccation room, the through-hole of big charging tray
The access of formation enters upper layer charging tray, and hot wind eddy flow from bottom to top is formed in desiccation room.
Embodiment 1:
As shown in Figure 1a, material desiccation machine of the invention includes desiccation room 1, heat pump 2, pressure fan 3, air supply tube 4, aid distributing pipe
5 and backwind tube 6, wherein desiccation room 1 is divided by big charging tray 7 and small charging tray 9 for multilayered structure, and the top of big charging tray 7 is along desiccation room 1
Big charging tray cloth solar or lunar halo 10 is arranged in inner wall, and small charging tray cloth solar or lunar halo 15, big charging tray cloth is arranged along 1 inner wall of desiccation room in the top of small charging tray 9
Solar or lunar halo 10 and small charging tray cloth solar or lunar halo 15 are connected to the air outlet of heat pump 2 by air supply tube 4 and aid distributing pipe 5 respectively.Big charging tray cloth wind
The big charging tray wind-distributing pipe 11 stretched out into desiccation room 1 is uniformly distributed on circle 10, big charging tray wind-distributing pipe 11 is towards setting at big charging tray 7
Big charging tray cloth air port 12.The small charging tray wind-distributing pipe 16 stretched out into desiccation room 1, small charging tray are uniformly distributed on small charging tray cloth solar or lunar halo 15
Wind-distributing pipe 16 is towards setting small charging tray cloth air port 17 at small charging tray 9.The desiccation room air outlet 18 at 1 top of desiccation room passes through backwind tube
The air intake vent of 6 connection heat pumps 2.The wind-distributing pipe of every layered material disk is 4~12.
Desiccation room 1 of the invention is vertical vortex turntable desiccation room, inside setting central axis 27, big charging tray 7 and small charging tray
9.Central axis 27 is vertically arranged in desiccation room 1, and the big charging tray of multiple groups is arranged in the radial direction interval on central axis 27 along desiccation room 1
7 and small charging tray 9.Central axis 27 drives rotation, big charging tray 7 and small charging tray 9 and 27 synchronous rotary of central axis by a driving motor.
The sum of big charging tray 7 and small charging tray 9 is odd number in the present embodiment, i.e. first layer is big charging tray 7, and the last layer is also big charging tray 7.
Wet feed entrance 29 is set at the top of desiccation room 1, and drier outlet 30 is arranged in bottom.
As shown in Figure 2 a, big charging tray 7 is hollow ring, and through-hole 31 is arranged in center, and the internal diameter of through-hole 31 is greater than central axis 27
Outer diameter, move down convenient for material and connect with central axis 27 with air-flow uplink, big charging tray 7 by bracket, big 7 outer edge of charging tray with do
Change 1 inner wall of room is close but does not contact.As shown in Figure 3a, small charging tray 9 is connect with central axis 27 by mounting hole, the internal diameter of mounting hole
It is fitted close with the outer diameter of central axis 27, has a fixed gap between 1 inner wall of outer rim and desiccation room of small charging tray 9, convenient under material
It moves and air-flow uplink.
To guarantee air-flow according to scheduled gas circuit uplink, the present embodiment is preferably on the central axis 27 above each through-hole 31
The wind loop 13 of annular is set, the hot wind downlink being passed through at big charging tray cloth air port 12 is prevented.In big charging tray 7 and 1 inner wall of desiccation room
Between gap above setting annular wind deflector 8, prevent the hot wind downlink being passed through at big charging tray cloth air port 12.
As shown in Fig. 2 b, Fig. 3 b, the first rake arms 23 is set above big charging tray 7, the second rake arms 25 is set above small charging tray 9,
One end of first rake arms 23 and the second rake arms 25 is connected on the inner wall of desiccation room 1, and the other end is free end.In first rake arms 23
Interior buck rake tooth 24 is set, and setting extends out rake teeth 26 in the second rake arms 25.The present embodiment preferably in buck rake tooth 24 and extend out rake teeth 26
The thin slice being vertically arranged, to i.e. thrust face is towards central axis 27 in interior 24 angle of buck rake tooth；It extends out outside 26 angle of rake teeth
To i.e. thrust face is towards 1 inner wall of desiccation room.
