CN208472081U - A kind of interior subregion stalk is stirred solid-state fermentation installation - Google Patents
A kind of interior subregion stalk is stirred solid-state fermentation installation Download PDFInfo
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- CN208472081U CN208472081U CN201820857773.5U CN201820857773U CN208472081U CN 208472081 U CN208472081 U CN 208472081U CN 201820857773 U CN201820857773 U CN 201820857773U CN 208472081 U CN208472081 U CN 208472081U
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- 238000010563 solid-state fermentation Methods 0.000 title claims abstract description 20
- 238000009434 installation Methods 0.000 title claims abstract description 17
- 239000000463 material Substances 0.000 claims abstract description 82
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 80
- 230000002262 irrigation Effects 0.000 claims abstract description 41
- 238000003973 irrigation Methods 0.000 claims abstract description 41
- 238000000855 fermentation Methods 0.000 claims abstract description 20
- 230000004151 fermentation Effects 0.000 claims abstract description 20
- 238000003756 stirring Methods 0.000 claims abstract description 18
- 239000008223 sterile water Substances 0.000 claims abstract description 9
- 230000008878 coupling Effects 0.000 claims description 3
- 238000010168 coupling process Methods 0.000 claims description 3
- 238000005859 coupling reaction Methods 0.000 claims description 3
- 239000000945 filler Substances 0.000 claims description 2
- 239000004744 fabric Substances 0.000 claims 1
- 230000008901 benefit Effects 0.000 abstract description 4
- 230000000694 effects Effects 0.000 abstract description 4
- 238000012544 monitoring process Methods 0.000 abstract description 4
- 230000008676 import Effects 0.000 abstract description 3
- 238000000034 method Methods 0.000 description 9
- 238000000638 solvent extraction Methods 0.000 description 8
- 238000002156 mixing Methods 0.000 description 7
- 238000007599 discharging Methods 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 5
- 238000009423 ventilation Methods 0.000 description 5
- 230000008569 process Effects 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 239000001963 growth medium Substances 0.000 description 3
- 230000036760 body temperature Effects 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 239000000498 cooling water Substances 0.000 description 2
- 238000011169 microbiological contamination Methods 0.000 description 2
- 239000011343 solid material Substances 0.000 description 2
- 238000004804 winding Methods 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 210000000476 body water Anatomy 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000010410 layer Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 239000010902 straw Substances 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 239000002344 surface layer Substances 0.000 description 1
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Abstract
The utility model belongs to light indusqtry machinery equipment technical field, more particularly to a kind of interior subregion stalk is stirred solid-state fermentation installation, including fermentation tank, set at least one division component of tank interior, one end is fixed on top of the tank and stirs the screw lifting component that end is goed deep into each division component, set at least one gas nozzle of tank base, the division component includes tubular shell, it is set in the housing the pipe with spiral pipe in portion, spiral tube and spiral drip irrigation pipe, the pipe with spiral pipe, spiral tube and spiral trickle irrigation bottom of the tube are respectively equipped with the water inlet for stretching out tank base, air inlet and sterile water inlet, pipe with spiral pipe bottom is additionally provided with water outlet, the division component quantity is identical as screw propulsion component count, and the stirring end of screw propulsion component is located at division component casing center position, the top of the tank is equipped with object Expect import, tank base is additionally provided with material outlet, and the utility model has the advantages that heat and mass effect is good, fermentation process can regulate and control monitoring.
Description
Technical field
The utility model belongs to light indusqtry machinery equipment technical field more particularly to a kind of interior subregion stalk is stirred admittedly
State installation for fermenting.
Background technique
Currently, the agricultural crop straw mixed allocation of China's routine mostly uses greatly Corkscrews charging gear.Due to stalk object
Expect that quality is soft, mobility is not strong, material wrapping phenomena is serious；And ideal length is difficult to ensure in cutting process, defeated
The feelings such as appearance bridging, knot doming effect are very universal during sending, therefore often have fluffy material when using this kind of device, and rotation is obstructed
Condition causes equipment performance unstable, influences to safely and steadily run.
