CN211586445U - Wet fermentation material adds feed proportioning system - Google Patents
Wet fermentation material adds feed proportioning system Download PDFInfo
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- CN211586445U CN211586445U CN201922476613.3U CN201922476613U CN211586445U CN 211586445 U CN211586445 U CN 211586445U CN 201922476613 U CN201922476613 U CN 201922476613U CN 211586445 U CN211586445 U CN 211586445U
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Abstract
The utility model discloses a wet fermentation material adds feed proportioning system, subtract heavy title, first conveyer, scattering machine, first air seal machinery, flexible coupling, air feeder, tuber pipe, first feeding device, saxon, mix machine, powder and subtract heavy title, second conveyer, second air seal machinery, second feeding device including wet material. The utility model provides a because of the big wet material of solid state fermentation fodder moisture content of not drying process has viscidity, wet fermentation material is difficult to with other material batching misce bene's problem, wet fermentation fodder can obtain high-efficient, stable rational processing and utilization.
Description
Technical Field
The utility model relates to a fermentation technical field, in particular to wet fermentation material adds feed proportioning system.
Background
The solid-state fermented feed is a biological feed product with high added value, which is obtained by treating feed raw materials such as agricultural and sideline products and the like by utilizing a biotechnology. In the production of solid-state fermented feed, the adopted fermentation raw materials have wide sources and low price, such as various cakes, bran, dregs and other low-value agricultural and sideline products, the fermentation materials are subjected to microbial fermentation treatment, the nutrition level is obviously improved, beneficial microorganisms secrete rich beneficial metabolites into the materials in the fermentation process, the original anti-nutritional factors in the raw materials are eliminated to a great extent, the palatability of the materials is improved, and the digestibility of the feed is improved.
When the solid-state fermented feed is produced, a large amount of zymophyte liquid is added into a fermentation substrate during inoculation, after fermentation is completed, the moisture content of a fermented feed product is high, the material is soaked by fermentation liquor for a long time, the material can soften and expand and can generate certain viscosity, meanwhile, after the material is subjected to microbial fermentation treatment, macromolecular protein is degraded, the material contains rich beneficial bacterium metabolites, the factors can increase the viscosity of the material, and the characteristic enables the wet fermented feed not to be easily mixed with other material ingredients uniformly.
During the production of solid fermented feed, the material after fermentation needs to be dried. However, the fermented beneficial bacteria commonly used in the production of solid fermented feed have poor high temperature resistance, and beneficial microorganisms in the solid fermented feed are killed by the high temperature in the drying process, so that abundant beneficial microorganisms contained in the fermented feed cannot play a probiotic nutritional role in animal intestinal tracts, and the probiotic biological activity of the fermented feed is greatly adversely affected. Meanwhile, thermosensitive nutrient components such as digestive enzymes, unknown growth factors, vitamins and the like generated in the fermentation process of the materials are damaged by high drying temperature, the excellent nutrient value of the solid-state fermented feed is greatly damaged, the utilization of the fermented feed product is not facilitated, the nutrient effect of the fermented feed product cannot be exerted to the maximum degree, and the economic value is reduced.
On the other hand, the investment of drying equipment is huge, and the energy consumption of the drying treatment link is high, so that the production cost of the fermented feed is higher, and the market promotion and economic benefit promotion of the fermented feed are not facilitated.
The prior treatment process obviously restricts the reasonable utilization of the fermented feed.
For the reasons, it is necessary to develop a reasonable treatment process system according to the material property and nutritional property of the solid fermented feed to exert the nutritional value of the solid fermented feed to the maximum extent.
Disclosure of Invention
An object of the utility model is to provide a wet fermentation material adds feed proportioning system, the utility model discloses a wet fermentation material adds feed proportioning system makes the material handle the completion back at solid state fermentation, need not carry out drying process to the wet fermentation material that obtains, but directly utilizes wet fermentation material, carries out the batching hybrid processing with wet fermentation material and other feed components together, makes the required animal feed of plant and carries out the animal and feeds.
Adopt the utility model discloses a wet fermentation material adds feed proportioning system can eliminate above-mentioned fermented feed because of a great deal of adverse effect that drying process produced, and the nutritive value of furthest performance solid state fermentation fodder.
The utility model provides a because of the big wet material of solid state fermentation fodder moisture content of not drying process has viscidity, wet fermentation material is difficult to with other material batching misce bene's problem, wet fermentation fodder can obtain high-efficient, stable rational processing and utilization.
