CN205295179U - Automatic fermented tower of control - Google Patents
Automatic fermented tower of control Download PDFInfo
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- CN205295179U CN205295179U CN201620006688.9U CN201620006688U CN205295179U CN 205295179 U CN205295179 U CN 205295179U CN 201620006688 U CN201620006688 U CN 201620006688U CN 205295179 U CN205295179 U CN 205295179U
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- tower body
- tower
- inlet
- automatically controlled
- zymocyte
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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 an automatic fermented tower of control, include: tower body and filling pipe system, be provided with agitating unit in the tower body, tower body bottom be provided with with the drive arrangement of agitating unit drive intercommunication, the tower body top be provided with a plurality of filling openings with the filling pipe system intercommunication, the tower body top still is provided with the feed inlet, the tower body bottom is provided with the discharge gate, agitating unit includes multilayer stirring paddle leaf, the last sprinkler that is provided with of stirring paddle leaf, a plurality of filling openings communicate respectively the last sprinkler of stirring paddle leaf, still be provided with multilayer detector and sampling device on the tower body, one side of tower body still is provided with a tail gas treatment ware, the tail gas treatment ware with the tail gas discharge port intercommunication at tower body top. The utility model discloses can improve the efficiency of fermentation translation.
Description
Technical field
This utility model relates to fermentation technical field, in particular, relates to a kind of fermentation tower automatically controlled.
Background technology
Zymolysis Equipment be employed with in large-scale food, Chemical Manufacture.
Produce upper that use and that domestic and international patent the is mentioned mode utilizing industrial or agricultural organic waste to produce organic fertilizer fermentation at present, mainly there are slot type, tower, drum-type, heap formula four kinds, it is designed with greatly the device of stirring of dynamic power machine, such as machineries of stirring such as plough, paddle, agitator type, turnover plate types, to reach to stir evenly the purpose with oxygenating.
The Chinese patent that application number is CN03240216.3 proposes a kind of automatic stirring air make-up fermentation tower, equipped with horizontally arranged multilamellar blowdown pipe inside fermentation tower, the blowdown pipe dislocation of each layer or installation of changing direction, tower body bottom is provided with discharging machine, top is equipped with material distributing machine, and tower body side is equipped with blender and crane. Fermentation raw material loads in fermentation tower by elevator after stirring evenly, and material, changing direction and declining in the blowdown pipe of arranged in dislocation, plays stirring action, simultaneously QI invigorating, promotes fermentation.
But, adjuvant can not be effectively mixed in material by the alr mode of this structure, can not well control temperature, humidity and amount of oxygen etc.
Utility model content
Technical problem to be solved in the utility model is to provide a kind of fermentation tower automatically controlled that effectively can be mixed into adjuvant, control temperature, humidity and amount of oxygen uniformly.
The purpose of this utility model is achieved through the following technical solutions:
A kind of fermentation tower automatically controlled, including: tower body and injected system; It is provided with agitating device in described tower body, it is provided with bottom described tower body and drives, with described agitating device, the driving device connected, described tower body top is provided with multiple inlet and connects with described injected system, and described tower body top is additionally provided with charging aperture, is provided with discharging opening bottom described tower body;
Described agitating device includes multiple impellers leaf, and described stirrer paddle is provided with flusher, and the plurality of inlet is respectively communicated with the flusher on described stirrer paddle;
Described tower body is additionally provided with multi-layer detector and sampler;
The side of described tower body is additionally provided with an exhaust gas treating device, and described exhaust gas treating device connects with the tail gas outlet at described tower body top.
Preferably, described driving device includes hydraulic motor and the Hydraulic Station connected with this hydraulic motor, described hydraulic motor includes two hydraulic cylinders and the master gear being in transmission connection with said two hydraulic cylinder, and described master gear is arranged on the main shaft of described agitating device.
Preferably, every layer of described detector includes: humiture probe, oxygen probe, bacterium probe, and described humiture probe, oxygen probe, bacterium probe are arranged on the tower wall of tower body.
Preferably, described sampler is the probe tube being arranged on tower body tower wall.
Preferably, described injected system includes: add zymocyte pump, humidification pump and oxygenation module, described in add zymocyte pump, humidification pump and oxygenation module respectively through pipeline communication to the plurality of inlet.
Preferably, described in add and between the pipeline that zymocyte pump connects with the plurality of inlet, be additionally provided with a zymocyte distributor, described zymocyte distributor connects to be distributed in multiple inlet zymocyte with multiple inlets respectively.