Solid state fermentation be in the presence of there is no or almost no Free water, in the water-insoluble matrix for having certain humidity,
With the bioprocesses of one or more microorganisms；Compared with liquid state fermentation, have culture medium is simple, source is wide, small investment,
The advantages that extraction process is simple afterwards, but the industrial-scale production of current solid state fermentation is rarely found, and reason mainly has the following:
1, heat and mass inefficient.Gravity-flow ventilation can only be such that solid material surface contacts with gas, and fermentation is also confined to material surface layer,
And Solid-state substrates thermal conductance is poor, and the heat generated in fermentation process is difficult to exhale in time, on heat production peak, bed temperature
It steeply rises, temperature gradient occurs, influence biological growth and product accumulation；2, gnotobasis is difficult to control, and microbiological contamination pollution rate is high,
Most of solid-state fermentation reactors operate separately the sterilizing of material with fermentation process, use gravity-flow ventilation during the fermentation,
It must consider the effect that cross-ventilation evaporates moisture, prevent excessive water loss；Large labor intensity, low efficiency, production capacity is small,
And it be easy to cause living contaminants in fermentation process；3, fermentation process monitoring is difficult, and solid material flowing property is poor, and fermentation process is difficult
With monitoring.
Summary of the invention
The purpose of the utility model is to provide a kind of interior subregion stalks to be stirred solid-state fermentation installation, has heat and mass
The advantages of microbiological contamination pollution rate is high in high-efficient, fermentation process, fermentation process is easy monitoring.
In order to achieve the above objectives, the technical solution adopted in the utility model is:
A kind of interior subregion stalk is stirred solid-state fermentation installation, including fermentation tank, set at least the one of tank interior
A division component, one end are fixed on top of the tank and stir the screw lifting component that end is goed deep into each division component, are set to tank
At least one gas nozzle of body bottom, each division component include tubular shell, are set in the housing pipe with spiral pipe, the spiral of wall
Tracheae and spiral drip irrigation pipe, the pipe with spiral pipe, spiral tube and spiral trickle irrigation bottom of the tube, which are respectively equipped with, stretches out tank base
Water inlet, air inlet and sterile water inlet, pipe with spiral pipe bottom are additionally provided with water outlet, the division component quantity and screw propulsion
Component count is identical, and the stirring end of screw propulsion component is located at division component casing center position, and the top of the tank is equipped with
Material inlet, tank base are additionally provided with material outlet.
Further, the pipe with spiral pipe, spiral tube and spiral drip irrigation pipe successively helically rise along inner walls
Winding shape is paved with inner walls and is fixedly connected respectively with inner walls, and pipe with spiral pipe, spiral tube and spiral drip irrigation pipe are in
Helical form, which circuits sequentially, arranges and is formed centrally within a circular channel, and the spiral tube side wall is equipped with one group along spiral gas
Manage equally distributed through-hole, spiral drip irrigation pipe side wall is equipped with one group along the equally distributed trickle irrigation tube head of spiral drip irrigation pipe, described
Shell is equipped with multiple equally distributed circular holes, the circular hole setting corresponding with the position of through-hole and trickle irrigation tube head on shell.
Further, the screw lifting component includes the motor for being installed on top of the tank, and what is connect with motor subtracts
Fast device, the rotation axis being connected by shaft coupling with retarder, rotation axis are equipped with helical blade, and spiral shell is goed deep into described rotation axis one end
It revolves in the central circular channel that water pipe, spiral tube and spiral drip irrigation pipe are formed, when specifically used, screw lifting component can be just
Turn, can invert, can be independently arranged.
Further, 7 division components are equipped in the tank body, a division component and edge including being located at tank body center
Equally distributed 6 division components in tank body center bay component periphery, the screw lifting component is also 7, each spiral
The position of lifting assembly and division component be arranged in a one-to-one correspondence up and down, i.e., the rotation axis axle center of each screw lifting component with
The central coaxial of each corresponding division component shell, the gas nozzle be it is multiple, be uniformly arranged each along tank base, point
Depending on the quantity of area assembly, screw lifting component and gas nozzle can be according to specific tank volume size and using needing.
Further, the outside of the tank body is equipped with collet, and collet top is equipped with collet water inlet, and collet lower part is equipped with folder
Water out is covered, the top of the tank body is additionally provided with gas outlet and pressure gauge port；The side wall of tank body is equipped with thermometer mouth, hygrometer mouth
And sample tap.
