CN203007164U - Dynamic high-temperature-composting fermentation system - Google Patents
Dynamic high-temperature-composting fermentation system Download PDFInfo
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- CN203007164U CN203007164U CN2012207403279U CN201220740327U CN203007164U CN 203007164 U CN203007164 U CN 203007164U CN 2012207403279 U CN2012207403279 U CN 2012207403279U CN 201220740327 U CN201220740327 U CN 201220740327U CN 203007164 U CN203007164 U CN 203007164U
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- fermentation
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- high temperature
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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 relates to fermentation systems and discloses a dynamic high-temperature-composting fermentation system. The fermentation system comprises a material charging subsystem, a material mixing and distributing machine, a fermentation tower and material discharging subsystems, wherein the material charging subsystem, the material mixing and distributing machine, the fermentation tower and the material discharging subsystems are sequentially arranged; the material charging subsystem is connected with the material mixing and distributing machine through a material pipe and is used for supplying materials to the material mixing and distributing machine; and fermentation chambers are arranged in the fermentation tower, traveling rails are arranged above the fermentation chambers, the material mixing and distributing machine is arranged on the traveling rails and can move along the traveling rails, aeration devices are arranged in the fermentation chambers, and the material discharging subsystems are arranged below the fermentation chambers. According to the dynamic high-temperature-composting fermentation system, the material mixing and distributing machine is adopted to carry out thorough material mixing before fermentation, and the traveling rails are arranged in the fermentation tower, so that the preliminary fermentation can be achieved during material mixing; and the system is compact in structure, small in floor area, low in energy consumption and high in automation degree, so that the high efficiency and energy saving for organic fertilizer production can be realized.
Description
Technical field
The utility model relates to a kind of fermentation system, particularly relates to a kind of dynamic high temperature heap fermentation system.
Background technology
Organic exhaust gas price value in plant residue, aquaculture feces of livestock and poultry, agricultural or grocery trade rubbish is cheap, volume is large, be not easy to carrying, and easily produce and pollute, but can under certain moisture, C/N ratio and ventilation condition, be converted into the bio-organic fertilizer of high-quality by the fermentative action of microorganism.How to improve the fermented quality of organic fertilizer product, reduce the production run cost, and do not produce the key that secondary pollution is all kinds of Technologies.
Processing method and the facility of fermentation are of a great variety, and for the production of fertilizer, at present most popular is exactly composting fermentation technology.In the compost fermentation technology, can realize three classes that mainly contain of mechanization production, be respectively that static aerobic fermentation, slot type or bar buttress formula plane is turned over and thrown fermentation and multilayer-tower fermentation.Static aerobic fermentation is that the organic exhaust gas raw material is deposited in together, obtains fertilizer at the condition bottom fermentation of ventilating, and treatment capacity is large, but the treatment time is longer, and running cost is high.Slot type or bar buttress formula plane is turned over and is thrown fermentation, piles generally that high more than 1 meter, floor space is large, opens wide fermentation, has secondary pollution, easily causes the propagation of pathogenic bacteria.Tower fermentation is to adopt the seal tower of layering vertical structure that material is fermented, and floor space is little, and the bed of material is thin, and dehydration is rapid, and fermentation period is short, but the multitower combination, production efficiency and level of automation are high, but yield poorly, and facility investment is large.
The utility model content
The technical problem that (one) will solve
The technical problems to be solved in the utility model is how to realize organic fertilizer production efficient and energy-conservation.
(2) technical scheme
In order to solve the problems of the technologies described above, the utility model provides a kind of dynamic high temperature heap fermentation system, comprises the material loading subsystem, mixing material distributing machine, fermentation tower and the discharging subsystem that set gradually; The logical charge tube of described material loading subsystem is connected with the mixing material distributing machine, is used for to mixing the material distributing machine feed; Be provided with fermentation cabin in described fermentation tower, the top of described fermentation cabin is provided with the walking track, described mixing material distributing machine is located on described walking track and can be provided with aerating apparatus in described fermentation cabin along described walking rail moving, and described discharging subsystem is located at the below of fermentation cabin.