Preferably, being additionally provided with a humidification distributor with the plurality of inlet between the pipeline that described humidification pump connects, described humidification distributor connects to be distributed in multiple inlet moisture content with multiple inlets respectively.
Preferably, described oxygenation module includes: oxygenerator that air compressor connects with air compressor and the adjustable oxygen distribution ware being connected respectively with the air line of oxygenerator and oxygen channel, described adjustable oxygen distribution ware is communicated to the plurality of inlet.
Preferably, described oxygenation module also includes steam generator and the steam heat-exchanging control oxygen distribution device connected with steam generator, and described steam heat-exchanging control oxygen distribution device is communicated to described adjustable oxygen distribution ware and the plurality of inlet.
Preferably, described flusher includes the conveyance conduit connected with described inlet and the blade shower nozzle being arranged on conveyance conduit.
Preferably, described stirrer paddle includes many groups, and often group stirrer paddle is made up of two panels stirrer paddle, and wherein, except one group of stirrer paddle of top, all the other stirrer paddles are provided with described flusher; In the described stirrer paddle being provided with flusher, often adjacent two groups independently control temperature, humidity, oxygen amount and zymocyte amount.
Preferably, the blade of described stirrer paddle is provided with tip configuration.
The benefit that this utility model brings is: the agitating device of fermentation tower includes multiple impellers leaf, and stirrer paddle is provided with flusher, thus the control being mixed into, including temperature, humidity etc. of adjuvant can be carried out in whipping process by connecting the flusher of injected system, so that the control of adjuvant, temperature, humidity can reach uniformly reliable, make fermentation reaction more abundant, in hgher efficiency.
Accompanying drawing explanation
Fig. 1 is the fermentation tower housing structure figure of this utility model embodiment;
Fig. 2 is the V-V sectional view of Fig. 1;
The tower body inlet that Fig. 3 is this utility model embodiment docks schematic diagram with the pipeline of injected system;
Fig. 4 is the injected system structural representation of this utility model embodiment;
Fig. 5 is the stirrer paddle structural representation of this utility model embodiment;
Fig. 6 is the lateral plan of Fig. 5.
Detailed description of the invention
Preferred implementation of the present utility model is described below, and those of ordinary skill in the art according to hereinafter described being realized by the correlation technique of this area, and will can will be apparent from innovation of the present utility model and the benefit brought.
Embodiment one
Being illustrated in figure 1 a kind of fermentation tower specific embodiment automatically controlled provided based on this utility model, this fermentation tower includes: tower body 100 and injected system 200; It is provided with agitating device in described tower body 100, it is provided with bottom described tower body and drives, with described agitating device, the driving device connected, described tower body 100 top is provided with multiple inlet and connects with described injected system, described tower body 100 top is additionally provided with charging aperture 101, is provided with discharging opening 102 bottom described tower body 100; Described agitating device includes multiple impellers leaf 122, and described stirrer paddle 122 is provided with flusher, and the plurality of inlet is respectively communicated with the flusher on described stirrer paddle 122; Described tower body 100 is additionally provided with multi-layer detector and sampler; The side of described tower body 100 is additionally provided with an exhaust gas treating device 150, and described exhaust gas treating device 150 connects with the tail gas outlet 151 at described tower body 100 top. Concrete, the inlet at described tower body 100 top includes: inlet 1a, inlet 2a, inlet 3a, inlet 4a, inlet 5a, inlet 1b, inlet 2b, inlet 3b, inlet 4b, inlet 5b; Stirrer paddle 122 includes: blade 1A, blade 2A, blade 3A, blade 4A, blade 5A, blade 1B, blade 2B, blade 3B, blade 4B, blade 5B; Above-mentioned blade corresponding inlet respectively is arranged, in whipping process, the control being mixed into, including temperature, humidity (temperature of gas, humidity) etc. of adjuvant (including oxygen, zymocyte etc.) is carried out by the flusher of inlet connection injected system, so that the control of adjuvant, temperature, humidity can reach uniformly reliable, make fermentation reaction more abundant, in hgher efficiency.
