CN205528747U - Fermenting installation is used in laboratory - Google Patents
Fermenting installation is used in laboratory Download PDFInfo
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- CN205528747U CN205528747U CN201620038783.7U CN201620038783U CN205528747U CN 205528747 U CN205528747 U CN 205528747U CN 201620038783 U CN201620038783 U CN 201620038783U CN 205528747 U CN205528747 U CN 205528747U
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- 238000009434 installation Methods 0.000 title claims abstract 8
- 238000000855 fermentation Methods 0.000 claims abstract description 42
- 230000004151 fermentation Effects 0.000 claims abstract description 38
- 238000000605 extraction Methods 0.000 claims abstract description 27
- 238000010438 heat treatment Methods 0.000 claims abstract description 9
- 239000002002 slurry Substances 0.000 claims description 51
- 238000007599 discharging Methods 0.000 claims 2
- 238000003756 stirring Methods 0.000 abstract description 43
- 239000002994 raw material Substances 0.000 abstract description 22
- 230000000694 effects Effects 0.000 abstract description 17
- 239000007788 liquid Substances 0.000 abstract description 17
- 239000000463 material Substances 0.000 abstract description 9
- 238000002156 mixing Methods 0.000 abstract description 7
- 239000006185 dispersion Substances 0.000 abstract description 5
- 238000010907 mechanical stirring Methods 0.000 abstract description 4
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 239000010902 straw Substances 0.000 abstract description 3
- 230000015572 biosynthetic process Effects 0.000 abstract 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 16
- 238000013019 agitation Methods 0.000 description 10
- 238000006243 chemical reaction Methods 0.000 description 7
- 241000894006 Bacteria Species 0.000 description 5
- 238000010008 shearing Methods 0.000 description 4
- 238000010992 reflux Methods 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 2
- 230000002301 combined effect Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000002699 waste material 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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Abstract
Description
技术领域 technical field
本实用新型公开了一种实验室用发酵装置,属于发酵设备领域。 The utility model discloses a laboratory fermentation device, which belongs to the field of fermentation equipment.
背景技术 Background technique
在实验室里采用厌氧发酵制沼气可以为实际的沼气生产提供有力的科学技术支撑,尤其是在实验室里所做的分析和实验所得的结论,对于实际生产具有重要的指导意义,好的厌氧发酵罐要通过搅拌,实现良好的传质和传热效果,并且功率消耗要低,常用的厌氧发酵罐存在内部搅拌不充分,搅拌消耗功率大的缺点,秸秆原料进入发酵罐后浮在液面上,容易产生结壳现象,并且大块的物料不能被破碎,不利于搅拌和发酵反应的继续。 The use of anaerobic fermentation to produce biogas in the laboratory can provide strong scientific and technical support for the actual biogas production, especially the conclusions obtained from the analysis and experiments done in the laboratory have important guiding significance for the actual production, okay The anaerobic fermentation tank should be stirred to achieve good mass and heat transfer effects, and the power consumption should be low. Commonly used anaerobic fermentation tanks have the disadvantages of insufficient internal stirring and high power consumption. Straw raw materials float after entering the fermentation tank. On the liquid surface, crusting is easy to occur, and large pieces of material cannot be broken, which is not conducive to the continuation of stirring and fermentation reactions.
甲烷菌群主要集中在发酵罐的中部和下部,现有技术为机械式搅拌,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,同时,机械产生的作用力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。 The methane bacteria group is mainly concentrated in the middle and lower parts of the fermenter. The existing technology is mechanical stirring. It is difficult to stir the methane bacteria in the middle and lower part of the fermenter to the upper part of the fermenter with ordinary mechanical stirring, so that the fermentation in the upper part of the fermenter is not complete, resulting in There is less methane gas, and it causes waste of raw materials. At the same time, the force generated by the machine is easy to cause damage to the methane bacteria in the middle and lower parts of the fermenter, which affects the effect of fermentation.
