CN203602514U - Tower-type self-coupling deodorizing high-temperature aerobic fermentation system - Google Patents
Tower-type self-coupling deodorizing high-temperature aerobic fermentation system Download PDFInfo
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- CN203602514U CN203602514U CN201320850808.XU CN201320850808U CN203602514U CN 203602514 U CN203602514 U CN 203602514U CN 201320850808 U CN201320850808 U CN 201320850808U CN 203602514 U CN203602514 U CN 203602514U
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- 238000010168 coupling process Methods 0.000 title claims abstract description 31
- 238000005859 coupling reaction Methods 0.000 title claims abstract description 31
- 230000001877 deodorizing effect Effects 0.000 title claims abstract description 22
- 238000010564 aerobic fermentation Methods 0.000 title claims abstract description 18
- 238000000855 fermentation Methods 0.000 claims abstract description 66
- 230000004151 fermentation Effects 0.000 claims abstract description 66
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 18
- 239000001301 oxygen Substances 0.000 claims abstract description 18
- 238000007599 discharging Methods 0.000 claims abstract description 13
- 238000009423 ventilation Methods 0.000 claims abstract description 13
- 230000008878 coupling Effects 0.000 claims description 27
- 239000000463 material Substances 0.000 claims description 26
- 239000007789 gas Substances 0.000 claims description 19
- 239000000109 continuous material Substances 0.000 claims description 7
- 210000003050 axon Anatomy 0.000 claims description 3
- 239000002361 compost Substances 0.000 abstract description 30
- 238000009264 composting Methods 0.000 abstract description 9
- 238000005070 sampling Methods 0.000 abstract 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 9
- 238000005516 engineering process Methods 0.000 description 8
- 238000000034 method Methods 0.000 description 6
- 239000002154 agricultural waste Substances 0.000 description 5
- 238000012545 processing Methods 0.000 description 4
- 238000013022 venting Methods 0.000 description 4
- 239000010410 layer Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000002689 soil Substances 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 238000001514 detection method Methods 0.000 description 2
- 210000003608 fece Anatomy 0.000 description 2
- 239000003337 fertilizer Substances 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 230000033001 locomotion Effects 0.000 description 2
- 238000012544 monitoring process Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 1
- 241000726221 Gemma Species 0.000 description 1
- 229910002651 NO3 Inorganic materials 0.000 description 1
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 235000011089 carbon dioxide Nutrition 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000004332 deodorization Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000010794 food waste Substances 0.000 description 1
- 210000002683 foot Anatomy 0.000 description 1
- 239000011229 interlayer Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 244000144972 livestock Species 0.000 description 1
- 239000010871 livestock manure Substances 0.000 description 1
- 244000005706 microflora Species 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 239000010815 organic waste Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 244000144977 poultry Species 0.000 description 1
- 238000000197 pyrolysis Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000003516 soil conditioner Substances 0.000 description 1
- 239000007790 solid phase Substances 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 239000010902 straw Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
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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
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
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- Fertilizers (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The utility model discloses a tower-type self-coupling deodorizing high-temperature aerobic fermentation system. A feed port, an exhaust outlet and continuous level sensors are arranged on the top of a fermentation tower body of the tower-type self-coupling deodorizing high-temperature aerobic fermentation system, a bridge discharging device is arranged at the bottom of the fermentation tower body, an upper limit level sensor and a lower limit level sensor are arranged on an upper side wall of the fermentation tower body, and a temperature-oxygen sensor and a sampling port are arranged on a side surface of the fermentation tower body at different heights along the axial direction; a forced ventilation system is formed by connecting a plurality of layers of ventilation pipes and blowers which are distributed and arranged in parallel in the fermentation tower body; a broken bridge discharging device is driven by a broken bridge discharge driving motor to discharge; a PLC (programmable logic controller) control system is connected with all the sensors, the forced ventilation system and the broken bridge discharging device, so that automatic control is achieved. The tower-type self-coupling deodorizing high-temperature aerobic fermentation system disclosed by the utility model is capable of ensuring stable quality of compost products, high degree of automation and low labor intensity, and solving the problem of investment and running costs of a collecting system and deodorizing equipment required by the conventional composting exhaust.
Description
Technical field
The utility model belongs to organic solid castoff and processes disposal technology field, specifically a kind of tower from coupling deodorizing high-temperature aerobic fermentation system.
Background technology
The annual organic solid castoff producing of China reaches tens tons, and the increase year by year of pollution incident and event, was taken seriously organic solid castoff gradually in recent years.Agricultural wastes are in process of production owing to can utilizing quality not high, complicated component, and secondary development cost is high, difficulty is large, lacks the guiding of policy and the input of fund simultaneously, causes agricultural wastes to pollute presenting that quantity is large, poor quality, the many features of harm.Composting technology has ancient history, also the harmless treatment that is widely used in changing food waste, feces of livestock and poultry, agricultural crop straw and excess sludge etc. in modern society and is rich in the organic waste of biodegradable, the product of compost treatment also contains abundant soil ulmin and plant nutrient, be applicable to soil utilization, make composting technology there is resource utilization and be worth.At present this technology has become and has processed agricultural wastes resource utilization, the important means that innoxious and minimizing utilizes.
Aerobic compost processing is one of common method of agricultural wastes resource utilization, innoxious and minimizing processing.Modern aerobic compost is to utilize composting arrangement to make agricultural wastes under aerobic conditions, make good use of oxygen animalcule effect to reach stabilization, innoxious, changes the method that is conducive to soil property improvement useful to crop growth for the high-quality fertilizer that easily absorb into.Current common slot type compost, bar stamps compost or reactor composting technology all needs supporting independent exhaust collection treatment system, causes system Construction investment and running cost to raise, and has limited to a certain extent the popularization of aerobic compost technology.
Utility model content
Technical problem to be solved in the utility model is to provide that a kind of can to eliminate the sealing of tail gas peculiar smell by compost flora tower from coupling deodorizing high-temperature aerobic fermentation system, and it can solve, and traditional open turning fermentation system level of automation such as slot type compost are low, exhaust collection treatment facility complexity, need the problem of special supporting vent gas treatment facility.
The utility model solves the problems of the technologies described above with following technical scheme:
The utility model is a kind of tower from coupling deodorizing high-temperature aerobic fermentation system, and it is mainly made up of fermentation tower body 3, forced ventilation system, PLC Controlling System and broken bridge dumping device 7; The top of fermentation tower body 3 is provided with opening for feed 1, tail gas outlet 2 and continuous material level sensor 10, bridge dumping device 7 is arranged on the bottom of fermentation tower body 3, the upper portion side wall of fermentation tower body 3 is provided with upper limit sensor 11 and lower limit sensor 12, and the side of fermentation tower body 3 is provided with temperature-oxygen sensor 13 and thief hole 6 vertically with different heights; Described forced ventilation system is arranged and is installed on the vent-pipe 4 of fermentation in tower body 3 and is connected and forms with gas blower by multilayer parallel; Described broken bridge dumping device 7 drives discharging by broken bridge discharging drive-motor 5; Described PLC Controlling System is connected to realize automatic control with all the sensors, forced ventilation system and broken bridge dumping device.
Described fermentation tower body aspect ratio is 2.0-4.5.
Described vent-pipe 4 is along fermentation tower axon to being evenly distributed and radially accessing in fermentation tower body, and vent-pipe 4 vertical direction are provided with vacuum breaker.
Described opening for feed 1 is located at fermentation tower body top center place, and tail gas outlet 2 and continuous material level sensor 10 lay respectively at opening for feed 2 both sides.
Described upper limit sensor 11 be positioned at lower limit sensor 12 directly over.
Described broken bridge dumping device is discharge auger device, it comprises that the many groups of worm conveyors 2 33 that are installed on side by side on screw unloading device frame 35 form, screw unloading device frame 35 is connected with fermentation tower body 3 bottom couplings, every group of worm conveyor is provided with discharge auger 32, fermentation tower body is all stretched out at the two ends of every group of worm conveyor, wherein one end is connected and realizes independent drive with group of motors 30 through shaft coupling 31, and the other end is provided with discharge port 2 34.
Described broken bridge dumping device is rotary unloading materials device, it forms by organizing to be installed on side by side on rotary unloading materials device framework 25 and with the rotary unloading material roller 29 of fin more, rotary unloading materials device framework 25 is connected with fermentation tower body 3 bottom couplings, between rotary unloading material roller 29, leave intermittently, not interlock mutually between described fin, every group of rotary unloading material roller 29 is connected with drive-motor 26.
Described broken bridge dumping device is hydraulic pressure balladeur train dumping device, it is made up of with the broken bridge balladeur train 17 of hydraulic pressure being slidably installed on hydraulic pressure balladeur train dumping device framework 21 and the worm conveyor 1 that is positioned at the broken bridge balladeur train of hydraulic pressure 17 belows at least two groups, hydraulic pressure balladeur train dumping device framework 21 is connected with fermentation tower body 3 bottom couplings, the broken bridge balladeur train 17 of hydraulic pressure is driven and can be swung back and forth by hydro-cylinder 20, fermentation tower body is all stretched out at the two ends of worm conveyor 1, wherein one end is connected with worm conveyor motor 22, and the other end is provided with discharge port 1.
The utility model compared with prior art, has the following advantages:
(1) the omnidistance heap temperature-oxygen concn of aerobic fermentation ventilates to realizing automatically by multilayer and controls, and the compost parameter of accuracy controlling different steps, guarantees composting production steady quality;
(2) compositing system feed distribution and compost delivery device, automatization, predigested running operation, reduces productive labor intensity;
(3) the utility model adopts modular design, can or organize fermentation tower more according to the supporting separate unit of compost treatment amount and meet production requirement.
(4) utilize the feature of different compost stage dominant bacterias in fermentation tower, tower compost structure by uniqueness combines During High-Temperature Composting with deodorizing biofilter, form from coupling tail gas deodorization mode, solved the investment working cost problem that conventional composting tail gas needs supporting gathering system and deodorizing device.
Accompanying drawing explanation
Fig. 1 is the tower front view from coupling deodorizing high-temperature aerobic fermentation system of the utility model;
Fig. 2 is the schematic top plan view of Fig. 1;
Fig. 3 is the vertical view of the hydraulic pressure balladeur train dumping device of the utility model employing;
Fig. 4 is the vertical view of the rotary unloading materials device of the utility model employing;
Fig. 5 is the vertical view of the discharge auger device of the utility model employing.
In figure: 1-opening for feed, the outlet of 2--tail gas, the 3--tower body that ferments, 4--vent-pipe, 5--vent-pipe bracing frame, 6--thief hole, 7--breaks bridge dumping device, 8--blanking port, 9--compost tower support, 10--continuous material level sensor, 11--upper limit sensor, 12--lower limit sensor, 13--temperature-oxygen sensor, 14--stiffening web, 15--breaks bridge discharging drive-motor, 16--electric machine support, 17--hydraulic pressure breaks bridge balladeur train, 19--discharge port one, 20--hydro-cylinder, 21--hydraulic pressure balladeur train dumping device framework, 22--worm conveyor motor, 23--worm conveyor one, 24--hydraulic push rod, 25--rotary unloading materials device framework, 26--drive-motor, 27--bearing, 28--motor cabinet, 29-rotary unloading material roller, 30--group of motors, 31--shaft coupling, 32--discharge auger, 33--worm conveyor two, 34--discharge port two, 35--screw unloading device frame.
Embodiment
Below in conjunction with embodiment and accompanying drawing, the utility model is described in further detail, and embodiment of the present utility model is not limited to the following example.
Below in conjunction with accompanying drawing, the utility model is described further, but the utility model is not limited to following examples.
As depicted in figs. 1 and 2, the top of this fermentation tower body 3 is provided with opening for feed 1, tail gas outlet 2 and continuous material level sensor 10, and opening for feed 1 is located at the mid-way at fermentation tower body 3 tops, and tail gas outlet 2 and continuous material level sensor 10 lay respectively at opening for feed 2 both sides; Bridge dumping device 7 is arranged on the bottom of fermentation tower body 3, and drive discharging by broken bridge discharging drive-motor 5, the end of bridge dumping device 7 is provided with blanking port 8, compost tower support 9 feets as whole fermentation tower body are established in broken bridge dumping device 7 bottoms, and compost tower support 9 sides connect the electric machine support 16 for bridge discharging drive-motor 5 is installed brokenly.The upper portion side wall of fermentation tower body 3 is provided with upper limit sensor 11 and the lower limit sensor 12 of vertically arranging vertically, upper limit sensor 11 be positioned at lower limit sensor 12 directly over.The side of fermentation tower body 3 is provided with temperature-oxygen sensor 13 and thief hole 6 vertically with different heights, and temperature-oxygen sensor 13 is for temperature and oxygen data in Real-time Collection heap body, and thief hole 6 is analyzed for the sample that gathers the each fermentation stage of heap body.Fermentation tower body 3 sides are provided with vent-pipe 4 that multilayer parallel arranges and by vent-pipe bracing frame 5 fixed supports, the multilayer vent-pipe 4 composition forced ventilation system that is connected with gas blower; All the sensors, forced ventilation system and the broken bridge dumping device that the utility model adopts all forms and is connected to realize automatic control with PLC Controlling System.
