CN206783664U - Aerobic fermentation system - Google Patents
Aerobic fermentation system Download PDFInfo
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- CN206783664U CN206783664U CN201720627342.5U CN201720627342U CN206783664U CN 206783664 U CN206783664 U CN 206783664U CN 201720627342 U CN201720627342 U CN 201720627342U CN 206783664 U CN206783664 U CN 206783664U
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- 238000010564 aerobic fermentation Methods 0.000 title claims abstract description 92
- 230000004151 fermentation Effects 0.000 claims abstract description 49
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 47
- 238000000855 fermentation Methods 0.000 claims abstract description 42
- 239000007789 gas Substances 0.000 claims abstract description 36
- 238000007791 dehumidification Methods 0.000 claims abstract description 8
- 238000005273 aeration Methods 0.000 claims description 100
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 32
- 239000001301 oxygen Substances 0.000 claims description 32
- 229910052760 oxygen Inorganic materials 0.000 claims description 32
- 238000003756 stirring Methods 0.000 claims description 28
- 238000001816 cooling Methods 0.000 claims description 27
- 238000012806 monitoring device Methods 0.000 claims description 22
- 238000010438 heat treatment Methods 0.000 claims description 18
- 238000011144 upstream manufacturing Methods 0.000 claims description 6
- 238000001514 detection method Methods 0.000 claims description 4
- 239000002912 waste gas Substances 0.000 abstract description 18
- 238000005276 aerator Methods 0.000 abstract 3
- 238000009833 condensation Methods 0.000 abstract 3
- 230000005494 condensation Effects 0.000 abstract 3
- 238000010304 firing Methods 0.000 abstract 1
- 238000004064 recycling Methods 0.000 abstract 1
- 239000000463 material Substances 0.000 description 32
- 230000000694 effects Effects 0.000 description 6
- 239000000047 product Substances 0.000 description 5
- 238000000034 method Methods 0.000 description 4
- 239000010802 sludge Substances 0.000 description 4
- 230000009471 action Effects 0.000 description 3
- 238000005265 energy consumption Methods 0.000 description 3
- 238000000605 extraction Methods 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 238000009825 accumulation Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000009264 composting Methods 0.000 description 2
- 239000000498 cooling water Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 229920006395 saturated elastomer Polymers 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 241001052560 Thallis Species 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000010954 inorganic particle Substances 0.000 description 1
- 239000012774 insulation material Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000008092 positive effect Effects 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 230000008054 signal transmission Effects 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 230000001502 supplementing effect Effects 0.000 description 1
- 230000001360 synchronised effect Effects 0.000 description 1
- 230000007306 turnover Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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- Apparatus Associated With Microorganisms And Enzymes (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
Embodiment of the present utility model provides a kind of aerobic fermentation system.Aerobic fermentation device is provided with aerobic fermentation system, gas collecting apparatus and condensation water collection portion are additionally provided with above aerobic fermentation device；Gas collecting apparatus is connected by pipeline with the aerator of aerobic fermentation device；Condensation water collection portion includes collection device and heat sink, is arranged in collection device formed with collecting chamber, heat sink in collecting chamber；Exhaust equipment is additionally provided with pipeline；The air inlet of exhaust equipment is connected with gas collecting apparatus, and the air outlet of exhaust equipment is connected with aerator；Pipeline is provided with least one in dehumidification equipment and firing equipment.The aerobic fermentation system that the utility model embodiment provides waste gas and condensed water caused by collectable fermentate fermentation, makes full use of the heat in system, while realize the recycling of waste gas and condensed water by setting gas collecting apparatus and condensation water collection portion；Gas collecting apparatus and aerator are connected by pipeline, reached the purpose of exhaust gas utilization.
Description
Technical Field
The utility model relates to an aerobic fermentation field especially relates to an aerobic fermentation system.