因此,有必要对现有的实验室用发酵装置进行改进,使得实验室用沼气发酵装置能够结构完善,发酵效率高。 Therefore, it is necessary to improve the existing laboratory fermentation device, so that the laboratory biogas fermentation device can have a perfect structure and high fermentation efficiency.
发明内容 Contents of the invention
为了克服背景技术中存在的问题,本实用新型提供了一种实验室用发酵装置,在发酵之前对物料进行预处理,使得发酵效果更好,发酵更完全;在发酵罐内部设置桨式搅拌叶,其产生的径向作用力具有强剪切作用,促使原料的分散和原料与沼液的充分混合,避免物料产生结壳现象;同时,利用螺杆泵使罐体内部的沼液循环流动,形成液体搅拌,将机械搅拌与液体搅拌共同作用,提高了搅拌效果,使反应进行的更彻底,有效降低搅拌消耗功率;本实用新型结构简单,成本低廉,而且操作方便。 In order to overcome the problems in the background technology, the utility model provides a laboratory fermentation device, which pretreats the material before fermentation, so that the fermentation effect is better and the fermentation is more complete; a paddle-type stirring blade is arranged inside the fermentation tank , the radial force produced by it has a strong shearing effect, which promotes the dispersion of raw materials and the full mixing of raw materials and biogas slurry, and avoids the phenomenon of crusting of materials; at the same time, the biogas slurry inside the tank is circulated by using a screw pump to form Liquid agitation, the combination of mechanical agitation and liquid agitation improves the agitation effect, makes the reaction more thorough, and effectively reduces the power consumption of agitation; the utility model has the advantages of simple structure, low cost and convenient operation.
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:
所述的实验室用发酵装置包括预处理装置和发酵罐,所述的发酵罐包括驱动装置、搅拌轴、搅拌叶、出料口、加热盘管、罐体、沼液抽取管、进料口、沼液回流管、排气口;所述的预处理装置与发酵罐的进料口连接,所述的驱动装置设置在罐体外部的正上方,罐体的顶部设有排气口,搅拌轴与驱动装置相连,搅拌轴上设置有搅拌叶,搅拌叶为桨式搅拌叶,罐体的底部一侧设有沼液抽取管,沼液抽取管连接沼液回流管,罐体的下部一侧设置有出料口,罐体的上部一侧设置有进料口,罐体内壁设有加热盘管。 The laboratory fermentation device includes a pretreatment device and a fermenter, and the fermenter includes a driving device, a stirring shaft, a stirring blade, a discharge port, a heating coil, a tank body, a biogas slurry extraction pipe, and a feed port , a biogas slurry return pipe, and an exhaust port; the pretreatment device is connected to the feed port of the fermenter, the drive device is arranged directly above the outside of the tank, and the top of the tank is provided with an exhaust port, stirring The shaft is connected with the driving device, and the stirring shaft is equipped with a stirring blade, which is a paddle-type stirring blade. The bottom side of the tank is provided with a biogas slurry extraction pipe, and the biogas slurry extraction pipe is connected to the biogas slurry return pipe. The lower part of the tank is a The side is provided with a discharge port, the upper side of the tank is provided with a feed port, and the inner wall of the tank is provided with a heating coil.
进一步,所述的搅拌叶安装在罐体内的上部。 Further, the stirring blade is installed on the upper part of the tank body.
进一步,所述的预处理装置和沼液抽取管上分别设有泵体Ⅰ和泵体Ⅱ。 Further, the pretreatment device and the biogas slurry extraction pipe are respectively provided with a pump body I and a pump body II.
进一步,所述的沼液抽取管与罐体连接处设有过滤网。 Further, a filter screen is provided at the connection between the biogas slurry extraction pipe and the tank body.
