CN201276559Y - Stereo internal circulation stirring organic floating slag crushing device of anaerobic reaction tank - Google Patents
Stereo internal circulation stirring organic floating slag crushing device of anaerobic reaction tank Download PDFInfo
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Abstract
一种厌氧反应罐立体内循环搅拌有机物浮渣破碎装置,其特征在于:该装置包括其底部安装有排渣管(13)和进料口(1)、其上端设置有厌氧罐顶盖(6)的厌氧反应罐体(10),以及安装在厌氧罐顶盖(6)中心处的沼气出气口(5)和设置在罐体侧上部的出料管(17);在罐体(10)的内壁上以均布的方式设置有至少两个导流竖直立管(9),所述导流竖直立管(9)的上端口位于厌氧反应罐体(10)内的厌氧反应发酵液面之下,导流竖直立管(9)的下端口与水平设置的导流罩(2)相连通,所述导流罩(2)的出液口均以同向偏置的方式设置,在导流罩(2)内设置有由动力源驱动的搅拌粉碎装置。
A three-dimensional internal circulation stirring organic scum crushing device in an anaerobic reaction tank, characterized in that the device includes a slag discharge pipe (13) and a feed port (1) installed at the bottom, and an anaerobic tank top cover installed at the upper end (6) the anaerobic reaction tank (10), and the biogas outlet (5) installed in the center of the anaerobic tank top cover (6) and the discharge pipe (17) arranged on the upper part of the tank side; The inner wall of the body (10) is provided with at least two diversion vertical risers (9) in a uniform manner, and the upper port of the diversion vertical riser (9) is located in the anaerobic reaction tank body (10) Under the surface of the anaerobic reaction fermentation liquid in the interior, the lower port of the diversion vertical standpipe (9) is connected with the horizontally arranged diversion cover (2), and the liquid outlets of the diversion cover (2) are all in the form of It is arranged in a biased manner in the same direction, and a stirring and pulverizing device driven by a power source is arranged in the flow guide cover (2).
Description
技术领域 technical field
本实用新型涉及一种用于厌氧反应罐立体内循环搅拌有机物浮渣破碎装置,该装置特别适合用于养殖类畜禽养殖粪便、屠宰污废水、城市生活废水、污泥等需要在厌氧反应罐内将发酵液和活性微生菌进行的反应的工艺过程。The utility model relates to a three-dimensional internal circulation stirring organic scum crushing device for an anaerobic reaction tank. The process of reacting fermentation broth and active microorganisms in the reaction tank.
背景技术 Background technique
当前广泛采用的将城镇生活污水、畜禽养殖粪便、淀粉废水以及污泥等在厌氧反应罐同活性微生菌进行发酵的工艺形式中,因有机物浮渣等比重小于水,浮在反应液的上部,逐渐在液面结成硬壳,同时还存在着厌氧发酵不完全,发生器内物料出现分层现象,直接影响到反应器的沼气产气率。为避免和减少上述状态发生,通常在厌氧反应过程中,采用将液体不间断地进行循环工艺方法。In the currently widely used process of fermenting urban domestic sewage, livestock and poultry manure, starch wastewater, and sludge in an anaerobic reaction tank with active microorganisms, the organic scum floats in the reaction solution because the proportion of organic matter scum is smaller than that of water. The upper part of the reactor gradually forms a hard shell on the liquid surface, and at the same time, there is still incomplete anaerobic fermentation, and the material in the generator is stratified, which directly affects the biogas production rate of the reactor. In order to avoid and reduce the occurrence of the above-mentioned state, usually in the process of anaerobic reaction, the process method of circulating the liquid continuously is adopted.
现有技术的搅拌和避免有机物浮渣、结壳产生的工艺方法和存在的问题如下:The stirring of the prior art and the process and existing problems of avoiding organic scum and crust production are as follows:
1.在厌氧底部中心处进行搅拌形式。虽然该工艺形式可将处于罐体下部的浓度含量较高菌种和上部浓度含量较低菌种的发酵液进行搅拌,但由于有机物浮渣是漂浮在液面上,长时间可使得发酵液表面形成结壳,直接影响沼气产量。1. Stirring form at the center of the anaerobic bottom. Although this process form can stir the fermented broth with higher concentration bacteria in the lower part of the tank and lower concentration bacteria in the upper part, because the organic matter scum is floating on the liquid surface, it can make the surface of the fermented liquid fermented for a long time. The formation of crusts directly affects the production of biogas.
