CN207527969U - A kind of new and effective double-cone dryer - Google Patents
A kind of new and effective double-cone dryer Download PDFInfo
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- CN207527969U CN207527969U CN201721653545.8U CN201721653545U CN207527969U CN 207527969 U CN207527969 U CN 207527969U CN 201721653545 U CN201721653545 U CN 201721653545U CN 207527969 U CN207527969 U CN 207527969U
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- lower cone
- diversion pipe
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Abstract
The utility model is related to a kind of new and effective double-cone dryer, including bearing base, load bearing arm, main rotary drive mechanism, transmission shaft and rotary tank, rotary tank is connect with bearing base upper surface by load bearing arm and is located at right over bearing base, and rotary tank is connect by transmission shaft with load bearing arm and main rotary drive mechanism respectively, the main rotary drive mechanism is mounted on load bearing arm, and rotary tank includes epicone tank, lower cone tank, straight-through tank, rabbling mechanism, vacuum filter, exhaust pipe, thermal medium diversion pipe, cold medium diversion pipe, negative pressure pump and circulating pump.On the one hand the utility model can effectively improve the working efficiency of material batch mixing, drying operation, reduce drying operation during into material loss, it on the other hand can be according to any one or two kinds be made in high temperature drying, low temperature drying mode to be carried out at the same time drying operation, the flexibility versatility of drying operation is improved, meets the needs of different material drying operation.
Description
Technical field
The utility model is related to a kind of drying equipments, are exactly a kind of new and effective double-cone dryers.
Background technology
Bicone drying unit be it is current carry out material mixing, drying operation important equipment, usage amount is very huge, but
It is found in actual use, in operation, on the one hand there are the work of material drying operation for currently used Bicone drying unit
It is relatively inefficient, and easily material is caused to damage due to material is Nian Jie with Bicone drying unit inner wall and exhaust gas discharges during drying operation
Consumption on the other hand during drying operation, is often only capable of using the one of which in high temperature drying and low temperature drying mode, from
And lead to current Bicone drying unit drying operation inefficiency, and drying operation poor universality, different material can not be met
To the needs of different drying modes operation, therefore for this problem, there is an urgent need to develop a kind of novel Bicone drying unit,
To meet the needs of actual use.
Utility model content
In view of the shortcomings of the prior art, the utility model provides a kind of new and effective double-cone dryer, this is novel
Simple in structure, flexible and convenient to use, versatility is good, and drying efficiency is high, on the one hand can effectively improve material batch mixing, drying operation
Working efficiency, reduce drying operation during, because material is Nian Jie with inner tank wall and is made with vacuum-pumping equipment drying operation
Into material loss, can be according to making in high temperature drying, low temperature drying mode on the other hand during dry and mixture operation
Any one or two kinds are carried out at the same time drying operation, so as to greatly improve the flexibility versatility of drying operation, meet different
The needs of dry materials operation.
To achieve these goals, the utility model is to realize by the following technical solutions：
A kind of new and effective double-cone dryer including bearing base, load bearing arm, main rotary drive mechanism, transmission shaft and returns
Turn tank body, rotary tank is connect with bearing base upper surface by load bearing arm and is located at right over bearing base, and rotary tank
It is connect respectively with load bearing arm and main rotary drive mechanism by transmission shaft, the main rotary drive mechanism is mounted on load bearing arm
On, rotary tank include epicone tank, lower cone tank, straight-through tank, rabbling mechanism, vacuum filter, exhaust pipe, thermal medium diversion pipe,
Cold medium diversion pipe, negative pressure pump and circulating pump, epicone tank, lower cone tank are conical bores structure, epicone tank, lower cone pot bottom
It is interconnected by straight-through tank, front end sets material adding mouth, and epicone tank, lower cone tank are symmetrically distributed in straight-through tank two with straight-through tank
Side is simultaneously coaxially distributed with straight-through tank, and mutually isolated by partition board between epicone tank, lower cone tank and straight-through tank, and is set on partition board few
Flow-guiding mouth, straight-through tank are interconnected by flow-guiding mouth with epicone tank, lower cone tank respectively, and rabbling mechanism, vacuum filter are embedded in
In straight-through tank, wherein rabbling mechanism both ends are connect with straight-through pot sidewall, and rabbling mechanism axis is vertical with straight-through tank axis and phase
It hands over, vacuum filter is at least one, is interconnected on straight-through top tank structure and with exhaust pipe front end, and exhaust pipe end is with bearing
Press pump is interconnected, and negative pressure pump is mounted on straight-through tank outer surface by sliding rail, and epicone tank, lower cone tank include containment wall, change
Hot liner, wherein heat-exchange inner container are coaxially distributed, and set between containment wall, heat-exchange inner container in containment wall and with containment wall
Width is 1-20 centimetres of heat exchanging chamber, and thermal medium diversion pipe is in spiral shell in the heat exchanging chamber of epicone tank, and around epicone tank axis
Shape distribution is revolved, cold medium diversion pipe is spirally distributed in lower cone tank heat exchanging chamber, and around lower cone tank axis, and thermal medium is led
Flow tube, cold medium diversion pipe are respectively interconnected at least one circulating pump, and circulating pump is respectively by sliding rail mounted on upper
On cone tank, lower cone tank outer surface.
