CN220689627U

CN220689627U - Colloidal particle drying device

Info

Publication number: CN220689627U
Application number: CN202322382052.7U
Authority: CN
Inventors: 邓应邦
Original assignee: Foshan Fengzheng Technology Co ltd
Current assignee: Foshan Fengzheng Technology Co ltd
Priority date: 2023-09-04
Filing date: 2023-09-04
Publication date: 2024-03-29
Anticipated expiration: 2033-09-04

Abstract

The utility model relates to the technical field of rubber additive masterbatch processing, in particular to a colloidal particle drying device, a drying box, wherein a drying mechanism is arranged in the drying box, an auxiliary component is arranged outside the drying box, the drying mechanism comprises a storage hopper fixedly connected with the drying box, an electromagnetic valve corresponding to the storage hopper in position is fixedly connected to the inner top wall of the drying box, a stirring component is arranged on the left side of the drying box, and a heating box and an air pump are fixedly connected to the right side of the drying box. This micelle drying device, through setting up drying mechanism, for micelle drying device increase circulation dry function, improved the drying efficiency to rubber auxiliary agent masterbatch, reduced thermal waste, saved the drying cost to rubber auxiliary agent masterbatch, solved not possess circulation dry function, influenced the drying efficiency to rubber auxiliary agent masterbatch, and caused thermal waste easily, increased micelle drying device's use cost's problem.

Description

Colloidal particle drying device

Technical Field

The utility model relates to the technical field of rubber auxiliary agent masterbatch processing, in particular to a colloidal particle drying device.

Background

The rubber auxiliary agent causes vulcanization of natural rubber, and after eighty years of research, the rubber auxiliary agent does not basically form a system until 20 th century to 30 th, along with industrialization of a basic variety of a vulcanization accelerator, namely 2-mercaptobenzothiazole, a second sulfonamide derivative and a p-phenylenediamine anti-aging agent. The rubber auxiliary agent is in a stable period, and the yield of the two main organic auxiliary agents, namely the vulcanization accelerator and the anti-aging agent, is about 4 percent of the consumption of raw rubber.

At present, in the production and processing of rubber auxiliary agent master batch, a rubber particle drying device is required to be used for drying the rubber auxiliary agent master batch.

Please refer to a rubber granule high-efficient desiccator of bulletin number CN207317423U, including first frame and second frame, first frame and second frame parallel arrangement, the inboard lower extreme of first frame is provided with the motor, the output shaft of motor has the speed reducer, the cover is equipped with first belt pulley on the output shaft of speed reducer, first belt pulley passes through the belt and is connected with the second belt pulley, the second belt pulley is installed in the one end of pivot.

However, the patent has a defect that the drying efficiency of the rubber auxiliary agent master batch is affected because the drying function is not provided, heat is easily wasted, and the use cost of the colloidal particle drying device is increased.

Disclosure of Invention

Aiming at the defects of the prior art, the utility model provides the colloidal particle drying device which has the advantages of cyclic drying, high efficiency, energy saving and the like, and solves the problems that the drying efficiency of rubber auxiliary agent master batch is affected, heat is wasted easily, and the use cost of the colloidal particle drying device is increased because the colloidal particle drying device does not have the function of cyclic drying.

In order to achieve the above purpose, the present utility model provides the following technical solutions: the colloidal particle drying device comprises a drying box, wherein a drying mechanism is arranged inside the drying box, and an auxiliary component is arranged outside the drying box;

the drying mechanism comprises a storage hopper fixedly connected with a drying box, an electromagnetic valve corresponding to the storage hopper is fixedly connected to the inner top wall of the drying box, a stirring assembly is arranged on the left side of the drying box, a heating box and an air pump are fixedly connected to the right side of the drying box, and an air inlet pipe is fixedly connected to the right side of the heating box;

the drying mechanism further comprises a filter screen fixedly connected with the air inlet pipe, the inside of the heating box is fixedly connected with a molecular sieve and a heating pipe, the input end of the air pump is fixedly connected with a first exhaust pipe fixedly connected with the drying box, the output end of the air pump is fixedly connected with a second exhaust pipe fixedly connected with the heating box, and the bottom of the drying box is fixedly connected with a discharge valve.

Optionally, the feed inlet has been seted up at the top of drying cabinet, the solenoid valve is linked together with the storage hopper through the feed inlet.

Through adopting above-mentioned technical scheme, conveniently carry out the material loading to micelle drying device, reduce thermal loss.

Optionally, the stirring subassembly includes variable speed motor, first gear, second gear and puddler, first gear and second gear engagement, the puddler is located the inside of drying cabinet.

