CN2600443Y - Anaerobic oxygen integral compost reaction device - Google Patents
Anaerobic oxygen integral compost reaction device Download PDFInfo
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- CN2600443Y CN2600443Y CNU032268343U CN03226834U CN2600443Y CN 2600443 Y CN2600443 Y CN 2600443Y CN U032268343 U CNU032268343 U CN U032268343U CN 03226834 U CN03226834 U CN 03226834U CN 2600443 Y CN2600443 Y CN 2600443Y
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- 238000006243 chemical reaction Methods 0.000 title claims abstract description 10
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 title description 4
- 239000001301 oxygen Substances 0.000 title description 4
- 229910052760 oxygen Inorganic materials 0.000 title description 4
- 239000002361 compost Substances 0.000 title description 3
- 238000000855 fermentation Methods 0.000 claims abstract description 42
- 230000004151 fermentation Effects 0.000 claims abstract description 41
- 239000007788 liquid Substances 0.000 claims abstract description 34
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 33
- 238000010438 heat treatment Methods 0.000 claims abstract description 27
- 238000009264 composting Methods 0.000 claims abstract description 25
- 230000029087 digestion Effects 0.000 claims abstract description 24
- 238000003756 stirring Methods 0.000 claims abstract description 22
- 238000009423 ventilation Methods 0.000 claims abstract description 14
- 239000000463 material Substances 0.000 claims abstract 2
- 238000000034 method Methods 0.000 claims description 9
- 238000001802 infusion Methods 0.000 claims description 3
- 229910001220 stainless steel Inorganic materials 0.000 claims description 2
- 239000010935 stainless steel Substances 0.000 claims description 2
- 239000010815 organic waste Substances 0.000 abstract 1
- 239000007787 solid Substances 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 10
- 238000010586 diagram Methods 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 238000010564 aerobic fermentation Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000003895 organic fertilizer Substances 0.000 description 1
- 230000020477 pH reduction Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000010992 reflux Methods 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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- 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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- Processing Of Solid Wastes (AREA)
- Fertilizers (AREA)
Abstract
本实用新型涉及将固体有机废物堆肥的厌氧好氧一体式反应装置,它包括发酵罐、通风系统、搅拌系统、加热系统;发酵罐内设有筛板,筛板上设有筛孔,筛板将发酵罐隔成两部分,搅拌轴设在发酵罐的中间且装在轴座中,由电动机驱动;搅拌叶片与搅拌轴连接在一起,其上设有中空气道和通气孔;发酵罐的顶端设有进出料口、出气口、进液口、进气口;发酵仓四周和底部设有循环水浴加热套,其上有进出水口,发酵仓的底部设有伸出加热套底部的出液管,出液管与进液口相连。本实用新型的发酵仓是密闭的,自由选择通风或关闭通风,即可实现在同一个设备内进行厌氧消化和好氧堆肥反应;采用循环水浴加热套加热,发酵仓内温度均匀;发酵罐可以串联使用。
The utility model relates to an anaerobic and aerobic integrated reaction device for composting solid organic waste, which comprises a fermentation tank, a ventilation system, a stirring system and a heating system; The plate divides the fermentation tank into two parts, the stirring shaft is set in the middle of the fermentation tank and installed in the shaft seat, driven by the motor; the stirring blade is connected with the stirring shaft, and there are hollow air passages and ventilation holes on it; the fermentation tank The top of the tank is provided with material inlet and outlet, air outlet, liquid inlet, and air inlet; the surrounding and bottom of the fermentation chamber are equipped with a circulating water bath heating jacket, with water inlet and outlet on it, and the bottom of the fermentation chamber is provided with an outlet extending from the bottom of the heating jacket. Liquid pipe, the liquid outlet pipe is connected with the liquid inlet. The fermentation chamber of the utility model is airtight, and the ventilation can be freely selected or closed to realize anaerobic digestion and aerobic composting reaction in the same equipment; the temperature in the fermentation chamber is uniform by adopting a circulating water bath heating jacket; Can be used in series.
Description
一、技术领域1. Technical field
本实用新型涉及一种垃圾堆肥反应装置,特别涉及一种有机物厌氧好氧一体式堆肥反应装置。The utility model relates to a garbage composting reaction device, in particular to an organic matter anaerobic and aerobic integrated composting reaction device.
