CN204752498U - Cow dung recycle system - Google Patents
Cow dung recycle system Download PDFInfo
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- CN204752498U CN204752498U CN201520253155.6U CN201520253155U CN204752498U CN 204752498 U CN204752498 U CN 204752498U CN 201520253155 U CN201520253155 U CN 201520253155U CN 204752498 U CN204752498 U CN 204752498U
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- 210000003608 fece Anatomy 0.000 title claims abstract description 102
- 238000000855 fermentation Methods 0.000 claims abstract description 41
- 239000010871 livestock manure Substances 0.000 claims abstract description 28
- 238000001035 drying Methods 0.000 claims abstract description 24
- 238000010438 heat treatment Methods 0.000 claims abstract description 6
- 238000011084 recovery Methods 0.000 claims abstract description 5
- 238000004064 recycling Methods 0.000 claims description 20
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 17
- 238000002485 combustion reaction Methods 0.000 claims description 16
- 238000006477 desulfuration reaction Methods 0.000 claims description 8
- 230000023556 desulfurization Effects 0.000 claims description 8
- 239000008236 heating water Substances 0.000 claims description 8
- 238000000034 method Methods 0.000 claims description 8
- 238000011010 flushing procedure Methods 0.000 claims description 4
- 239000011229 interlayer Substances 0.000 claims description 4
- 239000000835 fiber Substances 0.000 claims description 3
- 230000008569 process Effects 0.000 claims description 3
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 abstract description 12
- 239000007787 solid Substances 0.000 abstract description 9
- 210000002700 urine Anatomy 0.000 abstract description 4
- 241001465754 Metazoa Species 0.000 abstract description 2
- 230000003009 desulfurizing effect Effects 0.000 abstract 1
- 241000283690 Bos taurus Species 0.000 description 66
- 239000007788 liquid Substances 0.000 description 9
- 239000000463 material Substances 0.000 description 6
- 230000004151 fermentation Effects 0.000 description 5
- 238000000265 homogenisation Methods 0.000 description 4
- 239000002994 raw material Substances 0.000 description 3
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 2
- 238000009264 composting Methods 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 239000003337 fertilizer Substances 0.000 description 2
- 244000144972 livestock Species 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 239000003895 organic fertilizer Substances 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 230000002354 daily effect Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000003203 everyday effect Effects 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 244000144977 poultry Species 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000002002 slurry Substances 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
- Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
- Y02C20/00—Capture or disposal of greenhouse gases
- Y02C20/20—Capture or disposal of greenhouse gases of methane
-
- 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
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/20—Sludge processing
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- Treatment Of Sludge (AREA)
- Fertilizers (AREA)
Abstract
Description
技术领域 technical field
本实用新型属于畜禽粪便处理利用领域,特别涉及一种牛粪回收利用系统,更具体而言,涉及一种以牛粪为原料制备牛床垫料的回收利用系统。 The utility model belongs to the field of treatment and utilization of livestock and poultry manure, in particular to a cow manure recycling system, more specifically, to a recycling system for preparing cow bedding with cow manure as a raw material.
背景技术 Background technique
牛粪作为一种动物性有机肥料,是一种宝贵的资源,牛采食量大,每天所排出的粪尿比其他家畜多,一头成年牛,每昼夜排粪量幅度为28.4-48.1kg,每昼夜排尿量幅度为6.5-14.1kg,大量的牛粪尿不仅污染空气和水源,而且占据了大片的土地,目前在国内外牛粪的处理方法上主要用于堆肥和制备沼气。 As a kind of animal organic fertilizer, cow dung is a precious resource. Cattle eat a lot of food and excrete more feces and urine than other livestock every day. An adult cow excretes 28.4-48.1kg per day and night. The daily urine output ranges from 6.5 to 14.1kg. A large amount of cow dung not only pollutes the air and water sources, but also occupies a large area of land. At present, the treatment methods of cow dung at home and abroad are mainly used for composting and biogas preparation.
