CN201077838Y - Methane tank - Google Patents
Methane tank Download PDFInfo
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- CN201077838Y CN201077838Y CNU2007200634407U CN200720063440U CN201077838Y CN 201077838 Y CN201077838 Y CN 201077838Y CN U2007200634407 U CNU2007200634407 U CN U2007200634407U CN 200720063440 U CN200720063440 U CN 200720063440U CN 201077838 Y CN201077838 Y CN 201077838Y
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- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 title abstract description 6
- 210000003608 fece Anatomy 0.000 claims abstract description 8
- 230000007062 hydrolysis Effects 0.000 claims abstract description 8
- 238000006460 hydrolysis reaction Methods 0.000 claims abstract description 8
- 230000020477 pH reduction Effects 0.000 claims description 43
- 239000010871 livestock manure Substances 0.000 claims description 11
- 241001465754 Metazoa Species 0.000 claims description 7
- 239000011152 fibreglass Substances 0.000 claims description 7
- 238000004519 manufacturing process Methods 0.000 claims description 7
- 239000011148 porous material Substances 0.000 claims 1
- 238000000855 fermentation Methods 0.000 abstract description 49
- 230000004151 fermentation Effects 0.000 abstract description 49
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 9
- 239000000463 material Substances 0.000 abstract description 7
- 239000010902 straw Substances 0.000 abstract description 7
- 244000144972 livestock Species 0.000 abstract description 2
- 229920002430 Fibre-reinforced plastic Polymers 0.000 abstract 1
- 239000003365 glass fiber Substances 0.000 abstract 1
- 239000007788 liquid Substances 0.000 description 24
- 239000002994 raw material Substances 0.000 description 12
- 238000010276 construction Methods 0.000 description 8
- 238000004062 sedimentation Methods 0.000 description 8
- 238000007599 discharging Methods 0.000 description 7
- 239000004567 concrete Substances 0.000 description 6
- 230000003301 hydrolyzing effect Effects 0.000 description 6
- 230000007797 corrosion Effects 0.000 description 5
- 238000005260 corrosion Methods 0.000 description 5
- 238000000034 method Methods 0.000 description 4
- 238000005192 partition Methods 0.000 description 4
- 238000009434 installation Methods 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- 230000032683 aging Effects 0.000 description 2
- 239000011449 brick Substances 0.000 description 2
- 239000001913 cellulose Substances 0.000 description 2
- 229920002678 cellulose Polymers 0.000 description 2
- 239000011083 cement mortar Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229920005610 lignin Polymers 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 230000035882 stress Effects 0.000 description 2
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 230000003712 anti-aging effect Effects 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000004459 forage Substances 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000011150 reinforced concrete Substances 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000010904 stalk Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000004575 stone Substances 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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- Treatment Of Sludge (AREA)
Abstract
Description
技术领域 technical field
本实用新型涉及一种沼气池,特别是一种适合乡村农户使用的玻璃钢沼气池。The utility model relates to a biogas pool, in particular to a fiberglass biogas pool suitable for rural farmers.
背景技术 Background technique
目前农村建造的沼气池有两种模式:一种是直接用砖砌,混凝土现浇,用水泥砂浆作粘合料。一种是用钢筋混凝土制成预制板,然后运抵现场拼接,用水泥砂浆粘合而成。要完成沼气池的建筑、安装,需要备用水泥、砂、石、砖块等材料,特别是在山区农村或远离原材料源地的农户要修建一个沼气池,备料、搬运、费工、费时,建造成本高,农户经济承受能力有限。以上两种建池模式,池体气密难度大,稍有不慎很容易造成漏气。At present, there are two types of biogas digesters built in rural areas: one is directly built with bricks, concrete is cast on site, and cement mortar is used as a binding material. One is to make prefabricated panels with reinforced concrete, and then transport them to the site for splicing and bonding with cement mortar. To complete the construction and installation of a biogas digester, spare materials such as cement, sand, stones, bricks, etc. are needed, especially in rural areas in mountainous areas or farmers far away from the source of raw materials to build a biogas digester, material preparation, transportation, labor-intensive, time-consuming, construction The cost is high, and the economic affordability of farmers is limited. For the above two pool construction modes, the pool body is difficult to be airtight, and a little carelessness can easily cause air leakage.
