CN107906920A - For the dryer group containing low melting point solvent, the wet mash of solid-like - Google Patents
For the dryer group containing low melting point solvent, the wet mash of solid-like Download PDFInfo
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- CN107906920A CN107906920A CN201711074187.XA CN201711074187A CN107906920A CN 107906920 A CN107906920 A CN 107906920A CN 201711074187 A CN201711074187 A CN 201711074187A CN 107906920 A CN107906920 A CN 107906920A
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- vacuum
- tank body
- main tank
- feeding
- distributing device
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B15/00—Machines or apparatus for drying objects with progressive movement; Machines or apparatus with progressive movement for drying batches of material in compact form
- F26B15/10—Machines or apparatus for drying objects with progressive movement; Machines or apparatus with progressive movement for drying batches of material in compact form with movement in a path composed of one or more straight lines, e.g. compound, the movement being in alternate horizontal and vertical directions
- F26B15/12—Machines or apparatus for drying objects with progressive movement; Machines or apparatus with progressive movement for drying batches of material in compact form with movement in a path composed of one or more straight lines, e.g. compound, the movement being in alternate horizontal and vertical directions the lines being all horizontal or slightly inclined
- F26B15/18—Machines or apparatus for drying objects with progressive movement; Machines or apparatus with progressive movement for drying batches of material in compact form with movement in a path composed of one or more straight lines, e.g. compound, the movement being in alternate horizontal and vertical directions the lines being all horizontal or slightly inclined the objects or batches of materials being carried by endless belts
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- 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
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C19/00—Other disintegrating devices or methods
- B02C19/18—Use of auxiliary physical effects, e.g. ultrasonics, irradiation, for disintegrating
- B02C19/186—Use of cold or heat for disintegrating
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B1/00—Preliminary treatment of solid materials or objects to facilitate drying, e.g. mixing or backmixing the materials to be dried with predominantly dry solids
- F26B1/005—Preliminary treatment of solid materials or objects to facilitate drying, e.g. mixing or backmixing the materials to be dried with predominantly dry solids by means of disintegrating, e.g. crushing, shredding, milling the materials to be dried
-
- 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
- F26B23/00—Heating arrangements
- F26B23/10—Heating arrangements using tubes or passages containing heated fluids, e.g. acting as radiative elements; Closed-loop systems
-
- 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
-
- 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
- F26B5/00—Drying solid materials or objects by processes not involving the application of heat
- F26B5/04—Drying solid materials or objects by processes not involving the application of heat by evaporation or sublimation of moisture under reduced pressure, e.g. in a vacuum
- F26B5/041—Drying solid materials or objects by processes not involving the application of heat by evaporation or sublimation of moisture under reduced pressure, e.g. in a vacuum for drying flowable materials, e.g. suspensions, bulk goods, in a continuous operation, e.g. with locks or other air tight arrangements for charging/discharging
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B5/00—Drying solid materials or objects by processes not involving the application of heat
- F26B5/04—Drying solid materials or objects by processes not involving the application of heat by evaporation or sublimation of moisture under reduced pressure, e.g. in a vacuum
- F26B5/048—Drying solid materials or objects by processes not involving the application of heat by evaporation or sublimation of moisture under reduced pressure, e.g. in a vacuum in combination with heat developed by electro-magnetic means, e.g. microwave energy
Abstract
It is used for the dryer group containing low melting point solvent, the wet mash of solid-like the present invention relates to a kind of, dryer group includes：Vacuum belt drier, vacuum belt drier include cross direction profiles and closed main tank body, it is characterised in that：The feeding mouth of the main tank body front end is connected through the first sealing valve with the bottom discharge mouth of a granulator, and the top feeding mouth of granulator is connected through the second sealing valve with the bottom discharge mouth of a vacuum feeding tank；It is connected with pulverizer, the 3rd sealing valve, discharging intermediate bin on the discharge port of the main tank body rear end in turn；It is connected with and vacuumizes and solvent recovering system on the exhaust outlet of the main tank body.The feeding mouth of the neighbouring main tank body and the microwave applicator for being used for that the material on distributing device and neighbouring conveyer belt front end to be dried is equipped with above the distributing device, the inner side anteroposterior direction of the conveyer belt is successively equipped with the steam heater, hot-water heater and cooler with conveyer belt parallel distribution.
