CN206828525U - Honeybee van-type stalk fermentation system - Google Patents

Honeybee van-type stalk fermentation system Download PDF

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Publication number
CN206828525U
CN206828525U CN201720545482.8U CN201720545482U CN206828525U CN 206828525 U CN206828525 U CN 206828525U CN 201720545482 U CN201720545482 U CN 201720545482U CN 206828525 U CN206828525 U CN 206828525U
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CN
China
Prior art keywords
fermenting
installation
stalk
filler unit
zymotic fluid
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Withdrawn - After Issue
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CN201720545482.8U
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Chinese (zh)
Inventor
罗涛
梅自力
孔垂雪
李江
席江
李淑兰
段奇武
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Biogas Institute of Ministry of Agriculture
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Biogas Institute of Ministry of Agriculture
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Priority to CN201720545482.8U priority Critical patent/CN206828525U/en
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Abstract

The utility model discloses a kind of honeybee van-type stalk fermentation system, including installation for fermenting, multiple filler units for directly loading stalk are provided with installation for fermenting, the top surface of filler unit is located at the maximum water level in installation for fermenting, and the bottom surface of filler unit is located at the lowest water level line of installation for fermenting bottom;Filler unit includes stalk filling area and positioned at the zymotic fluid excessively stream area of stalk filling area end, adjacent two filler unit is positive and negative to be arranged in installation for fermenting, liquid baffling fermentation passage is formed in installation for fermenting by the zymotic fluid excessively stream area of positive and negative setting, the liquid feeding end of liquid baffling fermentation passage is connected with water influent pipeline, and outlet end is connected with circulation line.The utility model can effectively ensure that the abundant contact of anaerobe and stalk thing, improve the fermentation concentration and gas producing efficiency of fermentation reactor, and stalk need not be pre-processed, and reduce the pretreatment of raw material operating process of stalk engineering.