Further, described material loading subsystem comprises collecting tank, storage tank, sludge pump and solid-liquid separating machine, the logical charge tube of the opening for feed of described storage tank is connected with the discharge port of collecting tank, the discharge port of described storage tank is connected with the opening for feed of solid-liquid separating machine by penstock, and described sludge pump is connected with penstock; Described solid-liquid separating machine is located at the top of mixing material distributing machine, and its bottom is provided with liquid return hole, and described liquid return hole is connected with collecting tank by liquid returning tube.
Further, described material loading subsystem comprises feeding web, weighing belt and lift, after by feeding web, material being delivered to weighing belt and carried out weighing, is transported to the mixing material distributing machine by lift.
Further, described mixing material distributing machine comprises blending bunker and material distributing machine, and described mixing material distributing machine connects and can move with the chassis that switches tracks with the chassis that switches tracks, and the two ends of the described chassis that switches tracks are located on described walking track.
Further, described fermentation cabin is a plurality of of arranged transversely, and the top of each fermentation cabin is respectively equipped with two orthogonal walking tracks.
Further, described fermentation cabin is vertically arrange a plurality of, is provided with pluggable dividing plate between adjacent fermentation cabin.
Further, described aerating apparatus is the oscillatory type aerating apparatus.
Further, described fermentation tower is provided with Waste gas outlet, and described Waste gas outlet is connected with the waste gas collection device of being located at the fermentation tower outside.
Further, be provided with the biological deodorizing filter tank between described Waste gas outlet and waste gas collection device.
(3) beneficial effect
A kind of dynamic high temperature heap fermentation system that technique scheme provides, adopted the mixing material distributing machine to carry out abundant batch mixing before fermentation, the walking track is set in fermentation tower, making in the process of batch mixing can initial fermentation, makes fermentation fully, can realize the efficient and energy-conservation of organic fertilizer production, its compact construction, account at area littlely, energy consumption is little, and level of automation is high.
Description of drawings
Fig. 1 is the front view of the utility model dynamic high temperature heap fermentation system;
Fig. 2 is the vertical view of the utility model dynamic high temperature heap fermentation system.
Wherein, 11, collecting tank; 111, spillway; 12, storage tank; 13, solid-liquid separating machine; 131, intercepting basin; 132, solid-liquid separation screen cloth; 14, material pipe; 15, penstock; 16, liquid returning tube; 17, lift; 2, mix material distributing machine; 21, the chassis that switches tracks; 22, blending bunker; 3, fermentation tower; 31, fermentation cabin; 32, walking track; 33, dividing plate; 4, discharging subsystem; 5, air dehumidifier; 6, biological deodorizing filter tank.
Embodiment
Below in conjunction with drawings and Examples, embodiment of the present utility model is described in further detail.Following examples are used for explanation the utility model, but are not used for limiting scope of the present utility model.
As depicted in figs. 1 and 2, a kind of dynamic high temperature heap of the utility model fermentation system comprises the material loading subsystem, mixing material distributing machine 2, fermentation tower 3 and the discharging subsystem 4 that set gradually; The material loading subsystem is connected with mixing material distributing machine 2, is used for to mixing material distributing machine 2 feed; The interior look of fermentation tower 3 also has fermentation cabin 31, and the top in this ferment storehouse is provided with walking track 32, mixes material distributing machine 2 and is located on walking track 32 and can moves along this track 32 of walking; Be provided with aerating apparatus in fermentation cabin 31, discharging subsystem 4 is located at the below of fermentation cabin 31.
Wherein, aerating apparatus is the oscillatory type aerating apparatus.This vibration aerating system is by the integrated fast dewatering process that realizes material of several parts such as heat pump, blower fan, aerating pipelines and vibrating motor.Heat pump extracts heat energy and comes the heat drying air from air, can reduce greatly energy consumption and running cost, and by blower fan, the warm air of drying is sent in aerating pipelines material is carried out drying, adopt vibrating motor can effectively must prevent the generation of discharge port arch material phenomenon.