Further, the epicone tank, lower cone tank containment wall are an integral structure with straight-through pot sidewall or by fixed
Position mechanism is connected with each other.
Further, the partition board is and leads directly to the pyramidal structure that tank is coaxially distributed, the flow-guiding mouth and partition board
Coaxial distribution, and partition board side surface corresponding with straight-through tank sets at least one oscillating mechanism.
Further, set control valve at the flow-guiding mouth, and flow-guiding mouth by control valve respectively with epicone tank, lower cone
Tank, straight-through tank are interconnected.
The utility model is simple in structure, flexible and convenient to use, and versatility is good, and drying efficiency is high, on the one hand can effectively improve object
The working efficiency of batch mixing, drying operation is expected, during reducing drying operation, because material is Nian Jie with inner tank wall and with being vacuum-evacuated
Material loss caused by equipment drying operation, on the other hand during dry and mixture operation, can according to make high temperature drying,
Any one in low temperature drying mode or two kinds are carried out at the same time drying operation, so as to which the flexibility for greatly improving drying operation is led to
With property, meet the needs of different material drying operation.
Description of the drawings
It is described in detail the utility model with reference to the accompanying drawings and detailed description.
FIG. 1 is a schematic structural view of the utility model；
Fig. 2 is rotary tank structure diagram.
Specific embodiment
To be easy to understand technical means, creative features, achievable purpose and effectiveness of the utility model, below
With reference to specific embodiment, the utility model is expanded on further.
A kind of new and effective double-cone dryer as described in Fig. 1 and 2, including bearing base 1, load bearing arm 2, main rotation driving
Mechanism 3, transmission shaft 4 and rotary tank 5, rotary tank 5 are connect with 1 upper surface of bearing base by load bearing arm 2 and are located at carrying
Right over pedestal 1, and rotary tank 5 is connect by transmission shaft 4 with load bearing arm 2 and main rotary drive mechanism 3 respectively, the master
Rotary drive mechanism 3 is mounted on load bearing arm 2.
In the present embodiment, the rotary tank 5 include epicone tank 51, lower cone tank 52, straight-through tank 53, rabbling mechanism 54,
Vacuum filter 55, exhaust pipe 56, thermal medium diversion pipe 57, cold medium diversion pipe 58, negative pressure pump 59 and circulating pump 50, epicone tank
21st, lower cone tank 52 is conical bores structure, and epicone tank 51, lower cone 52 bottom of tank are interconnected by straight-through tank 53, front end
If material adding mouth 6, and epicone tank 51, lower cone tank 52 with straight-through tank 53 be symmetrically distributed in straight-through 53 both sides of tank and with straight-through tank 53
Coaxial distribution, and it is mutually isolated by partition board 7 between epicone tank 51, lower cone tank 52 and straight-through tank 53, and few water conservancy diversion is set on partition board 7
Mouth 8 leads directly to tank 53 and is interconnected respectively with epicone tank 51, lower cone tank 52 by flow-guiding mouth 8, rabbling mechanism 54, vacuum filter
55 in straight-through tank 53, and wherein 54 both ends of rabbling mechanism connects with straight-through 53 side wall of tank, and 54 axis of rabbling mechanism and directly
Logical 53 axis of tank is vertical and intersecting, and vacuum filter 55 is at least one, on straight-through 53 inner wall of tank and with before exhaust pipe 56
End is interconnected, and 56 end of exhaust pipe is interconnected with negative pressure pump 59, and negative pressure pump 59 is mounted on 53 appearance of straight-through tank by sliding rail 9
Face.