The desiccation room 1 of the present embodiment is vertical cylinder, and central axis 27 penetrates through desiccation room 1 from bottom to top, big charging tray 7 and small
Charging tray 9 is the circle that diameter does not wait；Driving motor is connected to the lower part of central axis 27, and fixes with the bottom of desiccation room 1.According to
To the desiccation demand of wet feed, revolving speed appropriate is arranged to driving motor, while the big of different groups of numbers can be set on central axis 27
Charging tray 7 and small charging tray 9.9 groups of numbers of big charging tray 7 and small charging tray in usual desiccation room 1 are 1~10 group, preferably 2~5 groups.
Driving motor reduces the revolving speed of central axis 27 by deceleration device, can adjust stop of the wet stock in desiccation room 1
It time, can also be according to the hot wind air quantity and wind speed that the humidity of wet stock accurately controls.In addition, the first rake arms 23, the second rake arms 25
Quantity and interior buck rake tooth 24 extend out that rake teeth 26 is in varying numbers, and residence time of the wet stock on each charging tray is adjusted.Therefore,
The cloth wind structure of low temperature eddy flow turntable material desiccation machine of the invention can run without interruption, and improve the drying efficiency of system.
The working principle of the present embodiment:
When in use, desiccation room 1 passes through bracket-suspending to the cloth wind structure of low temperature eddy flow turntable material desiccation machine of the invention
Setting opens driving motor and central axis 27 is driven to rotate, and the big charging tray 7 and small charging tray 9 being mounted on central axis 27 rotate synchronously.
Wet stock is added on the big charging tray 7 of 1 top layer of desiccation room by 29 uniformly continuous of wet feed entrance, and the first of big 7 corresponding position of charging tray
Interior buck rake tooth 24 in rake arms 23 is constantly dispersed, is struck off, is stirred, sheared and is crushed to the wet mud fallen on big charging tray 7,
It is heated evenly, while inwardly wet stock being pushed to transfer toward under at through-hole 31.The wet stock converged at through-hole 31 passes through through-hole 31
Small 9 middle part of charging tray of next layer is fallen into, wet stock is moved out by the rake teeth 26 that extends out in the second rake arms 25 of small 9 corresponding position of charging tray
It send, when wet stock crosses the outer rim of small charging tray 9, and falls on the big charging tray 7 of next layer.And so on, wet stock is gradually layer by layer
The hot wind cyclone drying for being transplanted on bottom charging tray, while being dried in room 1, the material after drying are exported by drier outlet 30.
In addition to the flowing of above-mentioned material, the invention also includes the airflow circulatings between desiccation room 1 and heat pump 2.Heat pump 2 be except
Damp and hot pump is provided simultaneously with and the cold wet working gas that the desiccation room air outlet 18 from 1 top of desiccation room recycles is dehumidified and added
The function of heat sends desiccation room back to after individually can also carrying out reheating to 1 inner air of desiccation room, makes working gas in desiccation room 1- heat
The closed loop cycle of the cold wet working gas of xeothermic working gas-is formed between pump 2.The xeothermic working gas that heat pump 2 generates is via sending
Air hose 4, big charging tray cloth solar or lunar halo 10, small charging tray cloth solar or lunar halo 15 are sent into desiccation room 1, then by big charging tray wind-distributing pipe 11 and small charging tray cloth
16 short distance of air hose purges the wet stock flowed between each layered material disk and charging tray, takes away the moisture on wet stock surface.
Since there is larger-diameter through-hole 31 at the center of big charging tray 7, and it is smaller with 1 inner wall spacing of desiccation room, and small charging tray 9
Inner edge is directly anchored on central axis 27, and working gas can not circulate, and can only pass through the outer rim and 1 inner wall of desiccation room of small charging tray 9
Between relatively books circulation.Thus the working gas of the purged wet stock of lower layer can only flow into aniseed by the through-hole 31 of big charging tray 7
It on disk 7, is flowed on small charging tray 9 by the gap of small charging tray 9 and 1 inner wall of desiccation room, so that it is upward to form rotation in desiccation room 1
Working gas eddy flow.
In this way, working gas is entrainment of steam, Corvolutional interleaving in layer from bottom to top, finally by desiccation room air outlet 18
Discharge, is step by step adequately taken away the steam in wet stock on each layered material disk using the heat of xeothermic working gas, to solve
The undesirable problem of box mesh belt machine desiccation effect.