As shown in Figure 2, in the present embodiment, described driving device includes hydraulic motor 130 and the Hydraulic Station 133 connected with this hydraulic motor 130, described hydraulic motor 130 includes two hydraulic cylinders 132 and the master gear 131 being in transmission connection with said two hydraulic cylinder 132, and described master gear 131 is arranged on the main shaft 121 of described agitating device. Two hydraulic cylinders 132 are sent control signal and open their electromagnetic valve by the hydraulic control system of Hydraulic Station 133, two hydraulic cylinders 132 are made to start alternation drive shaft 121, the many impulse strokes of mode of the comparable hydraulic cylinder works of mode of two hydraulic cylinders 132 alternation, such that it is able to accelerate the rotary speed of main shaft 121, improve stirring efficiency.
As it is shown in figure 5, described flusher includes the conveyance conduit 123 connected with described inlet and the blade shower nozzle 124 being arranged on conveyance conduit 123. Conveyance conduit 123 is arranged on the support rib of blade, can by the pipeline communication in or beyond main shaft 121 to inlet.
As it is shown in figure 1, in the present embodiment, every layer of described detector includes: humiture probe 111, oxygen probe 112, bacterium probe 113, and described humiture probe 111, oxygen probe 112, bacterium probe 113 are arranged on the tower wall of tower body. In the present embodiment, tower body sets 5 Layer Detection devices altogether, to monitor the humiture of differing heights position of whole tower body, oxygen content, zymocyte content etc. Being designed with sampler in every Layer Detection device, described sampler is the probe tube being arranged on tower body tower wall.
It is illustrated in figure 3 fermentation tower injected system and the pipeline connection diagram of inlet on tower body, Fig. 4 show the injected system structure chart of fermentation tower, described injected system 200 includes: add zymocyte pump 202, humidification pump 201 and oxygenation module, described in add zymocyte pump 202, humidification pump 201 and oxygenation module respectively through pipeline communication to the plurality of inlet.
The thalline needs adding zymocyte pump 202 are uniformly injected in each inlet, therefore, described adding, is additionally provided with a zymocyte distributor 208 with the plurality of inlet between the pipeline that zymocyte pump 202 connects, described zymocyte distributor 208 respectively with multiple inlets by pipeline communication so that zymocyte is distributed in multiple inlet. Certainly, the connection by pipeline communication non-substantivity described in the present embodiment, pipeline is further typically provided with valve to control the circulation of pipeline.
Same, it being additionally provided with a humidification distributor 209 with the plurality of inlet between the pipeline that described humidification pump 201 connects, described humidification distributor 209 connects to be distributed in multiple inlet moisture content with multiple inlets respectively.
In the present embodiment, described oxygenation module includes: oxygenerator 206 that air compressor 205 connects with air compressor 205 and the adjustable oxygen distribution ware 207 being connected respectively with the air line of oxygenerator 206 and oxygen channel, described adjustable oxygen distribution ware 207 is communicated to the plurality of inlet.
In addition, in the present embodiment, described oxygenation module also includes steam generator 203 and the steam heat-exchanging control oxygen distribution device 204 connected with steam generator 203, and described steam heat-exchanging control oxygen distribution device 204 is communicated to described adjustable oxygen distribution ware and the plurality of inlet.
During work, the raw material of fermentation enters from charging aperture 101, discharge at bottom discharge mouth 102, in continuous operation situation, fermentation raw material enters directly into the two-layer blade bottom fermentation tower, air enters into oxygenerator from oil-free air compressor, and the air door KF and oxygen valve YF that open oxygenerator are adjusted the concentration 30��80% of oxygen simultaneously to adjustable oxygen distribution ware.
Open valve KF: only normal air input extremely adjustable oxygen distribution ware
Open valve YF: be the oxygen input extremely adjustable oxygen distribution ware of oxygen content about 90%
Open valve ZQJR: steam enters mixture of oxygen body of can heating in steam heat-exchanging distributor
Open valve ZQF: steam and mixture of oxygen body are directly entered stirring vane in empty oxygen steam distributor mixing, and it is fast that fermented product temperature rises.
Mixing oxygen enters in described steam heat-exchanging control oxygen distribution device 204 by empty oxygen valve KYF after regulating, now described steam heat-exchanging control oxygen distribution device 204 is empty oxygen steam distributor, the steam valve ZQF that steam is from steam generator opens, vapor (steam) temperature is 100 DEG C and mixes at control oxygen steam distributor with mixture of oxygen body, opens valve 1R entrance fermentation tower bottom two layers stirring vane and heats.
When initial reaction stage, Hydraulic Station, oil-free air compressor, oxygenerator, steam generator, the valve (KF, YF, KYF, ZQF) of exhaust gas treating device is opened simultaneously.
