CN206037634U - Continuous drying device of paddle desiccator - Google Patents
Continuous drying device of paddle desiccator Download PDFInfo
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- CN206037634U CN206037634U CN201620951375.0U CN201620951375U CN206037634U CN 206037634 U CN206037634 U CN 206037634U CN 201620951375 U CN201620951375 U CN 201620951375U CN 206037634 U CN206037634 U CN 206037634U
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- valve
- pneumatic operated
- pipeline
- operated valve
- blade dryer
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Abstract
The utility model discloses a continuous drying device of paddle desiccator has overcome prior art, and among the rubber ingredient dry run drying capacity is low, problem that the energy consumption is high. The utility model discloses a contain the feeding storehouse, spiral pusher, rotatory feeding valve, paddle desiccator, first pneumatic valve, buffer stock bin, second pneumatic valve, play feed bin, third pneumatic valve, the bottom exit linkage spiral pusher in feeding storehouse, the import of rotating feeding valve, paddle desiccator, the export of paddle desiccator is passed through the first pneumatic valve of pipe connection, buffer stock bin, fender, second pneumatic valve, is gone out feed bin, third pneumatic valve, the dry chamber of paddle desiccator connects gradually sack cleaner and jet pump through the pipeline. This technique device is through the evacuation to locking gas to the business turn over material and arranging, keep the vacuum drying environment, reduce wet feed liquid attitude component boiling point, improve material mummification speed, the big rubber ingredient powder that carries on in batches is dry in succession, reduces glutinous wall risk.
Description
Technical field
The utility model is related to a kind of drying equipment, more particularly to a kind of blade dryer continuous drying apparatus.
Background technology
At present, domestic Rubber Accelerator Industry development is more environmentally friendly, efficient.Rubber chemicals demand increases year by year, also drives enterprise
Industry production capacity expands.In rubber chemicals production process, it is dried link and often restricts production capacity expansion key factor.Existing rubber is helped
Agent powder is mainly dried using driers such as flash distillation dryer, fluidized bed dryer, baking ovens.Above-mentioned drier is generally deposited
Drying capacity is low, high energy consumption, the high defect of maintenance cost.
Utility model content
The utility model is overcome in prior art, in rubber chemicals dry run, drying capacity is low, and high energy consumption is asked
Topic, there is provided a kind of simple structure, blade dryer continuous drying apparatus easy to use.
Technical solution of the present utility model is to provide a kind of dress of the blade dryer continuous drying with following structure
Put：It is containing feeding warehouse, screw feeder, rotatory feeder valve, blade dryer, the first pneumatic operated valve, buffer bin, second pneumatic
Valve, discharging bin, the 3rd pneumatic operated valve, the outlet at bottom connection screw feeder of feeding warehouse, screw feeder are revolved by pipeline connection
Turn feed valve, rotatory feeder valve connects the import of blade dryer by pipeline, and the outlet of blade dryer is connected by pipeline
First pneumatic operated valve, the first pneumatic operated valve by pipeline connect buffer bin, buffer bin by pipeline connection the second pneumatic operated valve, second
Pneumatic operated valve connects discharging bin, discharging bin by pipeline and connects the 3rd pneumatic operated valve, the drying chamber of the blade dryer by pipeline
Sack cleaner and jet pump are sequentially connected by pipeline.
The jet pump is water-jet pump.The heating medium of the blade dryer is steam, deep fat, water, is heated
Medium is passed through in the housing chuck of active paddle shaft, driven paddle shaft and blade dryer.
Compared with prior art, the utility model blade dryer continuous drying apparatus have advantages below：This device is fitted
For products such as rubber chemicals MZ, ZTC, EZ, device is by vacuumizing, and carries out locking gas arrangement to passing in and out material, maintains vacuum
Dry environment, reduces wet feed liquid composition boiling point, improves material mummification speed, continuously can in high volume carry out rubber chemicals powder and do
It is dry, reduce glutinous wall risk.
Description of the drawings
Fig. 1 is the facade arrangement structure schematic diagram one of the utility model blade dryer continuous drying apparatus；
Fig. 2 is the facade arrangement structure schematic diagram two of the utility model blade dryer continuous drying apparatus.
Specific embodiment
In description of the drawings, label 1 is feeding warehouse, and 2 is screw feeder, and 3 is sack cleaner, and 4 is rotatory feeder valve, and 5 are
Blade dryer, 6 is the first pneumatic operated valve, and 7 is buffer bin, and 8 is the second pneumatic operated valve, and 9 is discharging bin, and 10 is the 3rd pneumatic operated valve,
11 is jet pump.