Description
Technical field
The present invention relates to the field that drying equipment and wet mash are dried, more particularly to one kind is multi-functional, environment-friendly and energy-efficient is true
Blanking bar formula dryer group and application the unit powder drying means, in particular for containing low melting point solvent, solid-like it is wet
The dryer group of powder.
Background technology
The existing drying equipment for powder, there are certain security risk；Reason is the powder in air in drying process
Bulk concentration reaches certain proportion, just easily meets naked light and explodes.Therefore how to powder drying process, powder is reduced or avoided
The generation of dirt, and then ensure production safety, it is this area technical barrier to be solved.
The content of the invention
Done the technical problem to be solved in the present invention is to provide a kind of vacuum belt drier group and using the powder of the unit
Drying method, to solve the technical problem of powder drying process safety.
In order to solve the above technical problem, the present invention provides a kind of vacuum belt drier group, including：Vacuum belt is done
Dry machine, vacuum belt drier include cross direction profiles and closed main tank body, and the feeding mouth of the main tank body front end is through the first sealing
Valve is connected with the bottom discharge mouth of a granulator, bottom of the top feeding mouth through the second sealing valve Yu a vacuum feeding tank of granulator
Portion's discharge port is connected；It is connected with pulverizer, the 3rd sealing valve, discharging intermediate bin on the discharge port of the main tank body rear end in turn；
It is connected with and vacuumizes and solvent recovering system on the exhaust outlet of the main tank body.Wherein, connect and crush on the discharge port of main tank body
Machine so that pulverizer can be implemented to crush under vacuum conditions so that can directly be packed, avoided from the product of pulverizer output
Secondary pollution, moisture absorption, it is ensured that the aridity of product, and secondary operation is not required, simplify production process.
Distributing device is equipped with the main tank body and below the feeding mouth, is equipped with below the discharge end of the distributing device front and rear
Directional spreding, for sending the material entered from the main tank body feeding mouth to the conveyer belt of main tank body discharge port.Distributing device
Front and rear vibration and the dustpan body of inclined downward backward during including a job.Dustpan body is used to spread out material plastochondria, makes its thickness
It is uniformly distributed, while the material thickness for making to fall within conveyer belt is uniformly distributed, beneficial to dry abundant.Further preferred scheme
It is that conveyer belt uses chain drive, to solve the problems, such as that traditional conveyer belt causes guipure to wander off using roller transmission, fundamentally solves
The problem of guipure of having determined is rectified a deviation.
As the preferred of drying part, the feeding mouth of the neighbouring main tank body and be equipped with the distributing device above for pair
The microwave applicator that material on distributing device and neighbouring conveyer belt front end is dried, before the inner side of the conveyer belt
Rear direction is equipped with steam heater, hot-water heater and cooler with conveyer belt parallel distribution successively.Microwave applicator is used for
First time heating is carried out with microwave mode, moisture evaporated, gasified from inside to outside from material plastochondria, is then added using steam
Hot device, hot-water heater carry out second, heating and insulation respectively, make moisture evaporation, the gasification of material mitochondrial surface, and then make water
Divide the volatilization from material plastochondria from inside to outside, realize fully dry；Finally, material is cooled down through cooler, and cooling can make material
Particle shortcakeization, convenient follow-up crushing；The material of cooling is not easy to moisture absorption at the same time, it is ensured that the aridity of final products.Steam heater
Temperature determined according to the factor such as solvent-laden boiling point of institute in material characteristic, material, by controlling vapor (steam) temperature, in main tank body
The speed of material thickness and conveyer belt in vacuum, conveyer belt, to realize dry requirement.
The steam heater, hot-water heater and the preferred plate heat exchanger of cooler（It is small, efficient）, it is also optional
With the heat exchanger tube of snakelike planar alignment.
It is described to vacuumize and solvent recovering system includes：The condensate cooler that is connected with the exhaust outlet of the main tank body, with
Roots's water ring vacuum pump that the exhaust outlet of the condensate cooler is connected；The neighbouring exhaust ports in the main tank body of condensate cooler
Equipped with liquid blocker；The leakage fluid dram being connected with a recycling design tank is respectively equipped with the main tank body in the front and rear side of the liquid blocker.
The top vent of the vacuum feeding tank is connected by exhaust pipe with the main tank body of the vacuum belt drier,
Feed pipe and blow-down pipe are connected with the vacuum feeding tank；The 4th sealing valve is respectively equipped with exhaust pipe, feed pipe and blow-down pipe.