When heating-up temperature reaches 80 DEG C, valve (1R, ZQF) is closed and is opened valve 1Y continuation supply mixing oxygen simultaneously, is then turned on valve 1R, closes valve 1Y and steam valve ZQF when 65 DEG C. Opening steam heating valve ZQJR, now steam heat-exchanging control oxygen distribution device 204 is steam heat-exchanging distributor.
Start " adding zymocyte pump 202 ", more step Open valve 1J (can select open 3 seconds, close 10 seconds, open again 3 seconds, circulate with this, but concrete opening/closing time determines according to adding bacterium amount), by detecting, after zymocyte is saturated, closes valve 1J and add zymocyte pump 202.
When humidity is lower than 50%, (humidity is to be detected by humidity sensor), start humidification pump 201, open valve 1S simultaneously and (3 seconds can be selected open, close 10 seconds, then open 3 seconds, circulate with this, but concrete opening/closing time determines according to humidity amount), humidity reaches 60% closedown valve 1S and humidification pump 201.
The content of fermentation tower oxygen opens valve 1Y when declining, close valve KF, and air enters adjustable oxygen distribution ware by oxygenerator from valve YF, opens the high oxygen of valve 1Y content and is directly entered fermentation tower one layer. The content of oxygen reaches requirement and turns on valve KF, valve 1Y continuation for mixing oxygen.
If temperature is lower than 45%, the steam valve ZQF of steam generator opens, and vapor (steam) temperature is 100 DEG C and mixes at control oxygen steam distributor with mixture of oxygen body, and opening valve 1R and enter fermentation tower, two-layer stirring vane is heated.
In the present embodiment, described stirrer paddle includes many groups, and often group stirrer paddle is made up of two panels stirrer paddle, and wherein, except one group of stirrer paddle of top, all the other stirrer paddles are provided with described flusher; In the described stirrer paddle being provided with flusher, often adjacent two groups independently control temperature, humidity, oxygen amount and zymocyte amount. It is to say, the stirrer paddle of reaction tower top is the blade not having function, all the other every two groups of stirrer paddles independently control temperature, humidity, oxygen amount and zymocyte amount.
Raw material enters from the charging aperture at top, direct bottomed portion, and whole fermentation tower is straight-through, and every two-layer blade is all and is set forth above the same, independent controls. As shown in Figure 6, blade being provided with tip configuration, tip configuration is to be frictional dissipation in order to what reduce blade working process.
Above content is in conjunction with concrete preferred implementation further detailed description of the utility model, it is impossible to assert that of the present utility model being embodied as is confined to these explanations. For this utility model person of an ordinary skill in the technical field; without departing from the concept of the premise utility; some simple deduction or replace can also be made; as type of drive can adopt electric machine external or hydraulic power etc.; and tractive manner is except the above embodiments; can also adopting other tractive manner such as wirerope strand cable, these all should be considered as belonging to protection domain of the present utility model.
Claims (12)
1. the fermentation tower automatically controlled, it is characterised in that including: tower body and injected system; It is provided with agitating device in described tower body, it is provided with bottom described tower body and drives, with described agitating device, the driving device being connected, described tower body top is provided with multiple inlet and connects with described injected system, and described tower body top is additionally provided with charging aperture, is provided with discharging opening bottom described tower body;
Described agitating device includes multiple impellers leaf, and described stirrer paddle is provided with flusher, and the plurality of inlet is respectively communicated with the flusher on described stirrer paddle in order to the temperature in control tower, humidity, oxygen amount and zymocyte amount;
Described tower body is additionally provided with multi-layer detector and sampler;
The side of described tower body is additionally provided with an exhaust gas treating device, and described exhaust gas treating device connects with the tail gas outlet at described tower body top.
2. the fermentation tower automatically controlled as claimed in claim 1, it is characterized in that, described driving device includes hydraulic motor and the Hydraulic Station connected with this hydraulic motor, described hydraulic motor includes two hydraulic cylinders and the master gear being in transmission connection with said two hydraulic cylinder, and described master gear is arranged on the main shaft of described agitating device.
3. the fermentation tower automatically controlled as claimed in claim 1, it is characterised in that every layer of described detector includes: humiture probe, oxygen probe, bacterium probe, described humiture probe, oxygen probe, bacterium probe are arranged on the tower wall of tower body.