Further, for the division component case top lower than 100 ~ 200mm setting at the top of helical blade, housing bottom is high
It is arranged in 200 ~ 500mm of helical blade bottom, housing inner diameter is greater than 10 ~ 50mm of helical blade outer diameter；The screw propulsion component
Helical blade bottom away from 50 ~ 200mm of tank base, filler maximum height is lower than 50 ~ 200mm at the top of helical blade.
Further, the through-hole diameter in the spiral tube be 1 ~ 6mm, and the spacing between adjacent through-holes be 50 ~
300mm；The spacing of adjacent trickle irrigation tube head is 500mm on the spiral drip irrigation pipes.
Further, the gas nozzle is mounted on the position apart from 50 ~ 200mm of tank base.
Further, the water inlet of the pipe with spiral pipe is connected with the water inlet of collet, the water outlet of pipe with spiral pipe with
The water outlet of collet is connected.
Further, the water inlet of the water inlet of the pipe with spiral pipe, water outlet and collet, water outlet pass through switching
Valve and cold water, hot water or steam inlet and outlet connect, and when pipe with spiral pipe is connected to water pipe, inlet tube is in lower section, and outlet is upper
Side；When pipe with spiral pipe is connect with jet chimney, above, outlet is in lower section for inlet tube.
The utility model using the above structure after, when specifically used, when material being needed to be uniformly mixed, rotation axis is just
Turn, band movable vane piece gyrate, stirring submit bottoms material, fallen from partitioning device shell upper outer, bottoms material from
Gap below partitioning device shell enters, and is promoted by helical blade to top, and so on, realizes the stirring of material and mixes
It closes, when needing to sterilize to material, switching valve can be opened, be connected to jet chimney, steam enters pipe with spiral pipe, simultaneously
Rotation axis band movable vane piece rotates, and promotes mixed material, can quickly be heated to material by the heat of steam or condensed water；
By this method, when can sterilize to avoid existing solid-state fermentation tank to material, steam and material directly contact, steam exist
The condensed water formed in tank body is easy to make material conglutinate, and humidity greatly improves, and can not ferment when serious.
Existing material in tank, which is heated or cooled, is passed through steam, hot water or cooling water reality by the collet outside tank body mostly
Existing, this method is heated or cooled that speed is slow, and especially large-scale Zymolysis Equipment, temperature, the humidity of tank interior is difficult to control, meeting
There is temperature gradient phenomenon, seriously affect production, the present invention is too high or too low in the intracorporal temperature appearance of tank, needs cooling or adds
When hot, by switching valve, it is connected to the intake-outlet of collet, pipe with spiral pipe with cold water or hot water/steam inlet and outlet, starts simultaneously
Rotation axis constantly updates heat exchange interface, realizes the fast exchange of heat by the circulation stirring of material.
If needing air in fermentation process, the inlet and outlet of spiral tube can be switched into sterile sky by switching valve
Gas, while rotation axis is started, by the promotion, mixing and circulation of material, the contact surface of air and material is constantly updated, is enhanced
Mass transport process, if material is too dry in fermentation process, humidity is too low not to be reached requirement, and can open the import of spiral drip irrigation pipe
Valve is passed through sterile water, while starting agitating shaft, is mixed by the circulation of material, increases the water content in material, improves culture medium
Humidity, if humidity is too high, by open filtrated air valve, filtrated air is passed through by spiral tube, stirring is started, takes away object
Moisture in material.If necessary to discharge, material can be pushed to bottom, realize quickly discharging by rotation axis reversion.
When putting up a bridge occurs in material, knot arch, fluffy material when, the valve of control gas nozzle is opened, by high pressure sterile air from object
Material bottom is gone out, and using the expansion and impact strength of gas, destroys bridging, knot arch and the fluffy material state of storeroom.
