CN218955241U

CN218955241U - Vertical cooling device for bio-organic fertilizer particles

Info

Publication number: CN218955241U
Application number: CN202223364145.9U
Authority: CN
Inventors: 常军强
Original assignee: Baofeng Changjiang Biological Technology Co ltd
Current assignee: Baofeng Changjiang Biological Technology Co ltd
Priority date: 2022-12-15
Filing date: 2022-12-15
Publication date: 2023-05-02
Anticipated expiration: 2032-12-15

Abstract

The utility model relates to a bio-organic fertilizer particle vertical cooling device, a rotary support ring is sleeved in a main bearing ring, the bottom of the rotary support ring is connected with a middle blanking buffer device, a lower inclined blanking plate matched with three-quarter inner wall of a vertical barrel is fixedly arranged in the vertical barrel below the middle blanking buffer device, a lower bottom sealing plate matched with the inner wall of the vertical barrel and the lower inclined blanking plate is fixedly arranged at the bottom of the lower inclined blanking plate, an inclined blanking plate ventilation hole is also formed in the lower inclined blanking plate, a lower fan is fixedly arranged on the inner wall of the vertical barrel between the lower inclined blanking plate and the lower bottom sealing plate, the lower fan is communicated with a lower blast pipe arranged on the outer wall of the vertical barrel, and a material gathering hopper communicated with a discharge hole is fixedly arranged on the inner wall of the vertical barrel below the lower bottom sealing plate; the buffering blanking structure of upper portion, middle part and lower part has been set up, and whole area is little, make full use of vertical space to it is different with traditional bottom blowing blanking operation that the structure is complicated, overall structure sets up simply, easily operation and equipment, with low costs and easy realization.

Description

Vertical cooling device for bio-organic fertilizer particles

Technical Field

The utility model relates to a cooling device, in particular to a vertical cooling device for bio-organic fertilizer particles.

Background

The biological organic fertilizer is a fertilizer which is formed by compounding microorganism with specific functions and organic materials which mainly take animal and plant residues as sources and are subjected to innocent treatment and decomposition. Beneficial microorganisms in the biological organic fertilizer enter soil and then form a mutual symbiotic proliferation relation with the microorganisms in the soil, so that the growth of harmful bacteria is restrained, and the beneficial bacteria are converted into the beneficial bacteria, interact and promote each other to play a role in group synergism, and the beneficial bacteria generate a large amount of metabolites in the growth and reproduction process, so that the decomposition and conversion of organic matters are promoted, various nutrition and stimulation substances can be directly or indirectly provided for crops, and the growth of the crops is promoted and regulated.

The preparation process of the bio-organic fertilizer generally starts from fermentation, and after the fermentation is successful, the powdery organic fertilizer or the granular organic fertilizer is obtained through subsequent processing treatment. The granular organic fertilizer is prepared by granulating, drying, cooling and sieving on the basis of the powdery organic fertilizer. After the drying operation is finished, a large amount of moisture and heat exist in the particles, and the particles need to be cooled in time so as to timely discharge the excessive moisture and heat and smoothly enter the next process flow.

In the above operation, the cooling of the traditional bio-organic fertilizer particles is generally implemented by adopting a free blanking mode of a vertical barrel, and the air cooling blowing operation is matched during blanking, but the traditional air cooling device has certain defects, and the defects are concentrated in: firstly, in order to reduce the effective air cooling time of material falling, a horizontal transverse air cooling device is adopted, the occupied area of the device is large, the air cooling effect is low, so that a vertical barrel with higher height is generally adopted to implement free falling air cooling operation, the peripheral outer wall of the bottom of the barrel is communicated with a blower, the blowing direction of the blower faces the axial position of the barrel and is inclined upwards, a plurality of fans are required to be installed in the traditional air cooling operation mode, the installation position of the fans has stronger requirements, the operation must be carried out in the circumferential direction of the barrel, air outlets are required to be arranged obliquely upwards, the overall barrel is higher, the fan installation and arrangement operation is more difficult, the elimination operation of humidity and temperature can be realized only by the stronger air supply operation of the fans, the overall energy consumption is higher, the barrel arrangement is more difficult, and a certain production difficulty exists; secondly, the traditional air-cooling operation particles basically fall from top to bottom, then air cooling is carried out, the whole blanking speed is high, the phenomenon that air-cooling operation is incomplete exists, and even if some equipment adopts a mode that blanking is slowly carried out by a blanking plate, the blanking plate can only play a simple buffering operation and can not provide support for efficient operation of the air-cooling operation.

