CN204417501U - A kind of propelling stirring-type backflow anaerobic fermentation tank - Google Patents
A kind of propelling stirring-type backflow anaerobic fermentation tank Download PDFInfo
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Abstract
Description
技术领域 technical field
本实用新型公开了一种推进搅拌式回流厌氧发酵罐,属于发酵设备领域。 The utility model discloses a propulsion and stirring type reflux anaerobic fermentation tank, which belongs to the field of fermentation equipment.
背景技术 Background technique
厌氧发酵罐是沼气生产的重要设备,现有技术中常用的厌氧发酵罐采用多层机械式搅拌,搅拌的消耗功率大,在以秸秆为主要发酵原料的厌氧发酵罐中,大粒径固体物质主要集中在发酵罐罐体的上部,发酵罐罐体的中部和下部为小粒径固形物和液体的混合物,搅拌难以充分,甲烷菌主要集中在罐体的中部和下部,现有技术的多层机械式搅拌,容易对发酵罐内中下部的甲烷菌造成伤害,影响发酵的效果。 Anaerobic fermentation tank is an important equipment for biogas production. The anaerobic fermentation tank commonly used in the prior art adopts multi-layer mechanical stirring, which consumes a lot of power. In the anaerobic fermentation tank with straw as the main fermentation raw material, large grain The large diameter solid matter is mainly concentrated in the upper part of the fermenter tank body, and the middle and lower parts of the fermenter tank body are a mixture of small particle size solid matter and liquid, so it is difficult to fully stir, and the methane bacteria are mainly concentrated in the middle and lower part of the tank body. The multi-layer mechanical stirring of the technology is easy to cause damage to the methane bacteria in the middle and lower parts of the fermentation tank and affect the fermentation effect.
由于甲烷菌主要集中在发酵罐内的中下部,普通的机械式搅拌难以把中下部的甲烷菌搅拌到发酵罐的上部,使发酵罐上部的发酵不完全,产生的甲烷气体少,并且对原材料造成了浪费。 Since the methane bacteria are mainly concentrated in the middle and lower part of the fermenter, it is difficult to stir the methane bacteria in the middle and lower part of the fermenter to the upper part of the fermenter by ordinary mechanical stirring, so that the fermentation in the upper part of the fermenter is incomplete, the methane gas produced is less, and it is harmful to raw materials. caused waste.
发明内容 Contents of the invention
为了克服现有技术中存在的问题,本实用新型提供了一种新型角度回流混合搅拌式厌氧发酵罐,采用桨式搅拌叶的机械式搅拌形成的径向作用力,具有强剪切作用,促使大粒径固形物分散和与沼液充分混合,避免物料产生结壳现象;罐体底部的沼液抽取管在螺杆泵的抽取作用下迫使罐体内部的液体产生圆周方向的流动,形成液体循环搅拌;采用推进式搅拌叶形成的轴向作用力,剪切作用小,避免了对甲烷菌的伤害,桨式搅拌叶的机械式搅拌与沼液抽取管抽取沼液形成的液体回流搅拌共同作用,形成充分混合搅拌,提高了搅拌效果,有效降低搅拌消耗功率,本实用新型结构简单,操作方便,利于推广。 In order to overcome the problems existing in the prior art, the utility model provides a novel angle reflux mixing and agitating anaerobic fermentation tank, which adopts the radial force formed by the mechanical agitation of paddle-type agitating blades, and has a strong shearing effect, Promote the dispersion of large particle size solids and fully mix with the biogas slurry to avoid crusting of the material; the biogas slurry extraction pipe at the bottom of the tank forces the liquid inside the tank to flow in a circumferential direction under the action of the screw pump to form a liquid Circular stirring; the axial force formed by the propulsion stirring blade is used, the shearing effect is small, and the damage to the methane bacteria is avoided. The mechanical stirring of the paddle stirring blade is combined with the liquid return stirring formed by the biogas slurry extraction pipe The utility model has the advantages of simple structure, convenient operation and favorable popularization.