Strainer is equipped with the vacuum feeding tank and in place opposite with the interface of the exhaust pipe and blow-down pipe（It is preferred that sintered meshwork, can keep away
Omit bits phenomenon）, for preventing that travel fatigue in vacuum feeding tank, impurity from passing through the exhaust pipe and blow-down pipe is discharged；Work as emptying
When blow valve air on pipe implements emptying blanking, external air flow is directly blown by blow-down pipe, cleans strainer, it is not necessary to is separately set
Filter screen cleaning system, has purified device structure.
The main tank body of the vacuum belt drier be equipped with safety valve, visor, sterilizing gases input port, for
Spray water in main tank body to clean the water purification water connector of main inner tank wall；And the bottom of main tank body is equipped with sewage draining exit, the sewage draining exit
It is equipped with valve.
The liquid blocker includes：The waveform that the multi-disc parallel spaced-apart being fixed on the air flow path in the tower body is set
Plate, distributing alternately on the two sides of each corrugated sheet has multiple blend stops, and in hook-shaped, the concave surface of blend stop is adjacent with entrance for the section of blend stop
Airflow direction between corrugated sheet is opposite, for making air-flow produce cyclone, and then extends the residence time of air-flow, makes itself and waveform
Plate comes into full contact with heat exchange, improves condensation effect；The height of blend stop is less than the gap of adjacent corrugated sheet, prevents from blocking air-flow.
In order to increase the quantity, the frequency and the density that produce cyclone, and generate big cyclone and small cyclone, the blend stop include according to
The big blend stop and small blend stop of secondary alternate setting, big blend stop are arranged at the top of the circular arc of the neighbouring corrugated sheet, and small blend stop is arranged on adjacent
The big blend stop of a pair between.Big blend stop and small blend stop generate large and small cyclone respectively, and the large and small cyclone generated is adjacent, can improve
The density of cyclone, and then further improve condensation effect.
The powder drying means of above-mentioned vacuum belt drier group, it includes, and powder to be dried is used vacuum handling side
Formula is sent into vacuum feeding tank, is then fed into granulator and material plastochondria of the diameter in 3-20mm is made, then through vacuum belt type drying
After machine drying, crush and obtained through dry powder through pulverizer；Wherein, the biography in the main tank body of neighbouring vacuum belt drier
Send with the microwave applicator being equipped with above front end for material to be dried, the inner side anteroposterior direction of the conveyer belt is successively
Equipped with the steam heater, hot-water heater and cooler with conveyer belt parallel distribution；Using microwave applicator, with microwave mode
First time heating is carried out, moisture evaporated, gasified from inside to outside from material plastochondria, then using steam heater, hot water
Heater carries out second of heating and insulation respectively, makes moisture evaporation, the gasification of material mitochondrial surface；Finally, material is through cooling
Device cools down, so that material particles shortcakeization, embrittlement, beneficial to crushing.If without supercooling, temperature of charge is higher and material plastochondria is overall
It is softer, it is not easy to crush.
Above-mentioned powder drying means, further includes, and under the action of Roots's water ring vacuum pump, hot steam enters cold in main tank body
Solidifying cooler；Air-flow passes through between the corrugated sheet that the multi-disc parallel spaced-apart in liquid blocker is set, and in the two sides of each corrugated sheet
On the multiple end faces to distribute alternately be in hook-shaped blend stop under the action of, air-flow produce cyclone；Solvent warp and waveform in air-flow
Condensed after plate contact, and enter recycling design tank from the leakage fluid dram of recycling design pot bottom；In the main tank body and in it is described enter
The distributing device of front and rear vibration when being equipped with work below material mouth, the discharge end lower section of the distributing device are equipped with conveyer belt；Distributing device includes
One front and rear vibration when working and the backward dustpan body of inclined downward.