Background
Along with the development of urbanization in China, the discharge amount of sewage is larger and larger, so that more and more urban sludge is generated, and the sludge is a product after sewage treatment and is an extremely complex heterogeneous body consisting of organic residues, bacteria, thalli, inorganic particles, colloids and the like. The original sludge treatment methods comprise incineration, burying, sea filling and the like, so that the living environment is polluted, and the waste of resources is caused to a certain extent.
One of the processes adopted for sludge treatment is fermentation composting treatment, but during the fermentation process, a lot of waste gas which is far higher than normal temperature gas and contains a large amount of water vapor is generated, and the waste gas treatment in the prior art is usually to be directly discharged into the atmosphere or to be collected and then to be subjected to secondary treatment through a filter tank. Thus, the heat in the waste gas is not fully utilized, the water vapor is not effectively removed and recovered, the fermentation period is possibly prolonged, the fermentation effect is influenced, and the discharged gas can pollute the environment.
Partial fermentation and composting are carried out in open air, which not only affects the surrounding environment, but also causes the temperature change of the fermented materials caused by environment or human factors and the like to be large, and affects the fermentation effect.
SUMMERY OF THE UTILITY MODEL
The utility model provides an aerobic fermentation system to solve among the prior art fermentation process among the fermentation process that the low fermentation efficiency that arouses of oxygen suppliment temperature is low, the waste gas of production, comdenstion water do not have the problem of effective collection processing or utilization.
In order to achieve the above object, an embodiment of the present invention provides an aerobic fermentation system, wherein an aerobic fermentation device is provided, and a gas collecting device and a condensed water collecting portion are further provided above the aerobic fermentation device; the gas collection device is communicated with aeration equipment of the aerobic fermentation device through a pipeline; the condensed water collecting part comprises a collecting device and a cooling device, a collecting cavity is formed in the collecting device, and the cooling device is arranged in the collecting cavity; an air draft device is also arranged in the pipeline; an air inlet of the air draft equipment is communicated with the air collecting device, and an air outlet of the air draft equipment is communicated with the aeration equipment; at least one of a dehumidifying device and a heating device is arranged on the pipeline.
Optionally, the aerobic fermentation system further comprises a temperature sensor and a control device, the temperature sensor is connected with the control device, the temperature sensor is arranged at the downstream of the air draft device, the temperature sensor transmits a detection signal to the control device, and the control device sends an instruction to the heating device.
Optionally, still be equipped with oxygen concentration monitoring devices and air humidity monitoring devices on the pipeline, oxygen concentration monitoring devices with air humidity monitoring devices sets up the low reaches of air extraction equipment, oxygen concentration monitoring devices and air humidity monitoring devices transmits detected signal for controlgear, controlgear send the instruction give for oxygen equipment and dehumidification equipment.
Optionally, the collecting device includes a first side plate and a second side plate, the collecting cavity is located between the first side plate and the second side plate, a collecting portion is disposed on a side wall of one side of the second side plate away from the collecting cavity, a bottom portion close to the collecting portion is disposed on the second side plate, and a through hole communicating the collecting portion with the collecting cavity is disposed on the second side plate.
Optionally, the gas collecting device is communicated with a cooling loop of a cooling device; the cooling loop is arranged on one side, close to the collecting cavity, of the first side plate, or the cooling loop is arranged on one side, close to the collecting cavity, of the second side plate, or the cooling loop is arranged at other positions in the middle of the collecting cavity.
Optionally, the aeration equipment is of a plate-shaped structure with at least two independent aeration cavities inside, the aeration equipment is at least provided with a plurality of first aeration holes along the height direction, and the first aeration holes are formed in the surface of the aeration equipment and communicated with the aeration cavities; or, the aeration equipment is at least one row of aeration pipes, and the first aeration holes are formed in the surfaces of the aeration pipes.
Optionally, the aeration pressure of the first aeration holes located at different heights is different.
Optionally, at least one of the dehumidifying and heating apparatus is arranged upstream or downstream of the air extracting apparatus.
Optionally, an air inlet channel is arranged at the bottom of the aerobic fermentation device, and a plurality of second aeration holes are formed in the air inlet channel.
