CN106281988A - High solid circulation anaerobic reactor - Google Patents
High solid circulation anaerobic reactor Download PDFInfo
- Publication number
- CN106281988A CN106281988A CN201610676015.9A CN201610676015A CN106281988A CN 106281988 A CN106281988 A CN 106281988A CN 201610676015 A CN201610676015 A CN 201610676015A CN 106281988 A CN106281988 A CN 106281988A
- Authority
- CN
- China
- Prior art keywords
- tank body
- unit
- follower
- actuating device
- drivewheel
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M27/00—Means for mixing, agitating or circulating fluids in the vessel
- C12M27/02—Stirrer or mobile mixing elements
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M21/00—Bioreactors or fermenters specially adapted for specific uses
- C12M21/16—Solid state fermenters, e.g. for koji production
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Health & Medical Sciences (AREA)
- Zoology (AREA)
- Engineering & Computer Science (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Organic Chemistry (AREA)
- Chemical & Material Sciences (AREA)
- Wood Science & Technology (AREA)
- Genetics & Genomics (AREA)
- Biomedical Technology (AREA)
- Sustainable Development (AREA)
- Biochemistry (AREA)
- General Engineering & Computer Science (AREA)
- General Health & Medical Sciences (AREA)
- Microbiology (AREA)
- Biotechnology (AREA)
- Molecular Biology (AREA)
- Processing Of Solid Wastes (AREA)
- Treatment Of Sludge (AREA)
Abstract
A kind of high solid circulation anaerobic reactor, including tank body and at least one turn over and copy unit, each turns over copies unit and is arranged in tank body;Described turning over is copied unit and is included drivewheel, actuating device, bearing and follower, actuating device is arranged on the top of bearing, guide cylinder it is provided with on actuating device, the upper and lower of guide cylinder is respectively arranged with discharging opening and charging aperture, drivewheel is connected with the outfan of actuating device, follower is arranged on bearing bottom, and connecting between drivewheel and follower has transmission band, is distributed and turns over duplicate on transmission band.This device is by arranging circularly enhancing disturbance unit in tank body, material in tank body is promoted from bottom to top and falls again, material is made to form overall rolling agitation from bottom to top along tank body, it is particularly well-suited to the viscosity such as muddy, the high pasty state fermentation process compared with big or that solids content is big solid waste, strong adaptability, facilitating manufacture and maintenance, tank body wall and bottom do not result in deposits materials phenomenon.
Description
Technical field
The present invention relates to a kind of device for solid waste being carried out anaerobic fermentation process, belonging to anaerobic fermentation technology
Field.
Background technology
Anaerobic fermentation is one of effective way processing organic solid castoff, and garbage is under anaerobic by micro-life
The metabolic activity of thing and stabilized.Anaerobic fermentation is generally carried out in anaerobic fermentation tank, and anaerobic fermentation tank is the life of microorganism
The excellent condition of long offer, meets growth and the breeding of microorganism.In anaerobic fermentation tank, these its catalysis or the oldest of biological performance
The function of metabolism.Owing to can not there be dissolved oxygen, so need not stirring at a high speed in anaerobic fermentation tank, even if stirring the most only plays mixing
Effect.Also can be passed through nitrogen etc. in anaerobic fermentation tank, but operating cost can be improved.
Anaerobic fermentation tank is not suitable for viscosity compared with big or that solids content is big occasion, because so solid material is at fermentation liquid
Interior skewness, mass transfer effect is the best.To this end, be also equipped with agitating device in some anaerobic fermentation equipments.
Chinese patent literature CN104893958A discloses one " organic waste high-temperature dry-type anaerobic ferment devices ", including
Hydrolysis acidification case and horizontal anaerobic fermentation tank, be provided with auger propeller in anaerobic fermentation tank.But this auger
Angle of rake effect is to advance material by anaerobic fermentation tank feed end to drainage conduit, it is achieved the intermittent feeding of installation for fermenting, continuously
Work and automatic discharge, complete a fermentation period, and material is simply stirred in progradation, and stirring only plays the work of mixing
With, mass transfer is had little to no effect.