二、背景技术2. Background technology
城市垃圾在进行厌氧消化处理后进行好氧堆肥可以制成优质的有机堆肥。目前,由于受发酵设备的限制,在垃圾处理中,或只进行厌氧消化制沼气,或只进行好氧堆肥。在农村,采用厌氧消化制沼气,但沼渣不进行好氧堆肥就直接将沼渣作为肥料,这种肥料的肥效差;在城市垃圾堆肥厂,将垃圾为原料直接进行好氧堆肥而不进行厌氧消化,堆肥质量也差。进行厌氧消化制沼气的装置有气袋式、水压式、浮罩式和蛋型发酵仓等;进行好氧堆肥的装置有塔式和滚筒式发酵仓。这些装置都不能同时完成厌氧消化和好氧堆肥,垃圾处理的效果不佳。Aerobic composting of municipal waste after anaerobic digestion can make high-quality organic compost. At present, due to the limitation of fermentation equipment, in waste treatment, only anaerobic digestion is used to produce biogas, or only aerobic composting is performed. In rural areas, anaerobic digestion is used to produce biogas, but biogas residues are directly used as fertilizer without aerobic composting. Anaerobic digestion, compost quality is also poor. The devices for anaerobic digestion to produce biogas include air bag type, hydraulic type, floating cover type and egg-shaped fermentation bins, etc.; the devices for aerobic composting include tower type and drum type fermentation bins. None of these devices can complete anaerobic digestion and aerobic composting at the same time, and the effect of garbage treatment is not good.
三、发明内容3. Contents of the invention
本实用新型的目的是:为了解决厌氧消化和好氧堆肥不能在同一反应器内连续进行的问题,本实用新型特提供一种可以先进行厌氧消化,再进行有机物的好氧发酵而将垃圾制成优质有机肥的厌氧好氧一体式堆肥反应装置The purpose of this utility model is: in order to solve the problem that anaerobic digestion and aerobic composting cannot be continuously carried out in the same reactor, this utility model provides a method that can perform anaerobic digestion first, and then carry out aerobic fermentation of organic matter. Anaerobic and aerobic integrated composting reaction device for making high-quality organic fertilizer from garbage
本实用新型采用的技术方案是:它主要包括发酵罐、搅拌系统、通风系统、加热系统;其中发酵罐内设有筛板,筛板上设有筛孔,筛板将发酵罐隔成两部分,上部为可将垃圾在厌氧消化过程中产生的酸化液滤去的过滤床式发酵仓,下部为液体收集区;搅拌系统包括设在发酵仓中间且安装在轴座中的搅拌轴,搅拌轴为中空的金属管,搅拌轴上安装带有通气孔的叶片,搅拌轴由电动机驱动;通风系统包括鼓风机、输气管、叶片上的通风孔、搅拌轴的顶端的进气口,输气管与鼓风机相连;加热系统包括发酵罐四周和底部的循环水浴加热套及其内的恒温热水,加热套设有进水口和出水口,通过输液管与水泵和恒温热水源连接,使热水循环使用。发酵罐的顶部设有进出料口、出气口、进液口,出气口通过输气管与储气罐相连;发酵罐的底部设有出液管,出液管伸出加热层的底部,出液管通过水泵与进液口相连,可将液体收集区内的酸化液泵入发酵仓内用以调节好氧堆肥阶段发酵仓内所需的水分。The technical solution adopted by the utility model is: it mainly includes a fermentation tank, a stirring system, a ventilation system, and a heating system; wherein a sieve plate is arranged in the fermentation tank, and a sieve hole is arranged on the sieve plate, and the sieve plate divides the fermentation tank into two parts , the upper part is a filter bed type fermentation bin that can filter out the acidified liquid produced during the anaerobic digestion process of garbage, and the lower part is a liquid collection area; the stirring system includes a stirring shaft installed in the middle of the fermentation bin and installed in the shaft seat, stirring The shaft is a hollow metal tube, and blades with air holes are installed on the stirring shaft, and the stirring shaft is driven by a motor; the ventilation system includes a blower, an air pipe, air holes on the blades, an air inlet at the top of the stirring shaft, air pipes and The blower is connected; the heating system includes the circulating water bath heating jacket around and at the bottom of the fermentation tank and the constant temperature hot water inside. The heating jacket is provided with a water inlet and a water outlet, and is connected to the water pump and the constant temperature hot water source through the infusion pipe to make the hot water circulate. . The top of the fermentation tank is provided with inlet and outlet, gas outlet and liquid inlet, and the gas outlet is connected with the gas storage tank through the gas pipe; The pipe is connected to the liquid inlet through a water pump, and the acidified liquid in the liquid collection area can be pumped into the fermentation chamber to adjust the water required in the fermentation chamber during the aerobic composting stage.
本实用新型具有显著的有益效果:The utility model has remarkable beneficial effects:
1、本实用新型设有循环水浴加热套,温度控制在100℃以下,可以满足垃圾厌氧消化和好氧堆肥的温度需要,而且水浴加热较其它加热方法温和,不会因为温度的骤然升高或降低杀死微生物破坏降解过程,并保证加热的均匀。1. The utility model is equipped with a circulating water bath heating jacket, and the temperature is controlled below 100°C, which can meet the temperature requirements of anaerobic digestion and aerobic composting of garbage, and the water bath heating is milder than other heating methods, and will not be caused by a sudden increase in temperature. Or reduce to kill microorganisms to destroy the degradation process, and ensure uniform heating.