为达到上述目的,本实用新型提供如下技术方案: In order to achieve the above object, the utility model provides the following technical solutions:
一种推进搅拌式回流厌氧发酵罐,所述的推进搅拌式回流厌氧发酵罐包括驱动装置1、沼液喷淋口2、罐体3、沼液回流管4、桨式搅拌叶5、搅拌轴6、出料口7、螺杆泵8、沼液抽取管9、推进式搅拌叶10、进料口11、加热盘管12、取样口13、排气口14、气柜15;所述的驱动装置1设置在罐体3的正上方,搅拌轴6与驱动装置1连接,搅拌轴6的上部设置有桨式搅拌叶5,搅拌轴6的下部设置有推进式搅拌叶10,罐体3顶部设置有排气口14,排气口14与气柜15相通,罐体3另一侧设置有沼液喷淋口2,沼液喷淋口2与沼液回流管4相连,沼液回流管4与螺杆泵8连接,罐体3的底部设置有沼液抽取管9,沼液抽取管9与螺杆泵8相连,罐体3的下部设有进料口11,罐体3上部设有出料口7,罐体3内壁设有加热盘管12,取样口13设置在罐体3的中部。 A propulsion-stirring type reflux anaerobic fermenter, the propulsion-stirrer reflux anaerobic fermenter comprises a driving device 1, a biogas slurry spray port 2, a tank body 3, a biogas slurry return pipe 4, paddle-type stirring blades 5, Stirring shaft 6, discharge port 7, screw pump 8, biogas slurry extraction pipe 9, propulsion type stirring blade 10, feed port 11, heating coil 12, sampling port 13, exhaust port 14, gas cabinet 15; The driving device 1 is arranged directly above the tank body 3, the stirring shaft 6 is connected to the driving device 1, the top of the stirring shaft 6 is provided with a paddle type stirring blade 5, and the bottom part of the stirring shaft 6 is provided with a propulsion type stirring blade 10, the tank body 3 There is an exhaust port 14 on the top, and the exhaust port 14 communicates with the gas cabinet 15, and the other side of the tank body 3 is provided with a biogas slurry spray port 2, which is connected to the biogas slurry return pipe 4, and the biogas slurry The return pipe 4 is connected with the screw pump 8, the bottom of the tank body 3 is provided with a biogas slurry extraction pipe 9, the biogas slurry extraction tube 9 is connected with the screw pump 8, the lower part of the tank body 3 is provided with a feed port 11, and the upper part of the tank body 3 is provided with a There is a discharge port 7 , a heating coil 12 is provided on the inner wall of the tank body 3 , and a sampling port 13 is arranged in the middle of the tank body 3 .
所述的设置在罐体1底部的沼液抽取管9与水平面成10°到15°角,与罐体1中心成22°到25°角。 The biogas slurry extraction pipe 9 arranged at the bottom of the tank body 1 forms an angle of 10° to 15° with the horizontal plane, and an angle of 22° to 25° with the center of the tank body 1 .
本实用新型的有益效果:采用桨式搅拌叶的机械式搅拌形成的径向作用力,具有强剪切作用,促使大粒径固形物分散和与沼液充分混合,避免物料产生结壳现象;罐体底部的沼液抽取管在螺杆泵的抽取作用下迫使罐体内部的液体产生圆周方向的流动,形成液体循环搅拌;采用推进式搅拌叶形成的轴向作用力,剪切作用小,避免了对甲烷菌的伤害,桨式搅拌叶的机械式搅拌与沼液抽取管抽取沼液形成的液体回流搅拌共同作用,形成充分混合搅拌,提高了搅拌效果,有效降低搅拌消耗功率,本实用新型结构简单,操作方便,利于推广。 The beneficial effects of the utility model: the radial force formed by the mechanical stirring of the paddle stirring blade has a strong shearing effect, which promotes the dispersion of large particle diameter solids and fully mixes with the biogas slurry, and avoids the phenomenon of crusting of materials; Under the pumping effect of the screw pump, the biogas slurry extraction pipe at the bottom of the tank forces the liquid inside the tank to flow in the circumferential direction, forming liquid circulation and stirring; the axial force formed by the propulsive stirring blade is adopted, and the shearing effect is small, avoiding In order to avoid damage to methane bacteria, the mechanical stirring of the paddle-type stirring blade and the liquid reflux stirring formed by the biogas slurry extraction pipe work together to form sufficient mixing and stirring, which improves the stirring effect and effectively reduces the power consumption of stirring. The utility model The structure is simple, the operation is convenient, and it is beneficial to popularization.
