CN106403562A - Microwave drying system - Google Patents
Microwave drying system Download PDFInfo
- Publication number
- CN106403562A CN106403562A CN201610799948.7A CN201610799948A CN106403562A CN 106403562 A CN106403562 A CN 106403562A CN 201610799948 A CN201610799948 A CN 201610799948A CN 106403562 A CN106403562 A CN 106403562A
- Authority
- CN
- China
- Prior art keywords
- microwave
- drying
- speed
- dryer
- reduction
- 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
- F26B17/00—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement
- F26B17/02—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed by belts carrying the materials; with movement performed by belts or elements attached to endless belts or chains propelling the materials over stationary surfaces
- F26B17/04—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed by belts carrying the materials; with movement performed by belts or elements attached to endless belts or chains propelling the materials over stationary surfaces the belts being all horizontal or slightly inclined
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B23/00—Heating arrangements
- F26B23/04—Heating arrangements using electric heating
-
- 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
- F26B25/002—Handling, e.g. loading or unloading arrangements for bulk goods
-
- 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
- F26B25/005—Treatment of dryer exhaust gases
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B3/00—Drying solid materials or objects by processes involving the application of heat
- F26B3/32—Drying solid materials or objects by processes involving the application of heat by development of heat within the materials or objects to be dried, e.g. by fermentation or other microbiological action
- F26B3/34—Drying solid materials or objects by processes involving the application of heat by development of heat within the materials or objects to be dried, e.g. by fermentation or other microbiological action by using electrical effects
- F26B3/347—Electromagnetic heating, e.g. induction heating or heating using microwave energy
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B2200/00—Drying processes and machines for solid materials characterised by the specific requirements of the drying good
- F26B2200/08—Granular materials
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Microbiology (AREA)
- Health & Medical Sciences (AREA)
- Electromagnetism (AREA)
- Biomedical Technology (AREA)
- Biotechnology (AREA)
- Physics & Mathematics (AREA)
- Molecular Biology (AREA)
- Sustainable Development (AREA)
- Drying Of Solid Materials (AREA)
Abstract
The invention relates to the field of powder drying, in particular to a microwave drying system. The microwave drying system comprises a drying tunnel. The drying tunnel comprises an accelerating drying section, a constant-speed drying section and a decelerating drying section and further comprises a microwave drying device arranged along the drying tunnel. The microwave drying device is connected with a flue gas pipeline. A conveyer belt is arranged in the drying tunnel. The two ends of the conveyer belt are provided with a feeding device and a discharging device correspondingly. According to the microwave drying system, microwave directly irradiates the inner portion of powder, so that the heat loss of the microwave drying system is greatly lowered, and the energy utilization rate is improved; and meanwhile, lumpy coagula are not generated in the powder drying process, the drying efficiency is improved, and the drying time is shortened. When the microwave is used for drying the powder, a large amount of powder can be dried at the same time, the drying demand is met. The microwave drying process is easy to operate, intelligent and advanced in technology, the purposes of energy conservation and environment protection are also achieved through microwave drying, and the microwave drying system is environmentally friendly, clean, hygienic and free from pollution.
Description
Technical field
The present invention relates to powder drying field, in particular to a kind of microwave drying system.
Background technology
The drying process of powder body is a common technological process in Inorganic Non-metallic Materials experimentation, traditional at present
Drying meanss have：Natural seasoning, external heat source method, conductive drying method, endogenous pyrogen method, convective drying method etc..And it is traditional at present
Method all has certain defect to varying degrees, and such as prior art commonly uses convective drying to calcium carbonate powder granule
Method, is a kind of method granular solids material being dried with fluidization technology.In fluid bed, granule is dispersed in heat
In air-flow, stir up and down, mixing and collision mutually makes dry materials.Because the aqueous dose rate of calcium carbonate powder granular mass weight is high,
Fluidized bed drying process just can blow afloat with larger wind speed and be easier to lump, often formed false dry it is difficult to granulate.
Therefore, fluid bed drying energy resource consumption in dry run is big and low production efficiency.
And external heat source seasoning is so that the moisture in powder body is steamed by stronger external heat source by distributing higher heat
Send out, but because calcium carbonate powder granular mass water content is high, it is therefore desirable to the high evaporation for a long time of higher temperature just can make carbon
Sour calcium granule obtains drying.