Therefore, the biological organic fertilizer particle vertical cooling device is simple in structure, convenient to operate, moderate in overall height, small in longitudinal space occupation, simple and convenient to install and arrange, free of high-strength support and complex feeding operation, capable of reducing air cooling difficulty, improving sealing efficiency, even in material blanking buffering, capable of being matched with air cooling operation for use while buffering blanking, even and thorough in air cooling effect, and wide in market prospect.

Disclosure of Invention

Aiming at the defects of the prior art, the utility model provides the bio-organic fertilizer particle vertical cooling device which has the advantages of simple structure, convenient operation, moderate overall height, less longitudinal space occupation, simple installation and arrangement, no need of high-strength support and complex feeding operation, reduction of air cooling difficulty, improvement of sealing efficiency, uniform material blanking buffering, and uniform and thorough air cooling effect, is matched with the air cooling operation while buffering blanking, and is used for overcoming the defects in the prior art.

The technical scheme of the utility model is realized as follows: the vertical cooling device for the bio-organic fertilizer particles comprises a vertical barrel, a feed inlet arranged at the top of the vertical barrel, a discharge outlet arranged at the bottom of the vertical barrel, an air draft dehumidification opening arranged at the center of the top of the vertical barrel, an upper inclined blanking plate matched with three-quarters inner wall of the vertical barrel and fixedly arranged in the vertical barrel below the feed inlet, an upper bottom sealing plate matched with the inner wall of the vertical barrel and the upper inclined blanking plate and fixedly arranged at the bottom of the upper inclined blanking plate, an air ventilation hole of the inclined blanking plate is formed in the upper inclined blanking plate, an upper fan is fixedly arranged on the inner wall of the vertical barrel between the upper inclined blanking plate and the upper bottom sealing plate and communicated with an upper air supply pipe arranged on the outer wall of the vertical barrel, a main bearing ring is fixedly arranged on the inner wall of the vertical barrel below the upper bottom sealing plate, the main bearing ring is sleeved with a rotary supporting ring, the bottom of the rotary supporting ring is connected with a middle blanking buffer device, a lower inclined blanking plate matched with the inner wall of three quarters of the inner wall of the vertical barrel is fixedly arranged in the vertical barrel below the middle blanking buffer device, a lower bottom sealing plate matched with the inner wall of the vertical barrel and the lower inclined blanking plate is fixedly arranged at the bottom of the lower inclined blanking plate, an inclined blanking plate ventilation hole is also formed in the lower inclined blanking plate, a lower fan is fixedly arranged on the inner wall of the vertical barrel between the lower inclined blanking plate and the lower bottom sealing plate, the lower fan is communicated with a lower air supply pipe arranged on the outer wall of the vertical barrel, and a material gathering hopper communicated with a discharge hole is fixedly arranged on the inner wall of the vertical barrel below the lower bottom sealing plate.

The middle blanking buffer device comprises a middle buffering blanking funnel connected with the bottom of a rotary supporting ring, a side ventilation hole is formed in the middle buffering blanking funnel, a gear ring is fixedly arranged on the outer wall of the rotary supporting ring below a main bearing ring, the outer side of the gear ring is meshed with a driving gear arranged on the inner wall of a vertical barrel, the lower part of the driving gear is fixedly connected with the output end of a gear motor, a middle fan is fixedly arranged on the inner wall of the vertical barrel and symmetrically positioned with the output end of the gear motor, the middle fan is communicated with a middle air supply pipe arranged on the outer wall of the vertical barrel, and the air outlet direction of the middle fan horizontally faces the middle lower part of the middle buffering blanking funnel.

The upper inclined blanking plate is of a three-quarter circular sheet structure, the diameter of the upper inclined blanking plate is matched with the diameter of the inner wall of the vertical barrel, the upper inclined blanking plate is obliquely arranged on the inner wall of the vertical barrel, the included angle between the upper inclined blanking plate and the horizontal plane is 15-30 degrees, the arc-shaped edge of the top of the upper inclined blanking plate is located below the feeding port, the bottom edge of the upper inclined blanking plate is of a flush structure, the lower part of the flush structure is fixedly connected with one side of the upper bottom sealing plate, the upper bottom sealing plate is of a two-thirds circular sheet structure, the diameter of the upper bottom sealing plate is matched with the diameter of the inner wall of the vertical barrel, the upper bottom sealing plate is horizontally arranged on the inner wall of the vertical barrel, and the air outlet direction of the upper fan horizontally faces the axis of the vertical barrel.