2.气体搅拌工艺形式。采用气泵将发酵液表面已产生的沼气打回到发酵液下部完成上下液的内循环搅拌,该方案仍然不能避免液面结壳现象的产生。2. Gas stirring process form. The air pump is used to pump the biogas produced on the surface of the fermentation liquid back to the lower part of the fermentation liquid to complete the internal circulation and stirring of the upper and lower liquids. This scheme still cannot avoid the occurrence of crusting on the liquid surface.
3.厌氧反应罐液体罐外循环工艺形式。该工艺方案是在罐体的下部设有搅拌器,并通过设在罐体外部的泵,抽出罐体底部浓度含量较高菌种液,再将其打回罐体液面上部。虽然该工艺可降低结壳的形成,但一些有机物浮渣以及养殖畜禽粪便内含有的各类稻草、麦草、玉米秸等杂物仍然漂浮在液表面,不能有效地进行进行发酵,因而直接影响沼气的产量。3. Anaerobic reaction tank liquid tank external circulation process form. The process plan is to install a stirrer at the lower part of the tank, and pump out the bacteria liquid with high concentration at the bottom of the tank through the pump outside the tank, and then pump it back to the upper part of the liquid surface of the tank. Although this process can reduce the formation of crusts, some organic scum and all kinds of straw, wheat straw, corn stalks and other sundries contained in the manure of livestock and poultry are still floating on the surface of the liquid, and cannot be fermented effectively, thus directly affecting Biogas production.
发明内容 Contents of the invention
本实用新型的目的正是针对上述现有技术中所存在的不足之处而提供一种厌氧反应罐立体内循环搅拌有机物浮渣破碎装置The purpose of this utility model is to provide a three-dimensional internal circulation stirring organic scum breaking device for anaerobic reaction tank in view of the deficiencies in the above-mentioned prior art
本实用新型的目的可通过以下技术措施来实现的:The purpose of this utility model can be achieved through the following technical measures:
本实用新型的厌氧反应罐立体内循环搅拌有机物浮渣破碎装置包括其底部安装有排渣管和进料口、其上端设置有厌氧罐顶盖的厌氧反应罐体,以及安装在厌氧罐顶盖中心处的沼气出气口和设置在罐体侧上部的出料管;在罐体的内壁上以均布的方式设置有至少两个导流竖直立管(导流竖直立管的数量可根据厌氧反应罐体直径大小的不同来配备可以是两组或两组以上),所述导流竖直立管的上端口位于厌氧反应罐体内的厌氧反应发酵液面之下,导流竖直立管的下端口与水平设置的导流罩相连通,所述导流罩的出液口均以同向偏置的方式设置(以便最大化地使反应液体绕灌体内壁作切线方向分流动),在导流罩内设置有由动力源驱动的搅拌粉碎装置;以便将漂浮在液面上的有机物浮渣通过相通的导流竖直立管和水平导流罩经搅拌粉碎装置破碎后循环至反应液下部。The anaerobic reaction tank of the utility model has a three-dimensional internal circulation stirring organic scum crushing device, which includes an anaerobic reaction tank body with a slag discharge pipe and a feed port installed at the bottom, and an anaerobic tank top cover at the upper end, and an anaerobic reaction tank body installed on the anaerobic tank. The biogas outlet at the center of the top cover of the oxygen tank and the discharge pipe arranged on the upper part of the tank body; at least two diversion vertical risers (the diversion vertical vertical pipes) are evenly distributed on the inner wall of the tank body The number of pipes can be equipped according to the diameter of the anaerobic reaction tank (it can be two or more groups), and the upper port of the diversion vertical standpipe is located at the anaerobic reaction fermentation liquid level in the anaerobic reaction tank. Below, the lower port of the diversion vertical standpipe communicates with the horizontally arranged shroud, and the liquid outlets of the shroud are all set in the same direction biased mode (in order to maximize the reaction liquid around the irrigation The internal wall is divided into the tangential direction), and a stirring and pulverizing device driven by a power source is arranged in the shroud; in order to pass the organic scum floating on the liquid surface through the connected vertical vertical pipe and the horizontal shroud After being crushed by the stirring and crushing device, it is circulated to the lower part of the reaction liquid.