A kind of " dry type anaerobic fermentation system " disclosed in CN105647793A, including the feed arrangement being sequentially connected with, anaerobism
Installation for fermenting and drawing mechanism, anaerobic ferment devices includes anaerobic fermentation tank and Monitoring and Controlling mechanism, sets inside anaerobic fermentation tank
Agitating device, agitating device is had to include the many shafts being arranged side by side from fermentation tank charging aperture to discharging opening successively and oar thereof
Leaf, agitating device realizes the stirring successively that many shafts move in circles under the control of Monitoring and Controlling mechanism.Although this system
Realize the stirring successively that many shafts move in circles, adapt to the fermentation process of high impurity material, but this system is by stirring
Mix and reach material conveying and heat transfer (seeing its description the 0027th section).
Anaerobic fermentation tank in above two anaerobic fermentation equipment is all horizontal, and its internal agitating device is mainly used in
Conveying material, does not make solid material being sufficiently mixed in fermentation liquid, and mass transfer is not violent, is not particularly suited for viscosity relatively
Big or that solids content is big fixed-end forces.
CN102952746A disclosed " a kind of anaerobic fermentation tank ", including a tank body and multiple agitator, these agitators
All include a rotary shaft and be positioned at the agitator arm of this rotary shaft one end, the other end of each rotary shaft all with the inwall of this tank body
One join domain in face fixes connection and the axis of each rotary shaft has angle with the normal of this join domain.This fermentation tank leads to
Crossing the form that the normal of join domain that this rotary shaft is arranged to be secured to connect has angle promotes fermentation liquid to form edge
The axial tumble mixed of tank body and/or form the fermentation liquid tumble mixed along tank body radial direction, therefore improve solid material
Distribution consistency degree in fermentation liquid.Agitator in this fermentation tank mainly stirs fermentation liquid, makes fermentation liquid along tank body footpath
To local tumble mixed, it is impossible to enough form overall disturbance from bottom to top in tank body, therefore, the relatively big or solid for viscosity
The solid waste that content is big is also inapplicable.Simultaneously as rotary shaft is installed on the internal face of tank body, manufacture difficulty is relatively big and keeps in repair
Inconvenience.It addition, tank base cannot obtain being sufficiently stirred for of agitator, and it is frequently present of the raw material caused because stirring is uneven
Depositional phenomenon.
Need badly at present and a kind of can efficiently process the viscosity anaerobic fermentation compared with big or that solids content is big solid waste
Equipment.
Summary of the invention
The present invention is directed to the deficiency that existing anaerobic fermentation equipment exists, it is provided that a kind of volume yield rate is high, the suitability is strong, dimension
Protect the highest solid circulation anaerobic reactor.
The solid circulation anaerobic reactor of the height of the present invention, employing following technical proposals:
This device, including tank body and at least one turn over and copy unit, each turns over copies unit and is arranged in tank body;Described turning over copies list
Unit includes drivewheel, actuating device, bearing and follower, and actuating device is arranged on the top of bearing, and actuating device is provided with
Guide cylinder, the upper and lower of guide cylinder is respectively arranged with discharging opening and charging aperture, and drivewheel connects with the outfan of actuating device
Connecing, follower is arranged on bearing bottom, and connecting between drivewheel and follower has transmission band, drivewheel, follower and transmission band
It is placed in guide cylinder, is distributed on transmission band and turns over duplicate.
Copy unit offer an installing hole corresponding to each turning on the top cover of described tank body.
The sewage outfalls setting of described tank body is at the relative side bottom of the dog-house of tank body, to prevent charging from " short-circuit " occurring
Phenomenon.
It is provided with guiding cage, to install or to propose circularly enhancing disturbance unit turning over the periphery copying unit in described tank body
Time avoid mutual scratching.
The described duplicate that turns over is plate, dustpan shaped or bucket type.
Actuating device can use reductor or other device that drivewheel can be driven to rotate.
