CN2535407Y - Automatic circulating methane tank - Google Patents
Automatic circulating methane tank Download PDFInfo
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- CN2535407Y CN2535407Y CN02219867U CN02219867U CN2535407Y CN 2535407 Y CN2535407 Y CN 2535407Y CN 02219867 U CN02219867 U CN 02219867U CN 02219867 U CN02219867 U CN 02219867U CN 2535407 Y CN2535407 Y CN 2535407Y
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- room
- water pressure
- biogas
- communication hole
- control tank
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- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 title description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 36
- 239000007788 liquid Substances 0.000 claims abstract description 23
- 238000000855 fermentation Methods 0.000 claims abstract description 16
- 230000004151 fermentation Effects 0.000 claims abstract description 15
- 238000007667 floating Methods 0.000 claims abstract description 15
- 238000004891 communication Methods 0.000 claims abstract description 12
- 239000000463 material Substances 0.000 claims abstract description 8
- 238000003860 storage Methods 0.000 claims abstract description 8
- 230000003993 interaction Effects 0.000 abstract 2
- 239000002002 slurry Substances 0.000 description 10
- 238000004519 manufacturing process Methods 0.000 description 6
- 239000002994 raw material Substances 0.000 description 5
- 230000007547 defect Effects 0.000 description 3
- 230000007613 environmental effect Effects 0.000 description 3
- 210000003608 fece Anatomy 0.000 description 3
- 230000000630 rising effect Effects 0.000 description 3
- 239000010865 sewage Substances 0.000 description 3
- 241001465754 Metazoa Species 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 239000010871 livestock manure Substances 0.000 description 2
- 238000005192 partition Methods 0.000 description 2
- 239000013589 supplement Substances 0.000 description 2
- 244000025254 Cannabis sativa Species 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000029087 digestion Effects 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
- 238000011010 flushing procedure Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000010815 organic waste Substances 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 239000002984 plastic foam Substances 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 239000010902 straw Substances 0.000 description 1
- 230000001360 synchronised effect Effects 0.000 description 1
- 241001148471 unidentified anaerobic bacterium Species 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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- Apparatus Associated With Microorganisms And Enzymes (AREA)
Abstract
本实用新型涉及发生沼气装置结构改进技术领域,公开了一种自动循环沼气池。它主要由发酵间、储气间、进料口、出料口、水压间、活动盖、导气管、控制池所构成。通过出料口与水压间的上部溢流口、水压间与控制池下部连通孔,在控制池内连接连通孔的浮动升降软管和控制池与进水口下部连通孔的相互作用,使沼液由发酵间进入出料口,流入水压间,进入控制池,流入进料口,流回发酵间而自动循环。其特点是简便、可靠、造价低、效率高、运行畅通、劳动强度小,适用各种沼气池或厌氧装置中。
The utility model relates to the technical field of improving the structure of a biogas generating device, and discloses an automatic circulation biogas pit. It is mainly composed of a fermentation room, a gas storage room, a material inlet, a material outlet, a water pressure room, a movable cover, an air duct, and a control pool. Through the interaction between the upper overflow port between the discharge port and the water pressure, the communication hole between the water pressure room and the lower part of the control tank, the floating lifting hose connecting the communication hole in the control tank, and the interaction between the control tank and the lower communication hole of the water inlet, the biogas The liquid enters the discharge port from the fermentation room, flows into the water pressure room, enters the control tank, flows into the feed port, and flows back to the fermentation room for automatic circulation. It is characterized by simplicity, reliability, low cost, high efficiency, smooth operation, and low labor intensity, and is suitable for various biogas digesters or anaerobic devices.
Description
技术领域Technical field
本实用新型属生物化学酶学类,涉及发生沼气装置结构改进技术领域。The utility model belongs to the category of biochemical enzymology and relates to the technical field of structural improvement of biogas generating devices.