The lower part slope blanking plate be with upper portion slope blanking plate shape and the equal three-quarter circular sheet structure of size, the diameter of lower part slope blanking plate cooperatees with the diameter of upright barrel inner wall, lower part slope blanking plate slope sets up at upright barrel inner wall, the contained angle of lower part slope blanking plate and horizontal plane is 15 to 30 degrees, the bottom edge position of lower part slope blanking plate is the parallel and level form structure, the lower part of this parallel and level form structure and one side fixed connection of lower part bottom closing plate, the lower part bottom closing plate is with the equal two-thirds circular sheet structure of upper portion bottom closing plate shape and size, lower part bottom closing plate diameter cooperatees with the diameter of upright barrel inner wall, the horizontal level of lower part bottom closing plate sets up at upright barrel inner wall, the air-out direction level of lower part fan is towards the axle center of upright barrel.

The top outer wall of the material gathering bucket is fixedly connected with the inner wall of the vertical bucket, the bottom opening of the material gathering bucket is connected with the top opening of the discharge hole, the inner diameter of the bottom wall of the material gathering bucket is equal to the inner diameter of the top of the discharge hole, the included angle between the bottom of the material gathering bucket and the horizontal plane is 45 degrees, the top opening of the material gathering bucket is communicated with one side of the bottom of the lower bottom sealing plate, the reinforcing support ring is fixedly mounted on the outer side of the middle part of the vertical bucket, the supporting legs are fixedly mounted on the outer wall of the reinforcing support ring, the mounting position of the reinforcing support ring is located on the outer wall of the vertical bucket below the main bearing ring, and the air suction and dehumidification fan is mounted in the air suction and dehumidification hole.

The rotary support ring is of a circular annular structure, the outer wall of the rotary support ring is fixedly connected with the inner side rotary body of the main bearing ring, the outer side rotary body of the main bearing ring is fixedly connected with the inner wall of the vertical barrel, the length of the rotary support ring is not less than that of the main bearing ring, the gear ring is fixedly arranged on the outer wall of the lower portion of the rotary support ring, the middle of the rotary support ring is communicated with the top of the middle buffer blanking funnel, the bottom of the middle buffer blanking funnel is provided with a funnel blanking opening, the bottom of the funnel blanking opening is connected with the middle position of the top surface of the lower inclined blanking plate, and the plane where the bottom surface of the blanking opening is located above the plane where the bottom surface of the middle fan is located.

The inner diameter of the rotary supporting ring is equal to the inner diameter of the top of the middle buffer blanking funnel, a vertical line extension line between the bottom edge position of the upper inclined blanking plate and the horizontal plane is positioned in the inner diameter of the rotary supporting ring, a transfer inclined blanking plate matched with three-fourths inner walls of the vertical barrel is fixedly arranged between the bottom of the upper bottom sealing plate and the top of the rotary supporting ring, a transfer bottom sealing plate matched with the inner walls of the vertical barrel and the transfer inclined blanking plate is fixedly arranged at the bottom of the transfer inclined blanking plate, an inclined blanking plate ventilation hole is also formed in the transfer inclined blanking plate, a transfer fan is fixedly arranged on the inner wall of the vertical barrel between the transfer inclined blanking plate and the transfer bottom sealing plate, and the transfer fan is communicated with a transfer blast pipe arranged on the outer wall of the vertical barrel.

The utility model provides a three-quarter circular sheet structure that the slope blanking plate that transship is equal with upper portion slope blanking plate shape and size, the diameter of slope blanking plate that transship cooperatees with the diameter of upright bucket inner wall, slope setting of transship slope blanking plate is at upright bucket inner wall, the contained angle of slope blanking plate that transship and horizontal plane is 15 to 30 degrees, the bottom edge position of slope blanking plate that transship is the parallel and level form structure, the lower part of this parallel and level form structure and one side fixed connection of transship bottom closing plate, the transship bottom closing plate is with the two-thirds circular sheet structure that upper portion bottom closing plate shape and size are equal, the diameter of transship bottom closing plate cooperatees with the diameter of upright bucket inner wall, the horizontal level of transship bottom closing plate sets up at upright bucket inner wall, the air-out direction level orientation of transship fan is towards the axle center of upright bucket.

