CN207519590U - A kind of solid state fermentation system - Google Patents
A kind of solid state fermentation system Download PDFInfo
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- CN207519590U CN207519590U CN201721028396.6U CN201721028396U CN207519590U CN 207519590 U CN207519590 U CN 207519590U CN 201721028396 U CN201721028396 U CN 201721028396U CN 207519590 U CN207519590 U CN 207519590U
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Abstract
The utility model discloses a kind of solid state fermentation systems, including drawing-in device, siccative conveying device and vaccinization mixing arrangement, the outlet of drawing-in device is connected with the entrance of siccative conveying device, the outlet of siccative conveying device is connected with the feed inlet of vaccinization mixing arrangement, the discharge port of vaccinization mixing arrangement is connected by fermentation tank feed gate with the feed inlet of vertical solid-state anaerobism and aerobe fermentation tank, blender is equipped in fermentation tank, lower part is equipped with fermentation tank drawing mechanism, the outlet of fermentation tank drawing mechanism is connect by fermentation tank discharge gate with outfeed belt conveyor, the top vent of fermentation tank is vented gate by fermentation tank and is connected with the entrance of exhaust blower, the bottom air inlet of fermentation tank is connected by intake valve with pressurized gas system, the outer wall of fermentation tank is wound with fermentation tank coil pipe.The high degree of automation of the solid state fermentation system, yeasting control is easy, and low energy consumption, and ferment effect is good, takes up little area flexible arrangement, can meet anaerobism and require high strain fermentation.
Description
Technical field
Production system more particularly to a kind of solid state fermentation system the utility model is related to a kind of fermented feed, belong to hair
Ferment feed production technology field.
Background technology
Solid state fermentation feed is using microorganism, complex enzyme as the strain of biological feed fermentation agent, passes through microorganism itself
Metabolic activity, by the vegetalitas in the feedstuffs such as dregs of beans, wheat bran, corn flour, the anti-nutrition in animality and mineral substance
Factorization or conversion generate the feedstuff of the digestion that can more be searched for food by livestock, the nutrient higher absorbed and nonhazardous effect, can
Efficiently reduce or substitute part antibiotic.
The fermentation method of conventional solid-state fermented feed is after material is mixed, mixing is inoculated with by batch mixing machine, then
After the charging of artificial or jumbo bag, it is transported in ferment at constant temperature room by fork truck and ferments or be transported in fermentation tank by fork truck
Artificial covering and heat insulating film fermentation, transports out, manually throw into again in mixing apparatus or drying equipment by fork truck after fermentation.
Traditional solid state fermentation mode, the interior residual of batch mixing machine is big, easily grows miscellaneous bacteria, and artificial pack, fork truck is transported and unpacking people
Work intensity is big, and production run is of high cost, and yeasting is extensive, it is difficult to ensure that anaerobic environment, fermentation process is difficult to control, and influences to send out
Ferment quality can not ensure that product is stablized, and be stacked height limitation by fermentation materials, fermentation zone needs to take up a large area, to place
It limits larger.
Utility model content
To overcome problems of the prior art, the utility model provides a kind of solid state fermentation system, the degree of automation
Height, yeasting control is easy, and low energy consumption, and ferment effect is good, takes up little area flexible arrangement, can meet anaerobism and require high strain hair
Ferment.
For solution more than technical problem, a kind of solid state fermentation system of the utility model is conveyed including drawing-in device, siccative
Device and vaccinization mixing arrangement, the outlet of the drawing-in device are connected with the entrance of the siccative conveying device, described dry
The outlet of material conveying device is connected with the feed inlet of the vaccinization mixing arrangement, the discharging of the vaccinization mixing arrangement
Mouth is connected by fermentation tank feed gate with the feed inlet of vertical solid-state anaerobism and aerobe fermentation tank, the vertical solid-state anaerobism and oxygen
The inner cavity of fermentation tank is equipped with blender, and the lower part of the vertical solid-state anaerobism and aerobe fermentation tank is equipped with fermentation tank drawing mechanism, institute
The outlet for stating fermentation tank drawing mechanism is connected by the entrance of fermentation tank discharge gate and outfeed belt conveyor, and the vertical solid-state is detested
The top vent of oxygen and aerobe fermentation tank is vented gate by fermentation tank and is connected with the entrance of exhaust blower, the vertical solid-state anaerobism
And the bottom air inlet of aerobe fermentation tank is connected by intake valve with the outlet of pressurized gas system.