In order to achieve the above object, the utility model provides a following technical scheme:
a wet fermentation material adding and batching system comprises a wet material weight reducing scale, a first conveyor, a scattering machine, a first air seal machine, a flexible connection, an air supply device, an air pipe, a first feeding device, a saxolone, a mixer, a powder weight reducing scale, a second conveyor, a second air seal machine and a second feeding device; a first conveyor is arranged below the wet material weight reducing scale, a discharge port of the wet material weight reducing scale is communicated with a feed port of the first conveyor through flexible connection, a first feeding device is arranged on the air pipe, one end of the air pipe is communicated with an air outlet of the air supply device, the other end of the air pipe is communicated with an air inlet of the saxon, the mixing machine is arranged below a discharge port of the saxon, the discharge port of the saxon is communicated with the feed port of the mixing machine, the discharge port of the first conveyor is communicated with the feed port of the first feeding device through a scattering machine and a first air seal device in sequence downwards, and the horizontal height of the air inlet of the saxon is higher than the air outlet of the air supply device; the second feeding device is arranged on an air pipe between an air outlet of the air supply device and a feed inlet of the first feeding device, a second conveyor is arranged below the powder weight reducing scale, a discharge port of the powder weight reducing scale is communicated with a feed inlet of the second conveyor through flexible connection, and a discharge port of the second conveyor is communicated with the feed inlet of the second feeding device through a second air seal machine downwards.
Preferably, the dust remover is further included, and the air outlet of the saxolone is communicated with the air inlet of the dust remover.
Preferably, still include grid, first fill, the slide valve of keeping in, the upper end of first fill of keeping in sets up the grid, and the discharge gate of first fill of keeping in sets up the slide valve, and the discharge gate of slide valve is through the feed inlet intercommunication that the flexible coupling and wet material subtract the weight balance.
Preferably, the powder material temporary storage device further comprises a second temporary storage hopper, wherein a grid is arranged at the upper end of the second temporary storage hopper, a gate valve is arranged at a discharge port of the second temporary storage hopper, and the discharge port of the gate valve is communicated with a feed port of the powder material weight reducing scale through flexible connection.
Preferably, a screw conveyor is arranged at the bottom of the wet weight reducing scale, a discharge port of the wet weight reducing scale is arranged on the side surface of the wet weight reducing scale, and the discharge direction of the screw conveyor faces towards the discharge port.
Preferably, the number of the screw conveyors is not less than two, the plurality of screw conveyors are arranged at the bottom of the wet material weight reducing scale in parallel, and the discharging directions of the plurality of screw conveyors face the discharging opening.
Preferably, the gas supply device is a roots blower.
Preferably, the first feeding device is a three-way pipe.
Preferably, the second feeding device is a three-way pipe.
Preferably, the scattering machine is a hammer-type scattering machine or a chain type scattering machine.
The utility model has the advantages that:
the utility model discloses a wet fermentation material adds feed proportioning system makes the material handle the completion back at solid state fermentation, need not carry out drying process to the wet fermentation material that obtains, but directly utilizes wet fermentation material, will wet fermentation material and other feed components carry out the batching hybrid processing together, make the required animal feed of plant and carry out the animal and feed.
Adopt the utility model discloses a wet fermentation material adds feed proportioning system can eliminate above-mentioned fermented feed because of a great deal of adverse effect that drying process produced, and the nutritive value of furthest performance solid state fermentation fodder.
The utility model provides a wet fermentation material be difficult to with other material batching misce benes's problem, wet fermentation fodder can obtain high-efficient, stable rational processing and utilization.
The utility model discloses a wet fermentation material adds feed proportioning system has still solved from the department to the reinforced problem of the machine 13 that mixes of eminence, and it is more convenient that the production operation is smooth, realizes the effect of killing more.
Drawings
FIG. 1 is a schematic view of the feeding and batching system for wet fermentation material of the present invention.
Fig. 2 is a schematic structural diagram of an embodiment of the wet weight reducing scale of the present invention.
In the figure: 1-grid, 2-first temporary storage hopper, 3-gate valve, 4-wet material weight reducing scale, 5-first conveyor, 6-scattering machine, 7-first air seal machine, 8-flexible connection, 9-air supply device, 10-air pipe, 11-first feeding device, 12-saxon, 13-mixing machine, 14-second temporary storage hopper, 15-powder weight reducing scale, 16-second conveyor, 17-second air seal machine, 18-second feeding device, 19-dust remover, 20-bottom weighing, 21-spiral conveyor and 22-discharge opening.
