CN218688865U - Organic fertilizer's mixed processing mechanism - Google Patents

Abstract

The utility model belongs to the technical field of the bio-fertilizer is handled, a mixed processing mechanism of organic fertilizer is disclosed, be discharge valve, feed valve on top cap, the top cap of spherical crown shape, the detachable of tube-shape, be located the bleeder valve at the bottom of the storehouse of mixed defeated feed bin, wherein, the bottom of mixed defeated feed bin is provided with consecutive first undergauge portion, second undergauge portion, transition portion and third undergauge portion, still be fixed with well siphunculus in the mixed defeated feed bin, first admission valve has been seted up to two undergauge portions, the second admission valve has been seted up to third undergauge portion, well siphunculus be higher than the top of mixed defeated feed bin with be less than the bottom of mixed defeated feed bin. The utility model discloses when the raw and other materials mixing volume that is used for organic fertilizer is great, improve the mixed effect and the work efficiency of material.

Description

Organic fertilizer's mixed processing mechanism

Technical Field

The utility model relates to a material processing technology field especially relates to a mixed processing mechanism of organic fertilizer.

Background

Due to the higher level of modern agriculture, organic food is more and more valued by people. Accordingly, ecological agriculture is regarded as important, and only ecological agriculture can produce ecological food. Organic fertilizers, which are organic substances (compounds containing carbon elements) as fertilizers, include animal manures, composts, green manure, cake manures, biogas manures, and the like. In the aspect of production of organic fertilizers, great efforts are supported by a plurality of experts. Meanwhile, the device is greatly supported by the nation. At present, special equipment and special production lines for producing organic fertilizers are arranged in many places so as to produce better organic fertilizers. The organic fertilizer contains many nutrient elements in organic state, and is difficult to be directly utilized by crops, and through the action of microorganisms, various nutrient elements are slowly released, and the nutrients are continuously supplied to the crops. The application of the organic fertilizer can improve the soil structure, effectively coordinate water, fertilizer, gas and heat in the soil, and improve the soil fertility and the land productivity.

The organic fertilizer has a plurality of production raw materials, which can be specifically divided into the following categories of 1, agricultural wastes: such as straw, soybean meal, cottonseed meal, and the like. 2. Livestock and poultry manure such as chicken manure, cattle and sheep horse manure and rabbit manure. 3. Industrial waste: such as vinasse, vinegar residue, manioc waste, sugar residue, furfural residue and the like. 4. Domestic garbage: such as kitchen waste and the like.

In order to carry out good abundant effectual mixture with different organic fertilizer raw materials according to the demand of difference, can design the material mixing conveyor of various specialties usually, how to improve material mixing effect and mixing efficiency as far as, be one of the problem that the solution is needed at present.

SUMMERY OF THE UTILITY MODEL

An object of the utility model is to provide an organic fertilizer's mixed processing mechanism can be used for raw and other materials mixing volume when great, improves the mixed effect and the work efficiency of material.

In order to realize above-mentioned purpose, the utility model provides an organic fertilizer's mixed processing mechanism, be spherical crown's top cap, discharge valve, be located the feed valve on mixed transportation storehouse side top or the top cap, be located including mixed transportation storehouse, the bleeder valve at the bottom of mixed transportation storehouse, wherein, the bottom of mixed transportation storehouse down is provided with consecutive first undergauge portion, second undergauge portion, transition portion, third undergauge portion, still be fixed with well siphunculus in the mixed transportation storehouse, first admission valve has been seted up to two undergauge portions, the second admission valve has been seted up to third undergauge portion, well siphunculus be higher than the top of mixed transportation storehouse with be less than the bottom of mixed transportation storehouse.

Furthermore, the first air inlet valve and the second air inlet valve are respectively connected with the same air compressor through a first pipeline and a second pipeline.

Furthermore, the bottom end of the middle through pipe extends into the first reducing part and is positioned above the second reducing part, and the outer diameter of the bottom of the first reducing part is the same as that of the top of the second reducing part.

Further, the outer diameter of the middle through pipe is smaller than the outer diameter of the top of the second reducing portion, the transition portion is cylindrical, the outer diameter of the transition portion is the same as the outer diameter of the bottom of the second reducing portion, and the outer diameter of the top of the third reducing portion is larger than the outer diameter of the transition portion.

Further, the first air inlet valve is arranged at the upper end of the side of the first diameter-reducing portion, and the second air inlet valve is arranged at the top of the third diameter-reducing portion.

Further, the central pipe is superposed with the central line of the mixing and conveying bin.

Furthermore, the number of the feeding valves is two, one is positioned on the top cover, and the other is positioned above the side of the mixing and conveying bin; the discharge valve is a star-shaped discharge valve and is positioned below the third reducing part.