目前使用的沼气池大多是要以人畜粪便为发酵原料,然而有大部份农户养的牲畜很少,不能满足沼气池的需要。而采用稻草、秸杆等纤维素发酵,又存在产气速度慢、出料困难的问题,这些都是造成农村能源开发中修建沼气池工作进展缓慢的重要因素,稻草、秸杆的焚烧带来的环境污染一直是难以杜绝。Most of the biogas digesters currently in use use human and livestock manure as the fermentation material. However, most farmers have very few livestock, which cannot meet the needs of the biogas digesters. However, the use of cellulose fermentation such as straw and straw has the problems of slow gas production and difficult discharge. These are important factors that cause the slow progress in the construction of biogas digesters in rural energy development. The burning of straw and straw brings Environmental pollution has always been difficult to eliminate.
实用新型内容Utility model content
针对现有技术存在的缺陷,本实用新型的目的是提供一种改进的沼气池。它具有重量轻,以农作物秸秆为主要原料,进出料方便,建筑低,使用寿命长等优点。Aiming at the defects in the prior art, the purpose of the utility model is to provide an improved biogas digester. It has the advantages of light weight, using crop straw as the main raw material, convenient feeding and discharging, low construction and long service life.
为了实现上述目的,本实用新型采用的技术方案是:沼气池由玻璃钢球形薄壳结构的发酵间和水压酸化池组成;发酵间上设有进料装置和出料装置,顶部设有人孔、出气孔、人孔盖;进料装置和出料装置的底部分别有进料管和出料管伸入发酵间内腔,上部均设有安全盖;进料装置和出料装置分别通过设有单向阀的连通管与水压酸化池相连,其中出料装置的上部设有溢流管;水压酸化池由带过滤孔的隔板分隔成水解酸化池、人畜粪沉淀池,上部设有安全盖板。In order to achieve the above purpose, the technical solution adopted by the utility model is: the biogas digester is composed of a fermentation room with a glass-steel spherical thin shell structure and a hydraulic acidification tank; Air outlet and manhole cover; the bottom of the feeding device and the discharging device have feeding pipes and discharging pipes extending into the inner cavity of the fermentation room, and the upper part is equipped with a safety cover; the feeding device and the discharging device are respectively equipped with The connecting pipe of the one-way valve is connected with the hydraulic acidification tank, and the upper part of the discharge device is provided with an overflow pipe; the hydraulic acidification tank is divided into a hydrolytic acidification tank and a human and animal manure sedimentation tank by a partition with filter holes. Safety cover.
玻璃钢具有强度高、重量轻、耐腐蚀、耐老化、密封性好的特点。发酵间采用玻璃钢并设计成圆形,结构合理,受力状况好,采用工业化玻璃钢制作,可标准化生产,施工现场组装。从而使沼气池具有重量轻、运输安装方便、气密性好、不渗漏、耐腐蚀、使用寿命长的特点。FRP has the characteristics of high strength, light weight, corrosion resistance, aging resistance and good sealing. The fermentation room is made of glass fiber reinforced plastic and designed to be circular, with reasonable structure and good stress condition. It is made of industrialized glass fiber reinforced plastic, which can be standardized for production and assembled on the construction site. Therefore, the biogas digester has the characteristics of light weight, convenient transportation and installation, good air tightness, no leakage, corrosion resistance and long service life.