Simultaneously, the epicone tank 51 described in the present embodiment, lower cone tank 52 include containment wall 101, heat-exchange inner container
102, wherein heat-exchange inner container 102 in the containment wall 101 and with the coaxial distribution of containment wall 101, and containment wall 101, change
Width is set between hot liner 102 as 1-20 centimetres of heat exchanging chamber 103, thermal medium diversion pipe 57 is embedded in the heat exchanging chamber 103 of epicone tank 51
It is interior, and be spirally distributed around 51 axis of epicone tank, cold medium diversion pipe 58 is in lower cone 52 heat exchanging chamber 103 of tank, and ring
Around it is lower cone 52 axis of tank be spirally distributed, thermal medium diversion pipe 57, cold medium diversion pipe 58 respectively at least one cycle
Pump 50 is interconnected, and circulating pump 50 is respectively by sliding rail 9 on epicone tank 51,52 outer surface of lower cone tank.
In the present embodiment, the epicone tank 51, lower 52 containment wall 101 of cone tank and straight-through 53 side wall of tank are integral type knot
Structure is connected with each other by detent mechanism.
In the present embodiment, the partition board 7 is the pyramidal structure being coaxially distributed with straight-through tank 53, the flow-guiding mouth 8
With the coaxial distribution of partition board 7, and the partition board 7 sets at least one oscillating mechanism 10 with straight-through 53 corresponding side surface of tank.
In the present embodiment, set control valve 11 at the flow-guiding mouth 8, and flow-guiding mouth 8 by control valve 11 respectively with epicone
Tank 51, lower cone tank 52, straight-through tank 53 are interconnected.
The utility model in the specific implementation, complete first according to use need complete bearing base, load bearing arm, it is main rotation driving
Mechanism, transmission shaft and rotary tank assembling, it is then spare.
When operation is dried to material, material is respectively added to epicone tank, lower cone by material adding mouth first
In tank, and epicone tank, lower cone tank are sealed, then according to material characteristic, from selection drying mode, then will done accordingly
Dry medium by circulating pump be respectively delivered to any one or two in thermal medium diversion pipe and cold medium diversion pipe simultaneously into
Then row conveying makes thermal medium diversion pipe, cold medium diversion pipe and epicone tank, lower cone tank carry out heat exchange, and make in heat exchange
It while industry, is chosen to install by main rotary drive mechanism driving rotary tank so that the material in epicone tank, lower cone tank is turned over
Turn, and imported into straight-through tank and be mixed, at the same when being mixed by vacuum filter to air in straight-through tank into
The purpose excluded steam to dry materials operation is realized in row discharge.
Wherein when carrying out dry materials operation, when material needs to carry out high temperature drying, then by the thermal medium of epicone tank
Diversion pipe imports high-temperature medium, and material is dried；When material needs to carry out low temperature drying, then by the thermal medium of lower cone tank
Diversion pipe imports cryogenic media, and material is dried；When material need to drying mode without particular/special requirement when, then on the one hand by upper
The thermal medium diversion pipe for boring tank imports high-temperature medium, and material is dried, on the other hand by the thermal medium diversion pipe of lower cone tank
Import cryogenic media, material is dried, and during rotary tank chooses to install, to epicone tank, it is lower cone tank in material into
Row exchanges, and reaching increases the temperature difference between material and heat transferring medium, improves the purpose of drying operation efficiency.
The utility model is simple in structure, flexible and convenient to use, and versatility is good, and drying efficiency is high, on the one hand can effectively improve object
The working efficiency of batch mixing, drying operation is expected, during reducing drying operation, because material is Nian Jie with inner tank wall and with being vacuum-evacuated
Material loss caused by equipment drying operation, on the other hand during dry and mixture operation, can according to make high temperature drying,
Any one in low temperature drying mode or two kinds are carried out at the same time drying operation, so as to which the flexibility for greatly improving drying operation is led to
With property, meet the needs of different material drying operation.
It should be understood by those skilled in the art that the present utility model is not limited to the above embodiments.Above-described embodiment and
The principle for only illustrating the utility model described in specification.On the premise of not departing from the spirit and scope of the utility model,
The present invention also has various changes and improvements.These changes and improvements both fall within claimed the scope of the utility model
It is interior.The protection scope of the present invention is defined by the appended claims and their equivalents.
