CN201250232Y - Biogas pool with circulated material distribution - Google Patents
Biogas pool with circulated material distribution Download PDFInfo
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- CN201250232Y CN201250232Y CNU2008201886965U CN200820188696U CN201250232Y CN 201250232 Y CN201250232 Y CN 201250232Y CN U2008201886965 U CNU2008201886965 U CN U2008201886965U CN 200820188696 U CN200820188696 U CN 200820188696U CN 201250232 Y CN201250232 Y CN 201250232Y
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- 238000009826 distribution Methods 0.000 title claims abstract description 12
- 239000000463 material Substances 0.000 title claims abstract description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 107
- 238000005315 distribution function Methods 0.000 claims abstract description 4
- 238000005336 cracking Methods 0.000 claims description 2
- 239000002351 wastewater Substances 0.000 claims 1
- 239000004744 fabric Substances 0.000 abstract description 10
- 238000004519 manufacturing process Methods 0.000 abstract description 5
- 230000000694 effects Effects 0.000 abstract description 3
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 abstract 2
- 206010039509 Scab Diseases 0.000 abstract 1
- 238000010276 construction Methods 0.000 description 11
- 239000002994 raw material Substances 0.000 description 8
- 239000004568 cement Substances 0.000 description 7
- 208000028659 discharge Diseases 0.000 description 6
- 238000000855 fermentation Methods 0.000 description 6
- 239000011449 brick Substances 0.000 description 5
- 230000004151 fermentation Effects 0.000 description 5
- 239000002184 metal Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 239000002002 slurry Substances 0.000 description 4
- 210000003608 fece Anatomy 0.000 description 3
- 239000003337 fertilizer Substances 0.000 description 3
- 239000010802 sludge Substances 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 2
- 239000010871 livestock manure Substances 0.000 description 2
- 239000010815 organic waste Substances 0.000 description 2
- 230000001681 protective effect Effects 0.000 description 2
- 239000002893 slag Substances 0.000 description 2
- 241001465754 Metazoa Species 0.000 description 1
- 238000004364 calculation method Methods 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 239000004035 construction material Substances 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 208000019014 inability to feed Diseases 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 238000009372 pisciculture Methods 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 230000009466 transformation Effects 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
- 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
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Abstract
本实用新型公开了一种环流布料沼气池,旨在提供一种结构简单、产气效果较好的沼气池。它包括进水活动盖系统、沼气池主体和出水水压间系统。进水活动盖系统包括进水口天窗和中央进水管,进水不设专门的进水口而采用天窗进水,进水后使用中央进水管,并直接进入沼气池底端中央。沼气池主体是一个圆球形的闭合罐体,包括沼气池上半球体,沼气池圆柱体。沼气池底部采用凸型的结构,并在上面布置一个蜗壳形导流墙,在导流墙300mm以上每隔120mm处设置一个破壳齿,目的在于造成环流布料功能,增加布水流长度和自动解除表层结壳。本实用新型克服了现有的沼气池需要单独的进水口,而且会出现产气时进料困难的问题。
The utility model discloses a circulation cloth biogas pond, aiming at providing a biogas pond with simple structure and good gas production effect. It includes the water inlet movable cover system, the biogas tank main body and the water outlet water pressure room system. The water inlet movable cover system includes the water inlet skylight and the central water inlet pipe. There is no special water inlet for water inlet, but the skylight is used for water inlet. The main body of the digester is a spherical closed tank, including the upper hemisphere of the digester and the cylinder of the digester. The bottom of the biogas digester adopts a convex structure, and a volute-shaped diversion wall is arranged on it, and a shell-breaking tooth is set at every 120mm above the diversion wall 300mm, the purpose is to create a circular distribution function, increase the length of the distribution water flow and automatically Removes crusts. The utility model overcomes the problem that the existing methane pool requires a separate water inlet and that it is difficult to feed materials during gas production.
Description
技术领域 technical field
本发明涉及一种有机废水厌氧发酵制备沼气的装置,特别是一种环流布料沼气池。The invention relates to a device for preparing biogas by anaerobic fermentation of organic waste water, in particular to a circulation distribution biogas pond.