The fermentation tower body aspect ratio that this example adopts is 3.0; Stiffening web 14 is located at fermentation tower body 3 sides and strengthens tower body rigidity.
The vent-pipe 4 of this example is along fermentation tower axon to being evenly distributed and radially accessing in fermentation tower body, and vent-pipe 4 vertical direction are provided with vacuum breaker.
The broken bridge dumping device 7 that the utility model adopts has multiple way of realization, further illustrates below in conjunction with Fig. 3,4,5.
As shown in Figure 3, broken bridge dumping device 7 is hydraulic pressure balladeur train dumping device, it is made up of with the broken bridge balladeur train 17 of hydraulic pressure being slidably installed on hydraulic pressure balladeur train dumping device framework 21 and the worm conveyor 1 that is positioned at the broken bridge balladeur train of hydraulic pressure 17 belows at least two groups, hydraulic pressure balladeur train dumping device framework 21 is connected with fermentation tower body 3 bottom couplings, the broken bridge balladeur train 17 of hydraulic pressure is connected with the hydraulic push rod of hydro-cylinder 20, drive and realize broken bridge balladeur train 17 horizontal reciprocating movements of hydraulic pressure by hydro-cylinder 20, fermentation tower body is all stretched out at the two ends of worm conveyor 1, wherein one end is connected with worm conveyor motor 22, the other end is provided with discharge port 1.
When use, drive hydraulic push rod 24 by hydro-cylinder 20, and break bridge balladeur train 17 by broken the interior compost of fermentation tower body 3 and push to the worm conveyor 1 of fermentation tower body 3 bottoms by hydraulic pressure, finally complete discharge process to the discharge port 1 of worm conveyor one 23 ends.Hydraulic pressure balladeur train dumping device can, uniformly by successively broken collection of compost heap body, ensure that in fermentation tower, material is even axial flow falling state.
As shown in Figure 4: broken bridge dumping device 7 is rotary unloading materials device, it forms by organizing to support to be installed on rotary unloading materials device framework 25 and with the rotary unloading material roller 29 of fin by bearing 27 side by side more, rotary unloading materials device framework 25 is connected with fermentation tower body 3 bottom couplings, between rotary unloading material roller 29, leave intermittently, not interlock mutually between described fin, every group of rotary unloading material roller 29 is connected with drive-motor 26, and drive-motor 26 is arranged on motor cabinet 28.
When use, rotary unloading material roller 29 is driven by the drive-motor 26 being located on motor cabinet 28, between discharge rolls 29, there is gap to build bridge and blockade by compost, discharge rolls 29 rotation vertically can cause its top compost unstability to drop on the conveying belt that is located at the beneath side of tower and transport, thereby completes discharging and realize compost crushing function.
As described in Figure 5: broken bridge dumping device 7 is discharge auger device, it comprises that the many groups of worm conveyors 2 33 that are installed on side by side on screw unloading device frame 35 form, screw unloading device frame 35 is connected with fermentation tower body 3 bottom couplings, every group of worm conveyor is provided with discharge auger 32, fermentation tower body is all stretched out at the two ends of every group of worm conveyor, wherein one end is connected and realizes independent drive with group of motors 30 through shaft coupling 31, and the other end is provided with discharge port 2 34.
When use, drive 2 33 rotations of each worm conveyor by group of motors 30, in tower, compost relies on deadweight press at the bottom of tower discharge auger 32 and discharge compost tower bodies by the discharge port 2 34 of screw discharging machine two, thereby completes discharge process.