It is in negative pressure state in main tank body under the action of Roots's water ring vacuum pump during feeding（So that water, organic solvent
Boiling point is relatively low, beneficial to drying）, the control valve that vacuum feeding tank is connected on the pipeline of the main tank body opens, you can makes in vacuum
Batch can feeding, while the blow valve on the blow-down pipe of vacuum feeding tank is closed, then the inlet valve on vacuum feeding tank is beaten
Drive simultaneously feeding；When inlet amount reaches preset value, first sealing valve, inlet valve and control valve are closed, and then control second is close
Seal valve and blow valve to open, be in normal pressure at this time in vacuum feeding tank since the inner cavity of granulator is in negative pressure state, vacuum feeding tank
In material quickly sucked granulator and carry out a machine（Blanking efficiency is provided, avoids material ready-made in vacuum feeding tank
Bridging or wall built-up phenomenon, it can be ensured that material falls completely within granulator）, after the completion of granulation, the second sealing valve is closed successively, opens the
One sealing valve, material plastochondria are fallen into distributing device.
The invention has the advantages that（1）The vacuum belt drier group of the present invention, by powder to be dried through mechanism of pelletizing
Grain, after vacuum belt drier is dried, crushes through pulverizer and obtains through dry powder.Powder drying will not produce powder
Dirt, has discharged the security incident caused by dust is possible, and drying process security is higher.（2）Using microwave applicator, with microwave
Mode carries out first time heating, moisture evaporated, gasified from inside to outside from material plastochondria, then using steam heater,
Hot-water heater carries out second and heats and keep the temperature, and the moisture of material mitochondrial surface fully evaporated, gasified, whole process makes water
Divide the volatilization from material plastochondria from inside to outside, realize fully dry；Finally, material is cooled down through cooler, and cooling can make material
Particle shortcakeization, convenient follow-up crushing；The material of cooling is not easy to moisture absorption at the same time, instant packed and be not easy the moisture absorption in packaging process,
Ensure the aridity of final products.The use of microwave heating, relative to only with steam heater, hot-water heater and cooler
Combination, dry materials degree can lift 20-50%.
Brief description of the drawings
The present invention is further described with reference to the accompanying drawings and examples.
Fig. 1 shows the functional block diagram of vacuum belt drier group；
Fig. 2 shows the structure diagram of vacuum belt drier；
Fig. 3 shows the structure diagram of vacuum feeding component；
Fig. 4 shows the pulverizer being sequentially connected on the discharge port of the main tank body rear end, the 3rd sealing valve, discharging intermediate bin
Structure diagram；
Fig. 5 shows described vacuumize and the structure diagram of solvent recovering system；
Fig. 6 shows the structure diagram of a pair of adjacent corrugated sheet in the liquid blocker；
Fig. 7 shows the top view of the liquid blocker；
Fig. 8 shows the A direction views of the liquid blocker.
Embodiment
In conjunction with the accompanying drawings, the present invention is further explained in detail.These attached drawings are simplified schematic diagram, only with
Illustration illustrates the basic structure of the present invention, therefore it only shows composition related to the present invention.
Embodiment 1
Vacuum belt drier group includes：Vacuum belt drier, vacuum belt drier include cross direction profiles and closed master
Tank body 1, the feeding mouth of 1 front end of main tank body are connected through the first sealing valve 101 with the bottom discharge mouth of a granulator 2, granulator 2
Top feeding mouth be connected through the second sealing valve 102 with the bottom discharge mouth of a vacuum feeding tank 3；1 rear end of main tank body
It is connected with pulverizer 4, the 3rd sealing valve 103, discharging intermediate bin 105 on discharge port in turn；The top vent of the main tank body 1
On be connected with and vacuumize and solvent recovering system.
Distributing device 7 is equipped with the main tank body 1 and below the feeding mouth, is equipped with below the discharge end of the distributing device 7
Anteroposterior direction distribution, for sending the material entered from the feeding mouth of the main tank body 1 to the conveyer belt of main tank body discharge port
100.Distributing device 7 includes front and rear vibration and the dustpan body of inclined downward backward during a job.Dustpan body is used to spread material plastochondria
Open, be uniformly distributed its thickness, while the material thickness for making to fall within conveyer belt is uniformly distributed, beneficial to dry abundant.
The feeding mouth of the neighbouring main tank body 1 and it is equipped with the distributing device 7 above on distributing device 7 and adjacent
The microwave applicator 8 that material on the front end of nearly conveyer belt 100 is dried, the inner side anteroposterior direction of the conveyer belt 100
The steam heater 11, hot-water heater 12 and cooler 13 with conveyer belt parallel distribution are equipped with successively.Microwave applicator 8 is used for
First time heating is carried out with microwave mode, moisture evaporated, gasified from inside to outside from material plastochondria, is then added using steam
Hot device 11, hot-water heater 12 carry out the second heating and insulation respectively, make moisture evaporation, the gasification of material mitochondrial surface, and then
Make the volatilization of moisture from material plastochondria from inside to outside, realize fully dry；Finally, material is cooled down through cooler 13, and cooling can
Make material particles shortcakeization, convenient follow-up crushing；The material of cooling is not easy to moisture absorption at the same time, it is ensured that the aridity of final products.