When material was wet feed, the material loading subsystem of the present embodiment comprised collecting tank 11, storage tank 12, sludge pump and solid-liquid separating machine 13, and the logical charge tube 14 of the opening for feed of storage tank 12 is connected with the discharge port of collecting tank 11, and the bottom of collecting tank 11 is provided with spillway 111; The discharge port of storage tank 12 is connected with the opening for feed of solid-liquid separating machine 13 by penstock 15, and sludge pump is connected with penstock 15; Solid-liquid separating machine 13 is located at the top of mixing material distributing machine 2, this solid-liquid separating machine 13 comprises intercepting basin 131 and solid-liquid separation screen cloth 132, solid-liquid separation screen cloth 132 is located at the top of intercepting basin 131, be tilted to down, its opening is positioned at the top of mixing material distributing machine 2, and wet feed drops on solid-liquid separation screen cloth 132, and the moisture that contains in material flows in intercepting basin 131 through the mesh of solid-liquid separation screen cloth 132, dry material after dehydration is stayed on solid-liquid separation screen cloth 132, and falls into and mix material distributing machine 2 and carry out batch mixing; And be provided with liquid return hole in the bottom of intercepting basin 131, and liquid return hole is connected with collecting tank 11 by liquid returning tube 16, and waste water is back to by pipeline and carries out recycle in collecting tank 16, thereby has saved water consumption.
When material was siccative, the material loading subsystem of the present embodiment comprised feeding web, weighing belt and lift 17, after by feeding web, material being delivered to weighing belt and carried out weighing, was transported to by lift 17 and mixed material distributing machine 2.Wherein, lift 17 can be chapelet but is not limited to chapelet.
Have again when existing wet feed in the situation of siccative, above-mentioned two put the material for making clothes system can exist simultaneously.
The mixing material distributing machine 2 of the present embodiment comprises switch tracks chassis 21 and blending bunker 22, blending bunker 22 connects and can move with this chassis 21 that switches tracks with the chassis 21 that switches tracks, the switch tracks two ends of chassis 21 are located on walking track 32, this chassis 21 that switches tracks is driven on walking track 32 by hydraulic efficiency system and moves, and drive blending bunker 22 and mix, stir, thereby realize the mix and blend of material and the process of initial fermentation.
The fermentation cabin 31 of the present embodiment can be a plurality of of arranged transversely, and the top of each fermentation cabin 31 is respectively equipped with two orthogonal walking tracks 32, and these two orthogonal walking tracks 32 are positioned on same level, mixes the chassis 21 that switches tracks of material distributing machine 2.
Particularly, the fermentation cabin 31 of the present embodiment can be a plurality of of vertical setting, is provided with pluggable dividing plate 33 between adjacent fermentation cabin 31.
The fermentation tower 3 of the present embodiment is provided with Waste gas outlet, and this Waste gas outlet is connected with the waste gas collection device of being located at fermentation tower 3 outsides.Be provided with biological deodorizing filter tank 6 between Waste gas outlet and waste gas collection device, waste gas is carried out biological deodorizing, energy-conserving and environment-protective do not produce secondary pollution, and later maintenance is simple.Also be provided with air dehumidifier 5 in fermentation tower 3, be used for the air dewetting of fermentation tower 3, to keep a yeasting preferably.
The discharging subsystem 4 of the present embodiment comprises many parallel traveling beds and transverse onveyer, and drive mass transport after jointly realizing fermentation is completed by drive unit and go out and pack, wherein, conveying belt adopts receives limit formula conveying belt, to reduce to greatest extent overflowing of material.
In sum, a kind of dynamic high temperature heap fermentation system that technique scheme provides has the following advantages:
1, compact construction accounts at area littlely, and energy consumption is little, pollutes less, and level of automation is high, and material dewatering is rapid, and fermentation fully can realize efficient, the energy-conservation and environmental protection of organic fertilizer production.
2, wet feed adopts solid-liquid separating machine, and the dry material of separating enters the mixing material distributing machine, and waste water flows back in the pond that gathers materials by pipeline again and circulates, thereby has saved water consumption;
3, this fermentation system horizontal and vertical arranges respectively a plurality of fermentation cabin, and integrated slot type turns over the Core Superiority of throwing fermentation, multilayer-tower fermentation and three kinds of fermentation modes of static aerobic fermentation, and technique is advanced, and processing efficiency is high.