Description

Honeybee van-type stalk fermentation system
Technical field
A kind of stalk fermentation system, more particularly to a kind of honeybee van-type stalk fermentation system are the utility model is related to, belongs to natural pond Gas engineering field.
Background technology
Agricultural crop straw has easily floating, difficult mixing as a kind of special biogas fermentation material(Layering is serious), knot The features such as shell, uniform mass transfer and high-efficiency fermenting are highly detrimental in installation for fermenting.In engineer applied, there are different economy The biogas fermentation device of input and different fermentations scale.These devices are generally by changing the material characteristic of stalk --- crush Deng pretreatment, requirement of the existing installation for fermenting to fermentation materials characteristic is adapted to, to reach the purpose of smooth input and output material.For example, China Patent Publication No. CN203200264U discloses a kind of efficiently hybrid anaerobic fermentation device, and publication date is 09 month 2013 18 Day, including tank body, feed pipe, discharge nozzle, discharge pipeline, biogas pipe, biogas stirring pipe, tank deck stirring motor, stirrer paddle, waterpower Deflection plate, biogas protective cover and heating coil.The core of the patent is to reach equal by substantial amounts of mechanical agitation energy consumption input The purpose of even stirring.For another example, China Patent Publication No. CN102876566A discloses a kind of upper deflector type stalk type movable type natural pond Gas fermentation tank, publication date are on 01 16th, 2013, slanting baffle of at least three pieces arrangements for folding shape are provided with its tank body, every piece tiltedly The bottom of plate washer is provided with sediment mouth, in addition to the slant block board positioned at tank body topmost, the upper end of remaining slanting baffle and tank body Scum silica frost passage is left between inwall;The top of tank body is provided with feed hopper and gas outlet, the feed pipe being connected with feed hopper and returns Flow tube extends bottom in tank body;Tank body lower part is provided with the sediment residual cake valve below foot slanting baffle, and tank body top is provided with Scum silica frost residual cake valve below topmost slanting baffle.The patent does not consider anaerobe and stalk material in zymotic fluid Effectively mixing.
Above-mentioned prior art such as is required to crush stalk at the pretreatment.Cause existing stalk marsh gas continuous fermentation apparatus thing Expect that concentration is low(Ferment TS≤3%), generally existing fermentation operation energy consumption is big, gas producing efficiency is relatively low, and anaerobic digestion gas production efficiency is low etc. Deficiency, seriously constrain the long-term Effec-tive Function of rice straw biogas engineering.
Because rice straw is easy to the material characteristic that floats, even across the pretreatment of powder state, into installation for fermenting after, It is difficult to ensure that its uniform mass transfer.Further, since rice straw itself has higher content of lignin, the 10%- of its dry weight is accounted for 15%, it is difficult by anaerobe catabolism without processing so that its overall flow in the reactor is poor, easily makes Into line clogging.In addition, the floatation characteristic of rice straw, it is easily made to form scum silica frost on the surface of zymotic fluid, relative to feces of livestock and poultry Class reactor is easier to crust, and causes fermentation raw material to waste, while also inhibits the release of biogas.
Therefore, a kind of new anaerobic reactor for being suitable to section shape or whole strain rice straw is researched and developed, meets China's biogas engineering Development trend, there is good technical feasibility and application prospect.However, its key issue is to improve fermentation concentration, had The uniform mass transfer effect of realization of effect, so as to reach the purpose for improving engineering volume term rate.In China Patent No. A kind of van-type continuous feeding and discharging anaeroic digestor is disclosed in 2011205315851, its publication date is on 07 18th, 2012.Its The problem of existing is as follows:1st, need to set track in inside reactor, to keep the stabilization in fermentation railway carriage or compartment, the construction to fermentation system Level requirement is higher, and high in the operation level requirement of later stage operation maintenance process, and mass transfer effect is poor, it is clear that does not meet rural area The horizontal low present situation of Operation and Maintenance.2nd, the patent does not take into full account zymotic fluid and the mass exchange inside stalk fermentation area so that Stalk heap block is larger, is unfavorable for the infiltration and materials exchange of zymotic fluid.In addition, the device not to the flow field inside installation for fermenting just The effective design of row so that can not preferably realize that uniformly initiative, fermentation blind area are more.In this case, straw are easily caused Organic acid in stalk fermentation zone produces excessive, it is impossible to discharge in time, while the anaerobe in zymotic fluid is again less than enough Organic matter carry out metabolism so that the gas production rate of installation for fermenting is not high.
In addition, in German straw methane engineering, there is the two-phase zymotechnique of use " garage type ", set on installation for fermenting top Meter mouth spray, the method for the mouth that blows floating in installation for fermenting bottom design biogas, to realize having for stalk material and fermentative microorganism Effect contact, but such stalk soaks that rear heap block is larger, gravity is larger, it is necessary to larger power can just overturn stalk, and very Hardly possible upset is uniform, therefore is extremely difficult to uniformly mix purpose.
