CN206298599U - A kind of container solid bio-reactor - Google Patents
A kind of container solid bio-reactor Download PDFInfo
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- CN206298599U CN206298599U CN201621267774.1U CN201621267774U CN206298599U CN 206298599 U CN206298599 U CN 206298599U CN 201621267774 U CN201621267774 U CN 201621267774U CN 206298599 U CN206298599 U CN 206298599U
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- cylinder
- solid bio
- container solid
- reactor according
- container
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/40—Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse
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Abstract
The utility model discloses a kind of container solid bio-reactor.The container solid bio-reactor includes that, by the cylinder of transfer roller support device, the two ends of the rotatably cylinder horizontally set, and cylinder are connected respectively at the dynamic cooperation of fixed end cap；The feed end of the wherein fixed end cap of feed side is provided with charging aperture, and the discharge end of the fixed end cap of exit side is provided with discharging opening.The utility model treating capacity is big, energy consumption is low, is widely used.
Description
Technical field
The utility model is related to a kind of container solid bio-reactor, and belonging to can be widely used in the aerobic hair of biological organic matter
The container bioreaction technology field of ferment treatment.
Background technology
The advantage of drum-type biological organic matter aerobic fermentation is that decomposition rate is fast, cycle is short, and material fermentation is uniform, gas permeability
It is good.
The features such as drum type bioreactor has stirring intensity high, simple structure, continuously runs, in quick aerobic fermentation
There to be extensive prospect of the application etc. biological organic material treatment aspect.
Current drum type bioreactor has been applied, but is far from reaching due use scale, and reason is still setting
The understanding of biological organic matter the principle of fermentation, the balance of material reaction energy consumption and operating cost do not dropped in standby design lower
Etc. aspect, in addition it is also necessary to further improve, therefore, these development works of the present utility model development have important construction value
With social benefit background.
Utility model content
The utility model aims to provide a kind of container solid bio-reactor, and the solid bio-reactor treating capacity is big, energy
Consumption is low, is widely used.
To achieve these goals, the technical scheme that the utility model is used is：
A kind of container solid bio-reactor, including by the cylinder of transfer roller support device, it is structurally characterized in that, can turn
The dynamic cylinder horizontally set, and the two ends of cylinder are connected respectively at the dynamic cooperation of fixed end cap；The wherein fixation of feed side
The feed end of formula end cap is provided with charging aperture, and the discharge end of the fixed end cap of exit side is provided with discharging opening.
Thus, material, supplies and biological inoculum are entered by preliminary mixing from charging aperture, suitable raw in selection addition
Under thing bacterium and supplies effect, aerobic fermentation rapidly and efficiently is carried out, the material for fully completing fermentation is derived by discharging opening, is
System process discharges without external heat source, free from extraneous odour, continuous dynamic, practicality easy to operate.The fixed design at two ends can most volume dress
Material make cylinder container dischargeable capacity maximizes, so as to energy consumption also just it is minimum.
According to embodiment of the present utility model, further optimization can also be made to the utility model, below for optimization after
The technical scheme of formation：
Preferably, equipped with blower fan and the circulating line being connected with blower fan on the fixed end cap；The circulating line
The inner space of air outlet and the cylinder.Thus, the fixed design at two ends allows that equipment is fixed blower fan and added at two ends
Upper circular tube road, come controlling reaction temperature, aerobic amount, blast, reaction can be utilized by circulation this makes it possible to by air quantity
Heat so that energy consumption is also just lower so that without auxiliary thermal source；Systematic procedure reaches collection gas by the control of pipeline switch
Discharge, free from extraneous odour release.
The charging aperture is arranged on the top of feed end, and/or the discharging opening is arranged on the bottom of discharge end.
The cylinder is horizontally disposed, and charging aperture is higher than discharging opening.
It is provided with the cylinder and drives material from feed end to the flow-guiding structure of discharging extreme direction movement.Further, it is excellent
It is the blade construction extended along tubular axis direction to select the flow-guiding structure.
The cylinder is by drive device through actuator drives.
The hygrosensor of detection cylinder lumen temperature is respectively arranged with the feed end and discharge end.
The charging aperture of the feed end is provided with screw feeding structure or ribbon feeding structure.
The discharging opening of the discharge end is provided with belt conveyor or spiral conveying mechanism.
Biological reaction container equipment intermediate receptacle is the drum apparatus for turning rod brace type, two head end covers be it is fixed,
The top of feed end is provided with charging aperture, and the bottom of discharge end is provided with discharging opening.Using transfer roller support meanss, transmission device and blower fan
Plus circulating line.
Material enters shell from charging aperture, is set by the cooperation of control temperature and ventilation volume, in container Inner guide
The lower propulsion of guiding is applied, and as barrel body rotation is sufficiently mixed, is completed during this is advanced to discharging opening by charging aperture
The whole process of oxygen Rapid Fermentation.