背景技术 Background technique
我国农村中,以户用型沼气池为中心的生态农业正在方兴未艾的开展,沼气池一方面能够处理有机废弃物产生生物能源,另一方面能够发酵畜牧业产生的粪便为有机肥料,同时能够将影响农村环境中的污染物统统纳入沼气池中厌氧降解和转化,具有美化生态环境的作用,因而沼气已经成为新农村建设的关键技术,势必在我国农村发展中发挥越来越大的作用。结合我国农户的特征,一般使用的户用型沼气池有6m3、8m3和10m3三种形式。1984年中国标准出版社出版了国家标准局发布的GB/T4750-1984《农村家用水压式沼气池标准图集》提出了农村沼气池的结构,形状为圆形或球形,设有进料口、出料口、发酵间、气箱、活动盖、导气管、出料间兼用水压箱,因此称之为水压式沼气池。2002年中国标准出版社出版了国家质量监督检验检疫局发布的GB/T4750-2002《户用沼气池标准图集》中提出“曲流布料沼气池”,其特点是池底由进料口向出料口倾斜,在池底面设置了布料板,使发酵原料呈曲线流动,增加了扩散面,延长了发酵原料的运转。2007年科学技术文献出版社出版的西北农林科技大学邱凌在《庭院沼气高效生产与利用》书中叙述了“旋流布料沼气池”,其特点是,在底池上建设一个曲率半径为5D/8的圆弧型导流板将进出料隔断,使入池原料在导流板的导流作用下,必须沿导流板旋动才能到达循环管和抽渣管的下部,从而延长了入池发酵原料的流动路程和滞留时间,并且西北农林科技大学邱凌也提出了中国专利ZL97243731.2“旋流布料自动循环沼气池”,对旋流布料沼气池进行了技术描述。In rural areas of our country, ecological agriculture centered on household biogas digesters is in the ascendant. On the one hand, biogas digesters can process organic waste to generate bioenergy, and on the other hand, they can ferment manure produced by animal husbandry into organic fertilizers. Pollutants that affect the rural environment are all included in the biogas digester for anaerobic degradation and transformation, which has the effect of beautifying the ecological environment. Therefore, biogas has become a key technology in the construction of new countryside and is bound to play an increasingly important role in the development of rural areas in our country. Combined with the characteristics of farmers in our country, there are three types of household biogas digesters generally used: 6m 3 , 8m 3 and 10m 3 . In 1984, China Standard Publishing House published GB/T4750-1984 "Standard Atlas of Rural Household Hydraulic Biogas Digesters" issued by the National Bureau of Standards, which proposed the structure of rural biogas digesters, which are round or spherical in shape and equipped with feed inlets. , discharge port, fermentation room, air box, movable cover, air duct, discharge room and hydraulic tank, so it is called a hydraulic biogas digester. In 2002, China Standard Press published the GB/T4750-2002 "Standard Atlas of Household Biogas Digesters" issued by the National Bureau of Quality Supervision, Inspection and Quarantine. The discharge port is inclined, and a distributing plate is set on the bottom of the tank to make the fermentation raw materials flow in a curve, increase the diffusion surface, and prolong the operation of the fermentation raw materials. In 2007, Qiu Ling of Northwest Agriculture and Forestry University, published by Science and Technology Literature Publishing House, described the "swirling flow biogas digester" in the book "Efficient Production and Utilization of Garden Biogas", which is characterized in that a curvature radius of 5D/ The arc-shaped deflector of 8 separates the material in and out, so that the raw material entering the pool must swirl along the deflector under the flow guide of the deflector to reach the lower part of the circulation pipe and slag extraction pipe, thus extending the time of entering the pool. The flow path and residence time of fermentation raw materials, and Qiu Ling of Northwest Agriculture and Forestry University also proposed the Chinese patent ZL97243731.2 "Swirling flow cloth automatic circulation biogas digester", which gave a technical description of the swirl flow cloth biogas digester.