The utility model has the following positive effects: firstly, the simple vertical air cooling device is different from the traditional horizontal air cooling device in that space can be saved, the blanking operation is realized by utilizing the dead weight of materials, the buffer blanking structures at the upper part, the middle part and the lower part are arranged for the product, the whole occupied area is small, the longitudinal space is fully utilized, the device is different from the traditional bottom air blowing blanking operation with complex structure, the device is simple in whole structure, easy to operate and assemble, low in cost and easy to realize; secondly, the self-weight falling feeding operation of the materials is realized by utilizing the structure of the buffer blanking, the air cooling, cooling and dehumidifying operation of the particles are realized by utilizing the transverse blowing operation at each buffer blanking structure position, the buffer blanking is matched with the top air draft and dehumidifying port, the heat energy and the moisture are rapidly brought out of the vertical barrel, the full air cooling operation of uniformly falling and scattering falling bio-organic fertilizer particles is realized while blanking, the whole air cooling effect is obvious, and the operation is rapid and efficient; and thirdly, the product adopts the effect of buffering blanking and air cooling simultaneously, the transfer operation is implemented in the middle part, the rotating middle part buffering blanking funnel is utilized to implement rotating dispersion on the bio-organic fertilizer particles buffered and cooled on the upper part, then the bio-organic fertilizer particles are sent to the lower part to continue to implement continuous air cooling operation, and the effect of material adhesion placing and uniform air cooling is realized in the middle part transfer process, so that the product is obviously different from the traditional air cooling device.

Drawings

Fig. 1 is a schematic front view of the present utility model.

Fig. 2 is a schematic left-view structure of the present utility model.

Fig. 3 is a right-side view of the present utility model.

Fig. 4 is a schematic view of the internal structure of the present utility model.

FIG. 5 is a schematic view of the cross-sectional structure of FIG. 4 at A-A in accordance with the present utility model.

FIG. 6 is a schematic view of the cross-sectional structure of the portion B-B in FIG. 4 according to the present utility model.

Detailed Description

As shown in fig. 1, 2, 3, 4, 5 and 6, the vertical cooling device for the bio-organic fertilizer particles comprises a vertical barrel 1, a feed inlet 9 arranged at the top of the vertical barrel 1, a discharge outlet 8 arranged at the bottom of the vertical barrel 1, an air draft and dehumidification opening 10 arranged at the center of the top of the vertical barrel 1, an upper inclined blanking plate 12 matched with three-quarters of the inner wall of the vertical barrel 1 and fixedly arranged in the vertical barrel 1 below the feed inlet 9, an upper bottom sealing plate 13 matched with the inner wall of the vertical barrel 1 and the upper inclined blanking plate 12 and fixedly arranged at the bottom of the upper inclined blanking plate 12, an inclined blanking plate ventilation hole 30 arranged on the upper inclined blanking plate 12, an upper fan 14 fixedly arranged on the inner wall of the vertical barrel 1 and positioned between the upper inclined blanking plate 12 and the upper bottom sealing plate 13, and an upper fan 14 communicated with an upper air supply pipe 5 arranged on the outer wall of the vertical barrel 1, a main bearing ring 18 is fixedly arranged on the inner wall of the vertical barrel 1 below the upper bottom sealing plate 13, a rotary supporting ring 19 is sleeved in the main bearing ring 18, the bottom of the rotary supporting ring 19 is connected with a middle blanking buffer device, a lower inclined blanking plate 26 matched with the inner wall of three quarters of the inner wall of the vertical barrel 1 is fixedly arranged in the vertical barrel 1 below the middle blanking buffer device, a lower bottom sealing plate 27 matched with the inner wall of the vertical barrel 1 and the lower inclined blanking plate 26 is fixedly arranged at the bottom of the lower inclined blanking plate 26, an inclined blanking plate ventilation hole 30 is also arranged on the lower inclined blanking plate 26, a lower fan 28 is fixedly arranged on the inner wall of the vertical barrel 1 between the lower inclined blanking plate 26 and the lower bottom sealing plate 27, the lower fan 28 is communicated with a lower air supply pipe 7 arranged on the outer wall of the vertical barrel 1, a material gathering bucket 29 communicated with the discharge hole 8 is fixedly arranged on the inner wall of the vertical barrel 1 below the lower bottom sealing plate 27. The middle blanking buffer device comprises a middle buffer blanking funnel 21 connected with the bottom of a rotary support ring 19, a side vent hole 24 is formed in the middle buffer blanking funnel 21, a gear ring 20 is fixedly arranged on the outer wall of the rotary support ring 19 below a main bearing ring 18, the outer side of the gear ring 20 is meshed with a driving gear 22 arranged on the inner wall of a vertical barrel 1, the lower side of the driving gear 22 is fixedly connected with the output end of a gear motor 23, a middle fan 25 is fixedly arranged on the inner wall of the vertical barrel 1 and symmetrically positioned with the output end of the gear motor 23, the middle fan 25 is communicated with a middle air supply pipe 6 arranged on the outer wall of the vertical barrel 1, and the air outlet direction of the middle fan 25 horizontally faces the middle lower portion of the middle buffer blanking funnel 21.