Microwave drying is a kind of new drying mode.When being dried, microwave energy directly acts on medium molecule and is converted into heat
Energy.Make heating simultaneously inside and outside medium it is not necessary to conduction of heat because microwave has penetration performance, so firing rate is very fast, do
Dry taking greatly shortens.Material absorbs temperature after microwave energy changes into heat and raises, and the moisture that material includes is evaporated, dehydration
And drying.Because microwave drying is that material inside and outside is heated simultaneously, the internal-external temperature difference of material is little, homogeneous heating, thus without product
In raw conventional heating, scorched outside and underdone inside situation occurs, so that dry mass is greatly improved.If suitably controlling dewatering speed, right
The structure pine of material just can be allowed when material is dried thin, expanded.Compared to traditional drying mode, microwave drying is capable of thing
The pollution-free and uniform drying of material, can be greatly reduced baking temperature simultaneously, realize safety clean and produce.
But, because the microwave drying time is fast, effect is good, so grasping bad drying time and intensity to a certain extent
Material can be made agglomerating, not expanded and pine is dredged, and is unfavorable for the follow-up use of material.
Content of the invention
It is an object of the invention to provide a kind of microwave drying system, the drying of powder granule can be improved and keep powder body
The expanded and pine of grain is dredged.
The present invention is realized in：
A kind of microwave drying system, the microwave drier including drying alley with along drying alley setting.Microwave drying
Device is connected with flue, is provided with conveyer belt in drying alley.Conveyer belt two ends are respectively arranged with feeding device and discharging
Device, drying alley is disposed with acceleration dryer section, constant rate of drying section and fall from described feeding device to drawing mechanism direction
Fast dryer section.
Further, microwave drier includes drying device housing and microwave dryer, and microwave dryer is arranged on dry
In dry device case, drying device housing is connected with flue.
Further, microwave dryer includes accelerating microwave dryer, constant speed microwave dryer and reduction of speed microwave dryer.
Accelerate microwave dryer and be correspondingly arranged with accelerating dryer section, constant speed microwave dryer is correspondingly arranged with constant rate of drying section, and reduction of speed is micro-
Ripple exsiccator and deceleration drying section are correspondingly arranged.
Further, accelerate in microwave dryer, to be provided with the acceleration microwave energy generator being sequentially connected, accelerate microwave magnetic
Ferrum and accelerate Microwave emission end, is provided with the constant speed microwave energy generator being sequentially connected, constant speed micro- in constant speed microwave dryer
Ripple Magnet and constant speed Microwave emission end, are provided with the reduction of speed microwave energy generator being sequentially connected, fall in reduction of speed microwave dryer
Fast microwave Magnet and reduction of speed Microwave emission end.
Further, reduction of speed Microwave emission end, constant speed Microwave emission end and reduction of speed Microwave emission end respectively with vertical direction
Angle be 10 °～15 °, accelerate Microwave emission end, constant speed Microwave emission end and reduction of speed Microwave emission end respectively with conveyer belt it
Between angle be 75 °～80 °.
Further, feeding device includes loading hopper, and loading hopper is connected with described conveyer belt one end；Drawing mechanism bag
Include funnel, go out funnel and be connected with the conveyer belt other end.
Further, it is connected with flue gas between flue and housing to be in charge of；Flue gas be in charge of including accelerate flue gas be in charge of, etc.
Fast flue gas is in charge of and is in charge of with reduction of speed flue gas.
Further, accelerate flue gas to be in charge of to be connected with accelerating microwave dryer, constant speed flue gas is in charge of and constant speed microwave drying
Device connects, and reduction of speed flue gas is in charge of and is connected with reduction of speed microwave dryer.
Further, microwave drying system also includes controller, and controller includes microwave intensity actuator, and described microwave is strong
Degree actuator is connected with described microwave dryer.