目前我国农村主流上推广使用这几种沼气池,但是在建造过程中有如下缺点:1.需要设置一个进料口、一个出水口兼水压间、一个活动盖,一共三个开口,三个开口的建设需要设计和施工,所需要的费用大约需要总体造价的1/3,如果减少开口的数量,可能会减少造价和节省材料;2.活动盖建设不好,会发生漏气,如果漏气,容易引起火灾、或对人体健康造成危害;3.由于进料口建筑面积小和坡度小,容易造成进料漂浮、进料很难入池、进料被阻挡现象;4.由于进料口起水压间作用,会随沼气池内的气压大小而起伏,这样对进料造成不方便,如果沼气池内气压很大,会造成不能进料;5.由于沼气池下半球是凹型结构,沼渣不易外排。At present, these types of biogas digesters are popularized and used in the mainstream of rural areas in China, but they have the following disadvantages in the construction process: 1. It is necessary to set up a feed inlet, a water outlet and a water pressure room, and a movable cover, a total of three openings, three The construction of the opening requires design and construction, and the required cost is about 1/3 of the overall cost. If the number of openings is reduced, it may reduce the cost and save materials; 2. The construction of the movable cover is not good, and air leakage will occur. 3. Due to the small construction area and small slope of the feed inlet, it is easy to cause the feed to float, the feed is difficult to enter the pool, and the feed is blocked; 4. Due to the feed The mouth acts as a water pressure space, which will fluctuate with the air pressure in the biogas tank, which is inconvenient for feeding materials. If the gas pressure in the biogas tank is too high, it will cause inability to feed materials; 5. Since the lower hemisphere of the biogas tank is a concave structure, the biogas residue Not easy to discharge.
发明内容 Contents of the invention
本实用新型的目的在于提供一种使用和建设简单,形状为圆球型,沼气发酵效率较高的环流布料沼气池。The purpose of the utility model is to provide a circulating material biogas digester with simple use and construction, spherical shape and high biogas fermentation efficiency.
本实用新型的目的是通过提供一种具有如下结构的沼气池而实现的。The purpose of the utility model is achieved by providing a biogas tank with the following structure.
本实用新型的环流布料沼气池包括以下部分组成:The circulation distribution biogas pool of the utility model includes the following components:
进水活动盖系统、沼气池主体和出水系统组成。It consists of water inlet movable cover system, biogas tank main body and water outlet system.
进水活动盖系统包括进水口(天窗)和中央进水管;进水口,是处理水的入口,起收集和汇集处理水的作用,本实用新型取消了传统沼气池的进水口和进水管,采用天窗进水,进水后使用中央进水管;进水管,是联结天窗的水泥管,是处理水进入沼气池的管道,中央进水管直接进入沼气池底端中央,进水管内径300mm,底端开口200×200mm,这样的开口与蜗壳型布料墙联结,并形成环流布料。The water inlet movable cover system includes a water inlet (skylight) and a central water inlet pipe; the water inlet is the inlet of treated water, which plays the role of collecting and consolidating treated water. The skylight enters the water, and the central water inlet pipe is used after water intake; the water inlet pipe is the cement pipe connected to the skylight, and is the pipe for the treated water to enter the biogas digester. The central water inlet pipe directly enters the bottom center of the biogas digester. The inner diameter of the water inlet pipe is 300mm, and the bottom end is open 200×200mm, such an opening is connected with the volute-shaped fabric wall and forms a circulating fabric.
沼气池主体是一个圆球形的闭合罐体,分为两个部分,一是沼气池上半球,一是沼气池圆柱体。这两个部分与传统的水压式沼气池的结构是一致的,但是本实用新型的特点是沼气池底部不采用下凹的半球形,而是采用略有凸型的结构。这个凸型的结构上面布置一个蜗壳形的导流墙,目的在于造成环流布料功能,增加布水流长度。导流墙之间的距离不是固定的,是典型的蜗壳形结构,需要按照图4进行布置。导流墙的设置要使通过进水管的原料在沼气池沿着导流墙旋转流动一周,之后再分别从导流墙的出口处沿着沼气池内壁向前或向后自由流动半圈到沼气池的出水口。蜗壳形导流墙可以顺时针设置,也可以逆时针设置,本实用新型推荐顺时针设置。假设把沼气池按圆点分为四个数学象限,在图形的下半部即第三、四象限中有两条蜗壳形导流墙,而在图形的上半部即第一、二象限中只有一条导流墙,这个单条导流墙从2/5半径处开始到3/5半径处结束。而出现两条导流墙的象限,是从进水管开口处开始,经过半径的1/5处,至半径的2/5处与单条导流墙相接,最后一段导流墙是在半径4/5处结束,在半径的3/5处与单条导流墙相接。导流墙是蜗壳形结构,从而保证了环流布料。进水管的进水开口是与出水口相对位置的,而蜗壳形导流墙是在相对出水口最远端结束的。导流墙的高度要高于沼气池池身,但是不超过沼气池气室拱高的1/3。