CN201351162Y - Top pressure-type integration methane tank - Google Patents
Top pressure-type integration methane tank Download PDFInfo
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- CN201351162Y CN201351162Y CNU2008200990410U CN200820099041U CN201351162Y CN 201351162 Y CN201351162 Y CN 201351162Y CN U2008200990410 U CNU2008200990410 U CN U2008200990410U CN 200820099041 U CN200820099041 U CN 200820099041U CN 201351162 Y CN201351162 Y CN 201351162Y
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- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 title claims description 10
- 230000010354 integration Effects 0.000 title 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 35
- 239000007788 liquid Substances 0.000 claims abstract description 16
- 239000011152 fibreglass Substances 0.000 claims abstract description 4
- 238000003756 stirring Methods 0.000 claims description 4
- 238000010276 construction Methods 0.000 claims description 3
- 238000007599 discharging Methods 0.000 claims 1
- 239000011159 matrix material Substances 0.000 claims 1
- 238000000465 moulding Methods 0.000 claims 1
- 238000003860 storage Methods 0.000 abstract description 25
- 238000000855 fermentation Methods 0.000 abstract description 19
- 230000004151 fermentation Effects 0.000 abstract description 19
- 238000009434 installation Methods 0.000 abstract description 6
- 239000002131 composite material Substances 0.000 abstract description 3
- 238000005336 cracking Methods 0.000 abstract 1
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000011449 brick Substances 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 239000010791 domestic waste Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 244000144972 livestock Species 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000003014 reinforcing effect Effects 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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- C12M21/00—Bioreactors or fermenters specially adapted for specific uses
- C12M21/04—Bioreactors or fermenters specially adapted for specific uses for producing gas, e.g. biogas
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- C12M23/00—Constructional details, e.g. recesses, hinges
- C12M23/20—Material Coatings
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- C12M23/00—Constructional details, e.g. recesses, hinges
- C12M23/36—Means for collection or storage of gas; Gas holders
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- C12M23/38—Caps; Covers; Plugs; Pouring means
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- C12M29/00—Means for introduction, extraction or recirculation of materials, e.g. pumps
- C12M29/04—Filters; Permeable or porous membranes or plates, e.g. dialysis
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- C12M41/00—Means for regulation, monitoring, measurement or control, e.g. flow regulation
- C12M41/40—Means for regulation, monitoring, measurement or control, e.g. flow regulation of pressure
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- 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
本实用新型涉及一种顶压式一体化沼气池,由有机、无机玻璃钢或复合材料制作成型的壳体,所述壳体的上部与下部通过法兰连接为一体;所述壳体下部的空间为产生沼气的发酵室,所述壳体上部包括水压间、出料管和贮气室,贮气室与发酵室连通为一整体腔室,出料管贯穿贮气室上方的水压间与发酵室连通,水压间顶部设有出料口,出料口用出料口盖密封,贮气室顶部设有带有输气管的导气口,输气管的一端伸出水压间,出料管下端口与贮气室顶部之间设置有用于分割液面浮渣层的网,进料管与发酵室连通。本实用新型的水压间与池体上部为一体化整体结构,抗拉裂性能好;结构简单、牢固,具有运输方便、安装快捷的优点。
The utility model relates to a top-pressure integrated biogas digester, a shell made of organic, inorganic glass fiber reinforced plastic or composite materials, the upper part and the lower part of the shell are connected as a whole through flanges; the space in the lower part of the shell is As a fermentation chamber for biogas generation, the upper part of the housing includes a water pressure room, a discharge pipe and an air storage chamber, the air storage chamber and the fermentation chamber are connected to form an integral chamber, and the discharge pipe runs through the hydraulic chamber above the air storage chamber It is connected with the fermentation room, and the top of the water pressure room is equipped with a discharge port, which is sealed with a discharge port cover. The top of the air storage chamber is provided with an air guide port with an air delivery pipe, and one end of the air delivery pipe extends out of the water pressure room. A net for dividing the scum layer on the liquid surface is arranged between the lower port of the feed pipe and the top of the air storage chamber, and the feed pipe communicates with the fermentation chamber. The water pressure room and the upper part of the pool body of the utility model are an integral whole structure, which has good resistance to cracking; the structure is simple and firm, and has the advantages of convenient transportation and quick installation.