Further are made to the utility model blade dryer continuous drying apparatus with reference to the accompanying drawings and detailed description
Explanation：It is as illustrated, contain feeding warehouse in the present embodiment, screw feeder, rotatory feeder valve, blade dryer, first pneumatic
Valve, buffer bin, the second pneumatic operated valve, discharging bin, the 3rd pneumatic operated valve.The outlet at bottom of feeding warehouse is by pipeline connection rotation feed
Valve, rotatory feeder valve connect blade dryer import by pipeline, and the outlet of blade dryer is pneumatic by pipeline connection first
Valve, the first pneumatic operated valve connect buffer bin by pipeline, and buffer bin connects the second pneumatic operated valve, the second pneumatic operated valve by pipeline and leads to
Piping connection discharging bin, discharging bin connect the 3rd pneumatic operated valve by pipeline, and the drying chamber of the blade dryer passes through pipeline
Sack cleaner and jet pump is sequentially connected, is vacuumized by jet pump, it is negative inside formation blade dryer and sack cleaner
Pressure ring border, sack cleaner filter bag adopt PTFE antistatic filter bags, according to live vacuum table, so that it is determined that jet pump variable-frequency motor
Effective power, wait after reaching stable negative pressure, can be fed intake using the electric block at the top of feeding warehouse.
The jet pump is water-jet pump.The heating medium of blade dryer is steam, deep fat, water, and this device adopts
Heated with steam.Heating medium is passed through in the housing chuck of active paddle shaft, driven paddle shaft and blade dryer, and paddle is dried
Machine is a kind of efficient heat-conduction-type drying machine, and, under being stirred continuously of blade, heated drying, while to reach for material
It is dynamic.
Can be pumped in sack cleaner when the material to be dried in the course of work, having splashed is mingled with certain moisture,
Sack cleaner can carry out solid and gas separation, and the powder to be dried collected in which can be fallen dryer inner and continue drying.
The jet pump that device is equipped with is water-jet pump, by contrast properties curve, by perfect condition conversion evaporation water
Vapour volume（Do not consider that air is revealed）, it is to be understood that, minimum vacuum.Consider the injection tolerance of sack cleaner, rotary valve structure
Gas leakage, then after prediction transformation, system vacuum is about -0.035MPa（45℃）, under the vacuum, the boiling point of water is 88 DEG C, than just
About 12 DEG C are reduced often.In such circumstances, moisture is easier to be precipitated, and quick so as to realize, efficient powder is dried, while saving
For heat energy.
Dried material is opened by the alternating of the first pneumatic operated valve, the second pneumatic operated valve, the 3rd pneumatic operated valve, is discharged.
The first pneumatic operated valve is first driven, the second pneumatic operated valve is closed, is closed the 3rd pneumatic operated valve, at this time dried material can slowly fall into buffering
In feed bin, when feed bin to be buffered is soon expired, the first pneumatic operated valve is closed, the second pneumatic operated valve is opened, is closed the 3rd pneumatic operated valve, this
When buffer bin in material can fall into discharging bin, when treating discharging bin soon completely, at this time need to enter luggage to finished product
Car is transported, and just by closing the first pneumatic operated valve, closing the second pneumatic operated valve, open the 3rd pneumatic operated valve, carries out the dress bag of finished product materials.
The effect of pneumatic operated valve is to destroy blade drier internal vacuum when avoiding discharging.
Claims (3)
1. a kind of blade dryer continuous drying apparatus, containing feeding warehouse, screw feeder, rotatory feeder valve, blade dryer,
First pneumatic operated valve, buffer bin, the second pneumatic operated valve, discharging bin, the 3rd pneumatic operated valve,
The outlet at bottom connection screw feeder of feeding warehouse, screw feeder connect rotatory feeder valve, rotation feed by pipeline
Valve connects the import of blade dryer by pipeline, and the outlet of blade dryer connects the first pneumatic operated valve, the first gas by pipeline
Dynamic valve connects buffer bin by pipeline, and buffer bin is connected the second pneumatic operated valve, the second pneumatic operated valve by pipeline and connected by pipeline
Pick out feed bin, discharging bin and the 3rd pneumatic operated valve connected by pipeline, it is characterised in that：The drying chamber of the blade dryer is by pipe
Road is sequentially connected sack cleaner and jet pump.
2. blade dryer continuous drying apparatus according to claim 1, it is characterised in that：The jet pump is sprayed for water
Vavuum pump.
3. blade dryer continuous drying apparatus according to claim 1, it is characterised in that：The blade dryer plus
Thermal medium is steam, deep fat, water, heats the housing chuck that medium is passed through active paddle shaft, driven paddle shaft and blade dryer
In.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620951375.0U CN206037634U (en) | 2016-08-27 | 2016-08-27 | Continuous drying device of paddle desiccator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620951375.0U CN206037634U (en) | 2016-08-27 | 2016-08-27 | Continuous drying device of paddle desiccator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206037634U true CN206037634U (en) | 2017-03-22 |
Family
ID=58304312
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620951375.0U Active CN206037634U (en) | 2016-08-27 | 2016-08-27 | Continuous drying device of paddle desiccator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206037634U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115479461A (en) * | 2021-06-16 | 2022-12-16 | 天华化工机械及自动化研究设计院有限公司 | Degradable plastic degradation drying process and system |
-
2016
- 2016-08-27 CN CN201620951375.0U patent/CN206037634U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115479461A (en) * | 2021-06-16 | 2022-12-16 | 天华化工机械及自动化研究设计院有限公司 | Degradable plastic degradation drying process and system |
| CN115479461B (en) * | 2021-06-16 | 2024-03-01 | 天华化工机械及自动化研究设计院有限公司 | Degradation drying process and system for degradable plastic |
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|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |