CN206502756U - A kind of device of excess sludge mixture rubbish from cooking methane phase organic fertilizer - Google Patents
A kind of device of excess sludge mixture rubbish from cooking methane phase organic fertilizer Download PDFInfo
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- CN206502756U CN206502756U CN201621079720.2U CN201621079720U CN206502756U CN 206502756 U CN206502756 U CN 206502756U CN 201621079720 U CN201621079720 U CN 201621079720U CN 206502756 U CN206502756 U CN 206502756U
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- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 title claims abstract description 54
- 239000010802 sludge Substances 0.000 title claims abstract description 40
- 239000003895 organic fertilizer Substances 0.000 title claims abstract description 20
- 239000010813 municipal solid waste Substances 0.000 title claims description 14
- 239000000203 mixture Substances 0.000 title claims description 11
- 238000010411 cooking Methods 0.000 title claims 10
- 238000000855 fermentation Methods 0.000 claims abstract description 37
- 238000002156 mixing Methods 0.000 claims abstract description 18
- 230000004151 fermentation Effects 0.000 claims abstract description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 8
- 239000007788 liquid Substances 0.000 claims description 4
- 239000000463 material Substances 0.000 claims description 2
- 229910001220 stainless steel Inorganic materials 0.000 claims description 2
- 239000010935 stainless steel Substances 0.000 claims description 2
- 230000004888 barrier function Effects 0.000 claims 3
- 238000007599 discharging Methods 0.000 claims 2
- 238000005553 drilling Methods 0.000 claims 1
- 239000010806 kitchen waste Substances 0.000 abstract description 38
- 239000010865 sewage Substances 0.000 abstract description 14
- 238000005192 partition Methods 0.000 abstract description 10
- 239000007787 solid Substances 0.000 abstract description 4
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 238000007789 sealing Methods 0.000 abstract description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract 1
- 229910052760 oxygen Inorganic materials 0.000 abstract 1
- 239000001301 oxygen Substances 0.000 abstract 1
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 18
- 241000894006 Bacteria Species 0.000 description 7
- 238000000034 method Methods 0.000 description 7
- 239000005416 organic matter Substances 0.000 description 7
- 229910052739 hydrogen Inorganic materials 0.000 description 6
- 239000001257 hydrogen Substances 0.000 description 6
- 239000007789 gas Substances 0.000 description 5
- 239000002910 solid waste Substances 0.000 description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 4
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 description 4
- 244000005700 microbiome Species 0.000 description 3
- 241001148471 unidentified anaerobic bacterium Species 0.000 description 3
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-M Bicarbonate Chemical compound OC([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-M 0.000 description 2
- LCTONWCANYUPML-UHFFFAOYSA-M Pyruvate Chemical compound CC(=O)C([O-])=O LCTONWCANYUPML-UHFFFAOYSA-M 0.000 description 2
- 230000000789 acetogenic effect Effects 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 2
- 230000018044 dehydration Effects 0.000 description 2
- 238000006297 dehydration reaction Methods 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 235000014113 dietary fatty acids Nutrition 0.000 description 2
- 229930195729 fatty acid Natural products 0.000 description 2
- 239000000194 fatty acid Substances 0.000 description 2
- 150000004665 fatty acids Chemical class 0.000 description 2
- 235000013305 food Nutrition 0.000 description 2
- 235000019253 formic acid Nutrition 0.000 description 2
- 238000005469 granulation Methods 0.000 description 2
- 230000003179 granulation Effects 0.000 description 2
- 150000002431 hydrogen Chemical class 0.000 description 2
- 230000007062 hydrolysis Effects 0.000 description 2
- 238000006460 hydrolysis reaction Methods 0.000 description 2
- 235000021190 leftovers Nutrition 0.000 description 2
- 239000007791 liquid phase Substances 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 230000000696 methanogenic effect Effects 0.000 description 2