2、本实用新型在发酵罐内设有筛板,将发酵罐分为两部分,在厌氧消化阶段作为过滤床式厌氧发酵仓,其下部可以将酸化液收集起来,在好氧堆肥阶段,通过回流可以将液体收集区收集的酸化液方便地回送到发酵仓内调节好氧堆肥时所需水分。2. The utility model is equipped with a sieve plate in the fermenter, which divides the fermenter into two parts, and serves as a filter bed type anaerobic fermentation bin in the anaerobic digestion stage, and the lower part can collect the acidification liquid, and in the aerobic composting stage , through backflow, the acidified liquid collected in the liquid collection area can be conveniently returned to the fermentation bin to adjust the water required for aerobic composting.
3、本实用新型在搅拌叶片上设有通风系统,在不同的阶段选择通风或不通风而实现厌氧消化和好氧堆肥在同一设备中进行。3. The utility model is equipped with a ventilation system on the mixing blade, and the ventilation or non-ventilation is selected at different stages to realize anaerobic digestion and aerobic composting in the same equipment.
4、本实用新型在厌氧消化阶段是过滤床式消化方式,可以将其串联起来使用。4. In the anaerobic digestion stage, the utility model is a filter bed digestion method, which can be used in series.
四、附图说明4. Description of drawings
图1为本实用新型实施例的组成示意图Fig. 1 is the composition schematic diagram of the utility model embodiment
图2为发酵罐串联使用示意图Figure 2 is a schematic diagram of the use of fermentation tanks in series
图3为发酵仓的结构剖面示意图Figure 3 is a schematic cross-sectional view of the structure of the fermentation chamber
图4为搅拌轴和叶片的局部放大图Figure 4 is a partial enlarged view of the stirring shaft and blades
五、具体实施方式5. Specific implementation
本实用新型的实施例如图1、图3、图4所示,它主要包括发酵罐19、搅拌系统、通风系统、加热系统;其中圆柱体发酵罐19固定在支架16上,发酵罐19内设有筛板10,筛板10上设有筛孔26,筛板10将发酵罐19隔成两部分,上部为可将垃圾在厌氧消化过程中产生的酸化液滤去的过滤床式发酵仓3,下部为液体收集区2;搅拌系统包括设在发酵仓3的中间且安装在轴座20中的搅拌轴13,轴13为不锈钢空心管并由电动机5驱动;通风系统包括与轴13连接在一起的两层搅拌叶片14,叶片14上设有与轴13的中空气道25相通的中空气道23和通气孔24、轴13的顶端为进气口,通过输气管与鼓风机8相连,鼓风机送出的气体通过输气管、轴13的中空气道25、叶片14上的中空气道23和通气孔24向发酵仓3内输入新鲜空气,以保证好氧堆肥阶段氧气的供给;加热系统包括设在发酵罐19四周和底部的循环水浴加热套17,加热套17内有恒温热水21,恒温热水21由恒温热水源通过水泵22、加热套17底部的出水口11、侧面的进水口7循环供给;控温插口18设在两层搅拌叶片14之间的发酵罐19的侧壁上并伸出加热套17;发酵仓3的顶部设有进出料口4、出气口6、进液口15,出气口6通过输气管与储气罐9相连;液体收集区2的底部设有伸出加热套17的出液管12,出液管12通过水泵1与进液口15相连,将液体收集区2内的酸化液泵入发酵仓3内用以调节好氧堆肥阶段发酵仓内所需的水分。如图2所示,在厌氧消化阶段发酵罐19串联在一起使用。The embodiment of the present utility model is shown in Fig. 1, Fig. 3, Fig. 4, and it mainly comprises fermentation tank 19, stirring system, ventilation system, heating system; There is a sieve plate 10, and the sieve plate 10 is provided with a sieve hole 26. The sieve plate 10 divides the fermenter 19 into two parts, and the upper part is a filter bed type fermentation bin that can filter out the acidified liquid produced during the anaerobic digestion process. 3. The lower part is the liquid collection area 2; the stirring system includes a stirring shaft 13 located in the middle of the fermentation bin 3 and installed in the
本实用新型的工作过程是:将垃圾原料从进出口4装入发酵罐19内,首先进行厌氧消化,将垃圾的含水率调节至50-70%后密封发酵罐19,垃圾厌氧消化过程中产生的酸化液体通过筛板10上的筛孔26流入发酵罐19底部的液体收集区2,串联使用的发酵罐19使不同消化阶段的酸化液在各发酵罐内进行回流,给新鲜进料接种,调节各发酵罐内负荷;产生的沼气通过输气管输入储气罐9中备用。厌氧消化结束后,通过鼓风机进行供氧,空气经输气管、进气口、搅拌轴13的中空气道25、叶片14的中空气道23和通气孔24进入发酵仓3内,在叶片14旋转的同时新鲜的空气就不断的输入厌氧消化后的垃圾料中以满足好氧堆肥时微生物对氧气的需要。为了保证好氧堆肥过程的含水率,水泵1通过出液管12、输液管、进液管15,将液体收集区2内的酸化液回送到发酵仓3内,调节好氧堆肥阶段发酵仓3内所需的水分。