Optionally, the aerobic fermentation device further comprises a fermentation bin, wherein a stirring device is arranged in the fermentation bin, the stirring device comprises a stirring shaft and stirring blades, and the stirring blades are arranged along the axial direction and/or the circumferential direction of the stirring shaft at intervals.
The utility model has the advantages and positive effects that:
the embodiment of the aerobic fermentation system provided by the embodiment of the utility model has the advantages that the gas collecting device and the condensed water collecting part are arranged in the accommodating structure, so that waste gas and condensed water generated during fermentation of leavening can be collected, and the heat loss is reduced; the gas collecting device and the aeration equipment are connected through the pipeline, so that the waste gas treatment facility is reduced or avoided being newly added, the purpose of waste gas utilization is achieved, the residual heat in the steam is utilized, the fermentation efficiency is improved, and the energy consumption during fermentation is effectively reduced; by collecting the condensed water, the purpose of waste water utilization is achieved, and resources are effectively saved.
Drawings
FIG. 1 is a schematic structural diagram of an aerobic fermentation system provided in an embodiment of the present invention;
fig. 2 is a schematic structural view of a condensed water collecting portion provided in an embodiment of the present invention;
fig. 3 is a schematic structural diagram of an aeration apparatus provided in an embodiment of the present invention.
Description of reference numerals:
1. a gas collection device; 2. a condensed water collecting part; 21. a collection device; 211. a first side plate; 212. a second side plate; 213. a collecting section; 214. a through hole; 22. a cooling device; 23. a collection chamber; 3. a pipeline; 4. an aeration device; 41. an aeration hole; 5. air draft equipment; 6. a dehumidification device; 7. a heating device; 8. a stirring device; 9. a temperature sensor; 10. an oxygen concentration monitoring device; 11. an air humidity monitoring device; 12. an intake passage.
Detailed Description
Exemplary embodiments of the present invention will be described in detail below with reference to the accompanying drawings.
The embodiment of the utility model provides an aerobic fermentation system. An aerobic fermentation device is arranged in the aerobic fermentation system, and a gas collecting device 1 and a condensed water collecting part 2 are also arranged above the aerobic fermentation device; the gas collecting device 1 is communicated with an aeration device 4 of the aerobic fermentation device through a pipeline 3; the condensed water collecting part 2 comprises a collecting device 21 and a cooling device 22, a collecting cavity 23 is formed in the collecting device 21, and the cooling device 22 is arranged in the collecting cavity 23; an air draft device 5 is also arranged in the pipeline 3; an air inlet of the air draft device 5 is communicated with the air collecting device 1, and an air outlet of the air draft device 5 is communicated with the aeration device 4; at least one of a dehumidifying device 6 and a heating device 7 is also provided in the pipeline 3.
The aerobic fermentation system provided by the embodiment of the utility model is provided with the gas collecting device 1 and the condensed water collecting part 2, so that waste gas and condensed water generated during fermentation of fermented materials can be collected, the heat in the system is fully utilized, and the resource utilization of the waste gas and the condensed water is realized; the gas collecting device 1 and the aeration equipment 4 are connected through a pipeline, so that the purpose of waste gas utilization is achieved.
It should be noted that the aerobic fermentation system is not a completely sealed space, but a relatively sealed space, and a relatively negative pressure environment is formed in the aerobic fermentation system through the gas collecting device 1, so that odor is prevented from leaking out during the aerobic fermentation process, and fresh air is timely supplied to the aerobic fermentation system from the outside, thereby ensuring the oxygen content.
Specifically, as shown in fig. 1, the gas collecting device 1 is disposed above the aerobic fermentation device, and this is because the density of the waste gas generated by the fermentation product during the aerobic fermentation process, which is higher than the temperature of the normal temperature gas, tends to be lower than the density of the air, and therefore, the waste gas generated by the fermentation product during the aerobic fermentation process rises to the upper portion of the aerobic fermentation device. The gas collecting device 1 can collect waste gas generated by fermentation in the aerobic fermentation process on one hand, and can collect air in the aerobic fermentation device on the other hand, and the collected gas is introduced into the aeration equipment 4 through the pipeline 3 for aeration, so that the pollution of the waste gas to the environment is effectively reduced, and the energy consumption consumed by aeration is reduced.