Embodiment 2:
As shown in Figure 1 b, the present embodiment the difference from embodiment 1 is that, the charging tray arranged step by step in desiccation room 1 is divided into
Top charging tray and lower part charging tray, top charging tray, which is passed through, blows the wet feed on top by the reheating working gas of reheat loop heating
It sweeps, with this problem too low come the gas temperature for compensating top charging tray.Specifically include heat pump reheater 32, reheating backwind tube 19,
Reheating air supply tube 22, reheating cloth solar or lunar halo 33, reheating wind-distributing pipe 34, reheating cloth air port 35.Wherein heat pump reheater 32 can integrate
In heat pump 2, can also be independently of heat pump 2 except, the air intake vent of reheating backwind tube 19 is arranged in top charging tray and lower part charging tray
Between, air outlet connects the air intake vent of heat pump reheater 32.
The air outlet of one end connection heat pump reheater 32 of reheating air supply tube 22, it is corresponding that the other end connects each top charging tray
Reheating cloth solar or lunar halo 33 is uniformly distributed the reheating wind-distributing pipe 34 stretched out into each top charging tray, reheating cloth wind on reheating cloth solar or lunar halo 33
Pipe 34 is towards setting reheating cloth air port 35 at each top charging tray.
The main air supply tube 20 of reheating can be also arranged in the present embodiment above first layer charging tray, by the main air supply tube 20 of reheating towards
Reheating main air outlet 21 is set at first layer charging tray, to carry out to the wet stock entered on first layer charging tray by wet feed entrance 29
Concentrate purging.
Embodiment 3:
The difference of the present embodiment and Examples 1 and 2 is, between the first rake arms 23 and interior buck rake tooth 24, the second rake arms 25
Can be relatively movable between rake teeth 26 with extending out, i.e., rake teeth is socketed in rake arms, and it is not stuck, it can freely swing along rake arms, phase
Rake teeth angle on adjacent two layers of charging tray is opposite.
Meanwhile first rake arms 23, the second rake arms 25 are hollow structure, the first rake arms 23, the second rake arms 25 respectively with aniseed
Disk cloth solar or lunar halo 10 and the connection of small charging tray cloth solar or lunar halo 15, the first rake arms 23 is towards setting big charging tray cloth air port 12, second at big charging tray 7
Rake arms 25 is towards setting small charging tray cloth air port 17 at small charging tray 9.
The present embodiment is preferred, 0.5~15 meter of 1 diameter of desiccation room, and 1 height of desiccation room is 1~20 meter.
Fan 14 is arranged in the present embodiment at the top of desiccation room 1, increases the gas cyclone speed and strength in desiccation room 1, wind
The quantity of fan 14 is preferably 4-8.
The present invention can be used for sludge drying, it may also be used for the particle or block of the industries such as grain, feed, medicine, chemical industry
The desiccation of material.Although disclosing the embodiment of the present invention and attached drawing for the purpose of illustration, those skilled in the art can be managed
Solution: do not departing from the present invention and spirit and scope of the appended claims in, various substitutions, changes and modifications be all it is possible,
Therefore, the scope of the present invention is not limited to the embodiment and attached drawing disclosure of that.
Claims (10)
1. a kind of cloth wind structure of low temperature eddy flow turntable material desiccation machine, including desiccation room and heat pump, in the desiccation room in
Mandrel is staggered big charging tray and small charging tray, and the big charging tray and small charging tray and the central axis rotate synchronously, it is characterised in that:
On the inner wall of the desiccation room, cloth solar or lunar halo is respectively set in the position above corresponding big charging tray and small charging tray；The cloth solar or lunar halo with
The air outlet of the heat pump is connected to；Air distribution mechanism is set on the cloth solar or lunar halo, downward cloth air port is set on the air distribution mechanism；
Desiccation room air outlet is arranged in the top of the desiccation room, and desiccation room air outlet is connected to the inlet air of the heat pump by backwind tube
Mouthful.
2. a kind of cloth wind structure of low temperature eddy flow turntable material desiccation machine as described in claim 1, it is characterised in that: described big
Through-hole is arranged in charging tray center, and the internal diameter of the through-hole is greater than the outer diameter of the central axis, the outer rim of the small charging tray and the cylinder
There is gap between the inner wall of body；The hot wind exported by the wind-distributing pipe carries out the wet stock on the big charging tray and small charging tray straight
Connect purging, the hot wind of lower layer's charging tray via between the gap, small charging tray and big charging tray, the access that the through-hole is formed enter it is upper
Layered material disk forms hot wind eddy flow from bottom to top in the desiccation room.