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为本实用新型的俯视部分结构示意图; Fig. 2 is the structural schematic diagram of the top view part of the utility model;
图中, 1-驱动装置、2-沼液喷淋口、3-罐体、4-沼液回流管、5-桨式搅拌叶、6-搅拌轴、7-出料口、8-螺杆泵、9-沼液抽取管、10-推进式搅拌叶、11-进料口、12-加热盘管、13-取样口、14-排气口、15-气柜。 In the figure, 1-driving device, 2-biogas slurry spray port, 3-tank, 4-biogas slurry return pipe, 5-paddle stirring blade, 6-stirring shaft, 7-outlet, 8-screw pump , 9-biogas slurry extraction pipe, 10-propelled stirring blade, 11-feed inlet, 12-heating coil, 13-sampling port, 14-exhaust port, 15-gas cabinet.
具体实施方式 Detailed ways
为了使本实用新型的目的、技术方案和有益效果更加清楚,下面将结合附图,对本实用新型的优选实施例进行详细的说明,对本实用新型做进一步说明,以方便技术人员理解。 In order to make the purpose, technical solutions and beneficial effects of the utility model clearer, the preferred embodiments of the utility model will be described in detail below in conjunction with the accompanying drawings, and the utility model will be further explained to facilitate the understanding of technical personnel.
如图1所示,一种推进搅拌式回流厌氧发酵罐,所述的推进搅拌式回流厌氧发酵罐包括:驱动装置1、沼液喷淋口2、罐体3、沼液回流管4、桨式搅拌叶5、搅拌轴6、出料口7、螺杆泵8、沼液抽取管9、推进式搅拌叶10、进料口11、加热盘管12、取样口13、排气口14、气柜15; As shown in Figure 1, a push-stirring type reflux anaerobic fermentation tank, said push-stirring type reflux anaerobic fermentation tank includes: a driving device 1, a biogas slurry spray port 2, a tank body 3, and a biogas slurry return pipe 4 , Paddle type stirring blade 5, stirring shaft 6, discharge port 7, screw pump 8, biogas slurry extraction pipe 9, propulsion type stirring blade 10, feed port 11, heating coil 12, sampling port 13, exhaust port 14 , gas cabinet 15;
所述的驱动装置1设置在罐体3的正上方,搅拌轴6与驱动装置1连接,搅拌轴6的上部设置有桨式搅拌叶5,搅拌轴6的下部设置有推进式搅拌叶10;采用桨式搅拌叶的机械式搅拌形成的径向作用力,具有强剪切作用,促使大粒径固形物分散和与沼液充分混合,避免物料产生结壳现象;采用推进式搅拌叶形成的轴向作用力,剪切作用小,避免了对甲烷菌的伤害; The driving device 1 is arranged directly above the tank body 3, the stirring shaft 6 is connected to the driving device 1, the top of the stirring shaft 6 is provided with a paddle type stirring blade 5, and the bottom part of the stirring shaft 6 is provided with a propulsion type stirring blade 10; The radial force formed by the mechanical stirring of the paddle stirring blade has a strong shearing effect, which promotes the dispersion of large particle size solids and fully mixes with the biogas slurry, and avoids the phenomenon of crusting of the material; Axial force, small shearing effect, avoiding damage to methanogens;
所述的罐体3顶部设置有排气口14,排气口14与气柜15相通,罐体3另一侧设置有沼液喷淋口2,沼液喷淋口2与沼液回流管4相连,沼液回流管4与螺杆泵8连接,罐体3的底部设置有沼液抽取管9,沼液抽取管9与螺杆泵8相连;罐体底部的沼液抽取管在螺杆泵的抽取作用下迫使罐体内部的液体产生圆周方向的流动,形成液体循环搅拌,桨式搅拌叶的机械式搅拌与沼液抽取管抽取沼液形成的液体回流搅拌共同作用,形成充分混合搅拌,提高了搅拌效果,有效降低搅拌消耗功率; The top of the tank body 3 is provided with an exhaust port 14, the exhaust port 14 communicates with the gas cabinet 15, and the other side of the tank body 3 is provided with a biogas slurry spray port 2, and the biogas slurry spray port 2 is connected to the biogas slurry return pipe 4 are connected, the biogas slurry return pipe 4 is connected with the screw pump 8, the bottom of the tank body 3 is provided with a biogas slurry extraction pipe 9, and the biogas slurry extraction pipe 9 is