An air draft device 5 is arranged at the air outlet end of the air collecting device 1 and/or the air inlet end of the aeration device 4 and/or the middle section of the pipeline 3. The additional air draft device 5 aims to enhance the conversion efficiency of the hot gas collected by the gas collecting device 1 entering the aeration device 4, further improve the aerobic fermentation efficiency of the fermented product and shorten the aerobic fermentation period of the fermented product. Specifically, the air draft device 5 is arranged in a direction along the flow direction of the gas from the air inlet end to the air outlet end of the air draft device 5.
The purpose of arranging the dehumidifying equipment 6 is to remove the moisture in the pipeline 3 and avoid that the moisture removed in the aerobic fermentation process enters the material again to influence the effect of the aerobic fermentation. The heating device 7 is provided to heat the air in the pipeline 3 to ensure the temperature required for aerobic fermentation of the material. Of course, the heating device 7 may not be turned on when the temperature in the aerobic fermentation device is not lower than the temperature required for the aerobic fermentation of the material. Preferably, a dehumidification device 6 and a heating device 7 are arranged in the line 3.
Preferably, at least one of the dehumidifying device 6 and the heating device 7 is arranged upstream or downstream of the air extracting device 5.
The purpose of arranging the dehumidifying device 6 upstream of the air extracting device 5 is to prevent air which is not dehumidified from entering the air extracting device 5, affecting the service life of the air extracting device 5 or causing other problems; the heating device 7 is arranged at the upstream of the air extracting device 5, so that the air outlet end of the air extracting device 5 can blow out gas with a certain temperature, and the temperature required by aerobic fermentation of materials is ensured.
Preferably, in order to ensure that the temperature of the gas in the pipeline 3 does not decrease in the process of flowing through, the outside of the pipeline 3 is further wrapped with a thermal insulation material.
Preferably, the aerobic fermentation system further comprises a temperature sensor 9 and a control device, the temperature sensor 9 is connected with the control device, the temperature sensor is arranged at the downstream of the air draft device 5, the temperature sensor 9 transmits a detection signal to the control device, and the control device sends an instruction to the heating device 7; still be equipped with oxygen concentration monitoring devices 10 and air humidity monitoring devices 11 on the pipeline 3, oxygen concentration monitoring devices 10 with air humidity monitoring devices 11 sets up the low reaches of air drafting equipment 5, oxygen concentration monitoring devices 10 and air humidity monitoring devices 11 give detecting signal transmission for controlgear, controlgear send instruction for oxygen supply equipment and dehumidification equipment 6.
For example, the control device for controlling temperature, humidity and oxygen content may be a PLC control system, and a PLC control unit in the PLC control system is connected with the sensing devices (such as the temperature sensor 9, the oxygen concentration monitoring device 10, the air humidity monitoring device 11, and the like) and the related operation devices (such as the power device for controlling the rotation of the stirring device 8, and the like) in the aerobic fermentation device, so as to automatically control the operating state of the aerobic fermentation system in real time according to the PLC control unit. For example, when the temperature sensor 9 detects that the temperature of the air in the pipeline 3 is too low, the control device controls the heating device 7 to heat the air in the pipeline 3; when the temperature sensor 9 detects that the temperature of the air in the pipeline 3 is too high, the control device controls the heating device 7 to stop heating the air in the pipeline 3, and appropriately adjusts the air draft device 5 to increase the rotating speed so as to increase the flow rate of the air. When the humidity in the aerobic fermentation system is too low or too high, the aim of adjusting the humidity in the aerobic fermentation system can be achieved by controlling the opening or closing of the dehumidifying equipment 5. When the oxygen content in the aerobic fermentation system is not high, the supply amount of oxygen is adjusted by controlling the oxygen supply equipment connected with the aeration equipment 4 to supplement oxygen, and the aeration equipment 4 is used for supplementing oxygen to the materials. Therefore, the automation degree of the aerobic fermentation system provided by the embodiment of the utility model can be greatly improved.