沼气厌氧发酵过程分为水解、酸化和产甲烷三大步骤,根据这一理论,将标准水压式沼气池的水压间拓展为具有水解酸化和调节气压双功能的水压酸化池,采用混凝土材料制作。水压酸化池的两端分别与玻璃钢沼气池的进料斗、出料斗相连,分别装上单向阀,使水压酸化池中的液体只能从进料装置回流入发酵间,而不能从出料部装置入发酵间;而发酵间的液体只能从出料装置流入水压酸化间,而不能从进料装置流入水压酸化池。当发酵间的气压上升时,发酵间的发酵液通过出料装置,经过单向阀流向水压酸化池;当发酵间的气压下降时,水压酸化池的液体经过酸化池与进料装置的连通管及单向阀流入发酵间,从而形成了一个单向循环的料液流动体系。发酵间沼气压力的一升一降,完成了整个沼气池系统的液体循环,对发酵间中发酵液起到搅拌作用。因发酵间的上球壳是圆弧形,发酵间的发酵液的一升一降,使发酵液面时小时大,从而对发酵间液面的结壳起到破壳作用。水压酸化池中设有一带过滤孔的隔板,使每一个循环时,酸化池里的液体通过单向阀和进料管回流入发酵间,而还没水解酸化的原料及残渣留在水压酸化池中。将纤维性原料在敞口酸化池里完成水解和酸化两个阶段,酸化液通过单向阀自动进入发酵间发酵产气,剩余的以木质素为主体的残渣在水压酸化池内彻底分解后直接取出,从而解决了纤维性原料入池发酵出料困难的技术难题。也达到了利用所产沼气的动力实现发酵间的发酵液自动搅拌、自动循环的目的。The biogas anaerobic fermentation process is divided into three major steps: hydrolysis, acidification and methane production. According to this theory, the hydraulic chamber of the standard hydraulic biogas digester is expanded into a hydraulic acidification pond with dual functions of hydrolysis acidification and air pressure adjustment. Made of concrete material. The two ends of the hydraulic acidification tank are respectively connected with the feed hopper and discharge hopper of the FRP biogas digester, and are installed with one-way valves, so that the liquid in the hydraulic acidification tank can only flow back into the fermentation room from the feed device, and cannot flow from the feed device to the fermentation room. The discharge part is installed into the fermentation room; the liquid in the fermentation room can only flow into the hydraulic acidification room from the discharge device, but cannot flow into the hydraulic acidification tank from the feed device. When the air pressure in the fermentation room rises, the fermentation liquid in the fermentation room passes through the discharge device and flows to the hydraulic acidification tank through the one-way valve; when the air pressure in the fermentation room drops, the liquid in the hydraulic acidification tank passes through the acidification tank and the feeding device The connecting pipe and the one-way valve flow into the fermentation room, thus forming a one-way circulating material-liquid flow system. The rise and fall of the biogas pressure in the fermentation room completes the liquid circulation of the entire biogas system and stirs the fermentation liquid in the fermentation room. Because the upper spherical shell of the fermentation room is arc-shaped, the fermentation liquid in the fermentation room rises and falls, making the fermentation liquid level increase every hour, thereby breaking the crust on the liquid surface of the fermentation room. A partition with filter holes is installed in the hydraulic acidification tank, so that during each cycle, the liquid in the acidification tank flows back into the fermentation room through the one-way valve and the feed pipe, while the raw materials and residues that have not been hydrolyzed and acidified remain in the water. pressure acidification pool. The fibrous raw materials are hydrolyzed and acidified in the open acidification tank. The acidification liquid enters the fermentation room to ferment and produce gas automatically through the one-way valve. The remaining residue mainly composed of lignin is completely decomposed in the hydraulic acidification tank and directly Take it out, thus solving the technical problem that the fibrous raw material is difficult to enter the tank for fermentation and discharge. It also achieves the purpose of using the power of the produced biogas to realize the automatic stirring and automatic circulation of the fermentation liquid in the fermentation room.