技术背景 technical background
在资源、人口、环境面临着越来越大压力的当今社会,沼气池、厌氧池的大力发展,除了生产清洁能源沼气外,对环境保护、生态建设有着现实的重要意义,是当今社会关注的热点技术和产业。但现今大量运行的沼气池,厌氧池存在着各式各样的缺陷,如传统水压式沼气池,见图1,池容大,产气少,上浮层,下沉渣,进料易堵,出料更难;以及劳动强度大,管理麻烦等等。无论在农村处理人畜粪便、污水、作物秸杆,以生产沼气能源为主,保护环境为辅的农村户用沼气池,在城镇以环境保护、处理污染为主,生产沼气为辅的城镇沼气池,包括其他各种厌氧消化装置,能够减轻或消除以上各种缺陷,高效运行,自动循环这种技术难点和重点都非常关注。因为自动循环依靠自身的动力,始终不断地使出料口的沼液定向流入进料口,稀释进料发酵原料,使之易于进入池内发酵,使原料分布合理,增加与厌氧菌群的接触,提高产气率,增加产气量,省去了人工操作,不需设备投入和电力支出,大大提高经济效益。In today's society where resources, population, and the environment are facing increasing pressure, the vigorous development of biogas digesters and anaerobic digesters, in addition to producing clean energy biogas, has practical significance for environmental protection and ecological construction, and is the focus of today's society. hot technologies and industries. However, a large number of biogas digesters and anaerobic digesters currently in operation have various defects. For example, the traditional hydraulic biogas digester, as shown in Figure 1, has a large tank capacity, low gas production, floating layer, sinking slag, and easy blockage of feed. , It is more difficult to discharge the material; and the labor intensity is high, the management is troublesome, and so on. Regardless of the treatment of human and livestock manure, sewage, and crop straw in rural areas, rural household biogas digesters mainly produce biogas energy and supplement environmental protection, and urban biogas digesters mainly focus on environmental protection and pollution treatment and supplement biogas production in cities and towns , including other various anaerobic digestion devices, can alleviate or eliminate the above-mentioned various defects, operate efficiently, and the technical difficulties and key points of automatic circulation are very concerned. Because the automatic cycle relies on its own power, it always makes the biogas slurry at the discharge port flow into the feed port in a directional way, dilutes the feed fermentation raw materials, makes it easy to enter the tank for fermentation, makes the distribution of raw materials reasonable, and increases the contact with anaerobic bacteria. , improve gas production rate, increase gas production, save manual operation, no equipment investment and power expenditure, greatly improve economic benefits.
传统水压式沼气池(见图1)的运行方式是:人畜粪便、冲洗污水、作物秸杆、各种有机废水等发酵原料,从进料口(2)进入发酵间(1),发酵间产生的沼气升至储气间(12),料液被挤压,两旁的进料口(2),出料口(3),水压间(4)液面同步上升;当用气时,位差把沼气压出,进料口(2)、出料口(3)、水压间(4)两边料液回流,液面同步下降,如此不断地产气,用气,液面不断地上升、下降,一旦料液过多,就舀出做肥料或溢出流进另备的储粪池。The operation mode of the traditional hydraulic biogas digester (see Figure 1) is: human and animal manure, flushing sewage, crop stalks, various organic waste water and other fermentation materials enter the fermentation room (1) from the feed inlet (2), and the fermentation room The generated biogas rises to the gas storage room (12), and the feed liquid is squeezed, and the feed inlet (2) on both sides, the feed outlet (3), and the liquid level in the water pressure room (4) rise synchronously; when using gas, Potential difference pushes out the methane gas, and the feed liquid on both sides of the feed port (2), discharge port (3) and water pressure room (4) flows back, and the liquid level drops synchronously. In this way, the gas is produced continuously, and the liquid level continues to rise when the gas is used. , down, once the feed liquid is too much, it is scooped out as fertilizer or overflowed into another dung storage tank.