Material enters from charging aperture, by controlling the cooperation of temperature, humidity, aerobic amount and blast, selecting addition suitable
Under biological bacteria and supplies effect, through container Inner guide facility guidance, sufficient aerobic fermentation can be rapidly and efficiently carried out, completed
Fermentation materials are derived by discharging opening.
In above-mentioned technical proposal, the fixed design at two ends equipment barrel container can be horizontally mounted so that equipment can be more
Steadily, same volume can load more and make effective volume bigger, be provided with cylinder container beneficial to material propulsion flowing
Deflector.This design can do heavy load equipment using bigger container.
By said structure, material, supplies and biological inoculum can use belt-conveying or spiral by preliminary mixing
Transport and enter from charging aperture, by hygrosensor feedback information, adjust rotating cylinder and rotation speed of fan, coordinate control temperature, humidity,
Aerobic amount and blast, under selection addition suitable biological bacterium and supplies effect, through container Inner guide facility guidance, are carried out fast
Fast efficient aerobic fermentation, the material for fully completing fermentation is derived by discharging opening, can be transported to stockyard with belt-conveying or spiral
Storage（Or make other purposes）, systematic procedure discharges without external heat source, free from extraneous odour, continuous dynamic, practicality easy to operate.
Compared with prior art, the beneficial effects of the utility model are：This container biologic reaction equipment of the utility model
Aerobic fermentation treatment, the completion zymotechnique biological respinse of the quick low energy consumption of energy of various biological organic matters are can be widely applied to,
The fields such as organic fertilizer production, the enhancement of environment of plant, municipal sludge treatment, kitchen castoff treatment and forest gardens can be done
Go out big contribution.
The utility model is installed using transfer roller support meanss and equipment barrel vessel level and coordinated so that equipment stress is equal
Even, continuous dynamic even running, equipment is durable in use, maintenance cost is low, easy to operate.
Brief description of the drawings
Fig. 1 is the structure principle chart of the utility model one embodiment；
Fig. 2 is the right view of Fig. 1；
Fig. 3 is the left view of Fig. 1.
In figure
1- cylinders；2- feed ends；3- discharge ends；4- transfer roller support meanss；5- transmission devices；6- blower fans；7- circulation pipes
Road；8- hygrosensors；9- charging apertures；10- discharging openings.
Specific embodiment
Describe the utility model in detail below with reference to accompanying drawing and in conjunction with the embodiments.It should be noted that not conflicting
In the case of, the feature in embodiment and embodiment in the utility model can be mutually combined.For sake of convenience, hereinafter such as
Occur " on ", D score, "left", "right" printed words, only represent that upper and lower, left and right direction with accompanying drawing in itself is consistent, not to structure
Play restriction effect.
A kind of container solid bio-reactor of rapidly and efficiently low energy consumption, intermediate receptacle can be the cylinder 1 of rotation, cylinder
1 by the support rotating of transfer roller support meanss 4, and the two ends of cylinder 1 are fixed end cap, and the top of feed end is provided with charging aperture 2,
The bottom of discharge end is provided with discharging opening 3, using transfer roller support meanss 4, transmission device 5, blower fan 6, circulating line 7 and temperature sensing
Device 8.
The fixed end cap of bioreactor, the top of feed end is provided with charging aperture 2, and the bottom of discharge end is provided with
Discharging opening 3
The fixed end cap in bioreactor two ends, fixes blower fan 6 and circulating line 7, such energy on end cap
Oxygen amount, blast are controlled as needed and gas and control discharge is collected, and this device can also balanced reaction temp.
The fixed end cap in bioreactor two ends, end cap fixed installation hygrosensor 8, so can basis
Temperature requirements adjust the speed of blower fan and rotating cylinder.
The fixed end cap in bioreactor two ends is horizontally mounted by cylinder 1.
In above-mentioned technical proposal, cooperation is horizontally mounted using transfer roller support meanss 5 and cylinder 1 rolling is driven.This practicality is new
The bioreactor of type does not have assisted reaction thermal source, can completion treatment by material autoreactivity heat.
The utility model is introduced by taking the solid bio-reactor in vaccary as an example below：
Feed end：Operative processes the cow dung in vaccary by wringer, and excrement slag material spiral is transported from charging
Mouth enters, and adjusts rotating cylinder and rotation speed of fan；
In reaction vessel, coordinate control temperature, humidity, aerobic amount and blast, under biological bacteria and material effect, through container
Inner guide facility guidance, is carrying out the reaction of aerobic fermentation rapidly and efficiently；Workman only need to look after lower mechanical part without people's multitube
Whether to refuel, look at whether temperature needs adjustment.
Discharge end：Operative will check the complete material of fermentation by discharging opening derivation, then notify throat-fed, lead
The material belt-conveying for going out deliver to stockyard storage, place one week after, can be used as the high-quality organic fertilizer of no disease and pests harm or
Sell, can also be used as the place mat material of cattle pen.