Detailed Description
The present invention will be described in further detail with reference to the accompanying drawings and specific embodiments.
As shown in fig. 1-2, a wet fermentation material adding and batching system according to an embodiment of the present invention includes a wet material weight reduction scale 4, a first conveyor 5, a breaker 6, a first air seal 7, a flexible connection 8, an air supply device 9, an air pipe 10, a first feeding device 11, a saxolone 12, a mixer 13, a powder weight reduction scale 15, a second conveyor 16, a second air seal 17, and a second feeding device 18; a first conveyor 5 is arranged below the wet material weight reducing scale 4, a discharge port 22 of the wet material weight reducing scale 4 is communicated with a feed port of the first conveyor 5 through a flexible connection 8, a first feeding device 11 is arranged on an air pipe 10, one end of the air pipe 10 is communicated with an air outlet of an air supply device 9, the other end of the air pipe 10 is communicated with an air inlet of a saxolone 12, a mixer 13 is arranged below a discharge port of the saxolone 12, the discharge port of the saxolone 12 is communicated with the feed port of the mixer 13, the discharge port of the first conveyor 5 is communicated with the feed port of the first feeding device 11 through a scattering machine 6 and a first air seal 7 in sequence downwards, and the horizontal height of the air inlet of the saxolone 12 is higher than the air outlet of the air supply device 9; the second feeding device 18 is arranged on an air pipe 10 between an air outlet of the air supply device 9 and a feeding hole of the first feeding device 11, a second conveyor 16 is arranged below the powder weight reducing scale 15, a discharging hole of the powder weight reducing scale 15 is communicated with the feeding hole of the second conveyor 16 through a flexible connection 8, and a discharging hole of the second conveyor 16 is communicated with the feeding hole of the second feeding device 18 downwards through a second air seal 17.
Preferably, the device further comprises a dust remover 19, and the air outlet of the saxolone 12 is communicated with the air inlet of the dust remover 19.
Preferably, still include grid 1, first temporary storage fill 2, slide valve 3, the upper end of first temporary storage fill 2 sets up grid 1, and the discharge gate of first temporary storage fill 2 sets up slide valve 3, and the discharge gate of slide valve 3 is through the feed inlet intercommunication that flexible coupling 8 and wet material subtract heavy balance 4.
Preferably, the powder material temporary storage device further comprises a second temporary storage hopper 14, the upper end of the second temporary storage hopper 14 is provided with a grid 1, a discharge hole of the second temporary storage hopper 14 is provided with a gate valve 3, and a discharge hole of the gate valve 3 is communicated with a feed inlet of a powder material weight reducing scale 15 through a flexible connection 8.
Preferably, a screw conveyor 21 is arranged on a scale base 20 in the wet weight reducing scale 4, a discharge opening 22 of the wet weight reducing scale 4 is arranged on the side surface of the wet weight reducing scale 4, and the discharge direction of the screw conveyor 21 faces the discharge opening 22.
Preferably, the number of the screw conveyors 21 is not less than two, the screw conveyors 21 are arranged in parallel on the weighing bottom 20 inside the wet weight reducing scale 4, and the discharging directions of the screw conveyors 21 face the discharging opening 22.
Preferably, the gas supply device 9 is a roots blower.
Preferably, the first feeding device 11 is a three-way pipe.
Preferably, the second feeding device 18 is a tee.
Preferably, the scattering machine 6 is a hammer-type scattering machine or a chain-type scattering machine.
The utility model discloses a use method as follows:
the mixer 13, the dust remover 19, the air supply device 9, the first air seal machine 7, the breaker 6, the first conveyor 5, the second air seal machine 17 and the second conveyor 16 are started firstly.
According to the weight formula proportioning requirements of various material components when each batch of the mixer 13 is mixed, the batch weighing value of the wet material weight reducing scale 4 is set, and the batch weighing value of the powder weight reducing scale 15 is set.
Taking a proper amount of dry powdery material required by production, and adding the dry powdery material into the powder weight reducing scale 15.
If the dry powdery materials required by the actual production are various, the dry powdery materials can be uniformly mixed according to the formula requirement to prepare dry mixed powdery materials, and a proper amount of the dry mixed powdery materials is added into the powder weight reducing scale 15.
And starting the powder weight reducing scale 15 to supply materials to the second conveyor 16, wherein the powder weight reducing scale 15 obtains the accurate weight of the real-time output materials by calculating the real-time weight reducing mode. The second conveyor 16 uniformly conveys the materials to the second air seal machine 17, the second air seal machine 17 stably and uniformly outputs the materials to the second feeding device 18, and the materials stably enter the air pipe 10 through the second feeding device 18.