采用堆肥的处理方法,虽然牛粪经过生化加工工艺处理制成绿色有机肥料相对来说较环保,但是由于牛粪质地紧实,成分与猪粪相似,粪中含水量高,通气性差,分解缓慢,发酵温度低,肥效迟缓,故习称牛粪为“冷性肥料”。 Using the composting method, although the green organic fertilizer made from cow dung is relatively environmentally friendly through biochemical processing, but because the texture of cow dung is compact and its composition is similar to that of pig manure, the manure has high water content, poor aeration, and slow decomposition. , the fermentation temperature is low, and the fertilizer effect is slow, so cow dung is commonly called "cold fertilizer".
制备沼气的处理方法,直接将大量牛粪放在厌氧发酵设备内发酵以产生大量的沼气,发酵后,通常剩余的残渣的处理方法很难令人满意。 The treatment method for preparing biogas is to directly ferment a large amount of cow dung in anaerobic fermentation equipment to produce a large amount of biogas. After fermentation, the treatment method for the remaining residue is usually unsatisfactory.
为解决上述问题,目前出现了各种各样的解决方案,例如,中国专利文献公开了一种新型牛粪便处理系统[专利号ZL201320634426.3],其由蓄粪池、固液分离机、干燥器、粉碎机、沼气池组成,利用粪污冲洗泵将牛粪便通过原料输送管进入所述固液分离机进行固液分离,分离出的固态牛粪便由固液分离机的出料口输出,进入干燥器进行干燥处理,干燥后的牛粪便经过粉碎系统加工成牛床垫料,分离出的液体通过分离液输出管进入设于地下的沼气池。 In order to solve the above problems, various solutions have appeared at present. For example, Chinese patent literature discloses a new type of cow manure treatment system [Patent No. ZL201320634426.3], which consists of a septic tank, a solid-liquid separator, a drying Composed of a device, a pulverizer, and a biogas digester, the cow manure is sent to the solid-liquid separator through the raw material conveying pipe by the manure flushing pump for solid-liquid separation, and the separated solid cow manure is output from the outlet of the solid-liquid separator. Enter the drier for drying treatment, the dried cow manure is processed into cow bedding material through the crushing system, and the separated liquid enters the underground biogas digester through the separation liquid output pipe.
上述技术方案分离出的固态粪便可作为牛床垫料,分离出的液体实现了零排放,不会对环境造成污染。但是其存在至少两点缺陷:1、对粪便的利用率并不高,未进行有效的厌氧发酵流程并且只针对沼液产生的沼气进行利用,因此产生的沼气非常有限,特别是对产生的沼气的利用更是欠缺,并不能形成一个循环的回收利用系统,即利用粪便自身产生的沼气供给于固态粪便的加热干燥;2、由于沼气从厌氧发酵装置产出时,特别是在中温或高温发酵时,携带有大量的H2S,由于沼气中还有大量的水蒸汽存在,水与沼气中的H2S共同作用,加速了金属管道、阀门和流量计的腐蚀和堵塞。另外,H2S燃烧后生成SO2,与燃烧产物中的水蒸气结合成亚硫酸,使设备的金属表面产生腐蚀,并且还会造成对大气环境的污染,影响人体健康。因此,在使用沼气之前,必须脱除其中的H2S。综上所述,本案因此而生。 The solid feces separated by the above technical solution can be used as bedding material for cattle bedding, and the separated liquid realizes zero discharge and will not pollute the environment. However, it has at least two defects: 1. The utilization rate of feces is not high, no effective anaerobic fermentation process is carried out and only the biogas produced by biogas slurry is used, so the biogas produced is very limited, especially for the produced biogas The utilization of biogas is even more deficient, and a recycling system cannot be formed, that is, the biogas produced by the feces itself is used to supply the heating and drying of solid feces; During high-temperature fermentation, a large amount of H 2 S is carried. Since there is still a large amount of water vapor in the biogas, the water and the H 2 S in the biogas work together to accelerate the corrosion and blockage of metal pipes, valves and flow meters. In addition, H 2 S burns to generate SO 2 , which combines with water vapor in the combustion product to form sulfurous acid, which causes corrosion on the metal surface of the equipment, and also causes pollution to the atmospheric environment and affects human health. Therefore, before using the biogas, the H 2 S must be removed. Based on the above, this case arises.