The utility model has the advantage, that
It, will by the way that multiple screw lifting devices and partitioning device is arranged 1. the present apparatus enhances the effect of heat and mass transfer
The intracorporal material of tank is divided into several different regions, and the mixing, stirring and circulation of material may be implemented in each region, constantly updates
With the contact surface of storeroom, heat and mass transfer process is enhanced；
2. the present apparatus easily realizes temperature and humidity control, in tank body when extremes of temperature, it can not only pass through tank body external jacket
Heat exchange, can also be realized by pipe with spiral pipe in multiple partitioning devices and screw lifting component the promotion of material, mixing with
Heat exchange is passed through filtrated air by spiral tube and realizes ventilation, can also take away the water in material to guarantee that tank body temperature is uniform
Point, and sterile water is passed through using spiral drip irrigation pipe to humidify material, the equal control of material in tank humidity may be implemented；
3. the present apparatus can realize quickly discharging, inverted by rotation axis, material can be pushed to bottom, realizes quickly discharging；
4. the present apparatus avoids material bridging, knot arch, fluffy material, material is destroyed using the high pressure sterile air that gas nozzle sprays
Between bridging, knot arch and fluffy material state.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model.
Fig. 2 is division component and screw lifting components distribution schematic diagram in the utility model.
Fig. 3 is the structural schematic diagram of division component in the utility model.
1, tank body；11, collet；111, collet water inlet；112, collet water out；12, material inlet；13, discharge port；
14, pressure gauge port；15, gas outlet；16, thermometer mouth；17, hygrometer mouth；18, sample tap；2, division component；21, shell；
22, pipe with spiral pipe；221, water inlet；222, water outlet；23, spiral tube；231, air inlet；24, spiral drip irrigation pipe；241, nothing
Bacterium water inlet；3, spiral pushing device；4, gas nozzle.
Specific embodiment
Embodiment 1
As shown, a kind of interior subregion stalk is stirred solid-state fermentation installation, including fermentation tank 1, the tank body 1
Outside is equipped with collet 11, and 11 top of collet is equipped with collet water inlet 111, and 11 lower part of collet is equipped with collet water out 112, the tank
The top of body 1 is additionally provided with gas outlet 15 and pressure gauge port 14；The side wall of tank body 1 is equipped with thermometer mouth 16, hygrometer mouth 17 and takes
1 top of tank body is fixed on and deeply each point of stirring end in sample mouth 18, at least one division component 2 inside tank body 1, one end
Screw lifting component 3 in area assembly, the screw lifting component 3 includes the motor for being installed on 1 top of tank body, with motor
The retarder of connection, the rotation axis being connected by shaft coupling with retarder, rotation axis are equipped with helical blade, the rotation axis one
End is goed deep into the central circular channel that pipe with spiral pipe 22, spiral tube 23 and spiral drip irrigation pipe 24 are formed, when specifically used, spiral
Lifting assembly 3 can rotate forward, and can invert, and can be independently arranged；It further include at least one gas nozzle 4 set on 1 bottom of tank body, each
Division component 2 is including tubular shell 21, pipe with spiral pipe 22, spiral tube 23 and spiral drip irrigation pipe 24 inside shell 21,
The pipe with spiral pipe 22, spiral tube 23 and 23 bottom of spiral drip irrigation pipe be respectively equipped with stretch out 1 bottom of tank body water inlet 221,
Air inlet 231 and sterile water inlet 241,22 bottom of pipe with spiral pipe are additionally provided with water outlet 222, the water inlet of the pipe with spiral pipe 22
221 are connected with collet water inlet 111, and the water outlet 222 of pipe with spiral pipe 22 is connected with collet water out 112, the spiral
Water inlet 221, water outlet 222 and the collet water inlet 111 of water pipe 22, collet water out 112 by switching valve and cold water,
Hot water or steam inlet and outlet connection, when pipe with spiral pipe 22 is connected to water pipe, inlet tube is in lower section, and outlet is above；Work as spiral shell
When rotation water pipe is connect with jet chimney, above, outlet is in lower section for inlet tube；1 quantity of division component and screw propulsion
3 quantity of component is identical, and the stirring end of screw propulsion component 3 is located at 2 shell of division component, 21 center, and the tank body 1 pushes up
Portion is equipped with material inlet 12, and 1 bottom of tank body is additionally provided with material outlet 13, further, the pipe with spiral pipe 22, spiral tube 23
With spiral drip irrigation pipe 24 successively along 21 inner wall of shell helically rise winding shape be paved with 21 inner wall of shell and respectively with shell 21