- 239000000178 monomer Substances 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 239000007790 solid phase Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 241001122767 Theaceae Species 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 210000000988 bone and bone Anatomy 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000009264 composting Methods 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 210000003278 egg shell Anatomy 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- 235000012054 meals Nutrition 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 239000002957 persistent organic pollutant Substances 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000000751 protein extraction Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 150000003384 small molecules Chemical class 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 238000009270 solid waste treatment Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
Classifications
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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
-
- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
-
- 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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- Fertilizers (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
本实用新型公开了一种剩余污泥混配厨余垃圾产甲烷制有机肥的装置,包括污泥斗、厨余垃圾斗、混料仓、破碎轮刀、锁气器、进料管、厌氧发酵罐、桨式搅拌器、传感器模块、换热套管、多孔隔板、出料口、排水口、排气管、造粒机、履带、烘干机、甲烷收集器、空气净化器、放空管。与现有技术相比,本实用新型将厨余垃圾粉碎后与城市污水处理厂剩余污泥混合后在厌氧发酵罐中进行厌氧发酵,发酵所产生的甲烷收集利用,发酵后的固体残渣生产有机肥,该装置具有结构简单,运行稳定可靠,系统密封性好,安全性高的特点。
The utility model discloses a device for producing organic fertilizer by mixing excess sludge with kitchen waste and producing methane, which comprises a sludge hopper, a kitchen waste hopper, a mixing bin, a crushing wheel knife, an air lock, a feeding pipe, and a Oxygen fermenter, paddle agitator, sensor module, heat exchange sleeve, porous partition, discharge port, drain port, exhaust pipe, granulator, crawler belt, dryer, methane collector, air purifier, Vent the tube. Compared with the prior art, the utility model pulverizes the kitchen waste and mixes it with the remaining sludge of the urban sewage treatment plant, and then carries out anaerobic fermentation in the anaerobic fermentation tank. The methane produced by the fermentation is collected and utilized, and the solid residue after fermentation is For the production of organic fertilizer, the device has the characteristics of simple structure, stable and reliable operation, good system sealing and high safety.
Description
技术领域technical field
本实用新型涉及一种固体废弃物处理装置,属固废资源化利用领域领域,尤其涉及一种剩余污泥混配厨余垃圾产甲烷制有机肥的装置。The utility model relates to a solid waste treatment device, which belongs to the field of resource utilization of solid waste, in particular to a device for producing methane from surplus sludge mixed with kitchen waste to produce organic fertilizer.
背景技术Background technique
剩余污泥是活性污泥法处理生活污水过程中产生的一种副产物,其产量大,含水率高,资源化利用困难,尤其是近年来城市化进程的加快,人均用水量的增加,生活污水入场处理率的大幅度提升,使城市污水处理厂剩余污泥的产量迅速增加,剩余污泥已经成为城市固体废弃物的一个重要来源,是垃圾围城的重要组成部分,与其他的固体废弃物不同,由于剩余污泥中含有大量的有机物、动植物(微生物)的残体、纤维质、重金属等,若不能得以妥善处理,势必会对生态环境造成严重危害,同时,剩余污泥中因含有大量的水分,运输转移十分困难,因此,剩余污泥的处理有其独特的要求,需要尽快就近处理,需要进行稳定化、无害化、最好是资源化处理。典型的城市生活污水剩余污泥的处置方法主要有资源化(比如制备建材、路基材料等),能源化(比如产油、产气、焚烧发电、提取蛋白质),土地利用(比如堆肥、土壤改良等),填埋等。Excess sludge is a by-product produced in the process of treating domestic sewage by activated sludge method. Its output is large, its moisture content is high, and resource utilization is difficult. Especially in recent years, the urbanization process has accelerated, and the per capita water consumption has increased. The substantial increase in the sewage treatment rate has led to a rapid increase in the output of excess sludge in urban sewage treatment plants. Excess sludge has become an important source of urban solid waste and an important part of the garbage siege. It is different from other solid waste Because the remaining sludge contains a large amount of organic matter, animal and plant (microorganism) residues, fiber, heavy metals, etc., if it cannot be properly treated, it will definitely cause serious harm to the ecological environment. Containing a large amount of water, it is very difficult to transport and transfer. Therefore, the treatment of excess sludge has its own unique requirements. It needs to be treated as soon as possible and nearby, and it needs to be stabilized, harmless, and preferably resource-based. The disposal methods of typical urban domestic sewage residual sludge mainly include resource utilization (such as preparation of building materials, roadbed materials, etc.), energy utilization (such as oil production, gas production, incineration power generation, protein extraction), land utilization (such as composting, soil improvement, etc.) etc.), landfill, etc.