The working process of the present utility model is: put the garbage raw material into the fermentation tank 19 from the inlet and outlet 4, first carry out anaerobic digestion, adjust the water content of the garbage to 50-70%, and then seal the fermentation tank 19, the garbage anaerobic digestion process The acidified liquid produced in the sieve plate 10 flows into the liquid collection area 2 at the bottom of the fermenter 19 through the sieve hole 26 on the sieve plate 10, and the fermenter 19 used in series makes the acidified liquid in different digestion stages reflux in each fermenter to feed fresh feed Inoculate and adjust the internal load of each fermenter; the generated biogas is input into the gas storage tank 9 through the gas pipeline for standby. After the anaerobic digestion is completed, oxygen is supplied by a blower, and the air enters the fermentation chamber 3 through the air pipe, the air inlet, the
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Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100378039C (en) * | 2004-10-21 | 2008-04-02 | 上海神工环保股份有限公司 | Anaerobic fermentation technology in storehouse for organic garbage and equipment |
CN101804417A (en) * | 2010-05-10 | 2010-08-18 | 北京昊业怡生科技有限公司 | Active landfill method of urban domestic garbage |
CN102115345A (en) * | 2010-12-02 | 2011-07-06 | 北京工商大学 | Set of movable efficient aerobic composting processes for food waste |
CN102690754A (en) * | 2012-06-20 | 2012-09-26 | 鄂尔多斯市东胜区传祥垃圾处理有限责任公司 | Combined anaerobic fermentation tank |
CN102786363A (en) * | 2012-02-21 | 2012-11-21 | 天津生态城环保有限公司 | Novel kitchen garbage fermentation device and usage method |
CN103464076A (en) * | 2013-09-11 | 2013-12-25 | 宜兴天力化工纳米科技有限公司 | Energy-saving carbonization reactor |
CN108094979A (en) * | 2017-12-22 | 2018-06-01 | 邓威 | A kind of fermentation tank for ferment medical stone slag and shoot vegetable fibrous root |
CN108157151A (en) * | 2017-12-22 | 2018-06-15 | 邓威 | A kind of shoot vegetable and its production technology |
CN108949423A (en) * | 2018-07-26 | 2018-12-07 | 贵州省仁怀市致和酒业有限公司 | A kind of fermentor |
-
2003
- 2003-01-23 CN CNU032268343U patent/CN2600443Y/en not_active Expired - Fee Related
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100378039C (en) * | 2004-10-21 | 2008-04-02 | 上海神工环保股份有限公司 | Anaerobic fermentation technology in storehouse for organic garbage and equipment |
CN101804417A (en) * | 2010-05-10 | 2010-08-18 | 北京昊业怡生科技有限公司 | Active landfill method of urban domestic garbage |
CN101804417B (en) * | 2010-05-10 | 2013-01-23 | 北京昊业怡生科技有限公司 | Active landfill method of urban domestic garbage |
CN102115345A (en) * | 2010-12-02 | 2011-07-06 | 北京工商大学 | Set of movable efficient aerobic composting processes for food waste |
CN102786363A (en) * | 2012-02-21 | 2012-11-21 | 天津生态城环保有限公司 | Novel kitchen garbage fermentation device and usage method |
CN102690754A (en) * | 2012-06-20 | 2012-09-26 | 鄂尔多斯市东胜区传祥垃圾处理有限责任公司 | Combined anaerobic fermentation tank |
CN103464076A (en) * | 2013-09-11 | 2013-12-25 | 宜兴天力化工纳米科技有限公司 | Energy-saving carbonization reactor |
CN108094979A (en) * | 2017-12-22 | 2018-06-01 | 邓威 | A kind of fermentation tank for ferment medical stone slag and shoot vegetable fibrous root |
CN108157151A (en) * | 2017-12-22 | 2018-06-15 | 邓威 | A kind of shoot vegetable and its production technology |
CN108949423A (en) * | 2018-07-26 | 2018-12-07 | 贵州省仁怀市致和酒业有限公司 | A kind of fermentor |
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