CN218065798U - Tower type particle material drying equipment - Google Patents

Abstract

The utility model discloses a tower granule class material drying equipment, including vertical drying barrel, drying barrel is including vertical structure's riser, as shown in the figure, the riser is the structure of cylinder, and the feed inlet is seted up in the upper end of riser, the lower extreme is seted up to the discharge gate, the inside of riser is provided with helical structure's spiral pipe, a plurality of exhaust vents that are less than the particulate matter external diameter are evenly seted up along the plumb line direction to the spiral pipe, the spiral pipe is connected with the air heater, the air outlet and the spiral pipe intercommunication of air heater, and supply hot-blast to the inside of spiral pipe, the inside of hot-blast follow every exhaust vent afterwards, and blow hot-blast to the granule surface of free whereabouts in-process, increase particulate matter drying effect, simultaneously under by lower supreme atmospheric pressure effect, be convenient for with the quick discharge of the moisture of bottom.

Description

Tower type particle material drying equipment

Technical Field

The utility model relates to a dry field of tower granule especially relates to a tower granule class material drying equipment.

Background

The drying is to gasify moisture (moisture or other solvents) in wet materials by using heat energy, and take away the gasified moisture by using air flow or vacuum, thereby obtaining the operation of drying the materials.

SUMMERY OF THE UTILITY MODEL

In order to overcome prior art's is not enough, the utility model provides a tower granule class material drying equipment, the exhaust vent of the formula of running through of seting up through the spiral pipe that sets up and spiral pipe surface, the exhaust vent is connected with the air heater, the air heater is when supplying wind to the spiral pipe, the exhaust vent blows hot-blastly to the particulate matter, the dry-type drying of wind increases inside particulate matter surface and hot-blast contact effect, simultaneously, is convenient for accelerate outside the discharge with the moisture of bottom.

In order to solve the technical problem, the utility model provides a following technical scheme: the utility model provides a tower granule class material drying equipment, includes vertical drying barrel, drying barrel is including vertical structure's riser, the inside of riser is provided with helical structure's spiral pipe, a plurality of exhaust vents that are less than the particulate matter external diameter are evenly seted up along the plumb line direction to the spiral pipe, the spiral pipe is connected with the air heater, feed inlet, discharge gate have been seted up respectively at the both ends of riser, the top of feed inlet is provided with the quantitative conveyer to riser ration pay-off.

As a preferred technical scheme of the utility model, the drying barrel is still including being connected the tuber pipe that just link up with the spiral pipe, tuber pipe open-ended one end is connected with the air outlet of air heater.

As a preferred technical scheme of the utility model, quantitative conveyer is including the shell of cylinder dress structure, set up at inside and the rotatable roller bearing of shell, the roller bearing outer wall annular distribution has a plurality of recesses, the feed opening of run-through type is radially seted up to the shell outer wall, two feed opening one end is connected with the feed inlet, the axial one end of roller bearing is provided with the motor.

As a preferred technical scheme of the utility model, the motor is servo motor.

As an optimized technical scheme of the utility model, the exhaust fan has been seted up to the riser near one side of feed inlet.

As an optimized technical scheme of the utility model, the upper end the hopper that is trapezoidal structure is installed to the feed opening.

Compared with the prior art, the utility model discloses the beneficial effect that can reach is:

1. through the exhaust vent of the formula of running through that sets up on the spiral pipe and spiral pipe surface, the exhaust vent is connected with the air heater, and the air heater is when supplying wind to the spiral pipe, and the exhaust vent blows hot-blastly to the particulate matter, and the dry-type drying of wind increases inside particulate matter surface and hot-blast contact effect, simultaneously, is convenient for accelerate outside the discharge with the moisture of bottom.

Drawings

FIG. 1 is a schematic view of the present invention;

fig. 2 is a schematic cross-sectional structure diagram of the present invention;

fig. 3 is an enlarged schematic structural view of a point a in fig. 2 according to the present invention;

FIG. 4 is a schematic view of the spiral tube structure of the present invention;

FIG. 5 is a schematic view of the stand pipe structure of the present invention;

fig. 6 is a schematic structural view of the quantitative conveyor of the present invention;

fig. 7 is a schematic view of the explosion structure of the quantitative conveyor of the present invention.