本实用新型的有益效果: The beneficial effects of the utility model:
本实用新型采用在发酵罐之前设置有预处理装置,对原料在发酵之前进行预处理,使得发酵效果更好,发酵更完全;在发酵罐内部设置桨式搅拌叶,其产生的径向作用力具有强剪切作用,促使原料的分散和原料与沼液的充分混合,避免物料产生结壳现象;同时,利用泵体Ⅱ使罐体内部的沼液循环流动,形成液体搅拌,将机械搅拌与液体搅拌共同作用,提高了搅拌效果,使反应进行的更彻底,有效降低搅拌消耗功率;沼液抽取管与泵体连接处设有过滤网,能够在沼液进入沼液抽取管之前进行过滤,避免沼液抽取管的堵塞;本实用新型结构简单,成本低廉,而且操作方便。 The utility model adopts that a pretreatment device is arranged in front of the fermentation tank, and the raw materials are pretreated before fermentation, so that the fermentation effect is better and the fermentation is more complete; a paddle-type stirring blade is arranged inside the fermentation tank, and the radial force generated by it It has a strong shearing effect, promotes the dispersion of raw materials and the full mixing of raw materials and biogas slurry, and avoids the phenomenon of crusting of materials; at the same time, the pump body II is used to circulate the biogas slurry inside the tank to form liquid agitation, and mechanical agitation and biogas slurry are combined. The combined effect of liquid stirring improves the stirring effect, makes the reaction more thorough, and effectively reduces the power consumption of stirring; a filter is installed at the connection between the biogas slurry extraction pipe and the pump body, which can filter the biogas slurry before entering the biogas slurry extraction pipe, The blockage of the biogas slurry extraction pipe is avoided; the utility model has the advantages of simple structure, low cost and convenient operation.
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.
图中,1-预处理装置、2-发酵罐、3-驱动装置、4-搅拌轴、5-搅拌叶、6-出料口、7-加热盘管、8-罐体、9-沼液抽取管、10-进料口、11-沼液回流管、12-排气口、13-泵体Ⅰ、14-泵体Ⅱ、15-过滤网。 In the figure, 1-pretreatment device, 2-fermentation tank, 3-driving device, 4-stirring shaft, 5-stirring blade, 6-outlet, 7-heating coil, 8-tank, 9-biogas slurry Extraction pipe, 10-feed inlet, 11-biogas slurry return pipe, 12-exhaust port, 13-pump body I, 14-pump body II, 15-filter.
具体实施方式 detailed description
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,以方便技术人员理解。 In order to make the purpose, technical solutions and beneficial effects of the present utility model clearer, the preferred embodiments of the present utility model will be described in detail below in conjunction with the accompanying drawings, so as to facilitate the understanding of technical personnel.
如图1所示,所述的实验室用发酵装置包括预处理装置1和发酵罐2,所述的发酵罐2包括驱动装置3、搅拌轴4、搅拌叶5、出料口6、加热盘管7、罐体8、沼液抽取管9、进料口10、沼液回流管11、排气口12;所述的预处理装置1与发酵罐2的进料口10连接,预处理装置1上设有泵体Ⅰ13,对原料在发酵之前对其进行预处理,预处理完成之后的原料通过泵体Ⅰ13从进料口10进入到罐体8中,使得发酵效果更好,发酵更完全; As shown in Figure 1, the described laboratory fermentation device includes a pretreatment device 1 and a fermenter 2, and the fermenter 2 includes a driving device 3, a stirring shaft 4, a stirring blade 5, a discharge port 6, a heating plate Pipe 7, tank body 8, biogas slurry extraction pipe 9, feed port 10, biogas slurry return pipe 11, exhaust port 12; the pretreatment device 1 is connected to the feed port 10 of the fermenter 2, and the pretreatment device 1 is equipped with a pump body I13 to pretreat the raw materials before fermentation. After the pretreatment is completed, the raw materials enter the tank body 8 from the feed port 10 through the pump body I13, so that the fermentation effect is better and the fermentation is more complete. ;