实用新型内容 Utility model content
本实用新型的目的在于克服现有技术的不足,提供了一种以牛粪为原料制备牛床垫料的回收利用系统,其通过牛粪便厌氧发酵后制备的沼气燃烧加热牛粪残渣得到牛床垫料。 The purpose of the utility model is to overcome the deficiencies of the prior art, and to provide a recycling system for preparing cow bedding materials with cow dung as raw material, which uses the biogas prepared after anaerobic fermentation of cow manure to burn and heat the cow dung residue to obtain cow dung. Mattress.
本实用新型解决问题采用的技术方案是: The technical solution adopted by the utility model to solve the problem is:
一种牛粪回收利用系统,根据牛粪处理流程依次包括牛舍、集粪池、匀浆池、厌氧发酵罐、干湿分离机以及牛粪烘干室,所述的牛粪烘干室连接有加热源沼气燃烧室,该沼气燃烧室通过沼气输送管道连接到厌氧发酵罐,该沼气燃烧室与厌氧发酵罐之间设置有脱硫塔。 A cow dung recovery and utilization system, according to the cow dung treatment process, sequentially includes a cow house, a manure collection tank, a homogenization tank, an anaerobic fermentation tank, a dry-wet separator and a cow dung drying room, the cow dung drying room A heating source biogas combustion chamber is connected, and the biogas combustion chamber is connected to an anaerobic fermentation tank through a biogas transmission pipeline, and a desulfurization tower is arranged between the biogas combustion chamber and the anaerobic fermentation tank.
在上述一种牛粪回收利用系统中,所述的脱硫塔分别通过沼气输送管道连接于沼气燃烧室和加热水塔。 In the above cow dung recovery and utilization system, the desulfurization tower is connected to the biogas combustion chamber and the heating water tower respectively through the biogas delivery pipeline.
在上述一种牛粪回收利用系统中,所述的加热水塔与厌氧发酵罐相连,热水通过热水输送管道输送至厌氧发酵罐的内壁夹层。 In the above cow dung recycling system, the heating water tower is connected to the anaerobic fermentation tank, and the hot water is transported to the inner wall interlayer of the anaerobic fermentation tank through the hot water delivery pipeline.
在上述一种牛粪回收利用系统中,所述的厌氧发酵罐下方设置有排水口。 In the above-mentioned cow dung recycling system, a drain is provided below the anaerobic fermentation tank.
在上述一种牛粪回收利用系统中,所述的集粪池与匀浆池之间还设置有用于隔离长粗纤维的格栅。 In the above-mentioned cow dung recycling system, a grid for isolating long thick fibers is also provided between the manure collection tank and the homogenization tank.
在上述一种牛粪回收利用系统中,所述牛粪烘干室内设置有牛粪输送绞龙。 In the above cow dung recycling system, a cow dung conveying auger is arranged in the cow dung drying chamber.
在上述一种牛粪回收利用系统中,所述的牛粪烘干室还设置有排热气管道。 In the above cow dung recycling system, the cow dung drying chamber is also provided with a heat exhaust gas pipeline.
在上述一种牛粪回收利用系统中,所述的牛舍与集粪池之间设置有粪污冲洗泵。 In the above cow dung recycling system, a manure flushing pump is arranged between the cow house and the manure collection tank.
在上述一种牛粪回收利用系统中,所述的厌氧发酵罐顶部设置有沼气出口。 In the above cow dung recycling system, the top of the anaerobic fermentation tank is provided with a biogas outlet.
本实用新型的有益效果是:本实用新型通过对牛粪便厌氧发酵后产生的沼气来燃烧烘干固态粪便,干燥后的固态粪便作为牛床垫料,从而大大提高了牛粪便的利用率,实现了回收再利用,具有很强的经济、社会效益。并且沼气加热还可以用于加热水用来对厌氧发酵罐内保温和用于养殖场其他使用。 The beneficial effects of the utility model are: the utility model burns and dries the solid feces through the methane produced by the anaerobic fermentation of the cow feces, and the dried solid feces are used as the bedding material of the cow bed, thereby greatly improving the utilization rate of the cow feces, Recycling and reuse are realized, which has strong economic and social benefits. And biogas heating can also be used to heat water to keep warm in the anaerobic fermentation tank and other uses in the farm.
附图说明 Description of drawings
图1为本实用新型未示出加热水塔的结构示意图; Fig. 1 is the utility model not showing the structural representation of heating water tower;
图2为本实用新型结构示意图; Fig. 2 is a structural representation of the utility model;
图3为厌氧发酵罐的结构示意图。 Fig. 3 is a schematic structural diagram of an anaerobic fermentation tank.