Relative to the prior art, the utility model achieves following advantageous effect：Dry material enters siccative from drawing-in device
Conveying device is sent into the feed inlet of vaccinization mixing arrangement by siccative conveying device, is completed in vaccinization mixing arrangement
Bacterium solution with the inoculation of material with mixing, with bacterium solution after mixing, by fermentation tank feed gate into vertical solid-state detested by material
It ferments in oxygen and aerobe fermentation tank, fermentation tank feed gate, fermentation tank discharge gate, fermentation tank exhaust gate and intake valve are equal
For airtight valve, strain is made to be grown in the environment of complying fully with, blender can be stirred heat dissipation during the fermentation, fermentation
After the completion, material is discharged from fermentation tank drawing mechanism, and fermented tank discharge gate enters outfeed belt conveyor, complete by outfeed belt conveyor
Into discharging.Since the floor space of vertical solid-state anaerobism and aerobe fermentation tank is small, capacity is big, and bore seal is functional, temperature
It can reliably control, be convenient for automation control, fermentation quality is ensured, and the cleaning work amount after discharging is small.
As the improvement of the utility model, the outer wall of the vertical solid-state anaerobism and aerobe fermentation tank is wound with fermentation tank disk
Pipe, the lower end of the fermentation tank coil pipe are equipped with circulating water intake, and the upper end of the fermentation tank coil pipe is equipped with circulating water outlet.Pass through
Circulating water intake inputs the material that hot water can be in vertical solid-state anaerobism and aerobe fermentation tank into fermentation tank coil pipe and is heated,
Otherwise the material that cooling water can be in vertical solid-state anaerobism and aerobe fermentation tank is inputted into fermentation tank coil pipe to be cooled down, it can be with
The stringent and easily heating and cooling of control material improves fermentation efficiency.
As further improvement of the utility model, the vaccinization mixing arrangement is installed on transfer car(buggy).Transfer car(buggy)
Convenient for the movement of vaccinization mixing arrangement so that a vaccinization mixing arrangement can give multiple vertical solid-state anaerobism and oxygen
Fermentation tank is fed.
As further improvement of the utility model, the side wall of the vertical solid-state anaerobism and aerobe fermentation tank is equipped with detection
The thermometer and temperature sensor of temperature in tank.Convenient for monitoring and accurately controlling the material in vertical solid-state anaerobism and aerobe fermentation tank
Temperature.
As further improvement of the utility model, the exportable inert gas of the pressurized gas system, oxygen or air.
Inert gas, oxygen or air can be inputted to vertical solid-state anaerobism and aerobe fermentation tank according to anaerobism or the needs of simultaneous aerobe fermentation,
Intake valve can be cut off and stop gas supply.
As further improvement of the utility model, the hot water inlet of the vaccinization mixing arrangement is located at bacterium solution import
Front, the hot water inlet are connected by hot water stream gauge with the outlet of heat-exchanger pump, the entrance of the heat-exchanger pump and hot-water cylinder
Outlet is connected；The bacterium solution import is connected by bacterium solution flowmeter with the outlet that bacterium solution pumps, the entrance and bacterium solution of the bacterium solution pump
The entrance of tank is connected.Hot water is pumped into the hot water inlet of vaccinization mixing arrangement by hot water and is controlled by hot water stream gauge
Flow, bacterium solution are pumped into the bacterium solution import of vaccinization mixing arrangement by bacterium solution and control flow by bacterium solution flowmeter, even
The hot water inlet of continued access kind mixing arrangement is closer apart from feed inlet, is first mixed convenient for dry material with hot water, material temperature is improved
Afterwards, then with bacterium solution mix so that bacterium solution effect of inoculation it is more preferable.
Description of the drawings
Fig. 1 is the flow chart of the utility model solid state fermentation system.
In figure：1. drawing-in device；2. siccative conveying device；3. vaccinization mixing arrangement；3a. transfer car(buggy)s；It is 4. vertical solid
State anaerobism and aerobe fermentation tank；4a. fermentation tank feed gates；4b. fermentation tank drawing mechanisms；4c. fermentation tank discharge gates；4d. is sent out
Fermentation tank is vented gate；4e. fermentation tank coil pipes；4f. blenders；5. bacterium solution tank；6. bacterium solution pumps；7. bacterium solution flowmeter；8. hot-water cylinder；
9. heat-exchanger pump；10. hot water stream gauge；11. exhaust blower；12. pressurized gas system；12a. intake valves；13. outfeed belt conveyor；TI.
Thermometer；TE. temperature sensor.