Description
技术领域 technical field
本实用新型涉及污水、废渣、人畜粪便的处理设备,具体涉及一种顶压式一体化沼气池。The utility model relates to treatment equipment for sewage, waste residue, and human and animal excrement, in particular to a top-pressure integrated methane pool.
背景技术 Background technique
沼气是一种可再生能源,沼气的使用能减少由于煤或燃油燃烧对环境的污染,还能处理、利用人们的生活废物以及牲畜的排泄物,目前,我国城乡的户用沼气池多为砖混或混凝土结构,而混凝土沼气池施工难、密封性能差,容易漏气,效果不好的缺点。目前还出现了玻璃钢沼气池,玻璃钢沼气池具有重量轻、建池快、耐腐蚀、气密性好等优点,但市场上的玻璃钢沼气池多为进、出料管分别从左右斜侧斜插入主池体,水压间通出料管安装于主池体斜外上方。这种结构的沼气池结构分散、安装复杂、不易密封且无分割液面浮渣层的破壳网,如果遇到地基沉降或地质灾害,由于各部件是拼合固定连接而成,连接处极易被拉裂,造成漏气甚至池体报废。Biogas is a kind of renewable energy. The use of biogas can reduce the pollution of the environment due to coal or fuel combustion, and can also process and utilize people's domestic waste and livestock excrement. At present, most of the household biogas digesters in urban and rural areas in my country are made of bricks. Concrete or concrete structure, but the construction of concrete biogas digesters is difficult, the sealing performance is poor, easy to leak, and the effect is not good. At present, FRP biogas digesters have also appeared. FRP biogas digesters have the advantages of light weight, quick pool construction, corrosion resistance, and good air tightness. The main pool body and the discharge pipe between the water pressure chambers are installed on the oblique outer top of the main pool body. The structure of the biogas digester with this structure is scattered, the installation is complicated, it is not easy to seal, and there is no broken shell net that divides the scum layer on the liquid surface. Being pulled apart, causing air leakage or even scrapping the pool body.
发明内容 Contents of the invention
本实用新型针对现有技术的不足,提供一种顶压式一体化沼气池,它将水压间与池体上部设计为一体化的整体结构,使所述沼气池的抗拉裂性能好,并且有结构简单、运输方便、安装快捷、自动破壳的优点。Aiming at the deficiencies of the prior art, the utility model provides a top-pressure integrated biogas pit, which designs the water pressure chamber and the upper part of the pond body as an integrated overall structure, so that the biogas pit has good tensile crack resistance, And it has the advantages of simple structure, convenient transportation, quick installation and automatic shell breaking.
本实用新型的目的是这样实现的:顶压式一体化沼气池,包括由有机、无机玻璃钢或复合材料制作成型的壳体,所述壳体的上部与下部通过法兰连接为一体;所述壳体下部的空间为产生沼气的发酵室,所述壳体上部包括水压间、出料管和贮气室,贮气室与发酵室连通为一整体腔室,出料管贯穿贮气室上方的水压间与发酵室连通,水压间顶部设有出料口,出料口用出料口盖密封,贮气室顶部设有带有输气管的导气口,输气管的一端伸出水压间,出料管下端口与贮气室顶部之间设置有用于分割液面浮渣层的网,进料管与发酵室连通。The purpose of this utility model is achieved in this way: the top-pressure integrated biogas digester includes a shell made of organic, inorganic glass fiber reinforced plastic or composite materials, the upper part and the lower part of the shell are connected as a whole through flanges; The space in the lower part of the shell is the fermentation chamber for biogas generation. The upper part of the shell includes a hydraulic room, a discharge pipe and an air storage chamber. The air storage chamber and the fermentation chamber are connected to form an integral chamber, and the discharge pipe runs through the air storage chamber The upper water pressure room is connected with the fermentation room, and the top of the water pressure room is provided with a discharge port, which is sealed with a discharge port cover, and the top of the air storage chamber is provided with an air guide port with an air delivery pipe, and one end of the air delivery pipe protrudes In the water pressure room, a net for dividing the scum layer on the liquid surface is set between the lower port of the discharge pipe and the top of the air storage chamber, and the feed pipe communicates with the fermentation chamber.