图中:1、牛舍,2、粪污冲洗泵,4、集粪池,5、格栅,6、匀浆池,7、脱硫塔,8、厌氧发酵罐,81、厌氧发酵罐的内壁夹层,82、热水输送管道,83、排水口,84、沼气出口,9、干湿分离机,10、沼气燃烧室,11、牛粪烘干室,12、牛粪输送绞龙,13、牛床垫料,14、排热气管道,15、加热水塔。 In the figure: 1. Cowshed, 2. Manure flushing pump, 4. Septic tank, 5. Grille, 6. Homogenizer tank, 7. Desulfurization tower, 8. Anaerobic fermentation tank, 81. Anaerobic fermentation tank inner wall interlayer, 82, hot water delivery pipe, 83, water outlet, 84, biogas outlet, 9, wet and dry separator, 10, biogas combustion chamber, 11, cow dung drying room, 12, cow dung conveying auger, 13. Cattle mattress material, 14. Exhaust heat pipe, 15. Heating water tower.
具体实施方式 Detailed ways
以下结合附图和具体实施例对本实用新型作进一步说明 Below in conjunction with accompanying drawing and specific embodiment the utility model will be further described
如图1至图3所示,本实用新型提供了一种牛粪回收利用系统,根据牛粪处理流程依次包括牛舍1、集粪池4、匀浆池6、厌氧发酵罐8、干湿分离机9以及牛粪烘干室11,所述的牛粪烘干室11连接有加热源沼气燃烧室10,该沼气燃烧室10通过沼气输送管道连接到厌氧发酵罐8,该沼气燃烧室10与厌氧发酵罐8之间设置有脱硫塔7,脱硫塔7内使用氧化铁作为脱硫剂对沼气进行脱硫,脱硫后的沼气通过输送管道分别连接于沼气燃烧室10和加热水塔15,加热水塔15与厌氧发酵罐8相连,在低温状态下,热水通过热水输送管道82输送至厌氧发酵罐8的内壁夹层81,用于维持厌氧发酵罐8内的温度,厌氧发酵罐8下方设置有排水口83,可用于水的排放,牛粪烘干室11内设置有牛粪输送绞龙12用于牛粪输送,牛粪烘干室11对外还设置有排热气管道14,防止室内因空气温度过高发生危险,厌氧发酵罐8顶部设置有沼气出口84,沼气通过管道连接到所有使用处。 As shown in Fig. 1 to Fig. 3, the utility model provides a kind of cow dung recycling system, according to the cow dung treatment process, sequentially includes a cow house 1, a manure collecting tank 4, a homogenizing tank 6, anaerobic fermentation tank 8, dry Wet separator 9 and cow dung drying chamber 11, described cow dung drying chamber 11 is connected with heating source biogas combustion chamber 10, and this biogas combustion chamber 10 is connected to anaerobic fermentation tank 8 through biogas delivery pipeline, and this biogas combustion A desulfurization tower 7 is arranged between the chamber 10 and the anaerobic fermentation tank 8, and iron oxide is used as a desulfurizer in the desulfurization tower 7 to desulfurize the biogas, and the desulfurized biogas is connected to the biogas combustion chamber 10 and the heating water tower 15 respectively through the delivery pipeline. The heating water tower 15 is connected with the anaerobic fermentation tank 8, and in the low temperature state, hot water is transported to the inner wall interlayer 81 of the anaerobic fermentation tank 8 through the hot water delivery pipeline 82, for maintaining the temperature in the anaerobic fermentation tank 8. The bottom of the fermenter 8 is provided with a drain port 83, which can be used for water discharge. The cow dung drying chamber 11 is provided with a cow dung conveying auger 12 for conveying cow dung. The cow dung drying chamber 11 is also provided with a heat exhaust pipe. 14. To prevent indoor danger due to high air temperature, a biogas outlet 84 is provided on the top of the anaerobic fermentation tank 8, and the biogas is connected to all places of use through pipelines.