By adopting the technical scheme, the drying efficiency and the drying effect of the rubber auxiliary agent master batch are improved, and the drying time of the rubber auxiliary agent master batch is saved.

Optionally, an air inlet is formed in the right side of the heating box, and the air inlet pipe is communicated with the heating box through the air inlet.

Through adopting above-mentioned technical scheme, make things convenient for the air inlet of micelle drying device, dry through hot air rubber auxiliary agent masterbatch.

Optionally, a vent hole corresponding to the position of the heating box is formed in the right side of the drying box, and the heating box is communicated with the drying box through the vent hole.

By adopting the technical scheme, the hot air is utilized to dry the rubber auxiliary agent, so that the drying efficiency of the rubber auxiliary agent master batch is improved.

Optionally, an air suction hole is formed in the top of the drying box, and the first air suction pipe is communicated with the drying box through the air suction hole.

Through adopting above-mentioned technical scheme, carry out circulation drying to rubber auxiliary agent masterbatch, improve the drying efficiency to rubber auxiliary agent masterbatch, reduce thermal waste.

Optionally, a discharging hole is formed in the bottom of the drying box and is communicated with the drying box through the discharging valve and the discharging hole.

By adopting the technical scheme, the dried rubber auxiliary master batch is conveniently recovered, and the next processing is conveniently carried out.

Further, auxiliary assembly includes with drying cabinet fixed connection and quantity is two temperature sensor, the top fixedly connected with treater of heating cabinet.

By adopting the technical scheme, the rubber auxiliary agent master batch is conveniently dried at constant temperature, and the drying cost of the rubber auxiliary agent master batch is saved.

Compared with the prior art, the technical scheme of the application has the following beneficial effects:

1. this micelle drying device, through setting up drying mechanism, for micelle drying device increase circulation dry function, improved the drying efficiency to rubber auxiliary agent masterbatch, reduced thermal waste, saved the drying cost to rubber auxiliary agent masterbatch, solved not possess circulation dry function, influenced the drying efficiency to rubber auxiliary agent masterbatch, and caused thermal waste easily, increased micelle drying device's use cost's problem.

2. This micelle drying device through setting up auxiliary assembly, conveniently carries out constant temperature drying to rubber auxiliary agent masterbatch, has saved the drying cost to rubber auxiliary agent masterbatch.

Drawings

FIG. 1 is a cross-sectional view of the structure of the present utility model;

fig. 2 is a front view of the structure of the present utility model.

In the figure: 1. a drying box; 101. a feed inlet; 102. an air suction hole; 103. a vent hole; 104. a discharge port; 2. a storage hopper; 3. an electromagnetic valve; 4. a stirring assembly; 401. a variable speed motor; 402. a first gear; 403. a second gear; 404. a stirring rod; 5. a heating box; 501. an air inlet; 6. an air inlet pipe; 7. a filter screen; 8. a molecular sieve; 9. heating pipes; 10. an air pump; 11. a first exhaust pipe; 12. a second exhaust pipe; 13. a discharge valve; 14. a temperature sensor; 15. a processor.

Detailed Description

The following description of the embodiments of the present utility model will be made clearly and completely with reference to the accompanying drawings, in which it is apparent that the embodiments described are only some embodiments of the present utility model, but not all embodiments. All other embodiments, which can be made by those skilled in the art based on the embodiments of the utility model without making any inventive effort, are intended to be within the scope of the utility model.

Referring to fig. 1-2, a colloidal particle drying apparatus in this embodiment includes a drying box 1, a drying mechanism is disposed inside the drying box 1, and an auxiliary component is disposed outside the drying box 1.

In this embodiment, the drying mechanism includes the storage hopper 2 with drying cabinet 1 fixed connection, and the interior roof fixedly connected with of drying cabinet 1 is with the corresponding solenoid valve 3 of storage hopper 2 position, and feed inlet 101 has been seted up at the top of drying cabinet 1, and solenoid valve 3 is linked together with storage hopper 2 through feed inlet 101. The inside rubber auxiliary agent master batch material that has been deposited of storage hopper 2, solenoid valve 3 open, and the inside rubber auxiliary agent master batch material of storage hopper 2 gets into the inside of drying cabinet 1 through feed inlet 101 and solenoid valve 3.