The upper inclined blanking plate 12 is of a three-quarter circular sheet structure, the diameter of the upper inclined blanking plate 12 is matched with the diameter of the inner wall of the vertical barrel 1, the upper inclined blanking plate 12 is obliquely arranged on the inner wall of the vertical barrel 1, the included angle between the upper inclined blanking plate 12 and the horizontal plane is 15-30 degrees, the top arc-shaped edge of the upper inclined blanking plate 12 is positioned below the feed inlet 9, the bottom edge of the upper inclined blanking plate 12 is of a flush structure, the lower part of the flush structure is fixedly connected with one side of the upper bottom sealing plate 13, the upper bottom sealing plate 13 is of a two-third circular sheet structure, the diameter of the upper bottom sealing plate 13 is matched with the diameter of the inner wall of the vertical barrel 1, the upper bottom sealing plate 13 is horizontally arranged on the inner wall of the vertical barrel 1, and the air outlet direction of the upper fan 14 horizontally faces the axis of the vertical barrel 1. The lower inclined blanking plate 26 is of a three-quarter round sheet structure equal to the upper inclined blanking plate 12 in shape and size, the diameter of the lower inclined blanking plate 26 is matched with the diameter of the inner wall of the vertical barrel 1, the lower inclined blanking plate 26 is obliquely arranged on the inner wall of the vertical barrel 1, an included angle between the lower inclined blanking plate 26 and a horizontal plane is 15-30 degrees, the bottom edge position of the lower inclined blanking plate 26 is of a flush structure, the lower part of the flush structure is fixedly connected with one side of a lower bottom sealing plate 27, the lower bottom sealing plate 27 is of a two-thirds round sheet structure equal to the upper bottom sealing plate 13 in shape and size, the diameter of the lower bottom sealing plate 27 is matched with the diameter of the inner wall of the vertical barrel 1, the lower bottom sealing plate 27 is horizontally arranged on the inner wall of the vertical barrel 1, and the air outlet direction of the lower fan 28 horizontally faces the axis of the vertical barrel 1. The top outer wall of the material gathering bucket 29 is fixedly connected with the inner wall of the vertical barrel 1, the bottom opening of the material gathering bucket 29 is connected with the top opening of the discharge hole 8, the inner diameter of the bottom wall of the material gathering bucket 29 is equal to the inner diameter of the top of the discharge hole 8, the included angle between the bottom of the material gathering bucket 29 and the horizontal plane is 45 degrees, the top opening of the material gathering bucket 29 is communicated with one side of the bottom of the lower bottom sealing plate 27, the reinforcing support ring 2 is fixedly arranged on the outer side of the middle of the vertical barrel 1, the supporting leg 3 is fixedly arranged on the outer wall of the reinforcing support ring 2, the mounting position of the reinforcing support ring 2 is positioned on the outer wall of the vertical barrel 1 below the main bearing ring 18, and the air draft dehumidification fan 11 is arranged in the air draft dehumidification hole 10.