1 phase of main tank body that the top vent of the vacuum feeding tank 3 passes through exhaust pipe and the vacuum belt drier
Even, feed pipe and blow-down pipe are connected with the vacuum feeding tank；During feeding, under the action of Roots's water ring vacuum pump 62, main tank
It is in negative pressure state in body 1（So that the boiling point of water, organic solvent is relatively low, beneficial to drying）, vacuum feeding tank 3 connects the main tank body
Control valve 107 on 1 pipeline 106 is opened, you can and vacuum feeding tank 3 is implemented feeding, while by the emptying of vacuum feeding tank 3
Blow valve 108 on pipe is closed, and the inlet valve 109 on vacuum feeding tank 3 then is opened simultaneously feeding；When inlet amount reaches preset value
When, first sealing valve 101, inlet valve 109 and control valve 107 are closed, and then control the second sealing valve 102 and blow valve
108 open, and are in normal pressure at this time in vacuum feeding tank 3 since the inner cavity of granulator 2 is in negative pressure state, the thing in vacuum feeding tank 3
Material is quickly sucked granulator 2 and carries out a machine（Provide blanking efficiency, avoid material in vacuum feeding tank it is ready-made bridging or
Wall built-up phenomenon, it can be ensured that material falls completely within granulator）, after the completion of granulation, the second sealing valve 102 is closed successively, opens first
Sealing valve 101, material plastochondria are fallen into the distributing device 7 in main tank body 1.
The main tank body 1 be equipped with safety valve 110, visor 111, sterilizing gases input interface 112, for main tank
Spray water in vivo to clean the water purification water connector 113 of main inner tank wall；The bottom of main tank body 1 is equipped with sewage draining exit 114, the sewage draining exit
It is equipped with valve.
It is described to vacuumize and solvent recovering system 6 includes：The condensate cooler being connected with the exhaust outlet of the main tank body 1
61st, the Roots's water ring vacuum pump 62 being connected with the exhaust outlet of the condensate cooler 61；Condensate cooler 61 it is laterally setting, adopt
Liquid blocker 63 is equipped with the neighbouring exhaust ports in the tower body of spacer water cooling；In the front and rear side of the liquid blocker 63 in the tower body
It is respectively equipped with the leakage fluid dram being connected with a recycling design tank 64.
The liquid blocker 63 includes：The waveform that the multi-disc parallel spaced-apart being fixed on the air flow path in the tower body is set
Plate 630, it is in hook-shaped blend stop 631, the concave surface of blend stop 631 and entrance that distributing alternately on the two sides of each corrugated sheet, which has multiple sections,
Airflow direction between adjacent corrugated sheet 630 is opposite, and cyclone is produced for making to enter the air-flow in adjacent corrugated sheet 630, and then
Extend the residence time of air-flow, it is come into full contact with heat exchange with corrugated sheet 630, improve condensation effect；The height of blend stop 631 is less than
The gap of adjacent corrugated sheet, prevents from blocking air-flow.
In order to increase the quantity, the frequency and the density that produce cyclone, and generate big cyclone and small cyclone, the blend stop include according to
The big blend stop and small blend stop of secondary alternate setting, big blend stop are arranged at the top of the circular arc of the neighbouring corrugated sheet, and small blend stop is arranged on adjacent
The big blend stop of a pair between.Big blend stop and small blend stop generate large and small cyclone respectively, and the large and small cyclone generated is adjacent, can improve
The density of cyclone, and then further improve condensation effect.
The steam heater, hot-water heater and the preferred plate heat exchanger of cooler（It is small, efficient）, it is also optional
With the heat exchanger tube of snakelike planar alignment.
Strainer is equipped with the vacuum feeding tank and in place opposite with the interface of the exhaust pipe and blow-down pipe（It is preferred that sinter
Net, can avoid bits phenomenon）, for preventing that travel fatigue in vacuum feeding tank, impurity from passing through the exhaust pipe and blow-down pipe is discharged；
When the blow valve air on blow-down pipe implements emptying blanking, external air flow is directly blown by blow-down pipe, cleans strainer, is not required to
Filter screen cleaning system is separately set, has purified device structure.