As shown in fig. 2, the condensed water collecting section 2 is also provided above the aerobic fermentation apparatus. The reason for setting up like this lies in through the diversion of induced air system, can make the high temperature saturated vapor water diversion in the fermentation space to the top, and the produced vapor of aerobic fermentation can agglutinate and form the comdenstion water in the top of aerobic fermentation device, increases comdenstion water collecting part 2 and can realize the quick collection of moisture in the saturated vapor water, also can prevent simultaneously that the comdenstion water from dropping to influence fermentation effect in the aerobic fermentation system.
The condensed water collecting part 2 mainly comprises a collecting device 21 and a cooling device 22, a collecting cavity 23 in the collecting device 21 is used for collecting condensed water, the cooling device 22 is used for cooling water vapor, the cooling device 22 is arranged in the collecting cavity 23 so as to convert the water vapor in the collecting cavity 23 into the condensed water, and the cooling device 22 can be any device which can play a role of cooling water vapor at present.
Optionally, the collecting device 21 includes a first side plate 211 and a second side plate 212, the collecting cavity 23 is located between the first side plate 211 and the second side plate 212, a collecting portion 213 is disposed on a side wall of the second side plate 212 on a side far away from the collecting cavity 23, and a through hole 214 communicating the collecting portion 213 and the collecting cavity 23 is disposed on the second side plate 212 at a bottom near the collecting portion 213.
Specifically, the first side plate 211 and the second side plate 212 form the collecting cavity 23, and a diversion part for diversion and/or a drainage part for draining condensed water may be further provided on the first side plate 211 and/or the second side plate 212. The first side plate 211 faces away from the inner space of the aerobic fermentation system, the second side plate 212 faces towards the inner space of the aerobic fermentation system, and a collecting portion 213 for collecting condensed water is further disposed on a side wall of the second side plate 212 facing towards the inner space of the aerobic fermentation system. The collecting part 213 may be a plate-shaped structure or a groove-shaped structure protruding from the surface of the second side plate 212 and inclined upward, and the specific inclination angle may be determined according to actual needs. The collection portion 213 obliquely and upwardly disposed on the second side plate 212 not only can timely block and collect the moisture formed on the second side plate 212, but also can collect the back-dripping water formed on the lower surface of the collection portion 213 through the adjacent collection portion 213, and quickly flow back into the collection chamber 23 through the through hole 214 communicated with the collection chamber 23 through the through hole 214, so that the collection portion 213 can more sufficiently absorb the back-dripping moisture. The second side plate 212 and the collecting portion 213 may be welded or hinged. When the moisture in the collection cavity 23 falls down through the through hole 214, the collection part 213 can receive the moisture again to make the moisture flow back to the collection part 213, and then the moisture flows back to the collection cavity 23 through the through hole 214 at the bottom of the collection tank, so that the moisture is prevented from dripping back to the material to be evaporated. Meanwhile, the water vapor can be condensed on the lower surface of one collecting part 213, the condensed water flows downwards into the collecting part 213 below under the action of gravity, and flows back to the collecting cavity 23 through the through hole 214, so that the water is further prevented from dripping back into the material to be evaporated.
Optionally, the gas collecting device is communicated with a cooling loop of the cooling device 22; wherein, the cooling circuit is disposed on one side of the first side plate 211 close to the collecting cavity 23, or the cooling circuit is disposed on one side of the second side plate close to the collecting cavity 23, or the cooling circuit is disposed at other positions in the middle of the collecting cavity 23.
In particular, the cooling circuit is provided inside the collection chamber 23, in particular on the first lateral plate 211, but also on the second lateral plate 212. The temperature reduction loop reduces the temperature of the water vapor entering the collection cavity 23, the water vapor is reduced in temperature and condensed into water drops which are gathered in the collection cavity 23, and finally the water drops flow into a drainage part outside the collection cavity 23 through a flow guide part at the bottom of the collection cavity 23.