The rotary support ring 19 is of a circular annular structure, the outer wall of the rotary support ring 19 is fixedly connected with the inner side rotary body of the main bearing ring 18, the outer side rotary body of the main bearing ring 18 is fixedly connected with the inner wall of the vertical barrel 1, the length of the rotary support ring 19 is not smaller than that of the main bearing ring 18, the gear ring 20 is fixedly arranged on the outer wall of the lower portion of the rotary support ring 19, the middle portion of the rotary support ring 19 is communicated with the top of the middle buffering blanking funnel 21, a funnel blanking opening 31 is arranged at the bottom of the middle buffering blanking funnel 21, the bottom of the funnel blanking opening 31 is connected with the middle position of the top surface of the lower inclined blanking plate 26, and the plane where the bottom surface of the blanking opening 31 is located above the plane where the bottom surface of the middle fan 25 is located. The inner diameter of the rotary support ring 19 is equal to the inner diameter of the top of the middle buffer blanking funnel 21, the extension line of the vertical line between the edge position of the bottom of the upper inclined blanking plate 12 and the horizontal plane is positioned in the inner diameter of the rotary support ring 19, a transfer inclined blanking plate 15 matched with three-quarters inner wall of the vertical barrel 1 is fixedly arranged between the bottom of the upper bottom sealing plate 13 and the top of the rotary support ring 19, a transfer bottom sealing plate 16 matched with the inner wall of the vertical barrel 1 and the transfer inclined blanking plate 15 is fixedly arranged at the bottom of the transfer inclined blanking plate 15, an inclined blanking plate ventilation hole 30 is also formed in the transfer inclined blanking plate 15, a transfer fan 17 is fixedly arranged on the inner wall of the vertical barrel 1 between the transfer inclined blanking plate 15 and the transfer bottom sealing plate 16, and the transfer fan 17 is communicated with a transfer air supply pipe 4 arranged on the outer wall of the vertical barrel 1. The transfer inclined blanking plate 15 is of a three-quarter round sheet structure equal to the upper inclined blanking plate 12 in shape and size, the diameter of the transfer inclined blanking plate 15 is matched with the diameter of the inner wall of the vertical barrel 1, the transfer inclined blanking plate 15 is obliquely arranged on the inner wall of the vertical barrel 1, an included angle between the transfer inclined blanking plate 15 and a horizontal plane is 15-30 degrees, the bottom edge position of the transfer inclined blanking plate 15 is of a flush structure, the lower part of the flush structure is fixedly connected with one side of a transfer bottom sealing plate 16, the transfer bottom sealing plate 16 is of a two-thirds round sheet structure equal to the upper bottom sealing plate 13 in shape and size, the diameter of the transfer bottom sealing plate 16 is matched with the diameter of the inner wall of the vertical barrel 1, the transfer bottom sealing plate 16 is horizontally arranged on the inner wall of the vertical barrel 1, and the air outlet direction of the transfer fan 17 is horizontally oriented to the axis of the vertical barrel 1.

When the biological organic fertilizer particle separator is used, biological organic fertilizer particles enter the inner wall of the vertical barrel 1 through the feeding hole 9, and are carried out and accepted through the upper inclined blanking plate 12, under the dead weight effect of the particles and under the wind force effect of the blowing operation of the upper fan 14, the materials are blanked through the upper inclined blanking plate 12 which is obliquely arranged, the air cooling operation is carried out on the biological organic fertilizer particle separator by utilizing wind force when blanking, after the particulate materials fall onto the transfer inclined blanking plate 15 from the lower end of the upper inclined blanking plate 12, the transfer fan 17 carries out air cooling and continuous blanking operation on the particulate materials, then the particulate materials fall into the middle buffer blanking hopper 21 from the lower end of the transfer inclined blanking plate 15, meanwhile, the driving gear 22 drives the gear ring 20 to rotate, the middle buffer blanking hopper 21 rotates at the inner side of the main bearing ring 18, the particles blanked from the lower end of the transfer inclined blanking plate 15 are driven to rotate, the particles blanked from the lower end of the transfer inclined blanking plate 26 are cooled by wind and the dead weight of the lower fan 28, the final biological organic fertilizer falls into the middle buffer blanking hopper 21 from the lower end of the transfer inclined blanking plate 15, and the moisture is continuously discharged from the moisture continuously in the biological organic fertilizer drum 1 through the transfer fan 8, and the moisture continuously discharged from the moisture continuously in the moisture continuously discharged portion of the biological organic fertilizer is discharged from the biological organic fertilizer drum 1 through the air separator 11, and the moisture continuously discharged from the moisture continuously in the biological organic fertilizer is discharged from the biological organic fertilizer drum 1, and the moisture continuously in the humidity 1, and the moisture is discharged into the moisture is discharged by the moisture and wet organic fertilizer.