Main tank ground, to prevent security risk that electrostatic may be brought, avoids electrostatic dust, inflammable in main tank body
Explosive solvent forms dangerous；Main tank body is equipped with explosion relief valve.
Embodiment 2
The powder drying means of vacuum belt drier group described in above-described embodiment 1, it includes, by powder to be dried using true
Empty mode of movement is sent into vacuum feeding tank 3, is then fed into granulator 2 and material plastochondria of the diameter in 3-20mm is made, then through true
After empty band drier drying, crush and obtained through dry powder through pulverizer.
Wherein, be equipped with above the conveyer belt front end in the main tank body 1 of neighbouring vacuum belt drier be used for material into
The dry microwave applicator 8 of row, the inner side anteroposterior direction of the conveyer belt 100 are equipped with and 100 parallel distribution of conveyer belt successively
Steam heater 11, hot-water heater 12 and cooler 13；Using microwave applicator 8, first time heating is carried out with microwave mode,
Moisture evaporated, gasified from inside to outside from material plastochondria, then using steam heater 11, hot-water heater 12 respectively into
Second of heating of row and insulation, make moisture evaporation, the gasification of material mitochondrial surface；Finally, material is cooled down through cooler 13, so that
Material particles shortcakeization.
Above-mentioned powder drying means, further includes, under the action of Roots's water ring vacuum pump 62, in main tank body 1 hot steam into
Enter condensate cooler 6；Air-flow passes through between the corrugated sheet 630 that the multi-disc parallel spaced-apart in liquid blocker 63 is set, and in each waveform
The multiple end faces to distribute alternately on the two sides of plate 630 are in air-flow generation cyclone under the action of hook-shaped blend stop 631；Air-flow
In vapor, solvent condenses after being contacted with corrugated sheet 630, and enters recycling design from the leakage fluid dram of recycling design pot bottom
Tank 64；The distributing device 7 of front and rear vibration, the distributing device in the main tank body 1 and when being equipped with work below the feeding mouth of main tank body 1
Conveyer belt 100 is equipped with below 7 discharge end；Distributing device 7 includes front and rear vibration and the dustpan body of inclined downward backward during a job,
Using cylinder and linkage driving dustpan body action.
It is complete by above-mentioned description, relevant staff using the above-mentioned desirable embodiment according to the present invention as enlightenment
Various changes and amendments can be carried out without departing from the scope of the technological thought of the present invention' entirely.The technology of this invention
Property scope is not limited to the content on specification, it is necessary to determines its technical scope according to right.
Claims (4)
1. a kind of multi-functional, environment-friendly and energy-efficient vacuum belt drier group, including：Vacuum belt drier, vacuum belt type drying
Machine includes cross direction profiles and closed main tank body, it is characterised in that：The feeding mouth of the main tank body front end is through the first sealing valve and one
The bottom discharge mouth of granulator is connected, bottom discharge of the top feeding mouth through the second sealing valve Yu a vacuum feeding tank of granulator
Mouth is connected；
It is connected with pulverizer, the 3rd sealing valve, discharging intermediate bin on the discharge port of the main tank body rear end in turn；
It is connected with and vacuumizes and solvent recovering system on the exhaust outlet of the main tank body.
2. multi-functional, environment-friendly and energy-efficient vacuum belt drier group according to claim 1, it is characterised in that the master
Distributing device is equipped with tank body and below the feeding mouth, conveyer belt is equipped with below the discharge end of the distributing device；Distributing device includes
One front and rear vibration when working and the backward dustpan body of inclined downward.
3. multi-functional, environment-friendly and energy-efficient vacuum belt drier group according to claim 1 or 2, it is characterised in that described
Multi-functional, environment-friendly and energy-efficient vacuum belt drier group powder drying means, including, by powder to be dried using vacuum it is defeated
Send mode to be sent into vacuum feeding tank, be then fed into granulator and material plastochondria of the diameter in 3-20mm is made, then through vacuum belt
After drying machine drying, crush and obtained through dry powder through pulverizer；
Wherein, it is equipped with above the conveyer belt front end in the main tank body of neighbouring vacuum belt drier and is used to material be dried
Microwave applicator, the inner side anteroposterior direction of the conveyer belt is equipped with steam heater with conveyer belt parallel distribution, heat successively
Water heater and cooler；Using microwave applicator, first time heating is carried out with microwave mode, make moisture from material plastochondria by
Interior and nonlocal evaporation, gasification, then carry out second of heating and insulation using steam heater, hot-water heater, make thing respectively
Expect moisture evaporation, the gasification of mitochondrial surface；Finally, material is cooled down through cooler, so that material particles shortcakeization.