Optionally, the oxygen supply apparatus is provided upstream or downstream of the air extraction apparatus 5.
In this embodiment, the position of the oxygen supply device relative to the air draft device 5 can be flexibly set, but it should be noted that, in the preferred embodiment, the oxygen supply device is arranged at the downstream of the dehumidification device 6, so that the oxygen supplied by the oxygen supply device can not be polluted by air containing moisture, and the purity of the oxygen in the aerobic fermentation process of the material can be ensured.
Optionally, as shown in fig. 3, the aerobic fermentation device further comprises a fermentation chamber, and the aeration device 4 is arranged on the bottom wall of the fermentation chamber and extends upwards; the aeration equipment 4 can be an air outlet arranged at the bottom of the fermentation bin, and the air outlet is communicated with the air extraction equipment 5.
In a preferred embodiment, the aeration device 4 is a plate-shaped structure with at least two independent aeration cavities therein, and the first aeration holes 41 are opened on the surface of the aeration device 4 and communicated with the aeration cavities; alternatively, the aeration device 4 may be at least one row of aeration pipes, and the first aeration holes 41 may be formed on the surfaces of the aeration pipes.
Specifically, in one embodiment, the aeration device 4 is an aeration plate disposed on the bottom wall, and the aeration plate is a plate-shaped structure perpendicular to the bottom wall. The aeration plate is internally provided with a plurality of independent aeration cavities, and each aeration cavity is connected with different air supply devices (such as fans and the like) so as to provide different aeration pressures for the first aeration holes 41 with different heights, fully ensure that the materials with different heights are effectively supplied with oxygen and simultaneously prevent the gas from being discharged from the upper aeration holes with lower pressure in a centralized manner. Preferably, in order to prevent the first aeration holes 41 from being clogged with the material, the first aeration holes 41 may be elongated in a straight shape having good expandability and instantaneous closeness. Of course, the first aeration holes 41 may have other shapes, or an anti-suck back device may be disposed on the first aeration holes 41 to prevent the material from entering the aeration plate. In the practical application process, the aeration plate is not limited to be rectangular, and can also be in the shape of trapezoid and the like. The preferred shape is trapezoidal, i.e. the width of the bottom of the aeration plate is greater than the width of the top of the aeration plate. Thus being more beneficial to the full contact of the gas and the fermentation materials.
In another embodiment, at least one row of aeration pipes can be arranged along the length and/or width direction of the fermentation chamber. Preferably, a plurality of rows of aeration pipes are arranged in the fermentation bin, and the plurality of rows of aeration pipes are uniformly arranged at intervals. Each aeration pipe is provided with a plurality of first aeration holes 41. Correspondingly, the first aeration holes 41 may also be straight-line-shaped long holes or have other shapes, and an anti-suck-back device may also be arranged on each first aeration hole 41.
Preferably, in the above two embodiments, the aeration pressures of the first aeration holes 41 located at different heights are different. For example, the independent aeration chambers in the aeration device 4 can be uniformly arranged along the height direction of the aeration device 4, each independent aeration chamber is respectively communicated with different air supply devices, and the aeration chambers at the same height can be communicated with the same air supply device, so that the cost is saved, and the aeration pressure of the first aeration holes 41 at the same height is ensured to be the same. Preferably, the air supply pressure between different air supply devices is different, so that the aeration pressure of the first aeration holes 41 with different heights is different, the pressure difference of the materials with different heights in the fermentation bin is further met, the materials with different heights can be supplied with oxygen corresponding to the required aerobic fermentation amount, and the efficiency of material fermentation in the fermentation bin is effectively ensured. For example, the aeration pressure of the first aeration holes 41 located at a low position may be set to be greater than the aeration pressure of the first aeration holes 41 located at a high position. Therefore, the materials at the lower part can obtain better aeration effect, the materials at the higher part can realize aerobic fermentation under the combined action of the first aeration holes 41 and the oxygen in the air, and the oxygen supply amount is effectively saved.