Inner wall is fixedly connected, and pipe with spiral pipe 22, spiral tube 23 and spiral drip irrigation pipe 24 circuit sequentially arrangement and in the shape of a spiral
It is formed centrally a circular channel, 23 side wall of spiral tube is equipped with one group along the equally distributed through-hole of spiral tube 23, spiral shell
It revolves 24 side wall of drip irrigation pipe and is equipped with one group of leading on the equally distributed trickle irrigation tube head of spiral drip irrigation pipe 24, the spiral tube 23
Bore dia is 1 ~ 6mm, and the spacing between adjacent through-holes is 50 ~ 300mm；Adjacent trickle irrigation tube head on the spiral drip irrigation pipes 24
Spacing be 500mm, the shell 21 is equipped with multiple equally distributed circular holes, circular hole and through-hole and drip irrigation pipe on shell 21
The corresponding setting in position of head can will be heated or cooled into material into shape, together from the gas injection come out in through-hole in this way
When the sterile water come out from trickle irrigation tube head can also be humidified into material, may be implemented the equal control of material in tank humidity；
Multiple division components are equipped in tank body, the screw lifting component count is identical as the quantity of division component, each screw lifting
The position of component 3 and division component 2 is to be arranged in a one-to-one correspondence up and down, i.e., the rotation axis axle center of each screw lifting component 3 with
The central coaxial of each 2 shell 21 of corresponding division component, the gas nozzle 4 be it is multiple, uniformly set each along 1 bottom of tank body
Set, the gas nozzle 4 is mounted on the position apart from 1 50 ~ 200mm of bottom of tank body, division component 2, screw lifting component 3 and
Depending on the quantity of gas nozzle 4 can be according to specific 1 volume size of tank body and using needing；2 shell 21 of the division component top
Portion is arranged lower than 100 ~ 200mm setting at the top of helical blade, 21 bottom of shell higher than 200 ~ 500mm of helical blade bottom, shell
21 internal diameters are greater than 10 ~ 50mm of helical blade outer diameter；The helical blade bottom of the screw lifting component 3 away from 1 bottom 50 of tank body ~
200mm, material maximum height is lower than 50 ~ 200mm at the top of helical blade；
Embodiment 2
Embodiment 2 difference from example 1 is that: be equipped with 7 division components in the tank body, including be located at tank body
One division component at center and along equally distributed 6 division components in tank body center bay component periphery, the spiral mentions
Rising component is also 7, and the position of each screw lifting component 3 and division component 2 is to be arranged in a one-to-one correspondence up and down, i.e., each spiral
With the central coaxial of each corresponding 2 shell 21 of division component, the gas nozzle 4 is 9 in the rotation axis axle center of lifting assembly 3
A, it is 2 layers that 9 gas nozzles 4, which divide, has been uniformly arranged 3 gas nozzles, other 6 subregions dresses outside the component of center bay with one heart
It sets and outer be uniformly arranged 6 gas nozzles with one heart and be uniformly arranged each along 1 bottom of tank body.
When specifically used, when material being needed to be uniformly mixed, rotation axis is rotated forward, and band movable vane piece gyrates, and stirring submits
Bottoms material is fallen from partitioning device shell upper outer, and bottoms material enters from the gap below partitioning device shell, by spiral shell
Vane piece is promoted to top, and so on, realizes the stirring and mixing of material, when needing to sterilize to material, can be incited somebody to action
Switching valve is opened, and jet chimney is connected to, and steam enters pipe with spiral pipe, while rotation axis band movable vane piece rotates, and promotes mixed material,
Quickly material can be heated by the heat of steam or condensed water；By this method, it can be sent out to avoid existing solid
When fermentation tank sterilizes to material, steam and material directly contact, the condensed water that steam is formed in tank body are easy to keep material viscous
At one piece, humidity is greatly improved, and can not be fermented when serious.
Existing material in tank, which is heated or cooled, is passed through steam, hot water or cooling water reality by the collet outside tank body mostly
Existing, this method is heated or cooled that speed is slow, and especially large-scale Zymolysis Equipment, temperature, the humidity of tank interior is difficult to control, meeting
There is temperature gradient phenomenon, seriously affect production, the present invention is too high or too low in the intracorporal temperature appearance of tank, needs cooling or adds
When hot, by switching valve, it is connected to the intake-outlet of collet, pipe with spiral pipe with cold water or hot water/steam inlet and outlet, starts simultaneously
Rotation axis constantly updates heat exchange interface, realizes the fast exchange of heat by the circulation stirring of material.