4. the fermentation tower automatically controlled as claimed in claim 1, it is characterised in that described sampler is the probe tube being arranged on tower body tower wall.
5. the fermentation tower automatically controlled as claimed in claim 1, it is characterized in that, described injected system includes: add zymocyte pump, humidification pump and oxygenation module, described in add zymocyte pump, humidification pump and oxygenation module respectively through pipeline communication to the plurality of inlet.
6. the fermentation tower automatically controlled as claimed in claim 5, it is characterized in that, described adding, is additionally provided with a zymocyte distributor with the plurality of inlet between the pipeline that zymocyte pump connects, described zymocyte distributor connects to be distributed in multiple inlet zymocyte with multiple inlets respectively.
7. the fermentation tower automatically controlled as claimed in claim 5, it is characterized in that, being additionally provided with a humidification distributor with the plurality of inlet between the pipeline that described humidification pump connects, described humidification distributor connects to be distributed in multiple inlet moisture content with multiple inlets respectively.
8. the fermentation tower automatically controlled as claimed in claim 5, it is characterized in that, described oxygenation module includes: oxygenerator that air compressor connects with air compressor and the adjustable oxygen distribution ware being connected respectively with the air line of oxygenerator and oxygen channel, described adjustable oxygen distribution ware is communicated to the plurality of inlet.
9. the fermentation tower automatically controlled as claimed in claim 8, it is characterized in that, described oxygenation module also includes steam generator and the steam heat-exchanging control oxygen distribution device connected with steam generator, and described steam heat-exchanging control oxygen distribution device is communicated to described adjustable oxygen distribution ware and the plurality of inlet.
10. the fermentation tower automatically controlled as claimed in claim 1, it is characterised in that described flusher includes the conveyance conduit connected with described inlet and the blade shower nozzle being arranged on conveyance conduit.
11. the fermentation tower automatically controlled as claimed in claim 1, it is characterised in that described stirrer paddle includes many groups, often group stirrer paddle is made up of two panels stirrer paddle, wherein, except one group of stirrer paddle of top, all the other stirrer paddles are provided with described flusher; In the described stirrer paddle being provided with flusher, often adjacent two groups independently control temperature, humidity, oxygen amount and zymocyte amount.
12. the fermentation tower automatically controlled as claimed in claim 1, it is characterised in that be provided with tip configuration on the blade of described stirrer paddle.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620006688.9U CN205295179U (en) | 2016-01-04 | 2016-01-04 | Automatic fermented tower of control |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620006688.9U CN205295179U (en) | 2016-01-04 | 2016-01-04 | Automatic fermented tower of control |
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| CN205295179U true CN205295179U (en) | 2016-06-08 |
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| CN201620006688.9U Active CN205295179U (en) | 2016-01-04 | 2016-01-04 | Automatic fermented tower of control |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107164225A (en) * | 2017-06-12 | 2017-09-15 | 福州法莫优科机械科技有限公司 | Solid bacterium Slag treatment device and its application method |
| CN108218491A (en) * | 2018-01-20 | 2018-06-29 | 徐州市禾协肥业有限公司 | There is the belt installation for fermenting of temperature and humidity adjustment |
| CN109400238A (en) * | 2019-01-03 | 2019-03-01 | 占学宽 | Organic active fertilizer preparation process |
| CN109439510A (en) * | 2018-11-12 | 2019-03-08 | 北京天极视讯科技发展有限公司 | A kind of meter probe protection cleaning device, gas-detecting device and Zymolysis Equipment |
-
2016
- 2016-01-04 CN CN201620006688.9U patent/CN205295179U/en active Active
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107164225A (en) * | 2017-06-12 | 2017-09-15 | 福州法莫优科机械科技有限公司 | Solid bacterium Slag treatment device and its application method |
| CN108218491A (en) * | 2018-01-20 | 2018-06-29 | 徐州市禾协肥业有限公司 | There is the belt installation for fermenting of temperature and humidity adjustment |
| CN108218491B (en) * | 2018-01-20 | 2023-09-05 | 徐州市禾协肥业有限公司 | Belt fermentation device with temperature and humidity adjusting function |
| CN109439510A (en) * | 2018-11-12 | 2019-03-08 | 北京天极视讯科技发展有限公司 | A kind of meter probe protection cleaning device, gas-detecting device and Zymolysis Equipment |
| CN109400238A (en) * | 2019-01-03 | 2019-03-01 | 占学宽 | Organic active fertilizer preparation process |
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