When said apparatus runs, starting each and turn over and copy unit, reductor drives drivewheel to rotate, and transmission band turns over duplicate
Drive the material (fermentation liquid and solids) in tank body to promote from the bottom to top, formed big inside and outside guide cylinder inside and guide cylinder
The circulation of amplitude ground is stirred, strong mass transfer and strengthening circulation, makes material mixing fully, and mass-transfer efficiency greatly improves.Certain turns over and copies list
Unit breaks down when needing repairing, and is proposed by tank body.
The present invention copies unit by arranging to turn in tank body, is promoted from bottom to top by the material in tank body and falls, makes thing
Material (including solid and fermentation liquid) forms entirety rolling disturbance in tank body from bottom to top, and the room that bottom is formed is rapidly by periphery
Material low level under stress supplements, and therefore, relatively greatly or solids content greatly (can be particularly well-suited to the viscosity such as muddy, high pasty state
Reach 20%) the fermentation process of solid waste, strong adaptability, scale can be realized and process;Simultaneously as turn over copy unit can
Installed by tank body top, it is possible to overall by proposing maintenance in tank body, facilitate manufacture and maintenance.It addition, tank body wall and bottom
Material have also been obtained and is sufficiently stirred for, and does not results in deposits materials phenomenon.
Accompanying drawing explanation
Fig. 1 is the structural representation of the solid circulation anaerobic reactor of height of the present invention.
In figure: 1. tank body, 2. mounting flange, 3. hanger, 4. drivewheel, 5. reductor, 6. bearing, 7. transmission band, 8. turn over
Duplicate, 9. follower, 10. passive wheel seat, 11. guiding cages, 12. sewage draining exits, 13. dog-houses, 14. air vents, 15. guide cylinders,
16. discharging openings, 17. charging apertures.
Detailed description of the invention
As it is shown in figure 1, the solid circulation anaerobic reactor of the height of the present invention, including tank body 1 and at least one turn over and copy unit, each
Turn over that to copy unit vertical or be obliquely installed in tank body 1.Drawing two in Fig. 1 to turn over and copy unit, particular number can be according to tank body 1 internal diameter
Size and the treatment effect of requirement and efficiency determine according to experiment.Dog-house 13 and air vent 14 it is provided with on the top cover of tank body 1,
Bottom is provided with sewage draining exit 12.Solid waste is inserted in tank body 1 by dog-house 13, and the biogas that fermentation produces is by air vent 14 row
Going out, biogas residue and biogas liquid can be discharged by sewage draining exit 12.Sewage draining exit 12 is arranged on tank body 1 side bottom relative to dog-house 13, so that
Charging, fully through respectively turning over the agitation copying unit, prevents charging from " short-circuit " phenomenon occurring.
Copy unit offer an installing hole corresponding to each turning on the top cover of tank body 1.
Described turning over copies unit, including mounting flange 2, drivewheel 4, reductor 5, bearing 6, passive wheel seat 10 and follower 9,
Reductor 5 and passive wheel seat 10 are separately mounted to the upper and lower side of bearing 6, and drivewheel 4 is connected with the outfan of reductor 5, passively
Wheel 9 is arranged on passive wheel seat 10 by bearing, and connecting between drivewheel 4 and follower 9 has transmission band 7.It is distributed on transmission band 7
Turning over duplicate 8, turning over duplicate 8 can be plate, dustpan shaped or bucket type.Drivewheel 4 and follower 9 can be belt wheel or sprocket wheel,
Correspondingly transmission band 7 can be rubber strip or chain.Being also associated with mounting flange 2 on reductor 5, the bottom of mounting flange 2 sets
Being equipped with guide cylinder 15, drivewheel 4, reductor 5, bearing 6, passive wheel seat 10 and follower 9 are arranged in guide cylinder 15, guide
The upper and lower of cylinder 15 is respectively arranged with discharging opening 16 and charging aperture 17.Passive wheel seat 10 can be fixed on guide cylinder 15.
Reductor 5 is also placed in the top of guide cylinder 15, then is connected with drivewheel 4 by drive mechanism.
Whole turning over is copied unit and is inserted in tank body 1 by the installing hole on tank body 1 top cover, and is fixed on tank by mounting flange 2
On the top cover of body 1.For the ease of lifting, mounting flange 2 is provided with hanger 3.Owing to reductor 5 and passive wheel seat 10 are placed in
In tank body 1, the gap of its interior bearing and rotating part is in sealing state.