图1中可看出,由于发酵原料一直都是从进料口(2)进入,因此,进料口(2)料液浓度大,各种人畜粪便,秸杆,污水等都是聚积在靠近进料口(2)一旁,而另半边原料少,这不仅易造成进料堵塞难进,还因原料分布不均,减少产气量。因此,经常需要把出料口(3)水压间(4)的沼液舀到进料口(2),稀释进料口(2)料液浓度,并使之进入发酵间。这种操作既烦琐,又必须经常进行,管理麻烦,劳动强度大,若使用水泵抽取,既增加设备投入,又增加电力支出。As can be seen in Fig. 1, because the fermentation raw material all enters from feed inlet (2) all the time, therefore, feed inlet (2) feed liquid concentration is big, and various human and animal feces, stalk, sewage etc. all are to accumulate near One side of the feed inlet (2) has less raw materials, which not only easily causes the feed to be blocked and difficult to enter, but also reduces the gas production due to the uneven distribution of raw materials. Therefore, it is often necessary to scoop the biogas slurry in the water pressure room (4) of the discharge port (3) to the feed port (2) to dilute the feed liquid concentration of the feed port (2) and make it enter the fermentation room. This kind of operation is both loaded down with trivial details, must be carried out frequently again, and management is troublesome, and labor intensity is big, if use water pump to extract, not only increase equipment investment, but also increase power expenditure.
发明内容Contents of Invention
本实用新型要解决的技术问题是为克服上述传统水压式沼气池所存在的缺陷而提出了一种自动循环沼气池,它解决出料口水压间沼液能经常不断地进入进料口而自动循环起来。The technical problem to be solved by the utility model is to propose an automatic circulation biogas digester in order to overcome the above-mentioned defects in the traditional water pressure biogas digester, which solves the problem that the biogas liquid between the water pressure of the discharge port can often and continuously enter the feed port. Automatically cycle up.
本实用新型自动循环沼气池是由发酵间、储气间、进料口、出料口、水压间、活动盖、导气管、控制池所构成。其特征是发酵间和储气间为一整体大罐。出料口与水压间之间在上部设有溢流口通道,便于沼液能从出料口溢流至水压间。水压间与控制池之间下部设有连通孔,并在控制池内下部连通孔孔口装有浮动升降软管,且浮动升降软管另一端在控制池一侧内可自由升降浮动,由于软管端口浮在水面上,使沼液只能从水压间流入控制池中,而控制池内沼液不能返回水压间。控制池与进料口之间下部设有连通孔,使沼液从控制池流入进料口或进料口流入控制池。The automatic circulation biogas digester of the utility model is composed of a fermentation room, a gas storage room, a material inlet, a material outlet, a water pressure room, a movable cover, an air guide pipe, and a control pool. It is characterized in that the fermentation room and the gas storage room are a whole large tank. An overflow channel is provided on the upper part between the discharge port and the water pressure room, so that biogas slurry can overflow from the discharge port to the water pressure room. There is a communication hole in the lower part between the water pressure room and the control pool, and a floating lifting hose is installed at the opening of the lower communication hole in the control pool, and the other end of the floating lifting hose can be lifted and floated freely in one side of the control pool. The port floats on the water surface, so that the biogas slurry can only flow into the control tank from the hydraulic room, and the biogas slurry in the control tank cannot return to the hydraulic room. There is a communication hole at the lower part between the control pond and the feed inlet, so that the biogas slurry flows from the control pond into the feed inlet or the feed inlet flows into the control pond.
本实用新型优点:简便、可靠、造价低、效率高、运行畅通,不需人工循环沼液、劳动强度小,广泛适用于各种沼气池和各类厌氧装置中。The utility model has the advantages of simplicity, reliability, low cost, high efficiency, smooth operation, no need for artificial circulation of biogas slurry, low labor intensity, and is widely applicable to various biogas tanks and various anaerobic devices.
附图说明Description of drawings
图1为现有技术传统水压式沼气池结构示意图;Fig. 1 is the structural schematic diagram of prior art traditional hydraulic type biogas digester;
图2为本实用新型自动循环沼气池结构示意图;Fig. 2 is the structural schematic diagram of the automatic circulation biogas digester of the utility model;
图3为图2的俯视示意图。FIG. 3 is a schematic top view of FIG. 2 .
在各图中,1-发酵间;2-进料口;3-出料口;4-水压间;5-活动盖;6-导气管;7-控制池;8-浮动升降软管;9-溢流口;10-连通孔;11-连通孔;12-储气间。In each figure, 1-fermentation room; 2-feed inlet; 3-feed outlet; 4-water pressure room; 5-movable cover; 6-air duct; 7-control tank; 8-floating lifting hose; 9-overflow port; 10-communication hole; 11-communication hole; 12-gas storage room.