本实用新型的工作原理为:牛舍1内产生的牛粪便聚集到集粪池4内,牛舍1与集粪池4之间设置有粪污冲洗泵2,粪污冲洗泵2将集粪池4内液态粪便抽进牛舍1内冲刷粪便回流进集粪池4,形成循环,当集粪池4内的牛粪便达到一定的量便泵送至匀浆池6,集粪池4与匀浆池6之间设置有用于隔离长粗纤维的格栅5,再在厌氧发酵罐8内发酵,发酵后的剩渣通过干湿分离机9固液分离,固体牛粪进入牛粪烘干室11干燥,而牛粪烘干室11的热源是通过厌氧发酵罐8产生的沼气燃烧产生,厌氧发酵罐8产生的沼气首先经过脱硫塔7脱硫,一部分用于在沼气燃烧室10内燃烧干燥牛粪,一部分用于加热水用于在低温状态下保持厌氧发酵罐8内温度,最后经过牛粪烘干室11干燥粉碎后牛粪成为含水量约为30%的牛床垫料。 The working principle of the utility model is as follows: the cow feces produced in the cowshed 1 are gathered in the manure collection tank 4, and a manure washing pump 2 is arranged between the cow shed 1 and the manure collection tank 4, and the manure washing pump 2 will collect the manure The liquid manure in the pool 4 is pumped into the cowshed 1 to flush the manure back into the cesspool 4 to form a cycle. When the cow manure in the cesspool 4 reaches a certain amount, it is pumped to the homogenization tank 6, and the cesspool 4 and A grid 5 for isolating long and thick fibers is set between the homogenization tanks 6, and then fermented in the anaerobic fermentation tank 8, and the residue after fermentation is separated from the solid and liquid by the dry-wet separator 9, and the solid cow dung enters the cow dung drying process. The drying chamber 11 is dry, while the heat source of the cow dung drying chamber 11 is produced by the biogas combustion produced by the anaerobic fermentation tank 8. The biogas produced by the anaerobic fermentation tank 8 is firstly desulfurized by the desulfurization tower 7, and part of it is used in the biogas combustion chamber 10. The cow dung is internally burned and dried, and part of it is used to heat water to maintain the temperature in the anaerobic fermentation tank 8 at a low temperature. Finally, the cow dung is dried and pulverized in the cow dung drying chamber 11, and the cow dung becomes a cow mattress with a water content of about 30%. material.
以上所述仅是本实用新型的优选实施方式,应当指出,对于本技术领域的普通技术人员来说,在不脱离本实用新型原理的前提下,还可以对本实用新型进行若干改进和修饰,这些改进和修饰也落入本实用新型权利要求的保护范围内。 The above is only a preferred embodiment of the utility model, it should be pointed out that for those of ordinary skill in the art, without departing from the principle of the utility model, some improvements and modifications can also be made to the utility model, these Improvements and modifications also fall within the protection scope of the claims of the utility model.
Claims (9)
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CN201520253155.6U CN204752498U (en) | 2015-04-24 | 2015-04-24 | Cow dung recycle system |
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CN201520253155.6U CN204752498U (en) | 2015-04-24 | 2015-04-24 | Cow dung recycle system |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106145588A (en) * | 2015-04-24 | 2016-11-23 | 浙江景生态牧业有限公司 | A kind of cattle manure recycling system |
CN108862410A (en) * | 2018-06-26 | 2018-11-23 | 江西正合环保工程有限公司 | A kind of preposition pretreatment unit in homogenate pond and technique |
CN113968663A (en) * | 2020-07-22 | 2022-01-25 | 北京时代桃源环境科技股份有限公司 | Efficient pretreatment device and method for preparing biogas through cow dung anaerobic fermentation |
-
2015
- 2015-04-24 CN CN201520253155.6U patent/CN204752498U/en not_active Expired - Lifetime
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106145588A (en) * | 2015-04-24 | 2016-11-23 | 浙江景生态牧业有限公司 | A kind of cattle manure recycling system |
CN108862410A (en) * | 2018-06-26 | 2018-11-23 | 江西正合环保工程有限公司 | A kind of preposition pretreatment unit in homogenate pond and technique |
CN113968663A (en) * | 2020-07-22 | 2022-01-25 | 北京时代桃源环境科技股份有限公司 | Efficient pretreatment device and method for preparing biogas through cow dung anaerobic fermentation |
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