Specific embodiment
As shown in Figure 1, the solid state fermentation system of the utility model includes drawing-in device 1, siccative conveying device 2, continuously connects
Kind mixing arrangement 3 and vertical solid-state anaerobism and aerobe fermentation tank 4, the outlet of drawing-in device 1 and the entrance phase of siccative conveying device 2
Even, the outlet of siccative conveying device 2 is connected with the feed inlet of vaccinization mixing arrangement 3, the discharging of vaccinization mixing arrangement 3
Mouth is connected by fermentation tank feed gate 4a with the feed inlet of vertical solid-state anaerobism and aerobe fermentation tank 4, vertical solid-state anaerobism and oxygen
The inner cavity of fermentation tank 4 is equipped with blender 4f, and the lower part of vertical solid-state anaerobism and aerobe fermentation tank 4 is equipped with fermentation tank drawing mechanism 4b,
The outlet of fermentation tank drawing mechanism 4b is connect by fermentation tank discharge gate 4c with the entrance of outfeed belt conveyor 13, and vertical solid-state is detested
The top vent of oxygen and aerobe fermentation tank 4 is vented gate 4d by fermentation tank and is connected with the entrance of exhaust blower 11, and vertical solid-state is detested
The bottom air inlet of oxygen and aerobe fermentation tank 4 is connected by intake valve 12a with the outlet of pressurized gas system 12.
Dry material enters siccative conveying device 2 from drawing-in device 1, and vaccinization mixing dress is sent by siccative conveying device 2
3 feed inlet is put, bacterium solution is completed in vaccinization mixing arrangement 3 with the inoculation of material with mixing, material mixes with bacterium solution
After even, entered in vertical solid-state anaerobism and aerobe fermentation tank 4 by fermentation tank feed gate 4a and fermented, fermentation tank feed gate
4a, fermentation tank discharge gate 4c, fermentation tank exhaust gate 4d and intake valve 12a are airtight valve, are complying fully with strain
In the environment of grow, blender 4f can be stirred heat dissipation during the fermentation, after fermentation, material from fermentation tank discharge fill
4b discharges are put, fermented tank discharge gate 4c enters outfeed belt conveyor 13, completes to discharge by outfeed belt conveyor 13.Due to vertical solid
State anaerobism and the floor space of aerobe fermentation tank 4 are small, and capacity is big, and bore seal is functional, and temperature can be controlled reliably, be convenient for
Automation control is carried out, fermentation quality is ensured, and the cleaning work amount after discharging is small.
The outer wall of vertical solid-state anaerobism and aerobe fermentation tank 4 is wound with fermentation tank coil pipe 4e, and the lower end of fermentation tank coil pipe 4e is set
There is circulating water intake, the upper end of fermentation tank coil pipe 4e is equipped with circulating water outlet.By circulating water intake into fermentation tank coil pipe 4e
Input hot water can be in vertical solid-state anaerobism and aerobe fermentation tank 4 material heated, otherwise it is defeated into fermentation tank coil pipe 4e
Enter the material that cooling water can be in vertical solid-state anaerobism and aerobe fermentation tank 4 to be cooled down, can strictly and easily control object
The heating and cooling of material improve fermentation efficiency.
Vaccinization mixing arrangement 3 is installed on transfer car(buggy) 3a, convenient for the movement of vaccinization mixing arrangement 3 so that one
Platform vaccinization mixing arrangement 3 can give multiple vertical solid-state anaerobism and aerobe fermentation tank 4 to be fed.
The side wall of vertical solid-state anaerobism and aerobe fermentation tank 4 is equipped with the thermometer TI and temperature sensor of temperature in detection tank
TE, convenient for monitoring and accurately controlling the temperature of charge in vertical solid-state anaerobism and aerobe fermentation tank 4.
12 exportable inert gas of pressurized gas system, oxygen or air.Can according to anaerobism or and aerobe fermentation needs, to
Vertical solid-state anaerobism and aerobe fermentation tank 4 input inert gas, oxygen or air, can also cut off intake valve 12a and stop gas supply.
The hot water inlet of vaccinization mixing arrangement 3 is located in front of bacterium solution import, and hot water inlet passes through hot water stream gauge 10
Outlet with heat-exchanger pump 9 is connected, and the entrance of heat-exchanger pump 9 is connected with the outlet of hot-water cylinder 8；Bacterium solution import passes through bacterium solution flowmeter 7
Outlet with bacterium solution pump 6 is connected, and the entrance of bacterium solution pump 6 is connected with the entrance of bacterium solution tank 5.Hot water is sent into continuously by heat-exchanger pump 9
It is inoculated with the hot water inlet of mixing arrangement 3 and flow is controlled by hot water stream gauge 10, bacterium solution is sent into vaccinization by bacterium solution pump 6
The bacterium solution import of mixing arrangement 3 and pass through bacterium solution flowmeter 7 control flow, the hot water inlet distance of vaccinization mixing arrangement 3
Feed inlet is closer, is first mixed convenient for dry material with hot water, after material temperature is improved, then mixes with bacterium solution so that bacterium solution inoculation
Effect it is more preferable.