The main body of the biogas digester is a spherical closed tank, which is divided into two parts, one is the upper hemisphere of the biogas digester, and the other is the cylinder of the biogas digester. These two parts are consistent with the structure of the traditional hydraulic biogas tank, but the utility model is characterized in that the bottom of the biogas tank does not adopt a concave hemispherical shape, but a slightly convex structure. A volute-shaped diversion wall is arranged on the convex structure, the purpose of which is to create a circular distribution function and increase the length of the distribution flow. The distance between the diversion walls is not fixed, it is a typical volute structure, and it needs to be arranged according to Figure 4. The diversion wall is set so that the raw material passing through the water inlet pipe rotates and flows for a circle along the diversion wall in the biogas tank, and then flows freely forward or backward for half a circle from the outlet of the diversion wall along the inner wall of the biogas tank to the biogas. The outlet of the pool. The volute-shaped diversion wall can be set clockwise or counterclockwise, and the utility model recommends clockwise setting. Assuming that the biogas digester is divided into four mathematical quadrants by dots, there are two volute-shaped diversion walls in the third and fourth quadrants in the lower half of the graph, and the first and second quadrants in the upper half of the graph. There is only one diversion wall in , and this single diversion wall starts at 2/5 radius and ends at 3/5 radius. The quadrant where two diversion walls appear starts from the opening of the water inlet pipe, passes through 1/5 of the radius, and connects to a single diversion wall at 2/5 of the radius. The last diversion wall is at a radius of 4 It ends at /5 and meets a single diversion wall at 3/5 of the radius. The diversion wall is a volute structure, thus ensuring the circulation of the cloth. The water inlet opening of the water inlet pipe is positioned opposite to the water outlet, and the volute-shaped diversion wall ends at the farthest end relative to the water outlet. The height of the diversion wall should be higher than the body of the biogas digester, but not more than 1/3 of the arch height of the biogas chamber.
在沼气池出口前面0.5米处设置一个稳流墙,以保证有更长时间和有效的厌氧污泥能够停留在沼气池内。沼气池上盖为传统的水压式沼气池天窗兼做进料口,其密封方法与传统沼气池一样。在天窗旁边离进料管一定距离内,插设一个金属沼气管,这个金属管构成了沼气的起始接头。沼气池底板总体为一个凸形结构,为两层混凝土结构,并向出水口处的坡度为5%,以保证污泥向出口流动。Set up a steady flow wall 0.5 meters in front of the biogas digester outlet to ensure longer and effective anaerobic sludge can stay in the biogas digester. The upper cover of the biogas digester is a traditional water-pressure biogas digester skylight which doubles as a feed inlet, and its sealing method is the same as that of a traditional biogas digester. Next to the skylight at a certain distance from the feed pipe, a metal biogas pipe is inserted, which constitutes the starting connection for the biogas. The bottom plate of the biogas digester is generally a convex structure, which is a two-layer concrete structure, and the slope to the water outlet is 5% to ensure that the sludge flows to the outlet.
出水系统包括:出水口、出水间和水压间;出水口是在圆形沼气池的末端设置的一个长方形水口,是处理水的出口,在圆形沼气池的下方,设置形状为长方形,出口宽为1米,高根据沼气池设计的压力而定,一般而言,出水口的顶端距离沼气池顶盖有至少1米以上的距离,这样保证了沼气气压的稳定。出水间是建设在出水口之外,长宽各为1米的一个圆柱体或长方体管道,高度要高于出水口;水压间是出水间之外的供产气水压调节之用的,大小为本平流布料沼气池气室的1/3,一般设置为圆形或长方形,直径为沼气池半径的大小左右,深度为1米左右。The water outlet system includes: a water outlet, a water outlet room and a water pressure room; the water outlet is a rectangular water outlet set at the end of the circular biogas digester, which is the outlet of the treated water. The width is 1 meter, and the height depends on the design pressure of the biogas digester. Generally speaking, the top of the water outlet is at least 1 meter away from the top of the biogas digester, which ensures the stability of the biogas pressure. The water outlet room is built outside the water outlet, a cylindrical or cuboid pipe with a length and width of 1 meter, and the height is higher than the water outlet; the water pressure room is used for the adjustment of the gas production pressure outside the water outlet room. The size is 1/3 of the gas chamber of the advective distribution biogas digester, which is generally set as a circle or a rectangle, the diameter is about the size of the radius of the biogas digester, and the depth is about 1 meter.