Compared with the prior art, the utility model provides a mixed processing mechanism of organic fertilizer has following

Has the beneficial effects that:

1. the utility model discloses improve traditional material mixing storehouse structure, many compressed air pipelines that the cooperation set up, the spiral air current that effectively utilizes first pipeline to form and the combination of the perpendicular upward formula air current that forms of second pipeline for the continuous upset of raw materials is mixed, obtains higher degree of mixing, and in addition, the siphunculus also can improve work efficiency in setting up under the condition that does not increase the equipment volume.

Drawings

FIG. 1 is a schematic structural view of a mixing mechanism for organic fertilizer in an embodiment of the present invention;

FIG. 2 is another schematic structural diagram of the mixing mechanism for organic fertilizer in the embodiment of the present invention.

Detailed Description

In order to make the above objects, features and advantages of the present invention more comprehensible, embodiments of the present invention are described in detail with reference to the accompanying drawings. It is to be understood that the embodiments described are only some embodiments of the invention, and not all embodiments. Based on the embodiments of the present invention, all other embodiments obtained by a person skilled in the art without creative efforts all belong to the protection scope of the present invention.

Referring to fig. 1 and 2, an organic fertilizer mixing treatment mechanism provided in an embodiment of the present invention includes, from top to bottom: be spherical crown's top cap 1, cylindric mixing transportation storehouse 2, first undergauge portion 3, second undergauge portion 4, transition portion 5, third undergauge portion 6, the material export, wherein, top cap 1 is connected for dismantling with mixing transportation storehouse 2 tops, be provided with one or two discharge valve 23 on the top cap 1, feed valve 22 can set up on mixing transportation storehouse 2 lateral walls top or top cap 1, feed valve 22 can set up one or two, when feed valve 22 is two, a setting is on top cap 1, a setting is in mixing transportation storehouse 2 side top, the two can be used to the material of inputing different characteristics, for example powder or garrulous granule. The diameter of the material conveying bin can be 0.4-3 m, the material outlet faces downwards, a discharge valve 24 is arranged in the material conveying bin, and the discharge valve 24 is a star-shaped discharge valve 24 and is positioned below the third reducing part 6. The cross sections of the three reducing parts are isosceles trapezoids, the reducing parts, the transition parts 5 and the mixing and conveying bin 2 are sealed to form a whole, a middle through pipe 21 is further fixed at the center of the mixing and conveying bin 2, the outer side of the middle through pipe 21 is fixed on the inner wall of the mixing bin through two to four transverse supports 29, the middle through pipe 21 is overlapped with the central line (axial lead) of the mixing and conveying bin 2, the middle through pipe 21 is higher than the top end of the mixing and conveying bin 2 and lower than the bottom of the mixing and conveying bin 2, the top of the middle through pipe 21 slightly protrudes out of the top surface of the mixing and conveying bin 2 and extends into the inner side of the top cover 1 of the spherical crown shape, the bottom of the middle through pipe 21 is close to the bottom end face of the first reducing part 3 and has a small distance with the top end face of the second reducing part 4, the first air inlet valve is arranged on the second reducing part 4, the second air inlet valve is arranged on the third reducing part 6, air is blown into the mixing and also blown into the mixing and conveying bin 2 through the second air inlet valve.

In a preferred embodiment of the present invention, the bottom end of the middle tube 21 extends into the first reduced diameter portion 3 and is located above the second reduced diameter portion 4, and the bottom outer diameter of the first reduced diameter portion 3 is the same as the top outer diameter of the second reduced diameter portion 4, and the two are directly communicated with each other. The outer diameter of the middle through pipe 21 is smaller than the outer diameter of the top of the second reducing part 4, the transition part 5 is cylindrical, the diameter of the transition part is the same as the outer diameter of the bottom of the second reducing part 4, the outer diameter of the top of the third reducing part 6 is larger than the diameter of the transition part 5, and the outer diameter of the transition part 5 is equal to the outer diameter of the middle through pipe 21.

In a preferred embodiment of the present invention, the first intake valve is provided at an upper side end of the first reduced diameter portion 3, and the second intake valve is provided at a top portion of the third reduced diameter portion 6. First admission valve and second admission valve are respectively through first pipeline 7 and the same air compressor 9 of 8 connections of second pipeline, 7 transverse connection of first pipeline is on first admission valve, 8 vertical connections of second pipeline are on the second admission valve, can dismantle through the screw thread formation between each admission valve and the pipeline and be connected, first pipeline 7 and second pipeline 8 can be the plastic pipe that has certain elasticity, when not using, the pipeline can break away from the hybrid processing mechanism along with air compressor, can form certain contained angle between the inner wall of first pipeline 7 and second undergauge portion 4 and make the wind of entering follow along inner wall spiral motion. Of course, as shown in fig. 2, two sets of the first pipeline 7 and the second pipeline 8 may be provided, and similarly, two sets of the second air intake valves may be provided, and the two second air intake valves are symmetrical on the same diameter of the top surface of the third reduced diameter portion 6, of course, two sets of the compressor may also be used, which provide air flow for different sets of pipelines, respectively, and the two sets of the compressor may improve air supply amount and make air flow more uniform, and besides, the direction of the air flow entering the two first pipelines 7 is the same direction, such as clockwise rotation and rising or counterclockwise rotation.