厨余垃圾是指居民日常生活及食品加工、饮食服务、单位供餐等活动中产生的垃圾,包括丢弃不用的菜叶、剩菜、剩饭、果皮、蛋壳、茶渣、骨头等,其主要来源为家庭厨房、餐厅、饭店、食堂、市场及其他与食品加工有关的行业。具有含水率高,易腐烂,营养物质多的特点,若不能合理的进行处理和处置,将对人居环境和人体健康造成危害。近几年来,由于经济的发展,人们生活水平的提高,餐饮行业空前发展,厨余垃圾产生量大大增加,应运而生的,大量的厨余垃圾处理器随之产生,目前市场上的厨余垃圾处理器主要有两种,一种是将厨余垃圾粉碎后排入市政管网,这种厨余垃圾处理装置常用作家用厨余垃圾的处理;另一种是箱式厌氧堆肥处理垃圾处理装置,一般适合大规模的厨余垃圾的处理,常用于大型食堂、餐厅、酒店。第一类厨余垃圾处理器处理厨余垃圾的原理是将厨余垃圾处理后,在大量水的冲洗下排入下水管道,该方法没有从根本上处理厨余垃圾,而是将固体的厨余垃圾粉碎后经市政管网输送到了城市污水处理厂,这样的处理方法存在大量的潜在危害,比如大量水资源的浪费、污水处理厂处理量的增加、污水处理厂水污染负荷的提高、市政管网的沉积与拥堵、污水管网基建成本和维护成本的提升等。第二类厨余垃圾的处理原理是,将厨余垃圾粉碎后,在合适的环境条件下使厨余垃圾厌氧发酵,使厨余垃圾减量化,该类厨余垃圾处理器的运行稳定性有待提高,同时由于厌氧发酵过程中会产生甲烷和硫化氢气体,易导致餐厅、食堂、酒店空气出现异味。Kitchen waste refers to the waste generated in the daily life of residents and activities such as food processing, catering services, and unit meals, including discarded vegetable leaves, leftovers, leftovers, fruit peels, eggshells, tea dregs, bones, etc. The main sources are home kitchens, restaurants, restaurants, canteens, markets and other industries related to food processing. It has the characteristics of high moisture content, perishability, and rich nutrients. If it cannot be properly treated and disposed of, it will cause harm to the living environment and human health. In recent years, due to the development of the economy, the improvement of people's living standards, and the unprecedented development of the catering industry, the amount of kitchen waste has increased greatly. As the times require, a large number of kitchen waste processors have emerged. There are two main types of garbage processors. One is to crush kitchen waste and discharge it into the municipal pipe network. This kind of kitchen waste treatment device is commonly used to treat domestic kitchen waste; The treatment device is generally suitable for large-scale kitchen waste treatment, and is often used in large canteens, restaurants, and hotels. The principle of the first type of kitchen waste disposer to deal with kitchen waste is to discharge the kitchen waste into the sewer pipe after being washed with a large amount of water. This method does not fundamentally treat the kitchen waste, but treats the solid The remaining garbage is crushed and transported to the urban sewage treatment plant through the municipal pipe network. This treatment method has a large number of potential hazards, such as the waste of a large amount of water resources, the increase in the treatment capacity of the sewage treatment plant, the increase in the water pollution load of the sewage treatment plant, and the municipal The deposition and congestion of the pipe network, the increase in the infrastructure cost and maintenance cost of the sewage pipe network, etc. The treatment principle of the second type of kitchen waste is that after the kitchen waste is crushed, the kitchen waste is anaerobically fermented under suitable environmental conditions to reduce the amount of kitchen waste. The operation of this type of kitchen waste processor is stable At the same time, due to the generation of methane and hydrogen sulfide gas during anaerobic fermentation, it is easy to cause peculiar smell in the air of restaurants, canteens and hotels.
实用新型内容Utility model content
本实用新型的目的就在于为了解决现有城市生活污水剩余污泥和厨余垃圾的资源化方面的问题而提供一种剩余污泥混配厨余垃圾产甲烷制有机肥的装置。The purpose of the utility model is to provide a device for producing organic fertilizer by mixing residual sludge with kitchen waste to produce organic fertilizer in order to solve the problem of resource utilization of remaining sludge from urban domestic sewage and kitchen waste.