Claims (4)
1. a kind of new and effective double-cone dryer, including bearing base, load bearing arm, main rotary drive mechanism, transmission shaft and revolution
Tank body, rotary tank are connect with bearing base upper surface by load bearing arm and are located at right over bearing base, and rotary tank leads to
Transmission shaft to be crossed to connect with load bearing arm and main rotary drive mechanism respectively, the main rotary drive mechanism is mounted on load bearing arm,
It is characterized in that：The rotary tank include epicone tank, lower cone tank, straight-through tank, rabbling mechanism, vacuum filter, exhaust pipe,
Thermal medium diversion pipe, cold medium diversion pipe, negative pressure pump and circulating pump, the epicone tank, lower cone tank are conical bores knot
Structure, epicone tank, lower cone pot bottom are interconnected by straight-through tank, and front end sets material adding mouth, and the epicone tank, lower cone tank
Straight-through tank both sides are symmetrically distributed in straight-through tank and are coaxially distributed with straight-through tank, and the epicone tank, lower cone tank and straight-through tank
Between it is mutually isolated by partition board, and few flow-guiding mouth is set on partition board, lead directly to tank by flow-guiding mouth respectively with epicone tank, lower cone tank phase
Intercommunicated, the rabbling mechanism, vacuum filter are in straight-through tank, wherein the rabbling mechanism both ends and straight-through tank
Side wall connects, and rabbling mechanism axis is vertical with straight-through tank axis and intersects, and the vacuum filter is at least one, is mounted on
It is interconnected on straight-through top tank structure and with exhaust pipe front end, the exhaust pipe end is interconnected with negative pressure pump, and described is negative
Press pump is mounted on straight-through tank outer surface by sliding rail, and the epicone tank, lower cone tank include containment wall, heat-exchange inner container,
Described in heat-exchange inner container be coaxially distributed, and the containment wall, heat-exchange inner container in the containment wall and with containment wall
Between set width as 1-20 centimetres of heat exchanging chamber, the thermal medium diversion pipe is in the heat exchanging chamber of epicone tank, and around epicone
Tank axis is spirally distributed, and the cold medium diversion pipe is in spiral shell in lower cone tank heat exchanging chamber, and around lower cone tank axis
Shape distribution is revolved, the thermal medium diversion pipe, cold medium diversion pipe are respectively interconnected, and described at least one circulating pump
Circulating pump epicone tank is mounted on, on lower cone tank outer surface by sliding rail respectively.
2. a kind of new and effective double-cone dryer according to claim 1, it is characterised in that：The epicone tank, lower cone
Tank containment wall is an integral structure with straight-through pot sidewall or is connected with each other by detent mechanism.
3. a kind of new and effective double-cone dryer according to claim 1, it is characterised in that：The partition board be with directly
The pyramidal structure that logical tank is coaxially distributed, the flow-guiding mouth are coaxially distributed with partition board, and the partition board is corresponding with straight-through tank
Side surface sets at least one oscillating mechanism.
4. a kind of new and effective double-cone dryer according to claim 1, it is characterised in that：Control is set at the flow-guiding mouth
Valve processed, and flow-guiding mouth is interconnected by control valve with epicone tank, lower cone tank, straight-through tank respectively.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721653545.8U CN207527969U (en) | 2017-12-01 | 2017-12-01 | A kind of new and effective double-cone dryer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721653545.8U CN207527969U (en) | 2017-12-01 | 2017-12-01 | A kind of new and effective double-cone dryer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207527969U true CN207527969U (en) | 2018-06-22 |
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ID=62577611
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721653545.8U Active CN207527969U (en) | 2017-12-01 | 2017-12-01 | A kind of new and effective double-cone dryer |
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| Country | Link |
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| CN (1) | CN207527969U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117628852A (en) * | 2024-01-25 | 2024-03-01 | 常州市力度干燥设备有限公司 | Cylindrical cone three-in-one vacuum dryer |
-
2017
- 2017-12-01 CN CN201721653545.8U patent/CN207527969U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117628852A (en) * | 2024-01-25 | 2024-03-01 | 常州市力度干燥设备有限公司 | Cylindrical cone three-in-one vacuum dryer |
| CN117628852B (en) * | 2024-01-25 | 2024-04-12 | 常州市力度干燥设备有限公司 | Cylindrical cone three-in-one vacuum dryer |
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