Adding a proper amount of wet fermented feed materials after fermentation into the wet weight loss scale 4. And starting the wet material weight reducing scale 4 to supply materials to the first conveyor 5, and obtaining the accurate weight of the real-time output materials by the wet material weight reducing scale 4 through calculating the real-time weight reducing mode.
The first conveyor 5 uniformly conveys the materials to the scattering machine 6, after the materials enter the scattering machine 6, lumps such as caking materials in the materials are scattered into a scattered shape by the scattering machine 6, the scattered uniform materials processed by the scattering machine 6 are stably and uniformly output to the first feeding device 11 by the first air seal machine 7, and the materials stably enter the air pipe 10 through the first feeding device 11.
Preferably, the first conveyor 5, the scattering machine 6, the first air seal machine 7, the second conveyor 16 and the second air seal machine 17 are controlled in a frequency conversion mode, and the rotation frequency of the first conveyor 5, the scattering machine 6, the first air seal machine 7, the second conveyor 16 and the second air seal machine 17 can be adjusted according to needs to change the working processing speed of the first conveyor, the scattering machine 6, the first air seal machine 7, the second conveyor 16 and the second air seal machine 17.
The air supply device 9 inputs air flow required for conveying materials into the air pipe 10, and the powdery materials entering the air pipe 10 through the second feeding device 18 flow to the saxolone 12 along with the air flow in the air pipe 10. The wet fermented feed material entering the air duct 10 through the first feeding device 11 also flows to the saxolone 12 with the air flow in the air duct 10.
The saxolone 12 separates and discharges the mixed materials in the air duct 10 into the mixer 13, and the mixed materials are further uniformly mixed in the mixer 13. The gas discharged from the separation of the saxolone 12 is treated by a dust remover 19 and discharged.
The weight of the wet fermented feed material particles with the same volume is larger than that of the powdery material particles, in a proper air flow, particularly in an ascending section of the air pipe 10 (the horizontal height of an air inlet of the Sacolon 12 is higher than that of an air outlet of the air supply device 9), collision and rolling exist between the powdery material particles and the wet fermented feed material particles, namely the powdery material particles and the wet fermented feed material particles are mixed in the air flow by non-mechanical stirring, pressure generated by mechanical extrusion is avoided, the wet fermented feed material particles cannot be pressed into lumps, on the other hand, when the powdery material particles and the wet fermented feed material particles collide, roll and are mixed in the air flow, the powdery material particles are wrapped outside the wet fermented feed material particles, a powdery material particle protective layer is formed outside the wet fermented feed material particles, and the condition that the wet fermented feed material particles are adhered to external substances is damaged, the viscosity of the materials is greatly reduced, which is beneficial to the uniform mixing of the mixed materials in the mixer 13.
As mentioned above, the grid 1 can be arranged at the upper end of the first temporary storage hopper 2, the gate valve 3 is arranged at the discharge port of the first temporary storage hopper 2, and the discharge port of the gate valve 3 is communicated with the feed port of the wet material weight reducing scale 4 through the flexible connection 8. The grid 1 plays the purpose of rejecting debris in the material, avoids it to fall into in the first temporary storage fill 2. The first temporary storage hopper 2 plays the role of buffering the feeding time, so that smooth material supply in production is facilitated.
The upper end of the second temporary storage hopper 14 can be provided with a grid 1, the discharge hole of the second temporary storage hopper 14 is provided with a gate valve 3, and the discharge hole of the gate valve 3 is communicated with the feed inlet of the powder weight reducing scale 15 through a flexible connection 8. The grid 1 plays the purpose of rejecting debris in the material, avoids it to fall into in the second temporary storage hopper 14. The second temporary storage hopper 14 plays the purpose of buffering the feeding time, so that smooth material supply in production is facilitated.
The weighing bottom 20 in the wet material weight reducing scale 4 is provided with the screw conveyor 21, the discharge hole 22 of the wet material weight reducing scale 4 is formed in the side face of the wet material weight reducing scale 4, the discharge direction of the screw conveyor 21 faces the discharge hole 22, and the discharge mode that the wet material weight reducing scale 4 and the screw conveyor 21 are adopted is more beneficial to discharging wet fermented feed materials, so that the discharge is more stable and smooth. Preferably, the screw conveyor 21 has a pitch which increases in the direction of the discharge opening 22, so that the discharge of the wet fermented feed material is looser.