由于采用上述技术方案,将壳体上部和壳体下部通过法兰连接为一体,并将贮气室与发酵室连通为一整体腔室,出料管贯穿水压间与发酵室连通,使水压间、出料管、贮气室和进料管为位于沼气池的壳体上部的整体结构,在地基沉降等地质灾害发生时,所述沼气池能整体同步沉降,水压间、出料管、进料管和池体各部位受力较均匀,不会被拉裂,能够有效地防止漏气、漏液产生。在出料管下端口与贮气室顶部之间设置有用于分割搅动液面浮渣层的网,当发酵室内的发酵液面的涨落,可以有效地切割搅动发酵液面的浮渣层,防止浮渣结壳使沼气难以从发酵室逸出进入贮气室。所述壳体下部底部中心设有向上凸出部,使沼气池与地体接触面积更大,使安装更稳定,壳体下部底部中心设有向上凸出部,使得壳体底部的形状有变化,起到类似加强筋的作用,增加了壳体的强度,提高了壳体的耐压能力。本实用新型还具有结构简单、连接牢固,运输方便,安装快捷的优点。Due to the adoption of the above technical scheme, the upper part of the housing and the lower part of the housing are connected as a whole through flanges, and the air storage chamber and the fermentation chamber are connected to form an integral chamber. The pressure chamber, discharge pipe, gas storage chamber and feed pipe are an integral structure located on the upper part of the biogas digester shell. When geological disasters such as foundation subsidence occur, the biogas digester can settle synchronously as a whole. The force on the pipe, feed pipe and the tank body is relatively uniform and will not be pulled apart, which can effectively prevent air leakage and liquid leakage. Between the lower port of the discharge pipe and the top of the air storage chamber, a net for dividing and stirring the scum layer on the liquid surface is provided. When the fermentation liquid level in the fermentation chamber fluctuates, the scum layer on the stirring liquid surface can be effectively cut, Preventing scum encrustation makes it difficult for biogas to escape from the fermentation chamber into the gas storage chamber. The center of the bottom of the lower part of the housing is provided with an upward protruding part, which makes the contact area between the biogas tank and the ground larger and the installation is more stable. , which acts like a reinforcing rib, increases the strength of the shell, and improves the pressure resistance of the shell. The utility model also has the advantages of simple structure, firm connection, convenient transportation and quick installation.
附图说明 Description of drawings
图1为本实用新型的结构示意图;Fig. 1 is the structural representation of the utility model;
图2为图1的A-A剖视图。Fig. 2 is a sectional view along line A-A of Fig. 1 .
附图中,1为出料口盖,2为水压间,3为输气管,3a为导气口,4为出料管,5为隔网,6为贮气室,7为法兰,8为发酵室,9为凸出部,10为进料管,11a为壳体上部,11b为壳体下部。In the accompanying drawings, 1 is the discharge port cover, 2 is the water pressure room, 3 is the air delivery pipe, 3a is the air guide port, 4 is the discharge pipe, 5 is the screen, 6 is the air storage chamber, 7 is the flange, 8 9 is the protrusion, 10 is the feed pipe, 11a is the upper part of the housing, and 11b is the lower part of the housing.