Claims

1. The utility model provides a vertical cooling device of bio-organic fertilizer granule, includes upright bucket (1), installs feed inlet (9) at upright bucket (1) top, installs discharge gate (8) in upright bucket (1) bottom, its characterized in that: an exhaust dehumidifying port (10) is arranged in the center of the top of the vertical barrel (1), an upper inclined blanking plate (12) matched with three-quarters of the inner wall of the vertical barrel (1) is fixedly arranged in the vertical barrel (1) below the feeding port (9), an upper bottom sealing plate (13) matched with the inner wall of the vertical barrel (1) and the upper inclined blanking plate (12) is fixedly arranged at the bottom of the upper inclined blanking plate (12), an inclined blanking plate ventilation hole (30) is formed in the upper inclined blanking plate (12), an upper fan (14) is fixedly arranged on the inner wall of the vertical barrel (1) between the upper inclined blanking plate (12) and the upper bottom sealing plate (13), the upper fan (14) is communicated with an upper air supply pipe (5) arranged on the outer wall of the vertical barrel (1), a main bearing ring (18) is fixedly arranged on the inner wall of the vertical barrel (1) below the upper bottom sealing plate (13), a rotary supporting ring (19) is arranged on the main bearing ring (18), an inner sleeve (19) is arranged at the bottom of the rotary supporting ring (19) and is fixedly connected with the inner wall of the three-quarter of the vertical barrel (1) below the inner wall of the vertical barrel (1), the bottom of lower part slope blanking plate (26) fixed mounting have with erect barrel (1) inner wall and lower part slope blanking plate (26) matched with lower part bottom closing plate (27), also open on lower part slope blanking plate (26) and be equipped with slope blanking plate ventilation hole (30), it has lower fan (28) to lie in the barrel (1) inner wall fixed mounting between lower part slope blanking plate (26) and lower part bottom closing plate (27), lower fan (28) are linked together with lower blast pipe (7) that set up at the barrel (1) outer wall, it gathers together fill (29) to have the material that is linked together with discharge gate (8) to erect barrel (1) inner wall fixed mounting in lower part bottom closing plate (27) below.

2. The bio-organic fertilizer granule vertical cooling device according to claim 1, wherein: the middle blanking buffer device comprises a middle buffering blanking funnel (21) connected with the bottom of a rotary supporting ring (19), a side ventilation hole (24) is formed in the middle buffering blanking funnel (21), a gear ring (20) is fixedly arranged on the outer wall of the rotary supporting ring (19) below a main bearing ring (18), the outer side of the gear ring (20) is meshed with a driving gear (22) arranged on the inner wall of a vertical barrel (1), the lower side of the driving gear (22) is fixedly connected with the output end of a speed reducing motor (23), a middle fan (25) is fixedly arranged on the inner wall of the vertical barrel (1) at the symmetrical position of the output end of the speed reducing motor (23), and the middle fan (25) is communicated with a middle air supply pipe (6) arranged on the outer wall of the vertical barrel (1), and the air outlet direction of the middle fan (25) horizontally faces the middle lower part of the middle buffering blanking funnel (21).

3. The bio-organic fertilizer granule vertical cooling device according to claim 1, wherein: the upper inclined blanking plate (12) is of a three-quarter circular sheet structure, the diameter of the upper inclined blanking plate (12) is matched with the diameter of the inner wall of the vertical barrel (1), the upper inclined blanking plate (12) is obliquely arranged on the inner wall of the vertical barrel (1), the included angle between the upper inclined blanking plate (12) and the horizontal plane is 15-30 degrees, the top arc-shaped edge of the upper inclined blanking plate (12) is located below the feeding hole (9), the bottom edge of the upper inclined blanking plate (12) is of a flush structure, the lower part of the flush structure is fixedly connected with one side of the upper bottom sealing plate (13), the upper bottom sealing plate (13) is of a two-thirds circular sheet structure, the diameter of the upper bottom sealing plate (13) is matched with the diameter of the inner wall of the vertical barrel (1), the upper bottom sealing plate (13) is horizontally arranged on the inner wall of the vertical barrel (1), and the air outlet direction of the upper fan (14) horizontally faces the axis of the vertical barrel (1).

4. The bio-organic fertilizer granule vertical cooling device according to claim 1, wherein: the lower part slope blanking plate (26) be with upper portion slope blanking plate (12) shape and the equal three-quarter circular sheet structure of size, the diameter of lower part slope blanking plate (26) cooperatees with the diameter of upright bucket (1) inner wall, lower part slope blanking plate (26) slope sets up at upright bucket (1) inner wall, contained angle of lower part slope blanking plate (26) and horizontal plane is 15 to 30 degrees, the bottom edge position of lower part slope blanking plate (26) is the parallel and level form structure, the lower part of this parallel and level form structure and one side fixed connection of lower part bottom closing plate (27), lower part bottom closing plate (27) be with the equal two-thirds circular sheet structure of upper portion bottom closing plate (13) shape and size, lower part bottom closing plate (27) diameter cooperatees with the diameter of upright bucket (1) inner wall, lower part bottom closing plate (27) horizontal level sets up at upright bucket (1) inner wall, the wind direction level of lower part fan (28) is towards the axle center of upright bucket (1).