In order to make respectively to turn over copy load tank body 1 before and after unit during or proposed by tank body 1 will not in maintenance process
There is scratching phenomenon, can turn over each in tank body 1 and destroy unit periphery guiding cage 11 is set.
When said apparatus runs, solid waste inserted in tank body 1 by dog-house 13, starts each and turns over and copy unit, slows down
Machine 5 drives drivewheel 4 to rotate, and material is entered guide cylinder 15 by charging aperture 17, and transmission band 7 turns in duplicate 8 drives tank body 1
Material (fermentation liquid and solids) promotes in guide cylinder 15 from the bottom to top, and releases guide cylinder 15 at discharging opening 16, promotes
The room formed bottom tank body 1 in journey is supplemented by periphery material low level under stress rapidly, in the inside of guide cylinder 15 and lead
Being respectively formed inside and outside barrel 15 and circulate the strong mass transfer stirred significantly, make material mixing fully, mass-transfer efficiency greatly improves.Carry
High anaerobic fermentation efficiency and effect, volume yield rate is high.It is particularly well-suited to that the viscosity such as muddy, high pasty state is relatively big or solid
The fermentation process of the solid waste of content big (up to 20% (moisture content more than 80%)).
The biogas that fermentation produces is discharged by air vent 14, and biogas residue and biogas liquid can be discharged by sewage draining exit 12.Certain turns over and copies unit and go out
When existing fault needs repairing, proposed by tank body.
Claims (5)
1. a high solid circulation anaerobic reactor, is characterized in that: including that tank body and at least one are turned over and copy unit, each turns over copies unit
It is arranged in tank body;Described turning over is copied unit and is included drivewheel, actuating device, bearing and follower, and actuating device is arranged on bearing
Top, actuating device is provided with guide cylinder, the upper and lower of guide cylinder is respectively arranged with discharging opening and charging aperture, actively
Wheel is connected with the outfan of actuating device, and follower is arranged on bearing bottom, and connecting between drivewheel and follower has transmission band,
Drivewheel, follower and transmission band are placed in guide cylinder, be distributed and turn over duplicate on transmission band.
The solid circulation anaerobic reactor of height the most according to claim 1, is characterized in that: corresponding to every on the top cover of described tank body
Individual turning over is copied unit and is offered an installing hole.
The solid circulation anaerobic reactor of height the most according to claim 1, is characterized in that: the sewage outfalls setting of described tank body
The side bottom that charging aperture at tank body is relative.
The solid circulation anaerobic reactor of height the most according to claim 1, is characterized in that: copy outside unit turning in described tank body
Enclose and be provided with guiding cage.
The solid circulation anaerobic reactor of height the most according to claim 1, is characterized in that: described in turn over duplicate be plate, dustpan
Type or bucket type.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610676015.9A CN106281988A (en) | 2016-08-15 | 2016-08-15 | High solid circulation anaerobic reactor |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610676015.9A CN106281988A (en) | 2016-08-15 | 2016-08-15 | High solid circulation anaerobic reactor |
Publications (1)
Publication Number | Publication Date |
---|---|
CN106281988A true CN106281988A (en) | 2017-01-04 |
Family
ID=57678289
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201610676015.9A Pending CN106281988A (en) | 2016-08-15 | 2016-08-15 | High solid circulation anaerobic reactor |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN106281988A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108410717A (en) * | 2018-03-26 | 2018-08-17 | 湖北万禾源豆奶制品有限公司 | A kind of intelligent fermentation tank of Fermented vegetable protein beverage processing |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5879931A (en) * | 1994-02-03 | 1999-03-09 | Kim; Baik Ki | Aerobic fermentation promoting device of excrements, aerobic fermentation system using it and compost therefrom |