Below principle of work of the present utility model is described:
Delivered to fermentation tower top and entered fermentation tower body 3 from opening for feed 1 by material loading distribution conveyor, waste height in level meter monitoring tower stops charging in the time that thing position reaches upper limit sensor 11 in tower.
PLC Controlling System is on the basis of time control, the heap temperature providing according to temperature-oxygen detection system and oxygen concentration are controlling factor, forced ventilation system working order is controlled, principle of work is as follows: PLC Controlling System is take time, heap temperature and oxygen concentration as controlled variable, take blower fan start and stop and rate of venting as operational variable.Under conventional operation state, blower fan is according to the start and stop of PLC Controlling System setting program management blower fan, and when the heap temperature providing when temperature-oxygen detection system and oxygen concentration exceed setting range, program is adjusted blower fan start and stop or rate of venting automatically.For example, when heap temperature is higher than set(ting)value or oxygen concentration during lower than set(ting)value, PLC Controlling System termination time master mode, force start blower fan strengthens rate of venting heap body is carried out to forced cooling and oxygen supply; When heap temperature and oxygen concentration reach after setting range, PLC Controlling System automatically switches to time master mode, adjusts forced ventilation system working order according to setting-up time sequence of control.
Utilize PLC Controlling System control gas blower start and stop or rate of venting; according to the oxygen supply of each layer of material ferment strength; extend heap body in thermophilic fermentation (50 ℃-70 ℃) cycle; under half continuous batch of formula pattern, heap body can form overtemperature deodorizing district (60 ℃-70 ℃), pyrolysis zone (55-50 ℃) from top to bottom, the district (45 ℃ of <) of becoming thoroughly decomposed lowers the temperature.
Under the hot environment of top heap body, in the pore passage structure that compost material self has, can form natural biological filtering layer, under this environment, high temperature microbe formation dominant microflora decomposes rapidly water soluble organic substance.In tower, heap body interlayer is not isolated unit, and volatile molecules can successively spread to tower top with exhaust gas flow in tower, and the conversion between gas-liquid phase-solid phase occurs simultaneously.The peculiar smell molecule of filtering layer absorption tail gas by autotrophy thermophilic be water, carbonic acid gas, elemental sulfur and nitrate without flora oxygenolysis such as gemma, form compost autologous processing from coupled biological deodorizing filter bed, avoid the exhaust collection problem of open type compost, save independent investment of building vent gas treatment facility, solved the problem of composting tail gas processing.
The broken bridge dumping device being positioned at the bottom of tower makes to pile body unstability by level or axial motion, go out fermentation system from side under tower or side feed, complete the thermophilic fermentation that schedules to last 7-10 days, waste height in level meter monitoring tower stops brokenly the work of bridge dumping device in the time that thing position reaches lower limit sensor 12 in tower.
The compost of the one time fermentation Secondary Fermentation groove of still needing carries out compost maturity and finally forms vegetable mould, and the Secondary Fermentation cycle is 10-30 days, and the compost after stable is as soil conditioner or composite fertilizer's base manure recycling.
Claims (8)
1. tower from a coupling deodorizing high-temperature aerobic fermentation system, it is characterized in that: it is mainly made up of fermentation tower body (3), forced ventilation system, PLC Controlling System and broken bridge dumping device (7); The top of fermentation tower body (3) is provided with opening for feed (1), tail gas outlet (2) and continuous material level sensor (10), bridge dumping device (7) is arranged on the bottom of fermentation tower body (3), the upper portion side wall of fermentation tower body (3) is provided with upper limit sensor (11) and lower limit level transducer (12), and the side of fermentation tower body (3) is provided with temperature-oxygen sensor (13) and thief hole (6) vertically with different heights; Described forced ventilation system is connected and forms with gas blower by the multilayer parallel vent-pipe (4) being installed in fermentation tower body (3) of arranging; Described broken bridge dumping device (7) drives discharging by broken bridge discharging drive-motor (5); Described PLC Controlling System is connected to realize automatic control with all the sensors, forced ventilation system and broken bridge dumping device.
2. tower from coupling deodorizing high-temperature aerobic fermentation system according to claim 1, it is characterized in that: described fermentation tower body (3) aspect ratio is 2.0-4.5.