本实用新型通过以下技术方案来实现上述目的:一种剩余污泥混配厨余垃圾产甲烷制有机肥的装置,包括10污泥斗、11厨余垃圾斗、12混料仓、13破碎轮刀、14锁气器、15进料管、2厌氧发酵罐、21桨式搅拌器、22传感器模块、23换热套管、24多孔隔板、25出料口、26排水口、27排气管、3造粒机、30履带、4烘干机、5甲烷收集器、6空气净化器、60放空管。The utility model achieves the above-mentioned purpose through the following technical solutions: a device for producing organic fertilizer by mixing surplus sludge with kitchen waste, including 10 sludge hoppers, 11 kitchen waste hoppers, 12 mixing bins, and 13 crushing wheels Knife, 14 air locker, 15 feed pipe, 2 anaerobic fermentation tank, 21 paddle agitator, 22 sensor module, 23 heat exchange sleeve, 24 porous partition, 25 discharge port, 26 drain port, 27 row Air pipe, 3 granulator, 30 crawler, 4 dryer, 5 methane collector, 6 air cleaner, 60 vent pipe.
进一步的,所述的混料仓12的中心位置安装有破碎轮刀13。Further, a crushing wheel knife 13 is installed at the center of the mixing bin 12 .
进一步的,所述的锁气器13为重锤式锁气器。Further, the air locker 13 is a hammer type air locker.
进一步的,所述的厌氧发酵罐2上下两封头与罐体之间采用法兰连接,便于拆卸和维护,厌氧发酵罐2沿轴向在中心位置设有所述的桨式搅拌器21,顶部设有所述的排气管27,顶部内壁面安装有所述的传感器模块22,中下部设有多孔隔板24,底部设有所述的排水管26。Further, the upper and lower ends of the anaerobic fermentation tank 2 are flanged to the tank body, which is convenient for disassembly and maintenance. The anaerobic fermentation tank 2 is provided with the paddle agitator at the center along the axial direction 21. The exhaust pipe 27 is provided on the top, the sensor module 22 is installed on the inner wall of the top, the porous partition 24 is provided at the middle and lower part, and the drain pipe 26 is provided at the bottom.
进一步的,所述的传感器模块22至少包含温度传感器、压力传感器、pH传感器和液面传感器。Further, the sensor module 22 includes at least a temperature sensor, a pressure sensor, a pH sensor and a liquid level sensor.
进一步的,所述的换热套管23中通入热水或冷水,保持厌氧发酵罐2中的温度在48~58℃。Further, hot water or cold water is passed into the heat exchange sleeve 23 to keep the temperature in the anaerobic fermentation tank 2 at 48-58°C.
进一步的,所述的造粒机3优选为盘式造粒机。Further, the granulator 3 is preferably a pan granulator.
进一步的,所述的烘干机4优选为盘式干燥机。Further, the dryer 4 is preferably a tray dryer.
所述的污泥斗10、厨余垃圾斗11均通过管道连接于混料仓12,并采用法兰密封连接,所述的混料仓12底部安装有所述的锁气器14,所述的锁气器14通过所述的进料管15与所述的厌氧发酵罐2连通,并通过法兰密封,所述的厌氧发酵罐2为罐式装置,外壁面包覆有所述的换热套管23,所述的厌氧发酵罐2轴向中心位置安装有所述的桨式搅拌器21,所述的厌氧发酵罐2的顶部开孔并安装有排气管27,所述的厌氧发酵罐2的顶部内壁面安装有所述的传感器模块22,所述的厌氧发酵罐2中下部焊接有不锈钢板开孔而得的多孔隔板24;所述的厌氧发酵罐2底部设有所述的排水口26;所述的厌氧发酵罐2的侧壁面,在所述的多孔隔板24的上方开有所述的出料口25;所述的出料口25与所述的造粒机3通过管道连通;所述的造粒机3与所述的烘干机4通过履带30连通;所述的厌氧发酵罐2与所述的甲烷收集器5通过所述的排气管27连通,所述的甲烷收集器5末端接有所述的空气净化器6,所述的空气净化器6上设有放空管60。系统中的各装置间及各装置与管道间均采用法兰密封连接。The sludge hopper 10 and the kitchen waste hopper 11 are all connected to the mixing bin 12 through pipelines, and are connected by flange sealing. The bottom of the mixing bin 12 is equipped with the air locker 14, and the The air locker 14 communicates with the anaerobic fermenter 2 through the feed pipe 15, and is sealed by a flange. The anaerobic fermenter 2 is a tank-type device, and the outer wall is covered with the The heat exchange sleeve 23, the axial center position of the anaerobic fermentation tank 2 is equipped with the paddle agitator 21, the top of the anaerobic fermentation tank 2 is perforated and an exhaust pipe 27 is installed, The top inner wall of the anaerobic fermentation tank 2 is equipped with the sensor module 22, and the lower part of the anaerobic fermentation tank 2 is welded with a porous partition plate 24 obtained by opening holes in a stainless steel plate; The bottom of the fermenter 2 is provided with the drain port 26; the side wall of the anaerobic fermenter 2 has the discharge port 25 above the porous partition 24; The port 25 is communicated with the granulator 3 through a pipeline; the granulator 3 is communicated with the dryer 4 through a crawler belt 30; the anaerobic fermentation tank 2 is communicated with the methane collector 5 It communicates with the exhaust pipe 27, the end of the methane collector 5 is connected with the air cleaner 6, and the air cleaner 6 is provided with an emptying pipe 60. All devices in the system and between devices and pipelines are connected by flange seals.