The working principle of the utility model is as follows:

the excessive air in the mixing and conveying bin 2 is firstly discharged through an exhaust valve 23, a feed valve 22 is opened to start feeding, some raw materials of the organic fertilizer are subjected to pretreatment means such as drying and crushing in advance and then enter from the feed valve 22, when the feeding amount reaches a preset value, the feed valve 22 is closed, a first air inlet valve and a second air inlet valve are opened, the compressed air enters a second reducing part 4 through a first pipeline 7 and the first air inlet valve, and due to the fact that the compressed air transversely enters the second reducing part 4, spiral ascending air flow is formed along the inner surfaces of the second reducing part 4, the first reducing part 3 and the mixing and conveying bin 2 under the action of air flow inertia, and crushed granular or powdery raw materials are driven to stir and roll, the flowability and the mixing of the raw materials are fully improved, meanwhile, the compressed air also enters a third reducing part 6 through a second pipeline 8 and a second air inlet valve, because the compressed air enters vertically, the discharge valve is closed in advance, the vertical upward air flow is formed through the transition part 5, the diameter of the transition part 5 is the same as that of the middle through pipe 21, and on the same central line, the upward air flow mostly enters the middle through pipe 21, the raw materials in the middle through pipe 21 are sprayed out from the upper end port by the vertical upward air flow, are scattered to the periphery, move downwards along the outer side of the middle through pipe 21 and are strongly overturned and scattered together with the upward spiral air flow, thereby realizing the mixing operation of the powder materials, the raw materials can obtain higher mixing degree through repeated times of the mode, meanwhile, due to the arrangement of the middle through pipe 21, after the raw materials and the air flow enter the middle through pipe 21, the raw materials and the air flow are limited in the middle through pipe 21 without horizontal leakage, the working efficiency is improved, and the limitation of the maximum spraying height and the minimum spraying speed is eliminated by the existence of the middle through pipe 21, therefore, the volume of the mixture bin can be relatively large, and the working capacity of the equipment is improved. When the raw materials are mixed, the gas flowing out of the upper part is discharged into the air through the exhaust valve 23, after the material mixing is finished, the exhaust valve 23 is closed, the discharge valve 24 is opened, and the material is discharged into a designated storage bin from the discharge valve 24 in a material plug mode for subsequent treatment.

The above description is only for the specific embodiments of the present invention, but the protection scope of the present invention is not limited thereto, and any person skilled in the art can easily think of the changes or substitutions within the technical scope of the present invention, and all should be covered within the protection scope of the present invention. Therefore, the protection scope of the present invention shall be subject to the protection scope of the claims.

Claims (9)

1. The utility model provides a mixed processing mechanism of organic fertilizer, includes that mixed defeated feed bin, detachable of tube-shape are discharge valve, feed valve on top cap, the top cap of spherical crown shape, are located the bleeder valve at the bottom of mixed defeated feed bin's the storehouse, its characterized in that, the bottom of mixed defeated feed bin down is provided with consecutive first undergauge portion, second undergauge portion, transition portion and third undergauge portion, central authorities still are fixed with well siphunculus in the mixed defeated feed bin, first admission valve has been seted up to two undergauge portions, the second admission valve has been seted up to third undergauge portion, well siphunculus be higher than the top of mixed defeated feed bin with be less than the bottom of mixed defeated feed bin.

2. The hybrid processing mechanism of claim 1, wherein said first and second intake valves are connected to the same air compressor by first and second lines, respectively.

3. The mixing mechanism of claim 1, wherein the bottom end of the middle tube extends into the first reduced diameter portion and above the second reduced diameter portion, and wherein the bottom outer diameter of the first reduced diameter portion is the same as the top outer diameter of the second reduced diameter portion.

4. The mixing mechanism of claim 3, wherein the outer diameter of the intermediate pipe is smaller than the outer diameter of the top of the second reduced diameter portion, the transition portion is cylindrical, the outer diameter of the transition portion is the same as the outer diameter of the bottom of the second reduced diameter portion, and the outer diameter of the top of the third reduced diameter portion is larger than the outer diameter of the transition portion.

5. The mixing mechanism of claim 4, wherein the first intake valve opens at a lateral upper end of the first reduced diameter portion and the second intake valve opens at a top of the third reduced diameter portion.

6. The mixing mechanism of claim 1, wherein the central tube is coincident with a centerline of the mixing feed bin.

7. The mixing mechanism of claim 1, wherein the feed valves are two, one on the top cover and one above the side of the mixing feed bin.

8. The mixing mechanism of claim 1, wherein the discharge valve is a star-shaped discharge valve positioned below the third reduced diameter portion.

9. The mixing mechanism of claim 2, wherein there are two sets of first and second conduits.

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