3. tower from coupling deodorizing high-temperature aerobic fermentation system according to claim 1, it is characterized in that: described vent-pipe (4) is along fermentation tower axon to being evenly distributed and radially accessing in fermentation tower body, and vent-pipe (4) vertical direction is provided with vacuum breaker.
4. tower from coupling deodorizing high-temperature aerobic fermentation system according to claim 1, it is characterized in that: described opening for feed (1) is located at fermentation tower body top center place, and tail gas outlet (2) and continuous material level sensor (10) lay respectively at opening for feed (2) both sides.
5. tower from coupling deodorizing high-temperature aerobic fermentation system according to claim 1, it is characterized in that: described upper limit sensor (11) be positioned at lower limit sensor (12) directly over.
6. tower from coupling deodorizing high-temperature aerobic fermentation system according to claim 1, it is characterized in that: described broken bridge dumping device (7) is discharge auger device, it comprises that the many groups of worm conveyors two (33) that are installed on side by side on screw unloading device frame (35) form, screw unloading device frame (35) is connected with fermentation tower body (3) bottom coupling, every group of worm conveyor is provided with discharge auger (32), fermentation tower body is all stretched out at the two ends of every group of worm conveyor, wherein one end is connected and realizes independent drive with group of motors (30) through shaft coupling (31), the other end is provided with discharge port two (34).
7. tower from coupling deodorizing high-temperature aerobic fermentation system according to claim 1, it is characterized in that: described broken bridge dumping device (7) is rotary unloading materials device, it is installed on side by side rotary unloading materials device framework (25) above and forms with the rotary unloading material roller (29) of fin by organize more, rotary unloading materials device framework (25) is connected with fermentation tower body (3) bottom coupling, between rotary unloading material roller (29), leave intermittently, not interlock mutually between described fin, every group of rotary unloading material roller (29) is connected with drive-motor (26).
8. tower from coupling deodorizing high-temperature aerobic fermentation system according to claim 1, it is characterized in that: described broken bridge dumping device (7) is hydraulic pressure balladeur train dumping device, it is made up of with the broken bridge balladeur train (17) of hydraulic pressure being slidably installed on hydraulic pressure balladeur train dumping device framework (21) and the worm conveyor one (23) that is positioned at the broken bridge balladeur train (17) of hydraulic pressure below at least two groups, hydraulic pressure balladeur train dumping device framework (21) is connected with fermentation tower body (3) bottom coupling, the broken bridge balladeur train (17) of hydraulic pressure is driven and can be swung back and forth by hydro-cylinder (20), fermentation tower body is all stretched out at the two ends of worm conveyor one (23), wherein one end is connected with worm conveyor motor (22), the other end is provided with discharge port one (19).
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320850808.XU CN203602514U (en) | 2013-12-19 | 2013-12-19 | Tower-type self-coupling deodorizing high-temperature aerobic fermentation system |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201320850808.XU CN203602514U (en) | 2013-12-19 | 2013-12-19 | Tower-type self-coupling deodorizing high-temperature aerobic fermentation system |
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| CN203602514U true CN203602514U (en) | 2014-05-21 |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106701529A (en) * | 2015-11-16 | 2017-05-24 | 北京恩萨工程技术有限公司 | Efficient and continuousaerobic bioreactor system |
| CN107746294A (en) * | 2017-09-18 | 2018-03-02 | 中国农业科学院农田灌溉研究所 | A kind of organic fertilizer makes reforming unit |
| CN107954752A (en) * | 2017-09-18 | 2018-04-24 | 中国农业科学院农田灌溉研究所 | A kind of organic fertilizer makes method for transformation |
-
2013
- 2013-12-19 CN CN201320850808.XU patent/CN203602514U/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106701529A (en) * | 2015-11-16 | 2017-05-24 | 北京恩萨工程技术有限公司 | Efficient and continuousaerobic bioreactor system |
| CN107746294A (en) * | 2017-09-18 | 2018-03-02 | 中国农业科学院农田灌溉研究所 | A kind of organic fertilizer makes reforming unit |
| CN107954752A (en) * | 2017-09-18 | 2018-04-24 | 中国农业科学院农田灌溉研究所 | A kind of organic fertilizer makes method for transformation |
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