本实用新型的优点是:The utility model has the advantages of:
1.结构简单,可降低建设成本;2.取消传统沼气池的进料口,用天窗做进料口,这样减少漏气;3.由于取消了进料口,解决了进料口当气压高的时候,不能进料的问题,减少了进料漂浮问题,解决了进料水压阻碍问题;4.取消了传统沼气池圆柱体下半部的半球形结构,采用凸形结构,从而解决了沼渣滞留问题。1. The structure is simple, which can reduce the construction cost; 2. The feed port of the traditional biogas digester is canceled, and the skylight is used as the feed port, which reduces air leakage; 3. Since the feed port is canceled, the problem of high air pressure at the feed port 4. The hemispherical structure of the lower half of the cylinder of the traditional biogas digester is canceled and a convex structure is adopted, thus solving the problem of feed water pressure obstruction; Biogas residue retention problem.
附图说明 Description of drawings
图1为本实用新型沼气池实施的总体结构图(见图1);Fig. 1 is the overall structural diagram (seeing Fig. 1) that the utility model biogas digester implements;
图2为本实用新型沼气池的俯视图(图2);Fig. 2 is the top view (Fig. 2) of the utility model biogas digester;
图3为本实用新型沼气池的侧视图(图3);Fig. 3 is a side view (Fig. 3) of the utility model biogas digester;
图4为本实用新型沼气池的蜗壳形导流墙结构剖面图(图4);Fig. 4 is the volute shape diversion wall structure sectional view (Fig. 4) of the biogas digester of the present utility model;
图5为进水天窗结构与内部结构布置图(图5)。Fig. 5 is a water inlet skylight structure and internal structure layout (Fig. 5).
具体实施方式 Detailed ways
下面结合附图对本实用新型作进一步说明。Below in conjunction with accompanying drawing, the utility model is further described.
本实用新型属于能源生态型沼气利用模式,处理后的沼液和沼渣可以用于肥料或者养鱼。建设材料根据沼气池大小不同,采用不同的混凝土结构。The utility model belongs to an energy ecological biogas utilization mode, and the treated biogas slurry and biogas residue can be used for fertilizer or fish farming. The construction material adopts different concrete structures according to the size of the digester.
本实用新型沼气池容积计算方法,总体形状为圆柱削球型,设沼气池容积为V(立方米),ρ为曲率半径(米),f矢高(米),H为池墙高(米),D为池内直径(米),R为池内半径(米)。The utility model biogas tank volume calculation method, the overall shape is a cylindrical cut ball type, assuming that the volume of the biogas tank is V (cubic meters), ρ is the radius of curvature (meters), f is the height of the vector (meters), and H is the height of the pool wall (meters). , D is the inner diameter of the pool (meters), and R is the inner radius of the pool (meters).
那么,沼气池主池圆柱体V1=πR2H,Then, the cylinder of the main tank of the biogas digester V1=πR 2 H,
池盖的曲率半径为ρ=(4f2+D2)/8f,则削球池盖V2=πf2(3ρ-f)/3池底凸型体积忽略不计,那么,沼气池总体积为V=V1+V2The radius of curvature of the pool cover is ρ=(4f 2 +D 2 )/8f, then the ball-cutting pool cover V2=πf 2 (3ρ-f)/3 The convex volume of the bottom of the pool is ignored, then the total volume of the biogas tank is V =V1+V2
表1环流布料沼气池几何尺寸(米)Table 1 Geometric Dimensions of Circulation Distribution Biogas Digester (m)
本实用新型沼气池主要为户用型,体积不易太大。应用对象为农户、小型养殖场、小型食品加工厂等有机污水排放处理产生沼气使用。The biogas pool of the utility model is mainly a household type, and the volume is not easy to be too large. The application object is for the use of biogas produced by the organic sewage discharge treatment of farmers, small farms, and small food processing plants.