本实用新型中所述搅拌粉碎装置是由与导流罩同轴线方式安装在导流罩内的由电机驱动的传动主轴、安装在传动主轴前端的叶片组成;且叶片的外轮廓边缘为刃口结构。在由厌氧罐顶盖与发酵液上液面共同构成的密闭的储存气室部位安装有压力传感器和由电磁阀控制的压力安全阀。所述的压力传感器用于采集储存气室内的压力,当超过或低于预先设定的储存气室压力上限或下限时,经电磁阀控制压力安全阀关闭或打开,同时控制搅拌电机的开启工作或停机,从而保证密闭储存气室内压力恒定。The mixing and pulverizing device described in the utility model is composed of a motor-driven drive shaft installed in the wind guide coaxially with the wind guide, and a blade installed at the front end of the transmission shaft; and the outer contour edge of the blade is a blade mouth structure. A pressure sensor and a pressure safety valve controlled by a solenoid valve are installed in the airtight storage air chamber formed by the top cover of the anaerobic tank and the upper liquid surface of the fermentation broth. The pressure sensor is used to collect the pressure in the storage chamber. When it exceeds or falls below the preset upper or lower pressure limit of the storage chamber, the solenoid valve controls the pressure safety valve to close or open, and at the same time controls the stirring motor to start. Or shut down, thereby guaranteeing that the pressure in the airtight storage air chamber is constant.
本实用新型设置在反应罐体侧上部的出料管的进料管口位于发酵液的液面之下,出料管口位于发酵液的液面的上方。In the utility model, the feed pipe mouth of the discharge pipe arranged on the upper side of the reaction tank body is located below the liquid surface of the fermentation liquid, and the discharge pipe mouth is located above the liquid surface of the fermentation liquid.
本实用新型中所述的排渣管安装在厌氧反应罐体下部,位于厌氧反应罐体的内吸料口为锥形结构。The slag discharge pipe described in the utility model is installed in the lower part of the anaerobic reaction tank body, and the inner material suction port located in the anaerobic reaction tank body has a tapered structure.
本实用新型的工作原理如下:The working principle of the utility model is as follows:
当厌氧反应罐内装入一定量的发酵液和活性微生菌进行发酵经一段时间开始产生沼气时,启动搅拌粉碎装置,通过传动主轴驱动叶片对由导流竖直立管上端口进入水平导流罩内物料进行搅拌、粉碎,使处于反应液(发酵液)面上部的有机物浮渣在旋转搅拌、粉碎叶片的作用下,将反应罐上部的反应液连同有机物浮渣粉碎并强制交换至反应罐下部,有效地形成反应液立体循环和上下充分混和。由于搅拌、粉碎叶片的外轮廓为刃口结构,使得漂浮在发酵液面的有机物浮渣和其它漂浮物通过搅拌、粉碎叶片将其破碎,以防止在液面结成硬壳。When the anaerobic reaction tank is filled with a certain amount of fermentation liquid and active microorganisms for fermentation and biogas is produced after a period of time, the stirring and pulverizing device is started, and the blades are driven by the transmission shaft to enter the horizontal guide from the upper port of the vertical vertical pipe. The materials in the flow hood are stirred and crushed, so that the organic scum on the upper surface of the reaction liquid (fermentation liquid) is crushed and forced to exchange the organic scum on the upper part of the reaction tank with the action of the rotating stirring and crushing blades. The lower part of the tank effectively forms a three-dimensional circulation of the reaction liquid and fully mixes up and down. Because the outer contour of the stirring and crushing blades is a blade structure, the organic matter scum and other floating matter floating on the fermentation liquid surface are broken by the stirring and crushing blades to prevent hard shells from forming on the liquid surface.
反应过程中产生的沼气储存在位于发酵液上液面密闭的储存气室内,沼气的输出通过厌氧罐顶盖中心处的沼气出气口向外输送。沉淀在反应罐底部的沉渣通过其底部处安装的排渣管经外接泵抽出。进料口补充新的反应液。The biogas produced during the reaction is stored in a closed storage chamber located on the upper surface of the fermentation broth, and the output of the biogas is transported outward through the biogas outlet at the center of the top cover of the anaerobic tank. The sediment deposited at the bottom of the reaction tank is pumped out through the slag discharge pipe installed at the bottom through an external pump. The feed port is replenished with new reaction solution.