The content of the invention
The purpose of this utility model is to overcome above mentioned problem existing for prior art, there is provided a kind of honeybee van-type stalk fermentation System.The utility model can effectively ensure that the abundant contact of anaerobe and stalk thing, and the fermentation for improving fermentation reactor is dense Degree and gas producing efficiency, while prevent stalk floats from crusting, realize the smooth input and output material of material and simplify operation maintenance, and be not required to Stalk is pre-processed, reduce the pretreatment of raw material operating process of stalk engineering.
To achieve the above object, the technical solution adopted in the utility model is as follows:
A kind of honeybee van-type stalk fermentation system, it is characterised in that:Including installation for fermenting, sealing is provided with installation for fermenting Lid, installation for fermenting coordinate with closure water-stop, and multiple filler units for directly loading stalk, filler are provided with installation for fermenting The top surface of unit is located at the maximum water level in installation for fermenting, and the bottom surface of filler unit is located at the minimum water of installation for fermenting bottom At bit line;Filler unit includes stalk filling area and positioned at the zymotic fluid excessively stream area of stalk filling area end, adjacent two fillers list Member is positive and negative to be arranged in installation for fermenting, and liquid baffling is formed in installation for fermenting by the zymotic fluid excessively stream area of positive and negative setting ferments Passage, the liquid feeding end of liquid baffling fermentation passage are connected with water influent pipeline, and outlet end is connected with circulation line.
The adjacent positive and negative set-up mode of two filler units is the waterline position in the zymotic fluid excessively stream area of a filler unit In maximum water level, the waterline in the zymotic fluid excessively stream area of another filler unit is located at lowest water level line.
The concrete structure of the adjacent positive and negative setting of two filler units is that the zymotic fluid excessively stream area of a filler unit is located at Stalk filling area upper end, the zymotic fluid excessively stream area of another filler unit are located at stalk filling area lower end.
The stalk filling area is formed by entering material frame, and entering material frame end set has support, and zymotic fluid mistake is formed by support Flow area.
Be provided with the installation for fermenting inwall in the horizontal direction it is fixed enter material frame enter material frame guide groove, a charging Frame is correspondingly arranged two and enters material frame guide groove.
The length of the filler unit is adapted with the length of installation for fermenting, and the overall weight of filler unit is more than stalk Buoyancy, a filler unit enter two fixing sides after material frame guide groove is fixed by two and are in contact with installation for fermenting inwall.
The fermentation system also includes liquid reservoirs, and liquid reservoirs are connected by pipeline and water influent pipeline and circulation line Connect, control valve is provided with pipeline, liquid feeding pump is provided with water influent pipeline, control valve, fluid storage are provided with circulation line Pond is also associated with liquid supplementation pipe.
Water seal weir is provided with the top of the installation for fermenting, installation for fermenting is coordinated by water seal weir and closure water-stop, close Space between capping and maximum water level forms biogas storage area, and biogas pipe is provided with closure.
Overflow mechanism is additionally provided with the installation for fermenting, overflow mechanism includes overflow pipe and the overflow being connected with overflow pipe Groove, liquid feeding end and the maximum water level of overflow pipe coordinate, and overflow launder is connected to liquid reservoirs by pipeline.
The installation for fermenting bottom is provided with discharging tube, and control valve is provided with discharging tube.
Using the utility model has the advantage of:
1st, the utility model can effectively ensure that the abundant of anaerobe and stalk thing using the structure for copying sealing beehive Contact, improve the fermentation concentration and gas producing efficiency of fermentation reactor, while prevent stalk float crust, realize material it is smooth enter Discharging and simplification operation maintenance.
2nd, effective contact area of zymotic fluid and stalk fermentation region is expanded using the utility model so that organic matter energy It is enough sufficiently to be reacted with stalk material, improve the biogas production efficiency of installation for fermenting.Pass through the left side in stalk fermentation area Right infiltration, effectively take away organic matter caused by straw degradative and fermented to fluid zone, avoid the accumulation of organic acid.
3rd, the liquid baffling fermentation passage that the utility model is formed, it is ensured that zymotic fluid forms baffling in installation for fermenting, Installation for fermenting rear end will not be flowed directly to by feeding frame bottom, the anaerobe containing mass efficient in zymotic fluid, pass through Enter the baffling effect of the arrangement zymotic fluid of material frame, can maximize the contact area of anaerobe and fermented organic;Meanwhile The kinetic energy of zymotic fluid flowing can be good at overcoming the viscous resistance and inertia for permeating zymotic fluid into the stalk filling area of material frame Resistance so that zymotic fluid can sufficiently penetrate into the stalk filling area into material frame, to carry out effective fermentation gas.