CN202081094U (en) * | 2011-04-15 | 2011-12-21 | 江苏大学 | Special mixing device of vertical solid fermentation tank |
CN102441557A (en) * | 2011-10-21 | 2012-05-09 | 中国科学院过程工程研究所 | Aerobic-anaerobic combined solid state fermentation device and fermentation method thereof |
CN104673627A (en) * | 2015-01-10 | 2015-06-03 | 曹晓斌 | Solid-state material mixing equipment |
CN205874408U (en) * | 2016-08-15 | 2017-01-11 | 许中华 | Height anaerobic reactor that circulates admittedly |
-
2016
- 2016-08-15 CN CN201610676015.9A patent/CN106281988A/en active Pending
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5879931A (en) * | 1994-02-03 | 1999-03-09 | Kim; Baik Ki | Aerobic fermentation promoting device of excrements, aerobic fermentation system using it and compost therefrom |
CN202081094U (en) * | 2011-04-15 | 2011-12-21 | 江苏大学 | Special mixing device of vertical solid fermentation tank |
CN102441557A (en) * | 2011-10-21 | 2012-05-09 | 中国科学院过程工程研究所 | Aerobic-anaerobic combined solid state fermentation device and fermentation method thereof |
CN104673627A (en) * | 2015-01-10 | 2015-06-03 | 曹晓斌 | Solid-state material mixing equipment |
CN205874408U (en) * | 2016-08-15 | 2017-01-11 | 许中华 | Height anaerobic reactor that circulates admittedly |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108410717A (en) * | 2018-03-26 | 2018-08-17 | 湖北万禾源豆奶制品有限公司 | A kind of intelligent fermentation tank of Fermented vegetable protein beverage processing |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN106281986A (en) | High solid spiral anaerobic reactor | |
CN104211460B (en) | A kind of quickly aerobic compost reaction unit and application thereof | |
CN205874408U (en) | Height anaerobic reactor that circulates admittedly | |
CN110051021B (en) | Biological maggot protein standard industrial production device and working method thereof | |
CN107649036A (en) | Animal husbandry epidemic prevention drug and feed mixed stirring device | |
CN108440043B (en) | Tipping bucket device | |
CN107760584A (en) | The multilayer agitating device of large-scale feces of livestock and poultry mixed stalk raw material anaerobic fermentation tank | |
CN205874409U (en) | High solid spiral anaerobic reactor | |
CN106000195A (en) | Livestock dairy cow breeding feed stirrer | |
CN108004125A (en) | A kind of Novel anaerobic installation for fermenting | |
CN106281988A (en) | High solid circulation anaerobic reactor | |
CN109876699A (en) | A kind of livestock and poultry feces stirring holding vessel | |
CN208038338U (en) | A kind of hoisting type composting device | |
KR20130016481A (en) | Food disposal equipment | |
KR101789160B1 (en) | Hydraulic-powered auto-agitator sludge | |
KR101574263B1 (en) | Livestock waste stirring device | |
CN214076270U (en) | Agitated vessel is used in fertilizer production | |
CN115011440A (en) | Modularized dynamic aerobic fermentation device and method | |
CN210814886U (en) | Automatic inoculation agitated vessel of fermented feed | |
CN208649337U (en) | A kind of horizontal plug-flow anaerobic dry fermentation apparatus of organic waste | |
CN209721982U (en) | A kind of multi-element biological organic fertilizer production liquid fermentation device | |
CN113526655A (en) | Micro-oxygen hydrolysis acidification device for organic waste | |
CN216863942U (en) | Livestock and poultry manure fermentation device | |
CN112048427A (en) | Fermentation equipment for microbial fermentation of feed and fermentation process thereof | |
KR102128731B1 (en) | Ferment storage tank |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
TA01 | Transfer of patent application right | ||
TA01 | Transfer of patent application right |
Effective date of registration: 20180207 Address after: 250101 Ji'nan hi tech Zone, Shandong Province, No. 4733 A2-1 Applicant after: Shandong Xu China Environmental Protection Technology Co., Ltd. Address before: Licheng District 250101 Shandong city of Ji'nan Province Kang Hong Road flourishing garden 1-4-901 room Applicant before: Xu Zhonghua |
|
RJ01 | Rejection of invention patent application after publication | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20170104 |