本实用新型的优点在于:The utility model has the advantages of:
1、有效地避免了因长时间漂浮在反应液上部的有机物浮渣和其它漂浮物在液面结成硬壳,确保产气能正常进行。1. Effectively avoid the organic scum and other floating matter floating on the upper part of the reaction liquid for a long time to form a hard shell on the liquid surface, so as to ensure the normal production of gas.
2、充分地、最大化地将处于罐体下部的浓度含量较高菌种和上部浓度含量较低菌种的发酵液进行搅拌混和,使得在单位时间内生产出更多的沼气,降低生产成本,提高产气率。2. Fully and maximally stir and mix the fermented liquid with higher concentration bacteria in the lower part of the tank and lower concentration bacteria in the upper part, so as to produce more biogas per unit time and reduce production costs , to increase the gas production rate.
3、通过厌氧反应罐体上部储存气室内安装的压力传感器采集的储存气室内的压力数据,经控制程序按照设定的压力上限和压力下限,由电磁自动控制压力安全阀的开启和关闭,可以保证储存气室内的正常压力,确保了厌氧反应罐的安全。3. The pressure data in the storage gas chamber collected by the pressure sensor installed in the upper storage gas chamber of the anaerobic reaction tank is automatically controlled by the electromagnetic to open and close the pressure safety valve according to the set pressure upper limit and pressure lower limit through the control program. It can guarantee the normal pressure in the storage gas chamber and ensure the safety of the anaerobic reaction tank.
附图说明 Description of drawings
图1为实用新型主剖图。Fig. 1 is the main sectional view of the utility model.
图2为图1的横剖俯视图。FIG. 2 is a cross-sectional top view of FIG. 1 .
图1和图2中序号:Serial numbers in Figure 1 and Figure 2:
1-进料口,2-导流罩,3-电磁阀,4-压力安全阀,5-沼气出气口,6-反应罐顶盖,7-压力传感器,8-有机物浮渣,9-导流竖直立管,10-厌氧反应罐体,11-叶片,12-电机,13-排渣管,14-厌氧罐基座,15-传动主轴,16-储存气室,17.出料管。1-Feed inlet, 2-Diffuser, 3-Solenoid valve, 4-Pressure safety valve, 5-Biogas outlet, 6-Reaction tank top cover, 7-Pressure sensor, 8-Organic scum, 9-Guide Flow vertical standpipe, 10-anaerobic reaction tank body, 11-blade, 12-motor, 13-slag discharge pipe, 14-anaerobic tank base, 15-transmission spindle, 16-storage gas chamber, 17. Feed tube.
具体实施方式 Detailed ways
本实用新型以将下结合实施例(附图)做进一步描述:The utility model will be further described in conjunction with the following embodiments (accompanying drawings):
如图1和图2所示,本实用新型的厌氧反应罐立体内循环搅拌有机物浮渣破碎装置包括其底部安装有排渣管13和进料口1、其上端设置有厌氧罐顶盖6的厌氧反应罐体10,以及安装在厌氧罐顶盖6中心处的沼气出气口5和设置在罐体侧上部的出料管17;所述罐体10安装在厌氧罐基座14上,在罐体10的内壁上以均布的方式设置有至少两个导流竖直立管9,所述导流竖直立管9的上端口位于厌氧反应罐体10内的厌氧反应发酵液面之下,导流竖直立管9的下端口与水平设置的导流罩2相连通,所述导流罩2的出液口均以同向偏置的方式设置,在导流罩2内设置有由动力源驱动的搅拌粉碎装置;所述搅拌粉碎装置是由与导流罩2同轴线方式安装在导流罩内的由电机12驱动的传动主轴15、安装在传动主轴前端的叶片11组成;且叶片的外轮廓边缘为刃口结构,叶片11的数量可以是两片对称设置,也可以采用三片均布的方式设置。As shown in Fig. 1 and Fig. 2, the anaerobic reaction tank of the present utility model has a three-dimensional internal circulation stirring organic matter scum crushing device including a