具体实施方式 Detailed ways
参照图1与图2,本实用新型包括由有机、无机玻璃钢或复合材料制作成型的壳体,壳体分壳体上部11a和壳体下部11b两部分,壳体的上部与下部通过法兰7连接成一体,形成一个近似球体结构的沼气池。所述壳体下部11b为产生沼气的发酵室8,所述壳体下部的底部中心设有向壳体心部的凸起部9,以增加沼气池的耐压能力,同上增加、安装更稳定。所述壳体上部11a包括水压间2、出料管4和贮气室6,贮气室6与发酵室8连通形成一个整体结构的腔室,贮气室上方为水压间2,水压间与贮气室共同为一整体帽形结构或半球形结构,并组成上半部池体主体结构。出料管贯穿水压间2与发酵室8连通,出料管与水压间底为一整体结构,出料管位于水压间底的中部,出料管的底部经过贮气室伸入发酵间的液面下。出料管水压间上方设有出料口,出料口上用出料口盖1密封。打开出料口盖,通过出料管可出料或在气、液排放完后,作为维修人员的进、出池体的通道。贮气室顶部设有带有输气管3的导气口3a,输气管3的一端伸出水压间用于与用户燃器具连接。出料管下端口与贮气室顶部之间设置有用于分割液面浮渣层的网5,所述用于分割液面浮渣层的网一端与出料管下端连接另一端与贮气室顶部连接,呈锥形分布在出料管下端口与贮气室顶部之间。进料管上段插入壳体的上部,部分与壳体外壁固定连接,下段垂直伸进壳体的上部内,底部至法兰平面,用于作为加料的通道。Referring to Fig. 1 and Fig. 2, the utility model includes a shell made of organic, inorganic glass fiber reinforced plastic or composite materials, the shell is divided into two parts, the
本实用新型的工作过程:沼气池投料后,由发酵室内原料产生的沼气逸出发酵液面进入贮气室,当沼气集聚到一定量时,贮气室气压升高,将发酵室的上清液通过出料管压入水压间,随着产气增多气压增大,水压间水位不断上升;水压间的高水位与发酵间的低水位具有水位差,故而形成压力差,这个压力差对贮气室的沼气形成一个压力。当用户打开用气阀时,沼气被池内水压压入燃器具,随着沼气的消耗,水压间水位逐渐下降,当停止用时,随着贮气室沼气的增多又将发酵室清液压向水压间,如此往复,本实用新型所述沼气池将不断地产气-用气-产气的循环工作。同时,发酵室液面随着产气、用气而不断上下波动时,呈锥形分布的网反复分割、搅动浮渣层而起到了自动破壳的作用,保证了沼气池的高效产气及正常工作。The working process of the utility model: after the biogas tank is fed, the biogas produced by the raw materials in the fermentation chamber escapes from the fermentation liquid surface and enters the gas storage chamber. When the biogas accumulates to a certain amount, the air pressure in the gas storage chamber rises, and the supernatant The liquid is pressed into the water pressure room through the discharge pipe. As the gas production increases, the air pressure increases, and the water level in the water pressure room continues to rise; there is a water level difference between the high water level in the water pressure room and the low water level in the fermentation room, so a pressure difference is formed. This pressure The difference forms a pressure on the biogas in the gas storage chamber. When the user opens the gas valve, the biogas is pressed into the burning appliance by the water pressure in the pool. With the consumption of the biogas, the water level in the water pressure room gradually drops. In the water pressure room, reciprocating in this way, the biogas digester described in the utility model will continuously produce gas-use gas-gas-produce cycle work. At the same time, when the liquid level in the fermentation room fluctuates continuously with gas production and gas consumption, the conical distribution network repeatedly divides and stirs the scum layer to automatically break the shell, ensuring the high-efficiency gas production and normal work.
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| CNU2008200990410U CN201351162Y (en) | 2008-12-17 | 2008-12-17 | Top pressure-type integration methane tank |
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| CNU2008200990410U CN201351162Y (en) | 2008-12-17 | 2008-12-17 | Top pressure-type integration methane tank |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102604817A (en) * | 2011-01-25 | 2012-07-25 | 农业部沼气科学研究所 | Resultant-force push-up flow anaerobic reactor |
| CN110577885A (en) * | 2019-10-08 | 2019-12-17 | 黄冈师范学院 | Fresh water pressure gas digester |
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2008
- 2008-12-17 CN CNU2008200990410U patent/CN201351162Y/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102604817A (en) * | 2011-01-25 | 2012-07-25 | 农业部沼气科学研究所 | Resultant-force push-up flow anaerobic reactor |
| CN110577885A (en) * | 2019-10-08 | 2019-12-17 | 黄冈师范学院 | Fresh water pressure gas digester |
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