4th, using the utility model, zymotic fluid is made during the fermentation, to pass through opening along the fermentation passage flowing of liquid baffling Liquid feeding pump and connection circulation line can realize the return stirring of zymotic fluid so that the zymotic fluid in liquid baffling fermentation passage possesses Kinetic energy, driving fermentation, also stalk of the fermented bacterium effectively into stalk filling area is permeated so that zymotic fluid is with minimum Energy input, uniformly transferring for material, and the repetition contact of microorganism fungus kind and fermentation materials are realized, to reach optimal stalk Ferment effect.
5th, after using the utility model, biogas caused by the anaerobic digestion of stalk filling area, can be fermented by liquid baffling logical Road is effectively discharged, avoid stalk filling area it is blocked up caused by gas release blockage problem.
6th, the utility model is set into material frame guide groove in installation for fermenting inwall, it can be ensured that filler unit enters installation for fermenting After will not be moved in the horizontal direction.
What the 7th, the utility model was set enters material frame, primarily serves the entirety of control harvesting stalk, while causes fermentation liquid energy Enough penetrate into the stalk of material frame.
Brief description of the drawings
Fig. 1 is the utility model fermentation system cross-sectional view;
Fig. 2 is the utility model fermentation system overlooking the structure diagram.
In figure mark for:1. liquid reservoirs;2. liquid feeding pump;3. installation for fermenting;4. overflow mechanism;5. water seal weir;6. most High-water line;7. closure;8. biogas pipe;9. biogas storage area;10. filler unit;11. stalk filling area;12. liquid is rolled over Stream fermentation passage;13. zymotic fluid excessively stream area;14. circulation line;15. liquid supplementation pipe;16. enter material frame guide groove, 17, discharging tube.
Embodiment
Embodiment 1
A kind of honeybee van-type stalk fermentation system, including installation for fermenting 3, closure 7, fermentation dress are provided with installation for fermenting 3 Put 3 with the water-stop of closure 7 to coordinate, multiple filler units 10 for directly loading stalk, filler unit are provided with installation for fermenting 3 10 top surface is located at the maximum water level in installation for fermenting 3, and the bottom surface of filler unit 10 is located at the minimum of the bottom of installation for fermenting 3 At waterline;Filler unit 10 includes stalk filling area 11 and positioned at the zymotic fluid excessively stream area 13 of the end of stalk filling area 11, phase Adjacent two filler unit 10 is positive and negative to be arranged in installation for fermenting 3, by the zymotic fluid excessively stream area 13 of positive and negative setting in installation for fermenting 3 Liquid baffling fermentation passage 12 is formed, the liquid feeding end of liquid baffling fermentation passage 12 is connected with water influent pipeline, and outlet end is connected with Circulation line 14.
In the present embodiment, adjacent two filler units, the 10 positive and negative set-up mode is the zymotic fluid of a filler unit 10 The waterline in excessively stream area 13 is located at maximum water level 6, and the waterline in the zymotic fluid excessively stream area 13 of another filler unit 10 is positioned at most Low water line.
In the present embodiment, the concrete structure of adjacent two filler units, the 10 positive and negative setting is, filler unit 10 Zymotic fluid excessively stream area 13 is located at the upper end of stalk filling area 11, and the zymotic fluid excessively stream area 13 of another filler unit 10 is located at stalk filling The lower end of area 11.
In the present embodiment, the stalk filling area 11 is formed by entering material frame, and entering material frame end set has support, passes through support Form zymotic fluid excessively stream area 13.
In the present embodiment, be provided with the inwall of installation for fermenting 3 in the horizontal direction it is fixed enter material frame enter material frame Guide groove 16, one is entered material frame and is correspondingly arranged two to enter material frame guide groove 16.
In the present embodiment, the length of the filler unit 10 is adapted with the length of installation for fermenting 3, filler unit 10 it is whole Body weight is more than the buoyancy of stalk, and a filler unit 10 enters two fixing sides and fermentation after material frame guide groove 16 is fixed by two The inwall of device 3 is in contact.
In the present embodiment, the fermentation system also includes liquid reservoirs 1, and liquid reservoirs 1 pass through pipeline and feed tube Road and circulation line 14 are connected, and control valve is provided with pipeline, and liquid feeding pump 2 is provided with water influent pipeline, is set on circulation line 14 Control valve is equipped with, liquid reservoirs 1 are also associated with liquid supplementation pipe 15.
In the present embodiment, the top of installation for fermenting 3 is provided with water seal weir 5, and installation for fermenting 3 passes through water seal weir 5 and sealing The water-stop of lid 7 coordinates, and the space between closure 7 and maximum water level 6 forms biogas storage area 9, and natural pond is provided with closure 7 Tracheae 8.
In the present embodiment, the bottom of installation for fermenting 3 is provided with discharging tube 17, and installation for fermenting 3 fermented after a period of time, can By UNICOM's discharging tube 17, the zymotic fluid of installation for fermenting 3 is discharged, zymotic fluid is changed, avoids harmful substance from accumulating.