4, turn over the characteristics of throwing the trough type fermentation that chassis fully absorbs, driven by hydraulic efficiency system and turn over the throwing chassis, to-and-fro movement on the track of can walking, thus and drive the process with initial fermentation of mixing that the blending bunker rotation realizes material.On the other hand, whole feeding bin is realized again the function to different fermentations body feeding by the motion on fermentation cabin group track.
5, the fermentation subsystem is realized the tower fermentation of layering of material by multilayer warehouse structure and automatic discharger, has increased the contact area of material and air, has accelerated the dehydration of material, thereby has realized the abundant fermentation of material.
6, adopt the vibration aerating apparatus can realize the fast dewatering process of material and prevent that effectively discharge port from encircleing the generation of material phenomenon.
7, the discharging subsystem brings mass transport after realizing fermentation is completed to go out by many parallel traveling beds and lateral transfer to pack, and conveying belt adopts to be received limit formula discharging conveying belt and can reduce to greatest extent overflowing of material.
8, adopt biological deodorizing filter tank processing waste gas, energy-conserving and environment-protective do not produce secondary pollution, and later maintenance is simple.
The above is only preferred implementation of the present utility model; should be understood that; for those skilled in the art; under the prerequisite that does not break away from the utility model know-why; can also make some improvement and replacement, these improvement and replacement also should be considered as protection domain of the present utility model.
Claims (9)
1. a dynamic high temperature heap fermentation system, is characterized in that, comprises the material loading subsystem, mixing material distributing machine, fermentation tower and the discharging subsystem that set gradually; The logical charge tube of described material loading subsystem is connected with the mixing material distributing machine, is used for to mixing the material distributing machine feed; Be provided with fermentation cabin in described fermentation tower, the top of described fermentation cabin is provided with the walking track, described mixing material distributing machine is located on described walking track and can be provided with aerating apparatus in described fermentation cabin along described walking rail moving, and described discharging subsystem is located at the below of fermentation cabin.
2. dynamic high temperature as claimed in claim 1 is piled fermentation system, it is characterized in that, described material loading subsystem comprises collecting tank, storage tank, sludge pump and solid-liquid separating machine, the logical charge tube of the opening for feed of described storage tank is connected with the discharge port of collecting tank, the discharge port of described storage tank is connected with the opening for feed of solid-liquid separating machine by penstock, and described sludge pump is connected with penstock; Described solid-liquid separating machine is located at the below of mixing material distributing machine, and its bottom is provided with liquid return hole, and described liquid return hole is connected with collecting tank by liquid returning tube.
3. dynamic high temperature as claimed in claim 1 is piled fermentation system, it is characterized in that, described material loading subsystem comprises feeding web, weighing belt and lift, after by feeding web, material being delivered to weighing belt and carried out weighing, is transported to the mixing material distributing machine by lift.
4. dynamic high temperature as claimed in claim 1 is piled fermentation system, it is characterized in that, described mixing material distributing machine comprises switch tracks chassis and blending bunker, and described blending bunker connects and moves with the chassis that switches tracks with the chassis that switches tracks, and the two ends of the described chassis that switches tracks are located on described walking track.
5. dynamic high temperature compost fermentation as claimed in claim 1 system, is characterized in that, described fermentation cabin is a plurality of of arranged transversely, and the top of each fermentation cabin is respectively equipped with two orthogonal walking tracks.
6. dynamic high temperature heap fermentation system as claimed in claim 1, is characterized in that, described fermentation cabin is vertically arrange a plurality of, is provided with pluggable dividing plate between adjacent fermentation cabin.
7. dynamic high temperature fermentation system as claimed in claim 1, is characterized in that, described aerating apparatus is the oscillatory type aerating apparatus.
8. dynamic high temperature fermentation system as claimed in claim 1, is characterized in that, described fermentation tower is provided with Waste gas outlet, and described Waste gas outlet is connected with the waste gas collection device of being located at the fermentation tower outside.