进水口与活动盖天窗是共用的,本实用新型不设单独的进水口,进水天窗是内径为1米的圆形或者边长为1米的长方形,其设计和建造方式与传统的水压式沼气池一致(图5)。天窗中央设置一个中央进水管,中央进水管是一个内径为300mm的水泥管道,水泥管道最底端侧面开口大小为200×200mm,开口处正对沼气池的出水口,中央水泥管放置到沼气池中心,形成了一体化的天窗/进水装置。可见,本实用新型取消了传统沼气池的进水口和进水管,采用天窗进水,进水后使用中央进水管。进水管,是联结天窗的水泥管,是处理水进入沼气池的管道,中央进水管直接进入沼气池底端中央,进水管内径300mm,底端开口200×200mm,这样的开口与蜗壳型环流布料墙联结,并形成环流布料。The water inlet and the movable cover skylight are shared. The utility model does not have a separate water inlet. The water inlet skylight is a circle with an inner diameter of 1 meter or a rectangle with a side length of 1 meter. Its design and construction method are different from traditional water pressure. Type biogas digester consistent (Figure 5). A central water inlet pipe is set in the center of the skylight. The central water inlet pipe is a cement pipe with an inner diameter of 300mm. The bottom side opening of the cement pipe is 200×200mm in size. The opening is facing the water outlet of the biogas digester. The central cement pipe is placed in the biogas digester In the center, an integrated skylight/water inlet device is formed. It can be seen that the utility model cancels the water inlet and the water inlet pipe of the traditional biogas digester, adopts the skylight for water inlet, and uses the central water inlet pipe after the water inlet. The water inlet pipe is the cement pipe connected to the skylight. It is the pipe through which the treated water enters the biogas digester. The central water inlet pipe directly enters the bottom center of the biogas digester. The inner diameter of the water inlet pipe is 300mm, and the bottom opening is 200×200mm. The fabric walls join and create a circulating fabric.
关于沼气金属管位置的问题,在沼气池上盖部位设置一个沼气管,是一个插设在天窗或者沼气池气室上部的一个金属沼气管,这个金属管构成了沼气的起始接头。Regarding the location of the biogas metal pipe, a biogas pipe is installed on the upper cover of the biogas tank, which is a metal biogas pipe inserted in the skylight or the upper part of the biogas chamber. This metal pipe constitutes the starting joint of the biogas.
环流布料墙是建筑在主沼气池凸形池体上的导流墙,如图4所示。这个凸型的结构上面布置的导流墙是蜗壳形结构,其目的在于造成环流布料功能,增加布水流的长度。导流墙之间的距离不是固定的,是由进水管开口开始,沿着顺时针或逆时针方向旋转的蜗壳形结构墙,导流墙由进水管开口处的外侧开始,由沼气池的中央部位向沼气池外围扩张,并逐渐增加曲率半径。导流墙的设置要使通过进水管的原料在沼气池沿着导流墙旋转流动一周,之后再分别从导流墙的出口处沿着沼气池内壁向前或向后自由流动半圈到沼气池的出水口。蜗壳形导流墙可以顺时针设置,也可以逆时针设置,本实用新型推荐顺时针设置。假设把沼气池按圆点分为四个数学象限,如图4所示,在图形的下半部即第三、四象限中有两条蜗壳形导流墙,而在图形的上半部即第一、二象限中只有一条导流墙,这个单条导流墙从2/5半径处开始到3/5半径处结束。而出现两条导流墙的象限,是从进水管开口处开始,经过半径的1/5处,至半径的2/5处与单条导流墙相接,最后一段导流墙是在半径4/5处结束,在半径的3/5处与单条导流墙相接。导流墙是蜗壳形结构,从而保证了环流布料。进水管的出水口是与沼气池的出水口位置相对的,而蜗壳形导流墙是在相对于沼气池出水口最远端结束的,也就是说蜗壳形导流墙的末端是在沼气池出水口的相反一侧。本实用新型使用原料流动一圈的蜗壳形导流墙,太短显得作用不大和太长显得没有必要。所以导流墙长度可根据情况确定,如果水质可溶性好导流墙长度可长些,如果处理粪便等SS含量高的粪污,导流墙长度益短,以免造成堵塞和沉淀。蜗壳形导流墙的建设高度要高于沼气池池身,但是不超过沼气池气室拱高的1/3,可参考表1数据。The circulation distribution wall is a diversion wall built on the convex body of the main biogas digester, as shown in Figure 4. The diversion wall arranged on the convex structure is a volute structure, and its purpose is to create a circular distribution function and increase the length of the distribution flow. The distance between the diversion walls is not fixed. It starts from the opening of the water inlet pipe and rotates clockwise or counterclockwise. The central part expands toward the periphery of the digester, and gradually increases the radius of curvature. The diversion wall is set so that the raw material passing through the water inlet pipe rotates and flows for a circle along the diversion wall in the biogas tank, and then flows freely forward or backward for half