本实用新型的优点:Advantage of the utility model:
1、玻璃钢具有强度高、重量轻、耐腐蚀、耐老化、密封性好的特点。玻璃钢发酵间设计成圆形,结构合理,受力状况好,采用工业化玻璃钢制作,标准化生产,施工现场组装。从而使沼气池具有重量轻、运输安装方便、气密性好、不渗漏、耐腐蚀、使用寿命长的特点。1. FRP has the characteristics of high strength, light weight, corrosion resistance, aging resistance and good sealing. The FRP fermentation room is designed to be circular, with reasonable structure and good stress condition. It is made of industrialized FRP, standardized production, and assembled on the construction site. Therefore, the biogas digester has the characteristics of light weight, convenient transportation and installation, good air tightness, no leakage, corrosion resistance and long service life.
2、将纤维性原料在敞口酸化池里完成水解和酸化两个阶段,酸化液通过单向阀自动进入发酵间发酵产气,剩余的以木质素为主体的残渣在水压酸化池内彻底分解后直接取出,从而解决了纤维性原料入池发酵出料困难的技术难题。2. Complete the two stages of hydrolysis and acidification of fibrous raw materials in the open acidification tank. The acidification solution automatically enters the fermentation room to ferment and produce gas through the one-way valve, and the remaining residue mainly composed of lignin is completely decomposed in the hydraulic acidification tank. After that, it is directly taken out, thereby solving the technical problem that the fibrous raw material is difficult to enter the tank for fermentation and discharge.
3、依靠沼气原料发酵所产沼气的动力,实现自动搅拌、自动循环和自动破壳。3. Relying on the power of biogas produced by the fermentation of biogas raw materials, automatic stirring, automatic circulation and automatic shell breaking are realized.
4、水压间和酸化池一体化,简化了沼气池的结构,水解及酸化过程在发酵间外进行,在同等规格的发酵间,有效容积增大。在使用过程中,占地面积小,埋设方便,施工快捷,可满足了不同地区、不同地理环境的需要。在使用过程中无需对池体进行维护。4. The integration of the water pressure room and the acidification tank simplifies the structure of the biogas tank. The hydrolysis and acidification process is carried out outside the fermentation room. In the fermentation room of the same specification, the effective volume increases. In the process of use, it occupies a small area, is convenient to bury, and is fast in construction, which can meet the needs of different regions and different geographical environments. There is no need to maintain the pool body during use.
5、可工业化生产,标准规范,质量稳定;5. It can be produced industrially, with standardized standards and stable quality;
6、冬天气温较低时,地面结冻有可能导致混凝土沼气的损坏,而玻璃钢沼气池具有一定的弹性,不会被冻土挤裂。6. When the temperature is low in winter, the freezing of the ground may cause damage to the concrete biogas, while the fiberglass biogas digester has certain elasticity and will not be squeezed by the frozen soil.
7、玻璃钢导热系数为1.42kj(m.h.℃),,混凝土导热系数为5.44kj/(m.h.℃),可见玻璃钢热量损失远比混凝土少的多,故保证了较高的产气率。7. The thermal conductivity of FRP is 1.42kj (m.h.℃), and the thermal conductivity of concrete is 5.44kj/(m.h.℃). It can be seen that the heat loss of FRP is much less than that of concrete, so a higher gas production rate is guaranteed.
8、玻璃钢沼气池抗老化、耐腐蚀,使用寿命可长达30年之久。8. The fiberglass biogas digester is anti-aging and corrosion-resistant, and its service life can be as long as 30 years.
下面结合附图进一步说明本实用新型的技术方案。Further illustrate the technical scheme of the utility model below in conjunction with accompanying drawing.
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是图1的俯视图。FIG. 2 is a top view of FIG. 1 .
图3是图1的左视图。Fig. 3 is a left side view of Fig. 1 .