Wherein, the left side of drying cabinet 1 is provided with stirring subassembly 4, and stirring subassembly 4 includes gear motor 401, first gear 402, second gear 403 and puddler 404, and first gear 402 and the output fixed connection of gear motor 401, first gear 402 and second gear 403 meshing, puddler 404 are located the inside of drying cabinet 1. The variable speed motor 401 is electrified to drive the first gear 402 and the second gear 403 to rotate, and the stirring rod 404 is driven to stir the rubber auxiliary agent master batch material in the drying oven 1, so that the rubber auxiliary agent master batch material in the drying oven 1 is heated more uniformly, and the drying efficiency and the drying effect of the rubber auxiliary agent master batch are improved. The right side fixedly connected with heating cabinet 5 and air pump 10 of drying cabinet 1, air pump 10 are located the top of heating cabinet 5, and the right side fixedly connected with intake pipe 6 of heating cabinet 5, intake pipe 6 are connected with outside air pump output.

Wherein, drying mechanism still includes with intake pipe 6 fixed connection's filter screen 7, air inlet 501 has been seted up on the right side of heating cabinet 5, and intake pipe 6 is linked together with heating cabinet 5 through air inlet 501. The inside control valve that is provided with of intake pipe 6, dust and impurity in the filter screen 7 filtration air, control valve open, the outside air of heating cabinet 5 gets into inside the heating cabinet 5 through intake pipe 6 after the filtration of filter screen 7.

Wherein, molecular sieve 8 and heating pipe 9 are fixedly connected with in the inside of heating cabinet 5, and air vent 103 corresponding with the position of heating cabinet 5 is seted up on the right side of drying cabinet 1, and heating cabinet 5 is linked together with drying cabinet 1 through air vent 103. The heating pipe 9 in the heating box 5 is electrified to generate heat, the air entering the heating box 5 is heated, and the heated hot air enters the drying box 1 through the vent hole 103 to dry the rubber auxiliary agent master batch material.

Specifically, the input fixedly connected with of air pump 10 is with dry 1 fixed connection's first exhaust tube 11, the output fixedly connected with of air pump 10 is with 5 fixed connection's of heating cabinet second exhaust tube 12, and the gas vent 102 has been seted up at the top of dry 1, and first exhaust tube 11 is linked together with dry 1 through gas vent 102. The air pump 10 is electrified, hot air in the drying box 1 is pumped out through the first exhaust pipe 11, the pumped hot air is conveyed to the inside of the heating box 5 through the second exhaust pipe 12, after the molecular sieve 8 filters water vapor in the hot air, the hot air reenters the inside of the drying box 1, the rubber auxiliary agent master batch material is circularly dried, the heat waste is reduced, and the energy is saved.

Wherein, the bottom of the drying oven 1 is fixedly connected with a discharge valve 13. A discharge port 104 is arranged at the bottom of the drying box 1 and is communicated with the drying box 1 through the discharge port 104 by a discharge valve 13. The discharge valve 13 is opened, and the rubber auxiliary agent master batch material which is dried in the drying oven 1 is discharged through the discharge valve 13, so that the rubber auxiliary agent master batch material can be conveniently subjected to the next process.

It is to be noted that, through setting up drying mechanism, increase the dry function of circulation for micelle drying device, improved the drying efficiency to rubber auxiliary agent masterbatch, reduced the waste of heat, saved the drying cost to rubber auxiliary agent masterbatch, solved and not possess the dry function of circulation, influenced the drying efficiency to rubber auxiliary agent masterbatch, and caused the waste of heat easily, increased the problem of micelle drying device's use cost.

In this embodiment, the auxiliary assembly includes two temperature sensors 14 fixedly connected to the drying oven 1, and a processor 15 is fixedly connected to the top of the heating oven 5. The processor 15 comprises a signal receiving and transmitting module, a processing module and a control module, the temperature sensor 14 and the heating pipe 9 are connected with the processor 15 in a signal mode, the temperature sensor 14 monitors the temperature change inside the drying box 1 and sends temperature information to the processor 15, when the temperature inside the drying box 1 reaches a set temperature, the processor 15 enables the heating pipe 9 to be powered off and stops heating, and when the temperature inside the drying box 1 is lower than the set temperature, the processor 15 enables the heating pipe 9 to be powered on and re-heats air entering the drying box 1.

It is to be noted that, through setting up auxiliary assembly, the convenience carries out constant temperature drying to rubber auxiliary agent masterbatch, has saved the drying cost to rubber auxiliary agent masterbatch.