本实用新型的有益效果在于:本实用新型是一种剩余污泥混配厨余垃圾产甲烷制有机肥的装置,与现有技术相比,本实用新型将厨余垃圾粉碎后与城市污水处理厂剩余污泥混合,当温度和压力合适时,厌氧菌和兼性菌将粉碎后的厨余垃圾和城市污水处理厂剩余污泥进行水解,将固体废弃物中的大分子有机物转化为可溶性小分子有机单体,这些溶解性的有机物在微生物作用下继续发酵,生成氢气、甲酸、重碳酸盐、丙酮酸盐、乙醇及各类挥发性低级脂肪酸,接下来,在产氢产乙酸细菌的作用下简单有机物转化为乙酸和氢气,重碳酸盐转化为乙酸,最后,在产甲烷菌的作用下,乙酸、氢气、二氧化碳转化为甲烷,水解后的固体残渣可制备为农用有机肥。该装置即实现了固体废弃物的资源化,又将城市污水处理厂剩余污泥中对环境存在潜在威胁的有机污染物转化为了能源,水解后的固体熟料转化为农用有机肥,该装置结构简单,运行稳定可靠,系统密封性好,安全性高。The beneficial effect of the utility model lies in that the utility model is a device for producing organic fertilizer by mixing surplus sludge with kitchen waste and producing methane. When the temperature and pressure are appropriate, anaerobic and facultative bacteria will hydrolyze the pulverized kitchen waste and the remaining sludge of urban sewage treatment plants, and convert the macromolecular organic matter in solid waste into soluble Small-molecule organic monomers, these soluble organic substances continue to ferment under the action of microorganisms to generate hydrogen, formic acid, bicarbonate, pyruvate, ethanol and various volatile lower fatty acids. Next, hydrogen-producing acetogenic bacteria Under the action of simple organic matter is converted into acetic acid and hydrogen, bicarbonate is converted into acetic acid, and finally, under the action of methanogenic bacteria, acetic acid, hydrogen, and carbon dioxide are converted into methane, and the solid residue after hydrolysis can be prepared as agricultural organic fertilizer. The device not only realizes the recycling of solid waste, but also converts the organic pollutants that have potential threats to the environment in the residual sludge of urban sewage treatment plants into energy, and the solid clinker after hydrolysis is converted into agricultural organic fertilizer. The structure of the device Simple, stable and reliable operation, good system sealing and high safety.
附图说明Description of drawings
图1是本实用新型的结构示意图。Fig. 1 is the structural representation of the utility model.
图2混料仓结构示意图。Figure 2 Schematic diagram of the mixing bin structure.
图3为锁气器结构示意图。Figure 3 is a schematic diagram of the structure of the air locker.
图1~3中:10-污泥斗、11-厨余垃圾斗、12-混料仓、13-破碎轮刀、14-锁气器、15-进料管、2-厌氧发酵罐、21-桨式搅拌器、22-传感器模块、23-换热套管、24-多孔隔板、25-出料口、26-排水口、27-排气管、3-造粒机、30-履带、4-烘干机、5-甲烷收集器、6-空气净化器、60-放空管。In Figures 1 to 3: 10-sludge hopper, 11-kitchen waste hopper, 12-mixing bin, 13-crushing wheel knife, 14-air locker, 15-feeding pipe, 2-anaerobic fermentation tank, 21-paddle agitator, 22-sensor module, 23-heat exchange sleeve, 24-porous partition, 25-outlet, 26-drain, 27-exhaust pipe, 3-granulator, 30- Tracks, 4-dryer, 5-methane collector, 6-air cleaner, 60-vent pipe.