Wherein:

1. drying the barrel; 11. a riser; 111. a feed inlet; 112. a discharge port; 12. a spiral tube; 121. an air outlet; 13. an air duct;

2. a quantitative conveyor; 21. a housing; 211. a feeding port; 22. a roller; 221. a groove; 23. a motor; 24. a hopper;

3. a hot air blower;

4. an exhaust fan.

Detailed Description

In order to make the technical means, creation features, achievement objects and functions of the present invention easy to understand, the present invention will be further explained with reference to the following embodiments, however, the following embodiments are only preferred embodiments of the present invention, and not all embodiments are included. Based on the embodiments in the embodiment, those skilled in the art can obtain other embodiments without making creative efforts, and all of them belong to the protection scope of the present invention. The experimental methods in the following examples are conventional methods unless otherwise specified, and materials, reagents and the like used in the following examples are commercially available unless otherwise specified.

Example (b):

as shown in fig. 1-7, the utility model provides a tower granule class material drying equipment, including vertical drying barrel 1, drying barrel 1 is including vertical structure's riser 11, as shown in fig. 1, riser 11 is the structure of cylinder, and feed inlet 111 sets up the upper end at riser 11 (as the upper end in fig. 5), discharge gate 112 sets up at the lower extreme, the inside of riser 11 is provided with helical structure's spiral pipe 12, spiral pipe 12 has evenly seted up a plurality of exhaust vents 121 that are less than the particulate matter external diameter along the plumb line direction, spiral pipe 12 is connected with air heater 3, air heater 3's air outlet and spiral pipe 12 intercommunication, and supply hot-blast to the inside of spiral pipe 12, hot-blast inside discharge from every exhaust vent 121 afterwards, and blow hot-blast to the particle surface of free whereabouts in-process, increase particulate matter drying effect, simultaneously under the atmospheric pressure effect from lower supreme, be convenient for with the quick discharge of the moisture of bottom, feed inlet 111 has been seted up respectively at the both ends of riser 11, discharge gate 112, the top of feed inlet 111 is provided with quantitative conveyer 2 to the quantitative pay-off of riser 11, realize the inside ration of riser 11, avoid the unloading granule not even.

Preferably, the drying barrel 1 further comprises an air pipe 13 connected with and communicated with the spiral pipe 12, an open end of the air pipe 13 is connected with an air outlet of the air heater 3, as shown in fig. 2-4, the air pipe 13 is communicated with the spiral pipe 12, the air pipe 13 is connected with the air outlet of the air heater 3, the air pipe 13 is supplied with air through the air heater 3, the air pipe 13 supplies air to the inside of the spiral pipe 12, and finally, the surface of the particulate matter is dried through the air outlet 121.

Preferably, the quantitative conveyor 2 includes a housing 21 having a cylindrical structure, and a rotatable roller 22 disposed inside the housing 21, a plurality of grooves 221 are annularly distributed on an outer wall of the roller 22, a through-type feed opening 211 is radially formed in an outer wall of the housing 21, one end of each of the two feed openings 211 is connected to the feed opening 111, a motor 23 is disposed at one axial end of the roller 22, the motor 23 is a servo motor, as shown in fig. 6 and 7, the housing 21 has a horizontal cylindrical structure, an outer wall of the roller 22 is attached to a wall of the housing 21 and is rotatable, under the driving of the motor 23, when the grooves 221 filled with particles are filled with the particles, the roller rotates, the roller moves to the feed opening 211 at the lower end and quantitatively feeds the particles into the interior of the vertical pipe 11 through the feed opening 111, and the motor 23 is preferably a servo motor, so as to set a rotation frequency according to the number of the grooves 221 opened.

Preferably, the side of the vertical pipe 11 close to the feeding hole 111 is provided with an exhaust fan 4, as shown in fig. 1, the exhaust fan 4 is provided on the side of the vertical pipe 11 close to the feeding hole 111, and when the exhaust fan 4 operates, the exhaust fan exhausts air outwards to accelerate the discharge of moisture in the vertical pipe 11.