The working principle of the embodiment is as follows:

this micelle drying device, when needs carry out the drying to rubber auxiliary agent masterbatch, the air pump 10 circular telegram, with the drying cabinet 1 with the inside air extraction of heating cabinet 5, make drying cabinet 1 and the inside negative pressure that is in of heating cabinet 5, solenoid valve 3 opens, the inside of the inside rubber auxiliary agent masterbatch material of hopper 2 gets into the inside of drying cabinet 1 through feed inlet 101 and solenoid valve 3, the outside air of heating cabinet 5 gets into inside the heating cabinet 5 through intake pipe 6 after the filtration of filter screen 7, then, the heating pipe 9 circular telegram of heating cabinet 5 inside produces the heat, heat the inside air heating of entering heating cabinet 5, the hot air after the heating, get into the inside of drying cabinet 1 through air vent 103 and carry out the drying to rubber auxiliary agent masterbatch material, simultaneously, the air pump is through the inside hot air extraction of first exhaust tube 11 with the drying cabinet 1, and carry the inside of heating cabinet 5 through the second exhaust tube 12, after the steam that the steam in the steam of molecular sieve 8 to the steam filters, the inside of drying cabinet 1 reentry, thereby reach the work function that increases circulation drying for micelle drying device, carry out circulation drying to rubber auxiliary agent masterbatch material, improve the efficiency to rubber auxiliary agent masterbatch, the drying efficiency, the drying cost is saved to masterbatch.

It is noted that relational terms such as first and second, and the like are used solely to distinguish one entity or action from another entity or action without necessarily requiring or implying any actual such relationship or order between such entities or actions. Moreover, the terms "comprises," "comprising," or any other variation thereof, are intended to cover a non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements does not include only those elements but may include other elements not expressly listed or inherent to such process, method, article, or apparatus. Without further limitation, an element defined by the phrase "comprising one … …" does not exclude the presence of other like elements in a process, method, article, or apparatus that comprises the element.

Although embodiments of the present utility model have been shown and described, it will be understood by those skilled in the art that various changes, modifications, substitutions and alterations can be made therein without departing from the principles and spirit of the utility model, the scope of which is defined in the appended claims and their equivalents.

Claims

1. The utility model provides a micelle drying device, includes drying cabinet (1), its characterized in that: a drying mechanism is arranged inside the drying box (1), and an auxiliary component is arranged outside the drying box (1);

the drying mechanism comprises a storage hopper (2) fixedly connected with a drying box (1), an electromagnetic valve (3) corresponding to the storage hopper (2) in position is fixedly connected to the inner top wall of the drying box (1), a stirring assembly (4) is arranged on the left side of the drying box (1), a heating box (5) and an air pump (10) are fixedly connected to the right side of the drying box (1), and an air inlet pipe (6) is fixedly connected to the right side of the heating box (5);

the drying mechanism further comprises a filter screen (7) fixedly connected with the air inlet pipe (6), a molecular sieve (8) and a heating pipe (9) are fixedly connected to the inside of the heating box (5), a first exhaust pipe (11) fixedly connected with the drying box (1) is fixedly connected to the input end of the air pump (10), a second exhaust pipe (12) fixedly connected with the heating box (5) is fixedly connected to the output end of the air pump (10), and a discharge valve (13) is fixedly connected to the bottom of the drying box (1).

2. A colloidal particle drying apparatus as claimed in claim 1, characterized in that: the top of the drying box (1) is provided with a feed inlet (101), and the electromagnetic valve (3) is communicated with the storage hopper (2) through the feed inlet (101).

3. A colloidal particle drying apparatus as claimed in claim 1, characterized in that: the stirring assembly (4) comprises a variable speed motor (401), a first gear (402), a second gear (403) and a stirring rod (404), wherein the first gear (402) is meshed with the second gear (403), and the stirring rod (404) is located inside the drying oven (1).

4. A colloidal particle drying apparatus as claimed in claim 1, characterized in that: an air inlet (501) is formed in the right side of the heating box (5), and the air inlet pipe (6) is communicated with the heating box (5) through the air inlet (501).

5. A colloidal particle drying apparatus as claimed in claim 1, characterized in that: the right side of the drying box (1) is provided with a vent hole (103) corresponding to the position of the heating box (5), and the heating box (5) is communicated with the drying box (1) through the vent hole (103).

6. A colloidal particle drying apparatus as claimed in claim 1, characterized in that: the top of the drying box (1) is provided with an air suction hole (102), and the first air suction pipe (11) is communicated with the drying box (1) through the air suction hole (102).

7. A colloidal particle drying apparatus as claimed in claim 1, characterized in that: the bottom of the drying box (1) is provided with a discharge hole (104) which is communicated with the drying box (1) through a discharge valve (13) and the discharge hole (104).

8. A colloidal particle drying apparatus as claimed in claim 1, characterized in that: the auxiliary assembly comprises two temperature sensors (14) fixedly connected with the drying box (1), and a processor (15) is fixedly connected to the top of the heating box (5).