3. a kind of cloth wind structure of low temperature eddy flow turntable material desiccation machine as claimed in claim 2, it is characterised in that: in described
Mandrel is located at the wind loop of the setting of the position above through-hole annular, and the inner wall of the desiccation room is located above the aniseed plate edge
Position setting annular wind deflector.
4. a kind of cloth wind structure of low temperature eddy flow turntable material desiccation machine as described in claim 1, it is characterised in that: the cloth
Blower structure is wind-distributing pipe or distributing wind disc.
5. a kind of cloth wind structure of low temperature eddy flow turntable material desiccation machine as claimed in claim 1 or 2 or 3 or 4, feature exist
In: the first rake arms is arranged in the top of the big charging tray, and the second rake arms, first rake arms and institute is arranged in the top of the small charging tray
The one end for stating the second rake arms is fixed on the inner wall of the cylinder；Buck rake tooth in being arranged in first rake arms, second rake
Setting extends out rake teeth, the interior buck rake tooth and the thin slice for extending out rake teeth and being vertically arranged, the thrust of interior buck rake tooth on arm
Facing towards the central axis；The thrust face of rake teeth is extended out towards the inner wall of the cylinder.
6. a kind of cloth wind structure of low temperature eddy flow turntable material desiccation machine as claimed in claim 5, it is characterised in that: described the
One rake arms, the second rake arms are hollow structure, and first rake arms is connected to big charging tray cloth solar or lunar halo, second rake arms and small charging tray
The connection of cloth solar or lunar halo；First rake arms is towards at big charging tray and second rake arms is towards being respectively provided with cloth air port at small charging tray.
7. a kind of cloth wind structure of low temperature eddy flow turntable material desiccation machine as claimed in claim 1 or 2 or 3 or 4, feature exist
More than setting is connected to the air intake vent of heat pump reheater in the middle part of the desiccation room reheating backwind tube, the reheating backwind tube
Charging tray be top charging tray, reheating backwind tube charging tray below be lower part charging tray；The air outlet of the heat pump reheater is by again
Hot air-supply assembly is passed through top charging tray region.
8. a kind of cloth wind structure of low temperature eddy flow turntable material desiccation machine as claimed in claim 7, it is characterised in that: it is described again
Hot air-supply assembly include the desiccation room inner wall on correspond to the reheating cloth solar or lunar halo being arranged on position above each top charging tray, institute
State setting reheating air distribution mechanism on reheating cloth solar or lunar halo；The reheating air distribution mechanism passes through reheating cloth solar or lunar halo and the heat pump reheater
Air outlet connection.
9. a kind of cloth wind structure of low temperature eddy flow turntable material desiccation machine as claimed in claim 8, it is characterised in that: described
The main air supply tube of reheating, the outlet air of the main air supply tube of reheating and the heat pump reheater are set above first layer charging tray in desiccation room
Mouth connection.
10. a kind of cloth wind knot of low temperature eddy flow turntable material desiccation machine as described in claims 1 or 2 or 3 or 4 or 6 or 8 or 9
Structure, it is characterised in that: the heat pump is dehumidifying heat pump, and fan is arranged in desiccation room inside top.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811298947.XA CN109297285A (en) | 2018-11-01 | 2018-11-01 | A kind of cloth wind structure of low temperature eddy flow turntable material desiccation machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811298947.XA CN109297285A (en) | 2018-11-01 | 2018-11-01 | A kind of cloth wind structure of low temperature eddy flow turntable material desiccation machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN109297285A true CN109297285A (en) | 2019-02-01 |