connected with the screw pump 8; Under the action of extraction, the liquid inside the tank is forced to flow in the circumferential direction, forming a liquid circulation stirring. The mechanical stirring of the paddle type stirring blade and the liquid reflux stirring formed by the biogas slurry extraction pipe to extract the biogas slurry work together to form sufficient mixing and stirring, improving Improve the stirring effect and effectively reduce the power consumption of stirring;
本实用新型的工作过程: Working process of the present utility model:
秸秆原料从进料口11进入到罐体3内,与罐体3内的甲烷菌在一定的温度下发酵产生甲烷气体,部分秸秆原料浮在液面上,通过设置在搅拌轴6上部的桨式搅拌叶5把秸秆原料打碎,同时利用螺杆泵8通过沼液抽取管9把罐体3内下部的沼液抽出,进入沼液回流管4中,通过设置在沼液回流管4上的沼液喷淋口2把沼液喷洒在罐体3的上部,使得上部的物料也能与甲烷菌进行发酵反应,不断地进行抽出和喷洒,形成了环状的液体回流搅拌,发酵过程中产生的甲烷气体通过设置在罐体上部的排气口14排出并通过气柜15收集,反应完成后的物料通过出料口7排出。 The straw raw material enters the tank body 3 from the feed port 11, and is fermented with the methane bacteria in the tank body 3 at a certain temperature to produce methane gas. Type stirring blade 5 crushes the raw material of straw, and at the same time uses screw pump 8 to extract the biogas slurry in the lower part of the tank body 3 through the biogas slurry extraction pipe 9, enters the biogas slurry return pipe 4, passes through the biogas slurry return pipe 4 The biogas slurry spray port 2 sprays the biogas slurry on the upper part of the tank body 3, so that the upper material can also undergo fermentation reaction with the methane bacteria, and is continuously extracted and sprayed to form a ring-shaped liquid reflux stirring, and the fermentation process produces The methane gas is discharged through the exhaust port 14 arranged on the upper part of the tank body and collected through the gas cabinet 15, and the material after the reaction is completed is discharged through the discharge port 7.
本实用新型采用桨式搅拌叶的机械式搅拌形成的径向作用力,具有强剪切作用,促使大粒径固形物分散和与沼液充分混合,避免物料产生结壳现象;罐体底部的沼液抽取管在螺杆泵的抽取作用下迫使罐体内部的液体产生圆周方向的流动,形成液体循环搅拌;采用推进式搅拌叶形成的轴向作用力,剪切作用小,避免了对甲烷菌的伤害,桨式搅拌叶的机械式搅拌与沼液抽取管抽取沼液形成的液体回流搅拌共同作用,形成充分混合搅拌,提高了搅拌效果,有效降低搅拌消耗功率,本实用新型结构简单,操作方便,利于推广。 The utility model adopts the radial force formed by the mechanical stirring of the paddle-type stirring blades, which has a strong shearing effect, promotes the dispersion of large-diameter solids and fully mixes with the biogas slurry, and avoids the phenomenon of crusting of materials; the bottom of the tank body Under the pumping action of the screw pump, the biogas slurry extraction pipe forces the liquid inside the tank to flow in the circumferential direction, forming liquid circulation and stirring; the axial force formed by the propulsion stirring blade is used, and the shearing effect is small, which avoids the impact on the methane bacteria. damage, the mechanical stirring of the paddle stirring blades and the liquid reflux stirring formed by the biogas slurry extraction pipe extracting the biogas slurry work together to form sufficient mixing and stirring, which improves the stirring effect and effectively reduces the power consumption of the stirring. The utility model has a simple structure and is easy to operate. Convenient and conducive to promotion.