a circle from the outlet of the diversion wall along the inner wall of the biogas tank to the biogas. The outlet of the pool. The volute-shaped diversion wall can be set clockwise or counterclockwise, and the utility model recommends clockwise setting. Assuming that the biogas digester is divided into four mathematical quadrants by dots, as shown in Figure 4, there are two volute-shaped diversion walls in the lower half of the graph, namely the third and fourth quadrants, and in the upper half of the graph That is, there is only one diversion wall in the first and second quadrants, and this single diversion wall starts from the 2/5 radius and ends at the 3/5 radius. The quadrant where two diversion walls appear starts from the opening of the water inlet pipe, passes through 1/5 of the radius, and connects to a single diversion wall at 2/5 of the radius. The last diversion wall is at a radius of 4 It ends at /5 and meets a single diversion wall at 3/5 of the radius. The diversion wall is a volute structure, thus ensuring the circulation of the cloth. The water outlet of the water inlet pipe is opposite to the water outlet of the biogas tank, and the volute-shaped diversion wall ends at the farthest end relative to the water outlet of the biogas tank, that is to say, the end of the volute-shaped diversion wall is at the The opposite side of the digester outlet. The utility model uses a volute-shaped diversion wall in which the raw material flows in one circle, and if it is too short, it has little effect and if it is too long, it is unnecessary. Therefore, the length of the diversion wall can be determined according to the situation. If the water quality is good in solubility, the length of the diversion wall can be longer. If the feces and other manure with high SS content are treated, the length of the diversion wall should be shortened to avoid blockage and sedimentation. The construction height of the volute-shaped diversion wall should be higher than the body of the biogas digester, but not more than 1/3 of the arch height of the gas chamber of the biogas digester. Please refer to the data in Table 1.
蜗壳形导流墙上面设置有破壳齿(图4),破壳齿的结构是这样的,蜗壳形导流墙是砖混结构,砖为标准砖。主体墙宽120mm,在凸型沼气池底面上构筑而成,蜗壳形导流墙下面墙高300mm内没有破壳齿,即从凸形表面上平砌5层顺砖,而后每隔120mm高和120mm长处横砌一块侧立砖,由于砖长240mm,所以侧立砖分别伸出蜗壳形导流墙两面各60mm,从而形成破壳齿。破壳齿交叉排列,交错排列。只有蜗壳形导流墙下面300mm内不需要破壳齿,而从蜗壳形导流墙下面300mm以上,一直交叉排列破壳齿。由于蜗壳形导流墙两面均有破壳齿,从而使沼气池结壳自动破除。The volute-shaped diversion wall is provided with shell-breaking teeth (Fig. 4), and the structure of the shell-breaking teeth is such that the volute-shaped diversion wall is a brick-concrete structure, and the bricks are standard bricks. The main wall is 120mm wide and built on the bottom of the convex biogas tank. There are no cracking teeth within the wall height of 300mm under the volute-shaped diversion wall. Build a side vertical brick horizontally with the length of 120mm. Since the brick is 240mm long, the side vertical bricks protrude from both sides of the volute-shaped diversion wall by 60mm respectively, thereby forming shell-breaking teeth. Broken shell teeth are arranged in a cross, staggered arrangement. Only within 300mm below the volute-shaped diversion wall, the shell-breaking teeth are not needed, and the shell-breaking teeth are arranged crosswise from more than 300mm below the volute-shaped diversion wall. Because there are shell-breaking teeth on both sides of the volute-shaped diversion wall, the crust of the biogas digester is automatically broken.