图4是图3中A-A向视图Figure 4 is a view from A-A in Figure 3
具体实施方式 Detailed ways
见图1至图4,本实用新型的沼气池,由玻璃钢球形薄壳结构的发酵间和混凝土水压酸化池组成;发酵间由上下两个薄壳半球4、5组成,两个薄壳半球4、5的接合采用扣榫方式,发酵间上半球4设有进料装置和出料装置,顶部设有人孔10、出气孔11、人孔盖12;进料装置和出料装置的上部为斗状体,分别为进料斗2和出料斗7,进料斗2和出料斗7上部均设有安全盖1、9,底部分别有进料管3和出料管6伸入发酵间内腔,进料装置和出料装置分别通过设有单向阀13、16的连通管14、15与水压酸化池相连,其中出料斗7的上部设有溢流管8;水压酸化池内设有带过滤孔21的隔板19,并由隔板19分隔成水解酸化池17、人畜粪沉淀池20,水压酸化池上部设有安全盖板18。See Fig. 1 to Fig. 4, the biogas digester of the present utility model is made up of the fermentation room of glass fiber reinforced plastic spherical thin shell structure and the concrete hydraulic acidification tank; The connection of 4 and 5 adopts the buckle tenon method. The
将稻草、草料、秸杆等纤维素原料放入水解发酸池17内堆沤,放入水至要求水位。将人畜粪接入人畜粪沉淀池20。当发酵间产生的沼气压力上升时,将发酵间的发酵液压至进料斗2和出料斗7,在进料斗2,因单向阀13的作用,进料斗2中的发酵液不能流入人畜粪沉淀池20中,而出料斗7中的发酵液通过单向阀15流入水解酸化池17中,水解酸化池中的液体通过过滤隔板19流入人畜粪沉淀池20,水压酸化池中的液位随着发酵间中沼气的压力的升高而升高,当进料斗2、出料斗7、水压酸化池中的液位达到出料斗7的溢液管8位置时,多余液体从溢液管8流出。当发酵间的沼气压力下降时,进料斗2、出料斗7中的液体流回发酵间,因单向阀15的作用,水解酸化池17中的液体不能通过连通管16流入出料斗;而水解酸化池17中的原料的已水解酸化的液体通过过滤隔板19流入人畜粪沉淀池20,与人畜粪沉淀池20中的液体一起通过连通管14、单向阀13流入进料斗2流入发酵间。人畜粪沉淀池20中的沉淀物以及水解酸化池17中未水解酸化的原料仍留在水压酸化池中继续进行水解酸化,当彻底分解后可直接取出,这样既方便了纤维素原料进出料,又不因进出料而影响沼气池的连续产气。Cellulosic raw materials such as rice straw, forage, and stalks are put into the
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| Application Number | Priority Date | Filing Date | Title |
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| CNU2007200634407U CN201077838Y (en) | 2007-06-06 | 2007-06-06 | Methane tank |
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| Application Number | Priority Date | Filing Date | Title |
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| CNU2007200634407U CN201077838Y (en) | 2007-06-06 | 2007-06-06 | Methane tank |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102260019A (en) * | 2011-05-25 | 2011-11-30 | 衢州市土肥与农村能源技术推广站 | Separated two-phase anaerobic fermentation device |
| CN109280615A (en) * | 2016-08-10 | 2019-01-29 | 天津中天精科科技有限公司 | A kind of innoxious fermentation process system of organic isolate of the Biohazard Waste Disposal containing cloth bacterium device |
| CN106244427B (en) * | 2016-08-08 | 2019-06-04 | 郑州思辩科技有限公司 | Biomass hydrolysis and acidification unit |
-
2007
- 2007-06-06 CN CNU2007200634407U patent/CN201077838Y/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102260019A (en) * | 2011-05-25 | 2011-11-30 | 衢州市土肥与农村能源技术推广站 | Separated two-phase anaerobic fermentation device |
| CN106244427B (en) * | 2016-08-08 | 2019-06-04 | 郑州思辩科技有限公司 | Biomass hydrolysis and acidification unit |
| CN109280615A (en) * | 2016-08-10 | 2019-01-29 | 天津中天精科科技有限公司 | A kind of innoxious fermentation process system of organic isolate of the Biohazard Waste Disposal containing cloth bacterium device |
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