Further, microwave intensity actuator includes accelerating microwave intensity actuator, constant speed microwave intensity actuator, reduction of speed
Microwave intensity actuator, conveyer belt transfer rate setting device, loading hopper switch, discharging funnel switch and battery main switch.Plus
Fast microwave intensity actuator electrically connects with accelerating microwave dryer, and constant speed microwave intensity actuator and constant speed microwave dryer are electrically connected
Connect, described reduction of speed microwave intensity actuator is electrically connected with reduction of speed microwave dryer, conveyer belt transfer rate arranges device and conveyer belt
Electrical connection, loading hopper switch is electrically connected with loading hopper, and discharging funnel switch electrically connects with going out funnel
The beneficial effect of such scheme：
The invention provides a kind of microwave drying system, its heat loss is made significantly to drop by inside microwave direct irradiation powder body
Low, improve energy utilization rate, do not produce block concretion during powder drying simultaneously, improve drying efficiency, shorten
Drying time.Using greater number of powder body can be dried during microwave drying powder body simultaneously, meet and demand, microwave drying flow process are dried
Operation simple intelligent, technique is advanced, has also reached the target of energy-conserving and environment-protective, environment-protecting clean health, no dirt using microwave drying
Dye, more will not produce " three wastes " problem, meet the requirement of sustainable development.It is suitable for experiment powder drying, industrial powder material is done
The aspect application such as dry.
The present invention has further the advantage that：
The present invention enables the hot gas producing in dry run timely and effectively to arrange by the installation of heat smoke passage
Go out, it is to avoid powder body heated gas are moist.
The present invention is provided by three kinds of microwave driers, is provided with three kinds of drying stages, makes to drive by conveyer belt
Powder body transmission three drying stages of experience realize the drying to powder body, can efficiently quickly finish powder drying technique.And
The drying operation of material can be made by the drying operation controlling the microwave intensity of drying stage to realize for different material
Optimize.
The present invention can make material by adjusting the drying operation that the transfer rate of conveyer belt is realized for different material
Drying operation optimization.
Brief description
In order to be illustrated more clearly that the technical scheme of the embodiment of the present invention, below will be attached to use required in embodiment
Figure is briefly described it will be appreciated that the following drawings illustrate only certain embodiments of the present invention, and it is right to be therefore not construed as
The restriction of scope, for those of ordinary skill in the art, on the premise of not paying creative work, can also be according to this
A little accompanying drawings obtain other related accompanying drawings.
Fig. 1 shows the first microwave drier and the conveyer structure graph of a relation of present invention offer；
The top view of the first microwave drying system that Fig. 2 provides for the present invention；
The side view of the first microwave drying system that Fig. 3 provides for the present invention；
Microwave dryer structural representation in the microwave drying system that Fig. 4 provides for the present invention；
The overall structure diagram of the second microwave drying system that Fig. 5 provides for the present invention.
Description of reference numerals：
Microwave drying system 100,100a；Drying alley 110；Microwave drier 120；Conveyer belt 130；Flue
140；Flue gas is in charge of 150；Feeding device 160；Drawing mechanism 170；Controller 180；Accelerate dryer section 111；Constant rate of drying section
112；Deceleration drying section 113；Drying device housing 121；Microwave dryer 122；Accelerate microwave dryer 123；Constant speed microwave is done
Dry device 124；Reduction of speed microwave dryer 125；Magnet 126；Microwave energy generator 127；Transmitting terminal 128；Flue gas is accelerated to be in charge of
151；Constant speed flue gas is in charge of 152；Reduction of speed flue gas is in charge of 153；Accelerate microwave intensity actuator 181；Constant speed microwave intensity actuator
182；Reduction of speed microwave intensity actuator 183；Transfer rate arranges device 184；Loading hopper switch 185；Discharging funnel switch 186；
Battery main switch 187.
Specific embodiment
Purpose, technical scheme and advantage for making the embodiment of the present invention are clearer, below in conjunction with the embodiment of the present invention
In accompanying drawing, the technical scheme in the embodiment of the present invention is clearly and completely described it is clear that described embodiment is
The a part of embodiment of the present invention, rather than whole embodiments.The present invention generally described and illustrated in accompanying drawing herein is implemented
The assembly of example can be arranged with various different configurations and design.Therefore, the reality to the present invention providing in the accompanying drawings below
The detailed description applying example is not intended to limit the scope of claimed invention, but is merely representative of the selected enforcement of the present invention
Example.Based on the embodiment in the present invention, those of ordinary skill in the art are obtained under the premise of not making creative work
Every other embodiment, broadly falls into the scope of protection of the invention.