Preferably, the bottom of the aerobic fermentation device is provided with an air inlet channel 12, and the air inlet channel 12 is provided with a plurality of second aeration holes. Thus further improving the efficiency of the aerobic fermentation of the materials.
Preferably, the aerobic fermentation device further comprises a stirring device 8 arranged in the fermentation bin.
The stirring device 8 arranged in the fermentation bin can loosen the materials in the fermentation bin on the one hand and can meet the feeding and discharging requirements of the fermentation bin on the other hand. In the preferred embodiment, the stirring device 8 is movable, so that the operator can flexibly move the stirring device 8 to stir, loosen, feed and discharge the materials according to the specific condition of material accumulation in the fermentation bin.
In one embodiment, the stirring device 8 may be provided in the form of a combination of a stirring shaft and stirring paddles, the plurality of stirring paddles being uniformly arranged along the axial and/or radial direction of the stirring shaft. The power of the stirring paddle can be provided by a motor. For example, the paddles may be connected to the motor through a gear set and a speed reducer. In other embodiments, the stirring device 8 can be provided in other forms such as a blade.
Preferably, be provided with multiunit agitating unit 8 in the fermentation storehouse, can carry out effective stirring, loose to the material in the fermentation storehouse like this better.
Preferably, the operator can flexibly select synchronous and/or asynchronous actions of each group of stirring devices 8 according to actual conditions so as to flexibly adapt to materials with different accumulation degrees in the fermentation bin.
Optionally, the aerobic fermentation system further comprises an open and closed door and/or window. Through the arrangement of the openable door and/or window, an operator can conveniently observe the condition of the materials in the aerobic fermentation system, so that the parameters of the feeding and discharging speed of the materials, the temperature in the aerobic fermentation system and the like can be adjusted in time.
The utility model discloses following beneficial effect has:
the embodiment of the aerobic fermentation system provided by the embodiment of the utility model has the advantages that the gas collecting device and the condensed water collecting part are arranged in the aerobic fermentation system, so that waste gas and condensed water generated during aerobic fermentation of leavening can be collected, and the heat loss is reduced; the gas collecting device and the aeration equipment are connected through the pipeline, so that the purpose of waste gas utilization is achieved, and the energy consumption of the material during aerobic fermentation is effectively reduced; the purpose of waste water utilization is achieved by collecting the condensed water, and resources are saved. The dehumidification equipment can remove moisture in the pipeline, so that the situation that the moisture removed in the aerobic fermentation process enters the material again to influence the effect of the aerobic fermentation is avoided. Through setting up heating equipment, can heat the air in the pipeline to required temperature when guaranteeing the material aerobic fermentation. Through setting up agitated vessel, can loosen the material in the fermentation storehouse, on the other hand also can satisfy the business turn over material demand in fermentation storehouse. Through setting up temperature sensor and controlgear, greatly improved the utility model discloses aerobic fermentation system's that the embodiment provided degree of automation.
The above description is only for the specific embodiments of the present invention, but the protection scope of the present invention is not limited thereto, and any person skilled in the art can easily think of the changes or substitutions within the technical scope of the present invention, and all should be covered within the protection scope of the present invention. Therefore, the protection scope of the present invention shall be subject to the protection scope of the claims.
Claims (10)
1. An aerobic fermentation system is provided with an aerobic fermentation device, and is characterized in that a gas collecting device (1) and a condensed water collecting part (2) are also arranged above the aerobic fermentation device;
the gas collection device (1) is communicated with an aeration device (4) of the aerobic fermentation device through a pipeline (3);
the condensed water collecting part (2) comprises a collecting device (21) and a cooling device (22), a collecting cavity (23) is formed in the collecting device (21), and the cooling device (22) is arranged in the collecting cavity (23);
an air draft device (5) is also arranged in the pipeline (3); an air inlet of the air draft equipment (5) is communicated with the air collecting device (1), and an air outlet of the air draft equipment (5) is communicated with the aeration equipment (4);
at least one of a dehumidifying device (6) and a heating device (7) is arranged on the pipeline (3).