Family
ID=65145455
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811298947.XA Pending CN109297285A (en) | 2018-11-01 | 2018-11-01 | A kind of cloth wind structure of low temperature eddy flow turntable material desiccation machine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109297285A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113716834A (en) * | 2020-12-22 | 2021-11-30 | 吴植仁 | Wet sludge low-temperature air dryer |
| CN115466032A (en) * | 2022-09-29 | 2022-12-13 | 杨冬林 | Wastewater treatment sludge ventilation drying system and ventilation drying method |
Citations (20)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB618564A (en) * | 1946-11-05 | 1949-02-23 | Boulton Ltd William | Improvements in and relating to the drying of pottery ware and similar goods |
| DE4306757A1 (en) * | 1993-03-04 | 1995-02-02 | Chema Balcke Duerr Verfahrenst | Rotary thin-film dryer |
| CN2247319Y (en) * | 1995-11-24 | 1997-02-12 | 昆明化肥厂 | Turbulent type multi-layer disc drien |
| CN101210682A (en) * | 2006-12-29 | 2008-07-02 | 游钧杰 | Combustion furnace ash treatment device |
| CN202254699U (en) * | 2011-08-06 | 2012-05-30 | 王贵孝 | Novel disc dryer |
| CN203068923U (en) * | 2012-11-30 | 2013-07-17 | 北京通际同创燃烧技术有限公司 | Steelmaking alloy and auxiliary material drying system |
| CN204466859U (en) * | 2015-02-13 | 2015-07-15 | 陕西科技大学 | A kind of hot blast vacuum combination drying box |
| CN204574739U (en) * | 2015-04-03 | 2015-08-19 | 厦门市富桥机械有限公司 | A kind of multiple-layer airing machine |
| CN205002541U (en) * | 2015-10-09 | 2016-01-27 | 信丰县绿源人造板有限公司 | Even drying device of former billet of reel |
| CN106152711A (en) * | 2015-04-16 | 2016-11-23 | 中国科学院理化技术研究所 | A kind of tower type drying system and drying means thereof |
| TW201707762A (en) * | 2015-08-27 | 2017-03-01 | hong-xin Lai | Nitrogen drying method and drying device under normal temperature and normal pressure for providing benefits of wider application range and energy saving |
| CN206094809U (en) * | 2016-08-25 | 2017-04-12 | 宿迁市万和泰化工有限公司 | Tray dryer |
| CN206352952U (en) * | 2017-01-05 | 2017-07-25 | 天津市鑫霞烘干设备制造有限公司 | A kind of device for drying traditional Chinese medicinal materials |
| CN107101485A (en) * | 2017-05-06 | 2017-08-29 | 姚旺东 | The three-dimensional drying unit of multi-layer discs is fixed with a kind of cylinder |
| CN206504586U (en) * | 2017-01-20 | 2017-09-19 | 中国科学院理化技术研究所 | A kind of foodstuff adustion system |
| CN107270692A (en) * | 2017-07-18 | 2017-10-20 | 杨正清 | A kind of tray dryer machine |
| CN107300302A (en) * | 2017-06-27 | 2017-10-27 | 合肥朝霞机械科技有限公司 | A kind of novel foodstuff dryer and its application method |
| CN207317375U (en) * | 2017-09-19 | 2018-05-04 | 常州市震华干燥设备有限公司 | Boiling drier |
| CN108020051A (en) * | 2017-12-01 | 2018-05-11 | 陈传材 | A kind of Chinese medicine automatic processing apparatus |
| CN209783204U (en) * | 2018-11-01 | 2019-12-13 | 北京水木益华环保科技有限公司 | Air distribution structure of low-temperature rotational flow rotary disc material drying machine |
-
2018
- 2018-11-01 CN CN201811298947.XA patent/CN109297285A/en active Pending
Patent Citations (20)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB618564A (en) * | 1946-11-05 | 1949-02-23 | Boulton Ltd William | Improvements in and relating to the drying of pottery ware and similar goods |
| DE4306757A1 (en) * | 1993-03-04 | 1995-02-02 | Chema Balcke Duerr Verfahrenst | Rotary thin-film dryer |
| CN2247319Y (en) * | 1995-11-24 | 1997-02-12 | 昆明化肥厂 | Turbulent type multi-layer disc drien |
| CN101210682A (en) * | 2006-12-29 | 2008-07-02 | 游钧杰 | Combustion furnace ash treatment device |
| CN202254699U (en) * | 2011-08-06 | 2012-05-30 | 王贵孝 | Novel disc dryer |
| CN203068923U (en) * | 2012-11-30 | 2013-07-17 | 北京通际同创燃烧技术有限公司 | Steelmaking alloy and auxiliary material drying system |
| CN204466859U (en) * | 2015-02-13 | 2015-07-15 | 陕西科技大学 | A kind of hot blast vacuum combination drying box |