It should be noted that：Similar label and letter represent similar terms in following accompanying drawing, therefore, once a certain Xiang Yi
It is defined in individual accompanying drawing, then do not need it to be defined further and explains in subsequent accompanying drawing.
In describing the invention, it should be noted that term " " center ", " on ", D score, "left", "right", " vertical ",
The orientation of instruction such as " level ", " interior ", " outward " or position relationship are based on orientation shown in the drawings or position relationship, or should
Orientation or position relationship that invention product is usually put when using, are for only for ease of the description present invention and simplify description, and not
It is instruction or the hint device of indication or element must have specific orientation, with specific azimuth configuration and operation, therefore not
It is understood that as limitation of the present invention.Additionally, term " first ", " second ", " the 3rd " etc. are only used for distinguishing description, and can not manage
Solve as indicating or implying relative importance.
In describing the invention in addition it is also necessary to explanation, unless otherwise clearly defined and limited, term " setting ",
" installation ", " being connected ", " connection " should be interpreted broadly, for example, it may be being fixedly connected or being detachably connected, or one
Body ground connects；Can be to be mechanically connected or electrically connect；Can be joined directly together it is also possible to by intermediary indirect
It is connected, can be the connection of two element internals.For the ordinary skill in the art, can be with concrete condition understanding
State term concrete meaning in the present invention.
Refering to Fig. 1, present embodiments provide a kind of microwave drying system 100, including drying alley 110, drying alley 110
Inside it is provided with conveyer belt 130, conveyer belt 130 two ends are respectively arranged with feeding device 160 and drawing mechanism 170.Drying alley from
Feeding device to drawing mechanism direction is disposed with acceleration dryer section 111, constant rate of drying section 112 and deceleration drying section 113.Micro-
Ripple drying system 100 also includes the microwave drier 120 along drying alley 110 setting, and microwave drier 120 includes drying
Device case 121 and microwave dryer 122, microwave dryer 122 is arranged in described drying device housing 121, drying device
Housing 121 is in charge of 150 by flue gas and is connected with flue 140.
Specifically, refering to Fig. 2, Fig. 3, the conveyer belt 130 of microwave drying system 100 is circulus, feeding device 160 He
Drawing mechanism 170 is arranged on the two ends of endless conveyor belt 130, and feeding device 160 is arranged on the top position of conveyer belt 130,
Drawing mechanism 170 is arranged on the lower position of conveyer belt 130.Material is powder conveying to conveyer belt by feeding device 160 one end
On 130；Drawing mechanism 170 one end will be collected through dry powder body, leaves drying device by drawing mechanism 170.
In the present embodiment, material is thrown by feeding device 160 and is passed material by conveyer belt 130 on conveyer belt 130
Transport in drying alley 110, the method that microwave heating is utilized by the microwave drier 120 being arranged in drying alley 110
Operation is dried to it.In drying operation, the hydrone being attached on material can be evaporated, and evaporation then produces a certain amount of
Vapor, the steam of generation discharged by the flue 140 being connected with drying device housing 121, kept away by vapor
Having exempted from material is subject to steam to make moist.
The present embodiment is the powder body reaching technological requirement after being directed to primary drying, powder body can be passed through feeding device 160
Carry out redrying, until it reaches after technological requirement, collect powder body.
As shown in figure 4, being provided with microwave energy generator 127, Magnet 126 and transmitting terminal 128 in microwave dryer 122；
Microwave energy generator 127 one end is connected with Magnet 126 one end, and Magnet 126 other end is connected with transmitting terminal 128.
Refering to Fig. 1, microwave drier 120 is arranged along drying alley 110, and conveyer belt 130 is arranged on microwave drier
120 lower section is corresponding with microwave drier 120, is provided with microwave dryer 122, in microwave in microwave drier 120
Exsiccator 122 setting corresponding with conveyer belt 130；It is provided with microwave energy generator 127, Magnet 126 in microwave dryer 122
With transmitting terminal 128.The microwave action that wherein microwave energy generator 127 is produced by transmitting terminal 128 is in transfer tape, transmitting terminal 128
There is and transfer tape between certain angular relationship, wherein transmitting terminal 128 and vertical direction has 10 °～15 ° of angle, at this
It is preferably 13 ° in embodiment, there is 75 °～80 ° of angle, in the present embodiment preferably between transmitting terminal 128 and conveyer belt 130
For 77 °.