沼气池主体是一个圆柱体和一个半球体组合的封闭水泥池,是不漏气的罐体结构,沼气池圆柱体和上半球的数据结构见表1,与传统的水压式沼气池一致,只是进水口与天窗组合在一起。沼气池的池底取消了传统沼气池的凹型结构,因为这样不利于沼渣的排放。本实用新型沼气池池底采用凸形结构,这样一方面有利于原料从进水口向边缘的环流运动,另一方面免除了沼渣在沼气池池底不能外排的问题。本实用新型沼气池凸形底部的矢高为200-300mm(见表1),从而使环流顺畅进行。本实用新型沼气池池底的建设还有另外一个特点就是,沼气池池底有一个5%的坡度,这个坡度走向沼气池出水口,从而保证了沼液和沼渣向外流动的畅通。通过以上的环流装置和5%的坡度走向,使解决了沼渣外排问题(附图1)。在沼气池出口前面0.5米处设置一个稳流墙,以保证有更长时间和有效的厌氧污泥能够停留在沼气池内。稳流墙高度为0.5米,长度为沼气池宽度的1/3-出水口宽度的2倍。The main body of the biogas digester is a closed cement pond composed of a cylinder and a hemisphere. It is an airtight tank structure. The data structure of the cylinder and the upper hemisphere of the biogas digester is shown in Table 1, which is consistent with the traditional hydraulic biogas digester. It's just the water inlet combined with the sunroof. The bottom of the biogas digester cancels the concave structure of the traditional biogas digester, because it is not conducive to the discharge of biogas residues. The bottom of the biogas pond of the utility model adopts a convex structure, which on the one hand facilitates the circulation of raw materials from the water inlet to the edge, and on the other hand avoids the problem that the biogas residue cannot be discharged outside at the bottom of the biogas pond. The sagittal height of the convex bottom of the biogas pool of the utility model is 200-300mm (see Table 1), so that the circulation can be carried out smoothly. Another feature of the construction of the biogas tank bottom of the utility model is that there is a 5% slope at the bottom of the biogas tank, and this slope goes to the water outlet of the biogas tank, thereby ensuring the smooth flow of the biogas slurry and biogas residue. Through the above circulation device and 5% gradient direction, the problem of biogas slag discharge is solved (accompanying drawing 1). Set up a steady flow wall 0.5 meters in front of the biogas digester outlet to ensure longer and effective anaerobic sludge can stay in the biogas digester. The height of the steady flow wall is 0.5 meters, and the length is 1/3 of the width of the biogas digester-2 times of the width of the water outlet.
出水口是在沼气池的末端设置的一个长方形水口,位于沼气池后壁中央,是处理水的出口,在沼气池后壁末端的中央下方,是一个长方形出口,出口宽为1米,高根据沼气池设计的压力而定,一般而言,出水口的顶端距离沼气池顶盖有至少1米以上的距离,这构成了本实用新型的环流布料沼气池的气室,并保证沼气气压的稳定。出水间是建设在出水口之外,半径为1米或长宽各为1米的一个长方体管道,高度要高于出水口;水压间是出水间之外的供产气水压调节之用的,大小为本平流布料沼气池气室的1/3,一般设置为直径为沼气池半径的圆形或者长宽为沼气池半径的方形,深度为1米左右。水压间上盖需要使用防护装置,以免有人为危险,一般的防护装置为一个中间有1米方孔的水泥盖板,方孔是排放沼渣和沼液的。沼渣和沼液可以用做肥料使用。The water outlet is a rectangular water outlet set at the end of the biogas digester. It is located in the center of the rear wall of the biogas digester and is the outlet of the treated water. Below the center of the end of the rear wall of the biogas digester is a rectangular outlet with a width of 1 meter and a height according to The design pressure of the biogas digester depends on the design pressure. Generally speaking, the top of the water outlet is at least 1 meter away from the top cover of the biogas digester, which constitutes the gas chamber of the circulation cloth biogas digester of the present utility model and ensures the stability of the biogas pressure. . The water outlet room is a rectangular parallelepiped pipe with a radius of 1 meter or a length and width of 1 meter outside the water outlet, and the height is higher than the water outlet; the water pressure room is used for gas production and water pressure adjustment outside the water outlet room The size is 1/3 of the gas chamber of the advective distribution biogas digester. It is generally set as a circle with a diameter equal to the radius of the biogas digester or a square with a length and width equal to the radius of the biogas digester, and a depth of about 1 meter. The upper cover of the water pressure room needs to use a protective device to avoid human hazards. The general protective device is a cement cover with a 1-meter square hole in the middle. The square hole is used to discharge biogas residue and biogas slurry. Biogas residue and biogas slurry can be used as fertilizer.
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| CN103820308A (en) * | 2013-11-29 | 2014-05-28 | 廖佳袁 | Novel methane generation device |
| CN105036327A (en) * | 2015-09-23 | 2015-11-11 | 农业部沼气科学研究所 | Household domestic sewage purification device |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN103820308A (en) * | 2013-11-29 | 2014-05-28 | 廖佳袁 | Novel methane generation device |
| CN105036327A (en) * | 2015-09-23 | 2015-11-11 | 农业部沼气科学研究所 | Household domestic sewage purification device |
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