最后说明的是,以上优选实施例仅用以说明本实用新型的技术方案而非限制,尽管通过上述优选实施例已经对本实用新型进行了详细的描述,但本领域技术人员应当理解,可以在形式上和细节上对其作出各种各样的改变,而不偏离本实用新型权利要求书所限定的范围。 Finally, it is noted that the above preferred embodiments are only used to illustrate the technical solutions of the present utility model without limitation. Although the utility model has been described in detail through the above preferred embodiments, those skilled in the art should understand that it can be described in the form Various changes can be made in the above and in the details without departing from the scope defined by the claims of the present invention.
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Cited By (7)
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CN106085826A (en) * | 2016-06-29 | 2016-11-09 | 东北师范大学 | A kind of methane-generating pit surges and stirs the Multifunctional treatment device combined with pump drainage |
CN106316033A (en) * | 2016-10-31 | 2017-01-11 | 广东新农村环保能源有限公司 | Automatic sewage management system |
CN106947687A (en) * | 2017-05-06 | 2017-07-14 | 赤峰中元晟华生物燃气项目建设有限责任公司 | A kind of big-and-middle-sized marsh-gas fermentation tank |
CN107555563A (en) * | 2017-10-01 | 2018-01-09 | 江苏华晖环保科技有限公司 | Stirring depositing reservoir and its technique in high-concentration salt-containing wastewater handling process |
CN108117980A (en) * | 2018-02-26 | 2018-06-05 | 滨州学院 | A kind of biological reaction container |
CN111484926A (en) * | 2020-04-21 | 2020-08-04 | 中国科学院广州能源研究所 | Mechanical and liquid spraying combined stirring device matched with anaerobic fermentation system |
CN115948238A (en) * | 2023-03-08 | 2023-04-11 | 江苏久久和牧农牧科技有限公司 | Pig feed bio-enzyme preparation equipment and preparation method |
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2014
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Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
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CN106085826A (en) * | 2016-06-29 | 2016-11-09 | 东北师范大学 | A kind of methane-generating pit surges and stirs the Multifunctional treatment device combined with pump drainage |
CN106085826B (en) * | 2016-06-29 | 2018-03-16 | 东北师范大学 | A kind of methane-generating pit surges the Multifunctional treatment device that is combined with pump drainage of stirring |
CN106316033A (en) * | 2016-10-31 | 2017-01-11 | 广东新农村环保能源有限公司 | Automatic sewage management system |
CN106947687A (en) * | 2017-05-06 | 2017-07-14 | 赤峰中元晟华生物燃气项目建设有限责任公司 | A kind of big-and-middle-sized marsh-gas fermentation tank |
CN107555563A (en) * | 2017-10-01 | 2018-01-09 | 江苏华晖环保科技有限公司 | Stirring depositing reservoir and its technique in high-concentration salt-containing wastewater handling process |
CN107555563B (en) * | 2017-10-01 | 2023-06-27 | 江苏华晖环保科技有限公司 | Stirring clarifier in high-concentration salt-containing wastewater treatment process and process thereof |
CN108117980A (en) * | 2018-02-26 | 2018-06-05 | 滨州学院 | A kind of biological reaction container |
CN111484926A (en) * | 2020-04-21 | 2020-08-04 | 中国科学院广州能源研究所 | Mechanical and liquid spraying combined stirring device matched with anaerobic fermentation system |
CN115948238A (en) * | 2023-03-08 | 2023-04-11 | 江苏久久和牧农牧科技有限公司 | Pig feed bio-enzyme preparation equipment and preparation method |
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