Referring again to Fig. 4 it is known that, be not vertically arranged between transmitting terminal 128 and conveyer belt 130, have one between the two
Fixed angle, angle is 77 °.In the present embodiment, by being obliquely installed between conveyer belt 130 and transmitting terminal 128, be conducive to micro-
The microwave that ripple acoustical generator sends preferably is irradiated on the powder body on conveyer belt 130 zone face.
Refering to Fig. 5, inventive embodiments additionally provide a kind of microwave drying system with multiple microwave driers 120
100a.Microwave drying system 100 is differred primarily in that with microwave drying system 100a's, is provided with microwave drying system 100a
Multiple microwave driers 120, and accelerate dryer section 111, constant rate of drying section 112 and reduction of speed with being arranged in drying alley 110
The position of dryer section 113 corresponds to.
Specifically, microwave drying system 100a includes drying alley 110 and microwave drier 120, in drying alley 110
It is provided with conveyer belt 130, conveyer belt 130 two ends are respectively arranged with charging hopper and drawing mechanism 170, in drying alley 110
Acceleration dryer section 111, constant rate of drying section 112 and reduction of speed are disposed with from charging hopper to the direction of drawing mechanism 170 do
Dry section 113.
In the present embodiment, feeding device is loading hopper, and drawing mechanism is funnel.
Accelerate dryer section 111 and the corresponding setting of acceleration microwave dryer 123 in microwave drier 120, wait rapid-curing cutback
Dry section 112 setting corresponding with constant speed microwave dryer 124, deceleration drying section 113 is corresponding with reduction of speed microwave dryer 125 to be set
Put.Accelerate in microwave dryer 123, to be provided with acceleration microwave energy generator, accelerate microwave Magnet and accelerate Microwave emission end,
It is provided with constant speed microwave energy generator, constant speed microwave Magnet and constant speed Microwave emission end in figure in constant rate of drying section 112 not marking
Go out, in deceleration drying section 113, be provided with reduction of speed microwave energy generator, reduction of speed microwave Magnet and transmitting terminal.
Referring again to Fig. 5, microwave drying system is additionally provided with controller 180, and controller 180 includes accelerating microwave intensity to adjust
Section device 181, constant speed microwave intensity actuator 182, reduction of speed microwave intensity actuator 183, conveyer belt 130 transfer rate setting device
184th, loading hopper switch 185, discharging funnel switch 186 and battery main switch 187.Accelerate microwave intensity actuator 181, constant speed
Microwave intensity actuator 182 and reduction of speed microwave intensity actuator 183 respectively at accelerate microwave dryer 123 to be connected, constant speed micro-
Intensity of wave actuator 182 and reduction of speed microwave intensity actuator 183 connect；Conveyer belt 130 transfer rate setting device 184 and conveyer belt
130 connections, the motor connection of concrete and conveyer belt 130；Loading hopper switch 185 is connected with feeding device 160.
The operation principle of microwave drying system 100a is as follows：
First open on and off switch, open loading hopper switch 185, then by adjust accelerate microwave intensity actuator 181, etc.
Fast microwave intensity device 182 and reduction of speed microwave intensity actuator 183 setting acceleration, constant speed, falling-rate periods of drying parameter value, open afterwards again
Transmission switch.Material enters to conveyer belt 130 from loading hopper, enters to dry track by conveyer belt 130.Material is being dried
Enter in tunnel 110 and accelerate dryer section 111, accelerate to dry operation by accelerating microwave dryer 123 to carry out, accelerate exsiccator with
Accelerate microwave intensity actuator 181 to connect, carry out the regulation of microwave intensity by accelerating microwave intensity actuator 181, make microwave
Keep higher-strength, and quick drying operation is carried out to material by the microwave of higher-strength.Accelerate the thing after drying operation
Material enters constant rate of drying section 112, carries out constant speed by constant speed microwave dryer 124 and dries operation, constant rate of drying device is micro- with constant speed
Intensity of wave actuator 182 connects, and realizes the regulation of microwave intensity by constant speed microwave intensity actuator 182, makes microwave keep phase
To stable intensity, and material is dehydrated again, for removing the part moisture of residual.Enter fall with conveyer belt 130 again
Fast dryer section 113, carries out reduction of speed by falling-rate periods of drying device and dries operation, falling-rate periods of drying device and reduction of speed microwave intensity actuator 183
Connect, make microwave keep relatively low intensity, and triple dewatering is carried out to material, thoroughly material is dried.In drying operation
While the hot gas that produces 151, constant speed flue gas be in charge of by the acceleration flue gas being connected with microwave drier 120 be in charge of 152
It is in charge of 153 with reduction of speed flue gas to be emitted in flue 140, and discharged by vent.Material through being dried passes through drying
Tunnel 110 enters to out funnel, is collected discharging by going out funnel.Powder body after primary drying is unsatisfactory for back tender
Skill requires, and can enter in drying device material again by feeding device 160, carry out redrying process.
The microwave drying system 100 that the present embodiment provides, 100a are dried using microwave, and can be dried relatively simultaneously
Multi-quantity powder body, the early demand of gratification, drying process is simple, and technique is advanced, has also reached energy-conserving and environment-protective using microwave drying
Target, pollution-free, " three wastes " problem will not be produced, meet the requirement of sustainable development.
In the present embodiment, there is provided a kind of microwave drying system 100a being provided with many dryer section, set in many dryer section
It is equipped with multiple microwave dryers 122.The effect of so setting is can to produce different being dried and imitate in different dryer section
Really.Microwave energy generator is accelerated to be used for producing the larger microwave of intensity and extremely accelerating Microwave emission by transmitting terminal 128 dry
Powder body on dry section 111, for accelerating the powder body fast dewatering in dryer section 111；Constant speed microwave energy generator is used for producing
The little microwave of intensity simultaneously passes through transmitting terminal 128 by Microwave emission to constant rate of drying section 112 powder body, taking off again for powder body
Water；Reduction of speed microwave energy generator is used for producing the relatively low microwave of intensity and doing Microwave emission to reduction of speed by transmitting terminal 128
Powder body on dry section 113, for the third time dehydration of powder body.In the present embodiment, microwave dryer 123, constant speed microwave is accelerated to do
Dry device 124 is mutually isostructural microwave dryer 122 with reduction of speed microwave dryer 125, is controlled by the frequency adjusting three
The microwave intensity that three produces, thus realize accelerating the dry, constant rate of drying and falling-rate periods of drying.Combined by three kinds of drying modes,
Powder drying technique can efficiently be quickly finished, and the waste of the energy can be reduced.And it is possible to accelerate microwave to do by controlling
The unlatching of dry device 123, constant speed microwave dryer 124 and reduction of speed microwave dryer 125 and closure, realize controlling microwave intensity, enter
And realize the drying operation for different moisture content material.
The present embodiment can arrange device 184 by transfer rate and the transfer rate of conveyer belt 130 is defined.Thus
Transfer rate will be controlled and control microwave intensity to be combined, realize the optimization drying proposal for different material.When being done
When the water content of dry material is higher, microwave intensity can be increased to improve dry tenacity by reducing conveyer belt 130 speed, from
And complete the drying operation of material.When the water content of dried material is relatively low, can be by improving conveyer belt 130 speed, fall
Humble intensity of wave, to reduce dry tenacity, makes to complete the drying of material in the short time, and will not produce the unnecessary consumption of the energy.
The foregoing is only the preferred embodiments of the present invention, be not limited to the present invention, for the skill of this area
For art personnel, the present invention can have various modifications and variations.All within the spirit and principles in the present invention, made any repair
Change, equivalent, improvement etc., should be included within the scope of the present invention.
Claims (10)
1. a kind of microwave drying system is it is characterised in that include drying alley, the microwave drying dress along the setting of described drying alley
Put；Described microwave drier is connected with flue；It is provided with conveyer belt in described drying alley；Described conveyer belt two ends are divided
It is not provided with feeding device and drawing mechanism；Described drying alley sets from described feeding device successively to described drawing mechanism direction
It is equipped with acceleration dryer section, constant rate of drying section and deceleration drying section.
2. microwave drying system according to claim 1 is it is characterised in that described microwave drier includes drying device
Housing and microwave dryer, described microwave dryer is arranged in described drying device housing, described drying device housing and institute
State flue to connect.