Another face of fermenting, because wet fermented fodder is all at workshop's subaerial output, but smoothly consider (the discharge gate is in mixing machine 13 below) based on the ejection of compact that mixes machine 13, generally can set up mixing machine 13 on the operation panel, mix machine 13 and have certain height apart from ground, add wet fermented fodder to mixing machine 13 this moment and will have certain difficulty, need promote the wet fermented fodder on ground to the charge door that mixes machine 13, and the utility model discloses a wet fermented material adds feed proportioning system has solved the problem that mixes the machine 13 reinforced from the place to the eminence, and production operation is convenient more smoothly, realizes the effect of killing many birds with one stone.
Claims (10)
1. The utility model provides a wet fermentation material adds feed proportioning system which characterized in that: the device comprises a wet material weight reducing scale, a first conveyor, a scattering machine, a first air seal machine, a flexible connection, an air supply device, an air pipe, a first feeding device, a saxon, a mixing machine, a powder weight reducing scale, a second conveyor, a second air seal machine and a second feeding device; a first conveyor is arranged below the wet material weight reducing scale, a discharge port of the wet material weight reducing scale is communicated with a feed port of the first conveyor through flexible connection, a first feeding device is arranged on the air pipe, one end of the air pipe is communicated with an air outlet of the air supply device, the other end of the air pipe is communicated with an air inlet of the saxon, the mixing machine is arranged below a discharge port of the saxon, the discharge port of the saxon is communicated with the feed port of the mixing machine, the discharge port of the first conveyor is communicated with the feed port of the first feeding device through a scattering machine and a first air seal device in sequence downwards, and the horizontal height of the air inlet of the saxon is higher than the air outlet of the air supply device; the second feeding device is arranged on an air pipe between an air outlet of the air supply device and a feed inlet of the first feeding device, a second conveyor is arranged below the powder weight reducing scale, a discharge port of the powder weight reducing scale is communicated with a feed inlet of the second conveyor through flexible connection, and a discharge port of the second conveyor is communicated with the feed inlet of the second feeding device through a second air seal machine downwards.
2. The wet fermentation material dosing system of claim 1, wherein: the air outlet of the saxon is communicated with the air inlet of the dust remover.
3. The wet fermentation material dosing system of claim 1, wherein: still include grid, first fill, the slide valve of keeping in, the upper end of first fill of keeping in sets up the grid, and the discharge gate of first fill of keeping in sets up the slide valve, and the discharge gate of slide valve is through the feed inlet intercommunication that flexible coupling and wet material subtract the weight balance.
4. The wet fermentation material dosing system of claim 1, wherein: still include the second and keep in the fill, the upper end that the second kept in the fill sets up the grid, and the discharge gate that the second kept in the fill sets up the slide valve, and the discharge gate of slide valve subtracts the feed inlet intercommunication that weighs with the powder through the flexible coupling.
5. The wet fermentation material dosing system of claim 1, wherein: the bottom of the scale in the wet material weight reducing scale is provided with a screw conveyor, a discharge port of the wet material weight reducing scale is arranged on the side surface of the wet material weight reducing scale, and the discharge direction of the screw conveyor faces towards the discharge port.
6. The wet fermentation material dosing system of claim 5, wherein: two are no less than to screw conveyer's quantity, and a plurality of screw conveyer parallel arrangement are at the wet material and subtract the internal title end of heavy title, and a plurality of screw conveyer's ejection of compact direction all faces the bin outlet.
7. The wet fermentation material dosing system of claim 1, wherein: the gas supply device is a Roots blower.
8. The wet fermentation material dosing system of claim 1, wherein: the first feeding device is a three-way pipe.
9. The wet fermentation material dosing system of claim 1, wherein: the second feeding device is a three-way pipe.
10. The wet fermentation material dosing system of claim 1, wherein: the scattering machine is a hammer type scattering machine or a chain type scattering machine.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201922476613.3U CN211586445U (en) | 2019-12-31 | 2019-12-31 | Wet fermentation material adds feed proportioning system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201922476613.3U CN211586445U (en) | 2019-12-31 | 2019-12-31 | Wet fermentation material adds feed proportioning system |
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| Publication Number | Publication Date |
|---|---|
| CN211586445U true CN211586445U (en) | 2020-09-29 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201922476613.3U Active CN211586445U (en) | 2019-12-31 | 2019-12-31 | Wet fermentation material adds feed proportioning system |
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| CN (1) | CN211586445U (en) |
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2019
- 2019-12-31 CN CN201922476613.3U patent/CN211586445U/en active Active
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