具体实施方式 Detailed ways
结合图2和图3,叙述自动循环实施过程:当发酵间(1)正常产气,沼气升至储气间(12),把料液挤出进料口(2)与出料口(3),液面同步上升,出料口(3)液面上升到溢流口(9)时,沼液就从溢流口(9)进入水压间(4),而进料口(2)料液同时上升,经连通孔(11),(网格挡住进料口草类),进入控制池(7),上升的液面把浮动升降软管(8)一端浮起,进料口(2)、控制池(7)、水压间(4)与出料口(3)液面虽同步,因控制池(7)中升降软管(8)的浮托作用,上升的液面只能从出料口(3)溢流口(9)流进水压间(4),而不能从进料口(2)流进水压间(4),所以沼气池内的沼液,只能从出料口(3)定向流入水压间(4)。这里关键起作用的就是浮动升降软管(8)一头砌在控制池(7)与水压间(4)隔墙的下部,另一头用浮动的塑料泡沫,塑料球(如乒乓球类)捆绑在一起,在沼气池运行中,液面上升,把浮动升降软管(8)一端浮起,进料口(2)的料液不能进入水压间(4),液面下降时,浮动升降软管(8)下降,水压间(4)的水通过下降的浮动升降软管(8)定向流向进料口(2),因溢流口(9)在高位置上,水压间(4)的水被隔墙挡住,不可能回流到出料口(3),只能作定向流动。形成了沼气池产气,把出料口(3)上升的沼液经溢流口(9)流进水压间(4);用气,液面下降,水压间(4)的水经下降的浮动升降软管(8)经控制池(7)流入进料口(2)。随着产气、用气的不断转换而始终定向流动,把进料口(2)的料液稀释并带进发酵间(1),自动循环,高效运行。Combined with Figure 2 and Figure 3, the implementation process of automatic circulation is described: when the fermentation room (1) produces gas normally, the biogas rises to the gas storage room (12), and the feed liquid is squeezed out of the feed port (2) and the discharge port (3 ), the liquid level rises synchronously, when the liquid level of the discharge port (3) rises to the overflow port (9), the biogas slurry enters the water pressure room (4) from the overflow port (9), and the feed port (2) The feed liquid rises at the same time, passes through the communication hole (11), (the grid blocks the feed inlet grass), enters the control pool (7), and the rising liquid level floats one end of the floating lifting hose (8), and the feed inlet ( 2), although the control tank (7), water pressure room (4) and the liquid level of the discharge port (3) are synchronous, because of the floating effect of the lifting hose (8) in the control tank (7), the rising liquid level only It can flow into the water pressure room (4) from the discharge port (3) overflow port (9), but cannot flow into the water pressure room (4) from the feed port (2), so the biogas slurry in the biogas tank can only Directly flow into the water pressure room (4) from the discharge port (3). Here the key function is that one end of the floating lifting hose (8) is built on the bottom of the partition wall between the control pool (7) and the water pressure (4), and the other end is bound with floating plastic foam and plastic balls (such as table tennis balls). Together, during the operation of the biogas digester, the liquid level rises, and one end of the floating lifting hose (8) is floated, so that the feed liquid at the feed inlet (2) cannot enter the water pressure room (4), and when the liquid level drops, the floating lifting hose (8) The hose (8) descends, and the water in the water pressure room (4) flows directionally to the feed inlet (2) through the descending floating lifting hose (8). Because the overflow port (9) is at a high position, the water pressure room ( 4) The water in the water is blocked by the partition wall, so it is impossible to flow back to the discharge port (3), and it can only flow in a directional manner. A biogas digester is formed to produce gas, and the biogas slurry rising from the discharge port (3) flows into the water pressure room (4) through the overflow port (9); with gas, the liquid level drops, and the water in the water pressure room (4) passes through The descending floating lifting hose (8) flows into the feed inlet (2) through the control pool (7). With the continuous conversion of gas production and gas consumption, the flow is always directional, and the feed liquid at the feed inlet (2) is diluted and brought into the fermentation room (1), which is automatically circulated and operates efficiently.
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