In the present embodiment, overflow mechanism 4 is additionally provided with the installation for fermenting 3, overflow mechanism 4 includes overflow pipe and with overflowing The overflow launder of flow tube connection, liquid feeding end and the maximum water level 6 of overflow pipe coordinate, and overflow launder is connected to fluid storage by pipeline Pond 1.
Operation principle of the present utility model is:The whole strain stalk of section shape stalk or direct bundling loads the straw of filler unit Behind stalk filling area, filler unit is put into installation for fermenting according to the guiding for entering material frame guide groove in the way of a positive and a negative, then Lift closure with installation for fermenting water-stop to coordinate, installation for fermenting is in sealed environment;Water influent pipeline is connected, disconnects circulation pipe Road, zymotic fluid is injected in installation for fermenting, controls the zymotic fluid in installation for fermenting to disconnect water influent pipeline after maximum water level, Circulation line is connected, zymotic fluid is flowed in baffling fermentation passage, zymotic fluid forms baffling in installation for fermenting, expands fermentation Liquid and stalk contact area, make zymotic fluid fully penetrate into stalk filling area, and take away in stalk filling area caused by degraded Dissolved organic matter, make stalk filling area anaerobic digestion methane production.
Embodiment 2
The present embodiment combination accompanying drawing is described further to the utility model.
As illustrated in fig. 1 and 2, the installation for fermenting 3 of honeybee van-type stalk fermentation system is mainly by filler unit 10, the and of closure 7 Liquid baffling fermentation passage 12 is formed.Filler unit 10 includes stalk filling area 11 and the fermentation positioned at the end of stalk filling area 11 Liquid excessively stream area 13, stalk filling area is formed by entering material frame, and the inwall of installation for fermenting 3 is set into material frame guide groove 16, to ensure into material frame It will not be moved in the horizontal direction after into installation for fermenting 3.Enter material frame to be made up of steel bar, primarily serve control harvesting stalk It is overall, while zymotic fluid is penetrated into the stalk of material frame.The overall weight of filler unit 10 is more than stalk Buoyancy, filler unit 10 is set to be sunken to bottom all the time after entering installation for fermenting 3.
The whole strain stalk of section shape or direct bundling(The process that crushing, rubbing etc. reduce stalk size is eliminated, while not By feed arrangements such as pump, feeding screws), load into after material frame, according to the aligning method shown in Fig. 1, a positive and a negative according to The guiding for entering material frame guide groove 16 is put into installation for fermenting 3.Then lift closure 7 to arrive in water seal weir 5, then in water seal weir 5 Add water so that whole fermentation system is in sealed environment.Biogas pipe 8 is set on closure 7, produced for discharge anaerobic digestion Biogas.
The injection zymotic fluid in liquid reservoirs 1, disconnects the tunnel of circulation pipe 14, connects liquid supplementation pipe 15, opens liquid feeding pump 2, makes Zymotic fluid is filled in installation for fermenting 3.Overflow mechanism 4 is set on the top of installation for fermenting 3, realizes effective control of maximum water level 6. Filler unit 10 is put into the maximum water level 6 of the peak after installation for fermenting 3, as zymotic fluid.Afterwards, liquid supplementation pipe 15 is disconnected, Circulation line 14 is connected, opens liquid feeding pump 2 so that zymotic fluid can be fermented in liquid baffling, and passage 12 is interior to be flowed, and is ensured that Zymotic fluid forms baffling in installation for fermenting 3, will not flow directly to the rear end of installation for fermenting 3 by feeding frame bottom.In zymotic fluid Anaerobe containing mass efficient, acted on by the baffling of the arrangement zymotic fluid of filler unit 10, anaerobe can be made Maximized with the contact area of fermented organic.Meanwhile the kinetic energy of zymotic fluid flowing can be good at overcoming filler unit 10 The viscous resistance and inertia resistance that stalk filling area 11 is permeated to zymotic fluid so that zymotic fluid can sufficiently penetrate into filler list The stalk filling area 11 of member 10, to carry out effective fermentation gas.
Biogas caused by the anaerobic digestion of stalk filling area 11, the passage 12 that can be fermented by liquid baffling are effectively released Put, avoid stalk filling area 11 it is blocked up caused by gas release blockage problem.After the completion of fermentation, biogas pipe 8 is disconnected, is taken away close Capping 7, the filler unit 10 after the completion of fermentation is then taken out, changes and fill new stalk, then repeat above-mentioned sealing, you can The input and output material of reactor is completed, reconnects biogas pipe 8, it is possible to start anaerobic digestion methane production.
During the fermentation, the return stirring of zymotic fluid can be realized by opening liquid feeding pump 2 and connecting circulation line 14, made Zymotic fluid in liquid baffling fermentation passage 12 possesses kinetic energy, drive fermentation also fermented bacterium effectively to stalk filling area 11 Interior stalk is permeated so that zymotic fluid realizes uniformly transferring for material with the Energy input of minimum, and microorganism fungus kind and The repetition contact of fermentation materials, to reach optimal stalk fermentation effect.
Above-mentioned embodiment is to illustrate the utility model, rather than the utility model is limited, Spirit of the present utility model and any modifications and changes in scope of the claims, made to the utility model, all fall Enter the scope of protection of the utility model.