2. The aerobic fermentation system according to claim 1, wherein the aerobic fermentation system further comprises a temperature sensor (9) and a control device, wherein the temperature sensor (9) is connected with the control device, the temperature sensor (9) is arranged downstream of the air draft device (5), the temperature sensor (9) transmits a detection signal to the control device, and the control device sends an instruction to the heating device (7).
3. The aerobic fermentation system according to claim 2, wherein an oxygen concentration monitoring device (10) and an air humidity monitoring device (11) are further arranged on the pipeline (3), the oxygen concentration monitoring device (10) and the air humidity monitoring device (11) are arranged at the downstream of the air draft device (5), the oxygen concentration monitoring device (10) and the air humidity monitoring device (11) transmit detection signals to the control device, and the control device sends instructions to the oxygen supply device and the dehumidification device (6).
4. The aerobic fermentation system according to claim 1, wherein the collecting device (21) comprises a first side plate (211) and a second side plate (212), the collecting chamber (23) is located between the first side plate (211) and the second side plate (212), a collecting part (213) is provided on a side wall of the second side plate (212) on a side away from the collecting chamber (23), and a through hole (214) communicating the collecting part (213) and the collecting chamber (23) is provided on the second side plate (212) near a bottom of the collecting part (213).
5. The aerobic fermentation system according to claim 1, wherein the gas collecting device (1) is in communication with a cooling circuit of a cooling device (22); wherein,
the cooling loop is arranged on one side, close to the collecting cavity (23), of the first side plate (211), or the cooling loop is arranged on one side, close to the collecting cavity (23), of the second side plate (212), or the cooling loop is arranged at other positions in the middle of the collecting cavity (23).
6. The aerobic fermentation system according to claim 4, wherein the aeration device (4) is a plate-shaped structure with at least two independent aeration cavities therein, the aeration device (4) is provided with a plurality of first aeration holes (41) at least along the height direction, and the first aeration holes (41) are arranged on the surface of the aeration device (4) and communicated with the aeration cavities; or,
the aeration equipment (4) is at least one row of aeration pipes, and the first aeration holes (41) are formed in the surfaces of the aeration pipes.
7. The aerobic fermentation system according to claim 6, wherein the aeration pressure of the first aeration holes (41) at different heights is different.
8. The aerobic fermentation system according to claim 1, whereby at least one of the dehumidifying device (6) and the heating device (7) is arranged upstream or downstream of the air draft device (5).
9. The aerobic fermentation system of claim 1, wherein an air inlet channel (12) is disposed at the bottom of the aerobic fermentation device, and a plurality of second aeration holes are disposed on the air inlet channel (12).
10. The aerobic fermentation system according to claim 1, wherein the aerobic fermentation device further comprises a fermentation chamber, a stirring device (8) is arranged in the fermentation chamber, the stirring device (8) comprises a stirring shaft and stirring blades, and the stirring blades are arranged at intervals along the axial direction and/or the circumferential direction of the stirring shaft.
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107012073A (en) * | 2017-06-01 | 2017-08-04 | 北京首创污泥处置技术股份有限公司 | Aerobic fermentation system |
| CN109078968A (en) * | 2018-09-17 | 2018-12-25 | 绿水青山环保科技（大连）有限公司 | Low temperature infrared radiation coupled biological reaction method and its device |
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2017
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107012073A (en) * | 2017-06-01 | 2017-08-04 | 北京首创污泥处置技术股份有限公司 | Aerobic fermentation system |
| CN107012073B (en) * | 2017-06-01 | 2023-11-14 | 北京首创污泥处置技术有限公司 | Aerobic fermentation system |
| CN109078968A (en) * | 2018-09-17 | 2018-12-25 | 绿水青山环保科技（大连）有限公司 | Low temperature infrared radiation coupled biological reaction method and its device |
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