本实用新型在由厌氧罐顶盖6与发酵液上液面共同构成的密闭的储存气室16部位安装有压力传感器7和由电磁阀3控制的压力安全阀4,更具体讲,压力传感器7安装在反应罐顶盖6和发酵液上面之间构成的密闭储存气室16内,由电磁阀3控制的压力安全阀4安装在厌氧反应罐体10的外部,并与密闭储存气室16相通;当压力传感器7设定的压力上限和压力下限时,经控制程序启动电磁阀3控制压力安全阀4打开或关闭,从而保证密闭储存气室16内恒定压力。The utility model is equipped with a
设置在反应罐体10侧上部的出料管17的进料管口位于发酵液的液面之下,出料管口位于发酵液的液面的上方;所述排渣管13安装在厌氧反应罐体10下部,位于厌氧反应罐体的内吸料口为锥形结构。The feed nozzle of the
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Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102242058A (en) * | 2011-04-25 | 2011-11-16 | 北京愿景宏能源环保科技发展有限公司 | Anaerobic fermentation system |
CN102952746A (en) * | 2012-11-21 | 2013-03-06 | 上海亚达发搅拌设备有限公司 | Anaerobic fermentation tank |
CN102965275A (en) * | 2012-11-21 | 2013-03-13 | 上海亚达发搅拌设备有限公司 | Anaerobic fermentation tank |
CN104001598A (en) * | 2014-06-03 | 2014-08-27 | 安徽国祯环保节能科技股份有限公司 | Oxidation ditch dross crushing machine |
CN105087364A (en) * | 2015-08-31 | 2015-11-25 | 太仓百诺纳米科技有限公司 | Anaerobic treatment device and system |
CN105296342A (en) * | 2015-11-30 | 2016-02-03 | 周伟萌 | Anaerobic treatment device |
CN106497759A (en) * | 2016-11-30 | 2017-03-15 | 上海市政工程设计研究总院(集团)有限公司 | A kind of anaerobic jar scum silica frost EGR |
CN111170454A (en) * | 2020-03-19 | 2020-05-19 | 北京高能时代环境技术股份有限公司 | Anaerobic reactor's deslagging system |
-
2008
- 2008-05-20 CN CN200820070600.5U patent/CN201276559Y/en not_active Expired - Fee Related
Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
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CN102242058A (en) * | 2011-04-25 | 2011-11-16 | 北京愿景宏能源环保科技发展有限公司 | Anaerobic fermentation system |
CN102242058B (en) * | 2011-04-25 | 2012-12-26 | 北京愿景宏能源环保科技发展有限公司 | Anaerobic fermentation system |
CN102952746A (en) * | 2012-11-21 | 2013-03-06 | 上海亚达发搅拌设备有限公司 | Anaerobic fermentation tank |
CN102965275A (en) * | 2012-11-21 | 2013-03-13 | 上海亚达发搅拌设备有限公司 | Anaerobic fermentation tank |
CN102952746B (en) * | 2012-11-21 | 2014-05-07 | 上海亚达发搅拌设备有限公司 | Anaerobic fermentation tank |
CN102965275B (en) * | 2012-11-21 | 2014-05-07 | 上海亚达发搅拌设备有限公司 | Anaerobic fermentation tank |
CN104001598A (en) * | 2014-06-03 | 2014-08-27 | 安徽国祯环保节能科技股份有限公司 | Oxidation ditch dross crushing machine |
CN104001598B (en) * | 2014-06-03 | 2015-12-09 | 安徽国祯环保节能科技股份有限公司 | A kind of oxidation ditch scum silica frost disintegrating machine |
CN105087364A (en) * | 2015-08-31 | 2015-11-25 | 太仓百诺纳米科技有限公司 | Anaerobic treatment device and system |
CN105087364B (en) * | 2015-08-31 | 2018-05-22 | 太仓昊恒纳米科技有限公司 | A kind of anaerobic processing device and system |
CN105296342A (en) * | 2015-11-30 | 2016-02-03 | 周伟萌 | Anaerobic treatment device |
CN106497759A (en) * | 2016-11-30 | 2017-03-15 | 上海市政工程设计研究总院(集团)有限公司 | A kind of anaerobic jar scum silica frost EGR |
CN111170454A (en) * | 2020-03-19 | 2020-05-19 | 北京高能时代环境技术股份有限公司 | Anaerobic reactor's deslagging system |
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