Claims (10)

  1. A kind of 1. honeybee van-type stalk fermentation system, it is characterised in that:Including installation for fermenting(3), installation for fermenting(3)On be provided with it is close Capping(7), installation for fermenting(3)With closure(7)Water-stop coordinates, installation for fermenting(3)Inside it is provided with multiple directly filling stalks Filler unit(10), filler unit(10)Top surface be located at installation for fermenting(3)Interior maximum water level(6)Place, filler unit (10)Bottom surface be located at installation for fermenting(3)At the lowest water level line of bottom;Filler unit(10)Including stalk filling area(11)With Positioned at stalk filling area(11)The zymotic fluid excessively stream area of end(13), adjacent two filler unit(10)It is positive and negative to be arranged on installation for fermenting (3)It is interior, pass through the zymotic fluid excessively stream area of positive and negative setting(13)In installation for fermenting(3)Interior formation liquid baffling fermentation passage(12), Liquid baffling fermentation passage(12)Liquid feeding end be connected with water influent pipeline, outlet end is connected with circulation line(14).
  2. 2. honeybee van-type stalk fermentation system according to claim 1, it is characterised in that:Adjacent two filler unit(10) Positive and negative set-up mode is a filler unit(10)Zymotic fluid excessively stream area(13)Waterline be located at maximum water level(6), separately One filler unit(10)Zymotic fluid excessively stream area(13)Waterline be located at lowest water level line.
  3. 3. honeybee van-type stalk fermentation system according to claim 2, it is characterised in that:Adjacent two filler unit(10) The concrete structure of positive and negative setting is a filler unit(10)Zymotic fluid excessively stream area(13)Positioned at stalk filling area(11)On End, another filler unit(10)Zymotic fluid excessively stream area(13)Positioned at stalk filling area(11)Lower end.
  4. 4. the honeybee van-type stalk fermentation system according to claim 1,2 or 3, it is characterised in that:The stalk filling area (11)Formed by entering material frame, entering material frame end set has support, and zymotic fluid excessively stream area is formed by support(13).
  5. 5. honeybee van-type stalk fermentation system according to claim 4, it is characterised in that:The installation for fermenting(3)On inwall Be provided with the horizontal direction it is fixed enter material frame enter material frame guide groove(16), one is entered material frame and is correspondingly arranged two and enters material frame to lead Groove(16).
  6. 6. honeybee van-type stalk fermentation system according to claim 5, it is characterised in that:The filler unit(10)Length With installation for fermenting(3)Length be adapted, filler unit(10)Overall weight be more than stalk buoyancy, a filler unit (10)Enter material frame guide groove by two(16)Two fixing sides and installation for fermenting after fixation(3)Inwall is in contact.
  7. 7. honeybee van-type stalk fermentation system according to claim 6, it is characterised in that:The fermentation system also includes liquid Storage pool(1), liquid reservoirs(1)Pass through pipeline and water influent pipeline and circulation line(14)Connect, control is provided with pipeline Valve, liquid feeding pump is provided with water influent pipeline(2), circulation line(14)On be provided with control valve, liquid reservoirs(1)It is also associated with Liquid supplementation pipe(15).
  8. 8. honeybee van-type stalk fermentation system according to claim 7, it is characterised in that:The installation for fermenting(3)Top is set It is equipped with water seal weir(5), installation for fermenting(3)Pass through water seal weir(5)With closure(7)Water-stop coordinates, closure(7)With highest water Bit line(6)Between space form biogas storage area(9), closure(7)On be provided with biogas pipe(8).
  9. 9. honeybee van-type stalk fermentation system according to claim 8, it is characterised in that:The installation for fermenting(3)On also set It is equipped with overflow mechanism(4), overflow mechanism(4)The overflow launder being connected including overflow pipe and with overflow pipe, the liquid feeding end of overflow pipe with Maximum water level(6)Coordinate, overflow launder is connected to liquid reservoirs by pipeline(1).
  10. 10. honeybee van-type stalk fermentation system according to claim 9, it is characterised in that:The installation for fermenting(3)Bottom is set It is equipped with discharging tube(17), discharging tube(17)On be provided with control valve.
CN201720545482.8U 2017-05-17 2017-05-17 Honeybee van-type stalk fermentation system Withdrawn - After Issue CN206828525U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201720545482.8U CN206828525U (en) 2017-05-17 2017-05-17 Honeybee van-type stalk fermentation system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201720545482.8U CN206828525U (en) 2017-05-17 2017-05-17 Honeybee van-type stalk fermentation system

Publications (1)

Publication Number Publication Date
CN206828525U true CN206828525U (en) 2018-01-02

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CN201720545482.8U Withdrawn - After Issue CN206828525U (en) 2017-05-17 2017-05-17 Honeybee van-type stalk fermentation system

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106916732A (en) * 2017-05-17 2017-07-04 农业部沼气科学研究所 Honeybee van-type stalk fermentation system and its fermentation process

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106916732A (en) * 2017-05-17 2017-07-04 农业部沼气科学研究所 Honeybee van-type stalk fermentation system and its fermentation process
CN106916732B (en) * 2017-05-17 2019-01-01 农业部沼气科学研究所 Bee van-type stalk fermentation system and its fermentation process

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