| CN204574739U (en) * | 2015-04-03 | 2015-08-19 | 厦门市富桥机械有限公司 | A kind of multiple-layer airing machine |
| CN106152711A (en) * | 2015-04-16 | 2016-11-23 | 中国科学院理化技术研究所 | A kind of tower type drying system and drying means thereof |
| TW201707762A (en) * | 2015-08-27 | 2017-03-01 | hong-xin Lai | Nitrogen drying method and drying device under normal temperature and normal pressure for providing benefits of wider application range and energy saving |
| CN205002541U (en) * | 2015-10-09 | 2016-01-27 | 信丰县绿源人造板有限公司 | Even drying device of former billet of reel |
| CN206094809U (en) * | 2016-08-25 | 2017-04-12 | 宿迁市万和泰化工有限公司 | Tray dryer |
| CN206352952U (en) * | 2017-01-05 | 2017-07-25 | 天津市鑫霞烘干设备制造有限公司 | A kind of device for drying traditional Chinese medicinal materials |
| CN206504586U (en) * | 2017-01-20 | 2017-09-19 | 中国科学院理化技术研究所 | A kind of foodstuff adustion system |
| CN107101485A (en) * | 2017-05-06 | 2017-08-29 | 姚旺东 | The three-dimensional drying unit of multi-layer discs is fixed with a kind of cylinder |
| CN107300302A (en) * | 2017-06-27 | 2017-10-27 | 合肥朝霞机械科技有限公司 | A kind of novel foodstuff dryer and its application method |
| CN107270692A (en) * | 2017-07-18 | 2017-10-20 | 杨正清 | A kind of tray dryer machine |
| CN207317375U (en) * | 2017-09-19 | 2018-05-04 | 常州市震华干燥设备有限公司 | Boiling drier |
| CN108020051A (en) * | 2017-12-01 | 2018-05-11 | 陈传材 | A kind of Chinese medicine automatic processing apparatus |
| CN209783204U (en) * | 2018-11-01 | 2019-12-13 | 北京水木益华环保科技有限公司 | Air distribution structure of low-temperature rotational flow rotary disc material drying machine |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113716834A (en) * | 2020-12-22 | 2021-11-30 | 吴植仁 | Wet sludge low-temperature air dryer |
| CN115466032A (en) * | 2022-09-29 | 2022-12-13 | 杨冬林 | Wastewater treatment sludge ventilation drying system and ventilation drying method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN201571453U (en) | Drier for angular boxed food with variable cross section | |
| CN103673563A (en) | Rotary disk type air jet impact drying machine | |
| CN106403520A (en) | High-efficiency integrated through-flow type heat pump drying room | |
| CN109297285A (en) | A kind of cloth wind structure of low temperature eddy flow turntable material desiccation machine | |
| CN103925778A (en) | Drum drying machine | |
| CN113632833A (en) | Grain circulating dryer based on graphene far-infrared heating and drying method thereof | |
| CN206257933U (en) | Chain-and-slat drying machine | |
| CN109081548A (en) | A kind of low temperature eddy flow turntable material desiccation machine | |
| CN109269243B (en) | Multilayer partition drying device | |
| CN101053339B (en) | Composition heating type vegetable dewatering device | |
| CN2237824Y (en) | Electrothermic drier | |
| CN207214743U (en) | A kind of dryer for rice paddy seed processing | |
| CN209783204U (en) | Air distribution structure of low-temperature rotational flow rotary disc material drying machine | |
| CN101690607B (en) | Dehydrated vegetables continuous dryer | |
| CN108844324A (en) | A kind of drying machine of low clearance charging | |
| CN201108009Y (en) | Through-flow air supply assembly heating type vegetable press-pate machine | |
| CN112577293A (en) | Multilayer mesh belt formula tea-oil camellia seed drying device during layering accuse temperature accuse | |
| CN101176568A (en) | Heating type vegetable dewaterer combined with flow and air feed | |
| CN208434620U (en) | The drying system of heat pump room heated type Multilayer Network | |
| CN207123154U (en) | Conductive grain dryer | |
| CN206094828U (en) | Heat energy cyclic utilization's energy -conserving drying device of panel | |
| CN208635515U (en) | Recycling residual heat dryer | |
| CN207763418U (en) | A kind of crops circulation dryer convenient for safeguarding | |
| CN203672085U (en) | Rotation-vibration draining dryer | |
| CN111981788A (en) | Vertical dryer |
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 |