Equipment of the present utility model is horizontal, and equipment intermediate receptacle is rotary roller support rotating cylinder design, and two head end covers are consolidated
It is fixed, thus can most volume charging the dischargeable capacity of container is maximized, so that energy consumption is also just minimum.The top of feed end sets
The bottom for having charging aperture, discharge end is provided with discharging opening.Material enters from charging aperture, by controlling temperature, humidity, aerobic amount and wind
The cooperation of pressure, selection addition suitable biological bacterium and supplies effect under, through container Inner guide facility guidance, can be rapidly and efficiently
Sufficient aerobic fermentation is carried out, complete fermentation materials is derived by discharging opening, systematic procedure discharges without external heat source, free from extraneous odour, connects
Continuous dynamic, practicality easy to operate.
The content that above-described embodiment is illustrated should be understood to that these embodiments are only used for being illustrated more clearly that the utility model,
Rather than scope of the present utility model is limited, after the utility model has been read, those skilled in the art are new to this practicality
The modification of the various equivalent form of values of type each falls within the application appended claims limited range.
Claims (10)
1. a kind of container solid bio-reactor, including by transfer roller support meanss（4）The cylinder of support（1）, it is characterised in that can
The cylinder for rotating（1）Horizontally set, and cylinder（1）Two ends respectively at fixed end cap it is dynamic coordinate be connected；Wherein feed
The feed end of the fixed end cap of side（2）It is provided with charging aperture（9）, the discharge end of the fixed end cap of exit side（3）It is provided with
Discharging opening（10）.
2. container solid bio-reactor according to claim 1, it is characterised in that wind is housed on the fixed end cap
Machine（6）And with blower fan（6）Connected circulating line（7）；The circulating line（7）Air outlet and the cylinder（1）Inner chamber
Connection.
3. container solid bio-reactor according to claim 1, it is characterised in that the charging aperture（9）Be arranged on into
Material end（2）Top, and/or the discharging opening（10）It is arranged on discharge end（3）Bottom.
4. container solid bio-reactor according to claim 1, it is characterised in that the cylinder（1）It is horizontally disposed, and
Charging aperture is higher than discharging opening.
5. container solid bio-reactor according to claim 1, it is characterised in that the cylinder（1）Inside it is provided with driving
Material is from feed end（2）To discharge end（3）The flow-guiding structure of direction movement.
6. container solid bio-reactor according to claim 5, it is characterised in that the flow-guiding structure is along cylinder
（1）The blade construction that axis direction extends.
7. the container solid bio-reactor according to any one of claim 1-6, it is characterised in that the cylinder（1）
By drive device through transmission device（5）Drive.
8. the container solid bio-reactor according to any one of claim 1-6, it is characterised in that the feed end
（2）And discharge end（3）On be respectively arranged with detection cylinder（1）The hygrosensor of inner chamber temperature（8）.
9. the container solid bio-reactor according to any one of claim 1-6, it is characterised in that the feed end
（2）Charging aperture（9）It is provided with screw feeding structure or ribbon feeding structure.
10. the container solid bio-reactor according to any one of claim 1-6, it is characterised in that the discharge end
（3）Discharging opening（10）It is provided with belt conveyor or spiral conveying mechanism.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621267774.1U CN206298599U (en) | 2016-11-23 | 2016-11-23 | A kind of container solid bio-reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621267774.1U CN206298599U (en) | 2016-11-23 | 2016-11-23 | A kind of container solid bio-reactor |
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| Publication Number | Publication Date |
|---|---|
| CN206298599U true CN206298599U (en) | 2017-07-04 |
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ID=59211447
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621267774.1U Active CN206298599U (en) | 2016-11-23 | 2016-11-23 | A kind of container solid bio-reactor |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108094227A (en) * | 2018-01-31 | 2018-06-01 | 哈尔滨华美亿丰复合材料有限公司 | A kind of milk cow bed bedding and padding generating apparatus again |
| CN109355179A (en) * | 2018-11-15 | 2019-02-19 | 菽乡(重庆)农业科技有限责任公司 | A kind of Salt black bean installation for fermenting and zymotechnique |
-
2016
- 2016-11-23 CN CN201621267774.1U patent/CN206298599U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108094227A (en) * | 2018-01-31 | 2018-06-01 | 哈尔滨华美亿丰复合材料有限公司 | A kind of milk cow bed bedding and padding generating apparatus again |
| CN108094227B (en) * | 2018-01-31 | 2023-09-05 | 哈尔滨华美亿丰成套设备制造有限公司 | Milk cow bed pad regeneration facility |
| CN109355179A (en) * | 2018-11-15 | 2019-02-19 | 菽乡(重庆)农业科技有限责任公司 | A kind of Salt black bean installation for fermenting and zymotechnique |
| CN109355179B (en) * | 2018-11-15 | 2021-09-14 | 菽乡(重庆)农业科技有限责任公司 | Fermented soya bean fermentation device and fermentation process |
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