3. microwave drying system according to claim 2 is it is characterised in that described microwave dryer includes accelerating microwave to do
Dry device, constant speed microwave dryer and reduction of speed microwave dryer；Dryer section is corresponding sets with described acceleration for described acceleration microwave dryer
Put；Described constant speed microwave dryer is correspondingly arranged with described constant rate of drying section；Described reduction of speed microwave dryer is done with described reduction of speed
Dry section is correspondingly arranged.
4. microwave drying system according to claim 3 is it is characterised in that be provided with successively in described acceleration microwave dryer
Acceleration microwave energy generator, acceleration microwave Magnet and the acceleration Microwave emission end connecting, in described constant speed microwave dryer
It is provided with the constant speed microwave energy generator being sequentially connected, constant speed microwave Magnet and constant speed Microwave emission end, described reduction of speed microwave
It is provided with the reduction of speed microwave energy generator being sequentially connected, reduction of speed microwave Magnet and reduction of speed Microwave emission end in exsiccator.
5. microwave drying system according to claim 4 is it is characterised in that described reduction of speed Microwave emission end, constant speed microwave
Transmitting terminal and reduction of speed Microwave emission end with the angle of vertical direction are 10 °～15 ° respectively, described acceleration Microwave emission end, etc.
The angle and described conveyer belt between is 75 °～80 ° respectively for fast Microwave emission end and reduction of speed Microwave emission end.
6. a kind of microwave drying system according to any one of claim 1 to 5 is it is characterised in that described feeding device bag
Include loading hopper, described loading hopper is connected with described conveyer belt one end；Described drawing mechanism includes funnel, described discharging
Funnel is connected with the described conveyer belt other end.
7. a kind of microwave drying system according to one of claim 3 to 5 is it is characterised in that described flue and institute
State and be connected with flue gas between housing and be in charge of；Described flue gas be in charge of including accelerate flue gas is in charge of, constant speed flue gas is in charge of and reduction of speed flue gas
It is in charge of.
8. a kind of microwave drying system according to claim 7 it is characterised in that described acceleration flue gas be in charge of with described plus
Fast microwave dryer connects；Described constant speed flue gas is in charge of and is connected with described constant speed microwave dryer；Described reduction of speed flue gas be in charge of with
Described reduction of speed microwave dryer connects.
9. a kind of microwave drying system according to claim 4 is it is characterised in that described microwave drying system also includes controlling
Device processed；Described controller includes microwave intensity actuator, and described microwave intensity actuator is connected with described microwave dryer.
10. a kind of microwave drying system according to claim 9 is it is characterised in that described microwave intensity actuator includes
Accelerate microwave intensity actuator, constant speed microwave intensity actuator, reduction of speed microwave intensity actuator, the setting of conveyer belt transfer rate
Device, loading hopper switch, discharging funnel switch and battery main switch；Described acceleration microwave intensity actuator and described acceleration microwave
Exsiccator electrically connects；Described constant speed microwave intensity actuator is electrically connected with described constant speed microwave dryer；Described reduction of speed microwave is strong
Degree actuator is electrically connected with described reduction of speed microwave dryer；Described conveyer belt transfer rate setting device is electrically connected with described conveyer belt
Connect；Described loading hopper switch is electrically connected with described loading hopper；Described discharging funnel switch with described go out funnel electrically connect.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610799948.7A CN106403562A (en) | 2016-08-31 | 2016-08-31 | Microwave drying system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610799948.7A CN106403562A (en) | 2016-08-31 | 2016-08-31 | Microwave drying system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106403562A true CN106403562A (en) | 2017-02-15 |