Preferably, the hopper 24 with a ladder-shaped structure is installed at the upper end feed opening 211, and as shown in fig. 1, the hopper 24 with a ladder-shaped structure with a wide upper part and a narrow lower part is installed above the upper end feed opening 211, so as to facilitate the feeding of the particles.

The utility model discloses when using, add the particulate matter in the inside of hopper 24, rotate as motor 23, and make the opening of recess 221 towards behind the 24 bottom discharge ends of hopper, under the action of gravity, the particulate matter fills up recess 221, motor 23 drives roller bearing 22 afterwards, and make this recess 221 rotate to the top of feed inlet 111, the inside that riser 11 was dropped to this moment granule under the action of gravity, and roll to discharge gate 112's direction along spiral pipe 12's orbit direction, and meanwhile, hot-air blower 3 circular telegram operation, to tuber pipe 13 air feed, tuber pipe 13 is to spiral pipe 12's inside air feed, dry through blowing out vent 121 to the surface of particulate matter at last, hot-blast that hot-air blower 3 provided, make air outlet 121 department equipartition atmospheric pressure increase, the violent degree of rolling of particulate matter has been increased simultaneously, and then improve dry effect, simultaneously by supreme air-out, under the cooperation of exhaust fan 4 is quick, be convenient for discharge inside moisture.

In the present application, unless expressly stated or limited otherwise, the recitation of a first feature "on" or "under" a second feature may include the recitation of the first and second features being in direct contact, and may also include the recitation of the first and second features not being in direct contact, but being in contact with another feature between them. Also, the first feature being "on," "above" and "over" the second feature includes the first feature being directly on and obliquely above the second feature, or merely indicating that the first feature is at a higher level than the second feature. A first feature being "under," "below," and "beneath" a second feature includes the first feature being directly under and obliquely below the second feature, or simply meaning that the first feature is at a lesser elevation than the second feature.

The foregoing shows and describes the basic principles, essential features, and advantages of the invention. It should be understood by those skilled in the art that the present invention is not limited by the above embodiments, and the description in the above embodiments and the description is only preferred examples of the present invention, and is not intended to limit the present invention, and that the present invention can have various changes and modifications without departing from the spirit and scope of the present invention, and these changes and modifications all fall into the scope of the claimed invention. The scope of the invention is defined by the appended claims and equivalents thereof.

Claims (6)

1. The utility model provides a tower granule class material drying equipment which characterized in that: including vertical drying bucket (1), drying bucket (1) is including riser (11) of vertical structure, the inside of riser (11) is provided with helical structure's spiral pipe (12), a plurality of exhaust vents (121) that are less than the particulate matter external diameter are evenly seted up along the plumb line direction in spiral pipe (12), spiral pipe (12) are connected with air heater (3), feed inlet (111), discharge gate (112) have been seted up respectively to the both ends of riser (11), the top of feed inlet (111) is provided with quantitative conveyer (2) to riser (11) ration pay-off.

2. The tower type drying equipment for granular materials according to claim 1, wherein: the drying barrel (1) further comprises an air pipe (13) which is connected with the spiral pipe (12) and is communicated with the spiral pipe, and one open end of the air pipe (13) is connected with an air outlet of the air heater (3).

3. The tower type drying equipment for the granular materials according to claim 1, characterized in that: quantitative conveyer (2) including shell (21) that cylinder dress structure, set up at inside and rotatable roller bearing (22) of shell (21), roller bearing (22) outer wall annular distribution has a plurality of recesses (221), run through type feed opening (211) are radially seted up to shell (21) outer wall, two feed opening (211) one end is connected with feed inlet (111), the axial one end of roller bearing (22) is provided with motor (23).

4. The tower type drying equipment for the granular materials according to claim 3, characterized in that: the motor (23) is a servo motor.

5. The tower type drying equipment for granular materials according to claim 1, wherein: an exhaust fan (4) is arranged on one side of the vertical pipe (11) close to the feed inlet (111).

6. The tower type drying equipment for granular materials according to claim 3, characterized in that: the upper end feed opening (211) is installed and is hopper (24) that the ladder type structure.

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