The foregoing is merely the preferable possible embodiments of the utility model, non-therefore limitation the utility model patent
Protection domain.In addition to the implementation, the utility model can also have other embodiment.It is all to use equivalent replacement or equivalent change
The technical solution to be formed is changed, is all fallen in the protection domain of the requires of the utility model.Technology of the utility model without description is special
Sign can realize that details are not described herein by or using the prior art.
Claims (6)
1. a kind of solid state fermentation system, including drawing-in device, siccative conveying device and vaccinization mixing arrangement, the feeding dress
The outlet put is connected with the entrance of the siccative conveying device, and the outlet of the siccative conveying device is mixed with the vaccinization
The feed inlet of device is connected, it is characterized in that, the discharge port of the vaccinization mixing arrangement by fermentation tank feed gate and is stood
The feed inlet of formula solid-state anaerobism and aerobe fermentation tank is connected, and the inner cavity of the vertical solid-state anaerobism and aerobe fermentation tank is equipped with blender,
The lower part of the vertical solid-state anaerobism and aerobe fermentation tank is equipped with fermentation tank drawing mechanism, and the outlet of the fermentation tank drawing mechanism leads to
The entrance of everfermentation tank discharge gate and outfeed belt conveyor connects, the top vent of the vertical solid-state anaerobism and aerobe fermentation tank
Gate is vented by fermentation tank with the entrance of exhaust blower to be connected, the bottom air inlet of the vertical solid-state anaerobism and aerobe fermentation tank leads to
Intake valve is crossed with the outlet of pressurized gas system to be connected.
2. solid state fermentation system according to claim 1, it is characterized in that, the vertical solid-state anaerobism and aerobe fermentation tank it is outer
Wall is wound with fermentation tank coil pipe, and the lower end of the fermentation tank coil pipe is equipped with circulating water intake, and the upper end of the fermentation tank coil pipe is set
There is circulating water outlet.
3. solid state fermentation system according to claim 1, it is characterized in that, the vaccinization mixing arrangement is installed on transhipment
Che Shang.
4. solid state fermentation system according to claim 1, it is characterized in that, the side of the vertical solid-state anaerobism and aerobe fermentation tank
Wall is equipped with the thermometer and temperature sensor of temperature in detection tank.
5. solid state fermentation system according to claim 1, it is characterized in that, the exportable indifferent gas of pressurized gas system
Body, oxygen or air.
6. solid state fermentation system according to any one of claim 1 to 5, it is characterized in that, the vaccinization mixing dress
The hot water inlet put is located in front of bacterium solution import, and the hot water inlet is connected by hot water stream gauge with the outlet of heat-exchanger pump, institute
The entrance for stating heat-exchanger pump is connected with the outlet of hot-water cylinder；The outlet phase that the bacterium solution import is pumped by bacterium solution flowmeter with bacterium solution
Even, the entrance of the bacterium solution pump is connected with the entrance of bacterium solution tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721028396.6U CN207519590U (en) | 2017-08-17 | 2017-08-17 | A kind of solid state fermentation system |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201721028396.6U CN207519590U (en) | 2017-08-17 | 2017-08-17 | A kind of solid state fermentation system |
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| CN207519590U true CN207519590U (en) | 2018-06-22 |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109321438A (en) * | 2018-11-27 | 2019-02-12 | 迈安德集团有限公司 | The production system of anaerobic organism feed addictive after first aerobic |
| CN112410174A (en) * | 2020-11-24 | 2021-02-26 | 王斌 | Laminar flow fermentation device and fermentation method thereof |
-
2017
- 2017-08-17 CN CN201721028396.6U patent/CN207519590U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109321438A (en) * | 2018-11-27 | 2019-02-12 | 迈安德集团有限公司 | The production system of anaerobic organism feed addictive after first aerobic |
| CN112410174A (en) * | 2020-11-24 | 2021-02-26 | 王斌 | Laminar flow fermentation device and fermentation method thereof |
| CN112410174B (en) * | 2020-11-24 | 2023-08-11 | 王天浩 | Laminar flow fermentation device and fermentation method thereof |
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| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20210312 Address after: No.199, Ji'an South Road, Yangzhou hi tech Zone, Hanjiang District, Yangzhou City, Jiangsu Province Patentee after: JIANGSU MYANDE FOOD MACHINERY Co.,Ltd. Address before: No.199, Ji'an South Road, Yangzhou hi tech Zone, Hanjiang District, Yangzhou City, Jiangsu Province Patentee before: MYANDE GROUP Co.,Ltd. |