具体实施方式detailed description
下面结合附图1~3对本实用新型作进一步说明:Below in conjunction with accompanying drawing 1~3, the utility model is further described:
如图1~3所示:本实用新型包括污泥斗10、厨余垃圾斗11、混料仓12、破碎轮刀13、锁气器14、进料管15、厌氧发酵罐2、桨式搅拌器21、传感器模块22、换热套管23、多孔隔板24、出料口25、排水口26、排气管27、造粒机3、履带30、烘干机4、甲烷收集器5、空气净化器6、放空管60。As shown in Figures 1 to 3: the utility model includes a sludge hopper 10, a kitchen waste hopper 11, a mixing bin 12, a crushing wheel knife 13, an air lock 14, a feeding pipe 15, an anaerobic fermentation tank 2, a paddle type agitator 21, sensor module 22, heat exchange sleeve 23, porous partition 24, discharge port 25, drain port 26, exhaust pipe 27, granulator 3, crawler belt 30, dryer 4, methane collector 5, air purifier 6, vent pipe 60.
如图1~3所示:城市污水处理厂污泥脱水车间初步脱水后的污泥输送至污泥斗10待用,厨余垃圾输送至厨余垃圾斗11待用,当设备运行时,污泥斗10中的污泥和厨余垃圾斗11中的厨余垃圾进入混料仓12中经破碎轮刀13破碎,当混料仓中混入足够的剩余污泥和厨余垃圾后,锁气器14的平衡锤1上移,上翻板打开,混合均匀的剩余污泥和厨余垃圾进入锁气器14中,上翻板封闭,平衡锤2上移,锁气器14的下翻板打开,混合均匀的剩余污泥和厨余垃圾经进料管15进入厌氧发酵罐2中,经桨式搅拌器21搅拌后进一步混合,混合后的剩余污泥和厨余垃圾混合物分散于多孔隔板24上,在多孔隔板24上由重力初步进行固液分离,固相混合物在厌氧菌的作用下进行厌氧发酵,液相穿透多孔隔板24进入厌氧发酵罐2的底部,当液面达到一定高度时厌氧发酵罐2底部的排水口26开启,液相排出并循环至废水处理环节进行处理,厌氧发酵所需要的温度条件由热交换管23中的热交换媒介提供,当厌氧发酵罐2中温度、压力、pH值适合厌氧菌和兼氧菌繁殖时,厌氧菌和兼氧菌分解剩余污泥和厨余垃圾中的有机物,将固体废弃物中的大分子有机物转化为可溶性小分子有机单体,这些溶解性的有机物在微生物作用下继续发酵,生成氢气、甲酸、重碳酸盐、丙酮酸盐、乙醇及各类挥发性低级脂肪酸,接下来,在产氢产乙酸细菌的作用下简单有机物转化为乙酸和氢气,重碳酸盐转化为乙酸,最后,在产甲烷菌的作用下,乙酸、氢气、二氧化碳转化为甲烷,所产生的甲烷气体经排气管27排出进入甲烷收集器5中进行甲烷气体的收集,其他非甲烷气体则排出,经空气净化器6净化后由放空管60排出,厌氧发酵罐2中的温度、pH值和压力由传感器模块22监测获取,并根据监测结果控制厌氧发酵罐2中的反应,当厌氧发酵过程完成后,固相混合物即厌氧发酵的熟料成为制备有机肥的原料,出料口25开启,厌氧发酵的熟料经管道输送至造粒机3中进行有机肥造粒,造粒所得的有机肥经履带30输送至烘干机4中进行烘干,之后装袋出售。As shown in Figures 1 to 3: the sludge after preliminary dehydration in the sludge dehydration workshop of the urban sewage treatment plant is transported to the sludge hopper 10 for standby use, and the kitchen waste is transported to the kitchen waste hopper 11 for standby use. When the equipment is running, the sewage The sludge in the mud hopper 10 and the kitchen waste in the kitchen waste hopper 11 enter the mixing bin 12 and are crushed by the crushing wheel knife 13. When enough remaining sludge and kitchen waste are mixed in the mixing bin, the air lock The counterweight 1 of the device 14 moves upward, the upper flap is opened, the evenly mixed remaining sludge and kitchen waste enter the air lock 14, the upper flap is closed, the counterweight 2 moves upward, and the lower flap of the air lock 14 Open, and the uniformly mixed surplus sludge and kitchen waste enter the anaerobic fermentation tank 2 through the feed pipe 15, and are further mixed after being stirred by the paddle agitator 21, and the mixed surplus sludge and kitchen waste mixture is dispersed in the porous On the partition 24, the solid-liquid separation is initially carried out by gravity on the porous partition 24, the solid phase mixture is anaerobically fermented under the action of anaerobic bacteria, and the liquid phase penetrates the porous partition 24 and enters the bottom of the anaerobic fermentation tank 2 , when the liquid level reaches a certain height, the drain port 26 at the bottom of the anaerobic fermentation tank 2 is opened, and the liquid phase is discharged and circulated to the wastewater treatment link for treatment. It is provided that when the temperature, pressure, and pH value in the anaerobic