9. dynamic high temperature fermentation system as claimed in claim 8, is characterized in that, is provided with the biological deodorizing filter tank between described Waste gas outlet and waste gas collection device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012207403279U CN203007164U (en) | 2012-12-28 | 2012-12-28 | Dynamic high-temperature-composting fermentation system |
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| CN2012207403279U CN203007164U (en) | 2012-12-28 | 2012-12-28 | Dynamic high-temperature-composting fermentation system |
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| CN203007164U true CN203007164U (en) | 2013-06-19 |
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| CN2012207403279U Expired - Lifetime CN203007164U (en) | 2012-12-28 | 2012-12-28 | Dynamic high-temperature-composting fermentation system |
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Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105859083A (en) * | 2016-03-29 | 2016-08-17 | 浙江海洋学院 | Novel anaerobic fermentation equipment and method for sludge |
| CN106316489A (en) * | 2016-10-27 | 2017-01-11 | 威德环境科技股份有限公司 | Composting treatment system for kitchen waste biogas residues |
| 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 |
| CN106747747A (en) * | 2016-12-26 | 2017-05-31 | 天津海泰市政绿化有限公司 | A kind of garden waste manufactures the production line of ecological organic fertilizer |
| CN107365032A (en) * | 2017-09-04 | 2017-11-21 | 东莞市红树林环保科技有限公司 | A kind of device for livestock and poultry feces recycling |
| CN107673781A (en) * | 2017-08-24 | 2018-02-09 | 广西力源宝科技有限公司 | The tower fermentation system of automatic feed and feed process |
| CN109956637A (en) * | 2017-12-21 | 2019-07-02 | 蔡永辉 | Global function mud decrement harmless resource utilization treatment process system |
| CN113480339A (en) * | 2021-08-06 | 2021-10-08 | 广西壮族自治区畜牧研究所 | Fermentation device, and multi-stage mixed organic fertilizer fermentation system and method with same |
-
2012
- 2012-12-28 CN CN2012207403279U patent/CN203007164U/en not_active Expired - Lifetime
Cited By (10)
| 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 |
| CN105859083A (en) * | 2016-03-29 | 2016-08-17 | 浙江海洋学院 | Novel anaerobic fermentation equipment and method for sludge |
| CN106316489A (en) * | 2016-10-27 | 2017-01-11 | 威德环境科技股份有限公司 | Composting treatment system for kitchen waste biogas residues |
| CN106316489B (en) * | 2016-10-27 | 2022-11-18 | 威德环境科技股份有限公司 | Kitchen waste biogas residue composting treatment system |
| CN106747747A (en) * | 2016-12-26 | 2017-05-31 | 天津海泰市政绿化有限公司 | A kind of garden waste manufactures the production line of ecological organic fertilizer |
| CN107673781A (en) * | 2017-08-24 | 2018-02-09 | 广西力源宝科技有限公司 | The tower fermentation system of automatic feed and feed process |
| CN107365032A (en) * | 2017-09-04 | 2017-11-21 | 东莞市红树林环保科技有限公司 | A kind of device for livestock and poultry feces recycling |
| CN109956637A (en) * | 2017-12-21 | 2019-07-02 | 蔡永辉 | Global function mud decrement harmless resource utilization treatment process system |
| CN113480339A (en) * | 2021-08-06 | 2021-10-08 | 广西壮族自治区畜牧研究所 | Fermentation device, and multi-stage mixed organic fertilizer fermentation system and method with same |
| CN113480339B (en) * | 2021-08-06 | 2023-02-24 | 广西壮族自治区畜牧研究所 | Fermentation device, and multi-stage mixed organic fertilizer fermentation system and method with same |
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Effective date of registration: 20160523 Address after: 065000 Langfang province Hebei city Anci district emerging industries demonstration zone in Nantong Longxian Road West Renlu Patentee after: Langfang city farming world agricultural science and Technology Co.,Ltd. Address before: 102200 No. 11 Huatong Road, Changping District science and Technology Park, Beijing Patentee before: BEIJING SAIMENTE MACHINERY Co.,Ltd. |
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| CX01 | Expiry of patent term |
Granted publication date: 20130619 |
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| CX01 | Expiry of patent term |