5. The bio-organic fertilizer granule vertical cooling device according to claim 1, wherein: the top outer wall of the material gathering bucket (29) is fixedly connected with the inner wall of the vertical bucket (1), the bottom opening of the material gathering bucket (29) is connected with the top opening of the discharge hole (8), the bottom wall inner diameter of the material gathering bucket (29) is equal to the top inner diameter of the discharge hole (8), the included angle between the bottom of the material gathering bucket (29) and the horizontal plane is 45 degrees, the top opening of the material gathering bucket (29) is communicated with one side of the bottom of the lower bottom sealing plate (27), the middle outer side of the vertical bucket (1) is fixedly provided with a reinforcing support ring (2), the outer wall of the reinforcing support ring (2) is fixedly provided with a supporting leg (3), the mounting position of the reinforcing support ring (2) is positioned on the outer wall of the vertical bucket (1) below the main bearing ring (18), and an exhaust dehumidifying fan (11) is mounted in the exhaust dehumidifying port (10).

6. The bio-organic fertilizer granule vertical cooling device according to claim 2, wherein: the rotary support ring (19) is of a circular annular structure, the outer wall of the rotary support ring (19) is fixedly connected with the inner rotary body of the main bearing ring (18), the outer rotary body of the main bearing ring (18) is fixedly connected with the inner wall of the vertical barrel (1), the length of the rotary support ring (19) is not smaller than that of the main bearing ring (18), the gear ring (20) is fixedly arranged on the outer wall of the lower part of the rotary support ring (19), the middle part of the rotary support ring (19) is communicated with the top of the middle part buffer blanking funnel (21), a funnel blanking opening (31) is arranged at the bottom of the middle part buffer blanking funnel (21), the bottom of the funnel blanking opening (31) is connected with the middle position of the top surface of the lower part inclined blanking plate (26), and the plane where the bottom surface of the blanking opening (31) is located above the plane where the bottom surface of the middle fan (25).

7. The bio-organic fertilizer granule vertical cooling device according to claim 2, wherein: the inner diameter of the rotary support ring (19) is equal to the inner diameter of the top of the middle buffer blanking funnel (21), a vertical line extension line between the bottom edge position of the upper inclined blanking plate (12) and the horizontal plane is positioned in the inner diameter of the rotary support ring (19), a transfer inclined blanking plate (15) matched with three-quarters inner wall of the vertical barrel (1) is fixedly arranged between the bottom of the upper bottom sealing plate (13) and the top of the rotary support ring (19), a transfer bottom sealing plate (16) matched with the inner wall of the vertical barrel (1) and the transfer inclined blanking plate (15) is fixedly arranged at the bottom of the transfer inclined blanking plate (15), an inclined blanking plate ventilation hole (30) is also formed in the transfer inclined blanking plate (15), a transfer fan (17) is fixedly arranged on the inner wall of the vertical barrel (1) between the transfer inclined blanking plate (15) and the transfer bottom sealing plate (16), and the transfer fan (17) is communicated with a transfer air pipe (4) arranged on the outer wall of the vertical barrel (1).

8. The bio-organic fertilizer granule vertical cooling device according to claim 7, wherein: the utility model provides a three-quarter circular sheet structure that reload slope blanking plate (15) be equal with upper portion slope blanking plate (12) shape and size, the diameter of reload slope blanking plate (15) cooperatees with the diameter of standing barrel (1) inner wall, the slope of reload slope blanking plate (15) sets up at standing barrel (1) inner wall, the contained angle of reload slope blanking plate (15) and horizontal plane is 15 to 30 degrees, the bottom edge position of reload slope blanking plate (15) is the parallel and level form structure, the lower part of this parallel and level form structure and one side fixed connection of reload bottom closing plate (16), reload bottom closing plate (16) be with upper portion bottom closing plate (13) shape and two-thirds circular sheet structure that the size equals, reload bottom closing plate (16) diameter cooperatees with the diameter of standing barrel (1) inner wall, reload bottom closing plate (16) horizontal level sets up at standing barrel (1) inner wall, the wind direction level of reload fan (17) is towards the axle center of standing barrel (1).