If needing air in fermentation process, the inlet and outlet of spiral tube can be switched into sterile sky by switching valve
Gas, while rotation axis is started, by the promotion, mixing and circulation of material, the contact surface of air and material is constantly updated, is enhanced
Mass transport process, if material is too dry in fermentation process, humidity is too low not to be reached requirement, and can open the import of spiral drip irrigation pipe
Valve is passed through sterile water, while starting agitating shaft, is mixed by the circulation of material, increases the water content in material, improves culture medium
Humidity, if humidity is too high, by open filtrated air valve, filtrated air is passed through by spiral tube, stirring is started, takes away object
Moisture in material.If necessary to discharge, material can be pushed to bottom, realize quickly discharging by rotation axis reversion.
When putting up a bridge occurs in material, knot arch, fluffy material when, the valve of control gas nozzle is opened, by high pressure sterile air from object
Material bottom is gone out, and using the expansion and impact strength of gas, destroys bridging, knot arch and the fluffy material state of storeroom.
By the multiple screw lifting devices of setting and partitioning device, the intracorporal material of tank is divided into multiple and different regions,
The stirring, mixing and circulation of material may be implemented in each region, constantly updates the contact surface with storeroom, enhances heat and mass
Process is not only exchanged heat by tank body external jacket in tank body when extremes of temperature, can also be by multiple partitioning devices
Pipe with spiral pipe and spiral pushing device realize the promotion, mixing and heat exchange of material, to guarantee that tank body temperature is uniform；Pass through spiral shell
Rotation tracheae is passed through filtrated air and realizes ventilation, can also take away the moisture in material, and be passed through sterile water using spiral drip irrigation pipe
Material is humidified, may be implemented the equal control of material in tank humidity；It is inverted by rotation axis, material can be pushed to bottom
Portion realizes quickly discharging.By opening the valve of control gas nozzle, high pressure sterile air is gone out from material bottom, is utilized
The strength of gas expansion and impact destroys bridging, knot arch and the fluffy material shape of storeroom.
Claims (10)
1. a kind of interior subregion stalk is stirred solid-state fermentation installation, it is characterised in that: including fermentation tank, be set to tank interior
At least one division component, one end, which is fixed on top of the tank and stirs end, gos deep into screw lifting group in each division component
Part, set at least one gas nozzle of tank base, the division component includes tubular shell, is set in the housing the spiral in portion
Water pipe, spiral tube and spiral drip irrigation pipe, the pipe with spiral pipe, spiral tube and spiral trickle irrigation bottom of the tube are respectively equipped with stretching tank
Water inlet, air inlet and the sterile water inlet of body bottom, pipe with spiral pipe bottom are additionally provided with water outlet, the division component quantity with
Screw propulsion component count is identical, and the stirring end of screw propulsion component is located at division component casing center position, the tank body
Top is equipped with material inlet, and tank base is additionally provided with material outlet.
2. subregion stalk is stirred solid-state fermentation installation in as described in claim 1, it is characterised in that: the spiral water
Pipe, spiral tube and spiral drip irrigation pipe successively helically rises along inner walls wind shape be paved with inner walls and respectively with shell
Internal wall is fixedly connected, and pipe with spiral pipe, spiral tube and spiral drip irrigation pipe circuit sequentially arrangement and in middle heart in the shape of a spiral
At a circular channel, the spiral tube side wall is equipped with one group along the equally distributed through-hole of spiral tube, spiral drip irrigation pipe
Side wall is equipped with one group along the equally distributed trickle irrigation tube head of spiral drip irrigation pipe, and the shell is equipped with multiple equally distributed circles
Hole, the circular hole setting corresponding with the position of through-hole and trickle irrigation tube head on shell.