4. dryer group according to claim 3, it is characterised in that：Under the action of Roots's water ring vacuum pump, main tank body
Interior hot steam enters condensate cooler；Air-flow passes through between the corrugated sheet that the multi-disc parallel spaced-apart in liquid blocker is set, and each
The multiple end faces to distribute alternately on the two sides of corrugated sheet are in air-flow generation cyclone under the action of hook-shaped blend stop；In air-flow
Solvent condensed after being contacted with corrugated sheet, and enter recycling design tank from the leakage fluid dram of recycling design pot bottom；
The distributing device of front and rear vibration, the discharge end of the distributing device in the main tank body and when being equipped with work below the feeding mouth
Lower section is equipped with conveyer belt；Distributing device includes front and rear vibration and the dustpan body of inclined downward backward during a job；
Wherein, during feeding, under the action of Roots's water ring vacuum pump, interior main tank body is in negative pressure state, and vacuum feeding tank connects institute
The control valve stated on the pipeline of main tank body is opened, you can make vacuum feeding tank feeding, while by the blow-down pipe of vacuum feeding tank
Blow valve close, then by vacuum feeding tank inlet valve open and feeding；When inlet amount reaches preset value, described first
Sealing valve, inlet valve and control valve are closed, and then control the second sealing valve and blow valve to open, since the inner cavity of granulator is in negative
Pressure condition, is in normal pressure at this time in vacuum feeding tank, and the material in vacuum feeding tank is quickly sucked granulator and carries out a machine, is made
After the completion of grain, the second sealing valve is closed successively, opens the first sealing valve, material plastochondria is fallen into distributing device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711074187.XA CN107906920A (en) | 2014-11-10 | 2014-11-10 | For the dryer group containing low melting point solvent, the wet mash of solid-like |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410628905.3A CN105651006B (en) | 2014-11-10 | 2014-11-10 | Multi-functional, environment-friendly and energy-efficient vacuum belt drier group and its powder drying means |
| CN201711074187.XA CN107906920A (en) | 2014-11-10 | 2014-11-10 | For the dryer group containing low melting point solvent, the wet mash of solid-like |
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| CN201410628905.3A Division CN105651006B (en) | 2014-11-10 | 2014-11-10 | Multi-functional, environment-friendly and energy-efficient vacuum belt drier group and its powder drying means |
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| CN107906920A true CN107906920A (en) | 2018-04-13 |
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| CN201410628905.3A Active CN105651006B (en) | 2014-11-10 | 2014-11-10 | Multi-functional, environment-friendly and energy-efficient vacuum belt drier group and its powder drying means |
| CN201711074180.8A Pending CN107894156A (en) | 2014-11-10 | 2014-11-10 | Heated using microwave, the dryer group that security is higher |
| CN201711074187.XA Pending CN107906920A (en) | 2014-11-10 | 2014-11-10 | For the dryer group containing low melting point solvent, the wet mash of solid-like |
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| CN201711074180.8A Pending CN107894156A (en) | 2014-11-10 | 2014-11-10 | Heated using microwave, the dryer group that security is higher |
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| CN110487028A (en) * | 2019-08-08 | 2019-11-22 | 铜陵有色金属集团股份有限公司 | The drying means and drying system of the decopper(ing) earth of positive pole |
| CN114812100A (en) * | 2021-01-27 | 2022-07-29 | 永虹先进材料股份有限公司 | Mineral dewatering equipment and process |
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| CN111174556A (en) * | 2020-02-12 | 2020-05-19 | 中国科学院理化技术研究所 | Vacuum belt drying system |
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Also Published As
| Publication number | Publication date |
|---|---|
| CN107894156A (en) | 2018-04-10 |
| CN105651006A (en) | 2016-06-08 |
| CN105651006B (en) | 2017-11-17 |
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Application publication date: 20180413 |