Family
ID=57998580
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610799948.7A Pending CN106403562A (en) | 2016-08-31 | 2016-08-31 | Microwave drying system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106403562A (en) |
Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2043241U (en) * | 1988-12-31 | 1989-08-23 | 王师俊 | Bake-ware conveying type gelatin drying machinery |
| US5091079A (en) * | 1990-03-09 | 1992-02-25 | Danny Gayman | Sludge treatment apparatus |
| CN2268909Y (en) * | 1996-05-21 | 1997-11-26 | 抚顺石油化工公司腈纶化工厂 | Polymer drying apparatus |
| CN2418445Y (en) * | 2000-03-06 | 2001-02-07 | 刘显树 | Energy-saving type panel-turning-over air-flow drying machine |
| CN201074948Y (en) * | 2007-07-04 | 2008-06-18 | 天水华圆制药设备科技有限责任公司 | Fluid materials drier |
| KR20120028453A (en) * | 2010-09-15 | 2012-03-23 | 정인환 | Apparatus for drying sludge |
| CN203443282U (en) * | 2013-07-01 | 2014-02-19 | 厦门特伦生物药业有限公司 | Microwave drying and sterilizing device |
| CN203881085U (en) * | 2014-05-07 | 2014-10-15 | 四川农业大学 | Dewatering and drying device for vinasse |
| JP2015129617A (en) * | 2014-01-08 | 2015-07-16 | 新日鐵住金株式会社 | Microwave dryer and microwave drying method |
-
2016
- 2016-08-31 CN CN201610799948.7A patent/CN106403562A/en active Pending
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2043241U (en) * | 1988-12-31 | 1989-08-23 | 王师俊 | Bake-ware conveying type gelatin drying machinery |
| US5091079A (en) * | 1990-03-09 | 1992-02-25 | Danny Gayman | Sludge treatment apparatus |
| CN2268909Y (en) * | 1996-05-21 | 1997-11-26 | 抚顺石油化工公司腈纶化工厂 | Polymer drying apparatus |
| CN2418445Y (en) * | 2000-03-06 | 2001-02-07 | 刘显树 | Energy-saving type panel-turning-over air-flow drying machine |
| CN201074948Y (en) * | 2007-07-04 | 2008-06-18 | 天水华圆制药设备科技有限责任公司 | Fluid materials drier |
| KR20120028453A (en) * | 2010-09-15 | 2012-03-23 | 정인환 | Apparatus for drying sludge |
| CN203443282U (en) * | 2013-07-01 | 2014-02-19 | 厦门特伦生物药业有限公司 | Microwave drying and sterilizing device |
| JP2015129617A (en) * | 2014-01-08 | 2015-07-16 | 新日鐵住金株式会社 | Microwave dryer and microwave drying method |
| CN203881085U (en) * | 2014-05-07 | 2014-10-15 | 四川农业大学 | Dewatering and drying device for vinasse |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104677054B (en) | It is inverted the low temperature fluidized bed drying equipment of microwave | |
| CN101957128B (en) | Biomass material drying system | |
| CN104034127B (en) | Microwave fluid bed hot blast combined drying experimental provision | |
| CN207163103U (en) | A kind of timber processing dryer with sterilizing function | |
| CN104748512B (en) | Solar energy-microwave combined drying chamber | |
| CN202032847U (en) | Belt type dryer | |
| CN205784364U (en) | A kind of drying machine with spinfunction and dehumidifying uniform and complete | |
| CN203432251U (en) | Continuous microwave dryer | |
| CN106403562A (en) | Microwave drying system | |
| CN208108752U (en) | A kind of curtain type grain drying device | |
| CN201605216U (en) | Sludge drying processing equipment | |
| CN205784447U (en) | Continuous material microwave dryer | |
| CN105841468A (en) | Microwave dryer for polyacrylamide colloidal particles and microwave drying method | |
| CN110395873A (en) | A kind of city sludge van-type Minton dryer | |
| CN206512088U (en) | A kind of sludge rapid dryer | |
| CN206176938U (en) | Whirlwind formula flash drying system that hot air cycle utilized | |
| CN107619924A (en) | A kind of microwave substep strengthens the system and method for drying lateritic nickel ore | |
| CN206760726U (en) | Rotatable drum-type microwave dryer | |
| CN206817938U (en) | A kind of spiral dryer | |
| CN109341256A (en) | Novel high wind damping wheel dryer | |
| CN220669986U (en) | Dryer convenient to refining | |
| CN206019238U (en) | A kind of band drier | |
| CN103868338B (en) | Novel percolation adds quiet bed classification drying system | |
| CN108532253A (en) | A kind of clothes drying apparatus of environmental protection and energy saving | |
| CN204063863U (en) | Novel percolation adds quiet bed classification drying system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20170215 |