fermentation tank 2 are suitable for the reproduction of anaerobic bacteria and facultative bacteria, the anaerobic bacteria and facultative bacteria decompose the organic matter in the remaining sludge and kitchen waste, and the solid waste The macromolecular organic matter is converted into soluble small molecular organic monomers, and these soluble organic matter continue to ferment under the action of microorganisms to generate hydrogen, formic acid, bicarbonate, pyruvate, ethanol and various volatile lower fatty acids, and then , under the action of hydrogen-producing acetogenic bacteria, simple organic matter is converted into acetic acid and hydrogen, bicarbonate is converted into acetic acid, and finally, under the action of methanogenic bacteria, acetic acid, hydrogen, and carbon dioxide are converted into methane, and the methane gas produced It is discharged into the methane collector 5 through the exhaust pipe 27 to collect methane gas, and other non-methane gases are discharged. After being purified by the air cleaner 6, they are discharged from the vent pipe 60. The temperature and pH value in the anaerobic fermentation tank 2 The pressure and pressure are monitored and obtained by the sensor module 22, and the reaction in the anaerobic fermentation tank 2 is controlled according to the monitoring results. After the anaerobic fermentation process is completed, the solid-phase mixture, that is, the clinker of the anaerobic fermentation, becomes the raw material for preparing organic fertilizer, and the output The mouth 25 is opened, and the clinker of anaerobic fermentation is transported to the granulator 3 through the pipeline for organic fertilizer granulation, and the organic fertilizer obtained from the granulation is transported to the dryer 4 through the crawler belt 30 for drying, and then bagged for sale.
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107056552A (en) * | 2017-06-10 | 2017-08-18 | 陕西理工学院 | A kind of utilization excess sludge and agriculture and forestry organic waste material prepare the device of fertilizer |
CN108018206A (en) * | 2017-12-18 | 2018-05-11 | 四川万兆羊机电科技有限公司 | A kind of fermentation system based on ultrasonic wave |
CN110818214A (en) * | 2019-11-11 | 2020-02-21 | 大连理工大学 | High solid kitchen garbage of content and city excess sludge co-fermentation device are reinforceed to charcoal |
CN117383972A (en) * | 2022-12-29 | 2024-01-12 | 刘明 | Easy-to-ferment household garbage accumulation equipment |
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2016
- 2016-09-27 CN CN201621079720.2U patent/CN206502756U/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107056552A (en) * | 2017-06-10 | 2017-08-18 | 陕西理工学院 | A kind of utilization excess sludge and agriculture and forestry organic waste material prepare the device of fertilizer |
CN108018206A (en) * | 2017-12-18 | 2018-05-11 | 四川万兆羊机电科技有限公司 | A kind of fermentation system based on ultrasonic wave |
CN110818214A (en) * | 2019-11-11 | 2020-02-21 | 大连理工大学 | High solid kitchen garbage of content and city excess sludge co-fermentation device are reinforceed to charcoal |
CN117383972A (en) * | 2022-12-29 | 2024-01-12 | 刘明 | Easy-to-ferment household garbage accumulation equipment |
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