3. subregion stalk is stirred solid-state fermentation installation in as claimed in claim 2, it is characterised in that: the screw lifting
Component includes the motor for being installed on top of the tank, and the retarder connecting with motor is connected by shaft coupling with retarder
Rotation axis, rotation axis are equipped with helical blade, and it is tubular that pipe with spiral pipe, spiral tube and spiral trickle irrigation are goed deep into described rotation axis one end
At central circular channel in.
4. subregion stalk is stirred solid-state fermentation installation in as claimed in claim 3, it is characterised in that: set in the tank body
There are 7 division components, including being located at a division component at tank body center and uniformly dividing along tank body center bay component periphery
6 division components of cloth, the screw lifting component are also 7, and the position of each screw lifting component and division component is upper
Under be arranged in a one-to-one correspondence, i.e., the rotation axis axle center of each screw lifting component with the center of each corresponding division component shell
Coaxially, the gas nozzle is multiple, is uniformly arranged each along tank base.
5. subregion stalk is stirred solid-state fermentation installation in as claimed in claim 4, it is characterised in that: outside the tank body
Portion is equipped with collet, and collet top is equipped with collet water inlet, and collet lower part is equipped with collet water out, and the top of the tank body is additionally provided with
Gas outlet and pressure gauge port；The side wall of tank body is equipped with thermometer mouth, hygrometer mouth and sample tap.
6. subregion stalk is stirred solid-state fermentation installation in as claimed in claim 5, it is characterised in that: the division component
Case top is arranged lower than 100 ~ 200mm setting at the top of helical blade, housing bottom higher than 200 ~ 500mm of helical blade bottom,
Housing inner diameter is greater than 10 ~ 50mm of helical blade outer diameter；The helical blade bottom of the screw propulsion component away from tank base 50 ~
200mm, filler maximum height is lower than 50 ~ 200mm at the top of helical blade.
7. subregion stalk is stirred solid-state fermentation installation in as claimed in claim 6, it is characterised in that: the spiral tube
On through-hole diameter be 1 ~ 6mm, and the spacing between adjacent through-holes be 50 ~ 300mm；Adjacent trickle irrigation on the spiral drip irrigation pipes
The spacing of tube head is 500mm.
8. subregion stalk is stirred solid-state fermentation installation in as claimed in claim 7, it is characterised in that: the gas nozzle
It is mounted on the position apart from 50 ~ 200mm of tank base.
9. subregion stalk is stirred solid-state fermentation installation in as claimed in claim 8, it is characterised in that: the pipe with spiral pipe
Water inlet be connected with the water inlet of collet, the water outlet of pipe with spiral pipe is connected with the water outlet of collet.
10. subregion stalk is stirred solid-state fermentation installation in as claimed in claim 9, it is characterised in that: the spiral water
The water inlet of pipe, the water inlet of water outlet and collet, water outlet pass through switching valve and cold water, hot water or steam inlet and outlet connect
It connects.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820857773.5U CN208472081U (en) | 2018-06-05 | 2018-06-05 | A kind of interior subregion stalk is stirred solid-state fermentation installation |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820857773.5U CN208472081U (en) | 2018-06-05 | 2018-06-05 | A kind of interior subregion stalk is stirred solid-state fermentation installation |
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| Publication Number | Publication Date |
|---|---|
| CN208472081U true CN208472081U (en) | 2019-02-05 |
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| CN201820857773.5U Expired - Fee Related CN208472081U (en) | 2018-06-05 | 2018-06-05 | A kind of interior subregion stalk is stirred solid-state fermentation installation |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108485934A (en) * | 2018-06-05 | 2018-09-04 | 郑州大学 | A kind of interior subregion stalk is stirred solid-state fermentation installation |
| CN112868904A (en) * | 2021-01-27 | 2021-06-01 | 湖南普菲克生物科技有限公司 | Method for producing peptide-rich prebiotic-rich feed by fermenting soybean meal and manufacturing device thereof |
-
2018
- 2018-06-05 CN CN201820857773.5U patent/CN208472081U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108485934A (en) * | 2018-06-05 | 2018-09-04 | 郑州大学 | A kind of interior subregion stalk is stirred solid-state fermentation installation |
| CN112868904A (en) * | 2021-01-27 | 2021-06-01 | 湖南普菲克生物科技有限公司 | Method for producing peptide-rich prebiotic-rich feed by fermenting soybean meal and manufacturing device thereof |
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