所述的驱动装置3设置在罐体8外部的正上方,罐体8的顶部设有排气口12,搅拌轴4与驱动装置3相连,搅拌轴4上设置有搅拌叶5,搅拌叶5安装在罐体8内的上部,搅拌叶5为桨式搅拌叶,设置在罐体内上部的搅拌叶5产生的径向作用力具有强剪切作用,促使原料的分散和原料与沼液的充分混合作用,并避免物料产生结壳现象; The drive device 3 is arranged directly above the outside of the tank body 8, the top of the tank body 8 is provided with an air outlet 12, the stirring shaft 4 is connected to the drive device 3, the stirring shaft 4 is provided with a stirring blade 5, and the stirring blade 5 Installed in the upper part of the tank body 8, the stirring blade 5 is a paddle-type stirring blade, and the radial force generated by the stirring blade 5 arranged on the upper part of the tank body has a strong shearing effect, which promotes the dispersion of raw materials and the full mixing of raw materials and biogas slurry. Mixing effect and avoid crusting of materials;
罐体8的底部一侧设有沼液抽取管9,沼液抽取管9连接沼液回流管11,沼液抽取管9上设有泵体Ⅱ14,罐体8的下部一侧设置有出料口6,罐体8的上部一侧设置有进料口10,罐体8内壁设有加热盘管7,罐体8底部的沼液在泵体Ⅱ14的抽取作用下迫使罐体8内部的沼液循环流动,形成液体搅拌,桨式搅拌叶的机械搅拌与沼液抽取回流的循环流动,对沼液共同作用,充分的混合搅拌,提高了搅拌效果,使反应进行的更彻底,有效降低搅拌消耗功率,加热盘管7能够对原料进行加热,加快发酵速率; A biogas slurry extraction pipe 9 is provided on the bottom side of the tank body 8, and the biogas slurry extraction pipe 9 is connected to the biogas slurry return pipe 11. The biogas slurry extraction pipe 9 is provided with a pump body II14, and the bottom side of the tank body 8 is provided with a discharge 6, the upper side of the tank body 8 is provided with a feed inlet 10, and the inner wall of the tank body 8 is provided with a heating coil 7, and the biogas slurry at the bottom of the tank body 8 is forced by the pump body II14 to force the biogas slurry inside the tank body 8 Liquid circulation flow forms liquid stirring. The mechanical stirring of paddle stirring blades and the circulating flow of biogas slurry extraction and reflux work together on the biogas slurry to fully mix and stir, which improves the stirring effect, makes the reaction more thorough, and effectively reduces the agitation. Power consumption, the heating coil 7 can heat the raw materials to speed up the fermentation rate;
沼液抽取管9与罐体连接处设有过滤网15,能够在沼液进入沼液抽取管9之前进行过滤,避免沼液抽取管9的堵塞;本实用新型结构简单,成本低廉,而且操作方便。 A filter screen 15 is provided at the connection between the biogas slurry extraction pipe 9 and the tank body, which can filter the biogas slurry before entering the biogas slurry extraction pipe 9, so as to avoid the blockage of the biogas slurry extraction pipe 9; the utility model has simple structure, low cost, and easy operation convenient.
本实用新型的工作过程: Working process of the present utility model:
对原料在发酵之前对其进行预处理,预处理完成之后的原料通过泵体Ⅰ13从进料口10进入到罐体8中,原料通过进料口10进入到罐体8内,与罐体8内的甲烷菌在一定的温度下发酵产生甲烷气体,部分原料浮在液面上,通过设置在搅拌轴4上的搅拌叶5把原料打碎,同时利用泵体Ⅱ14通过沼液抽取管9把罐体8下部的沼液抽出,在进入罐体8之前,过滤网15将沼液进行过滤,通过沼液回流管11回流到罐体8内,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、回流,形成了液体回流搅拌,发酵过程中产生的甲烷气体通过设置在罐体8上部的排气口12排出并收集,反应完成后的物料通过出料口6排出。 The raw materials are pretreated before fermentation. After the pretreatment, the raw materials enter the tank body 8 from the feed port 10 through the pump body I13, and the raw materials enter the tank body 8 through the feed port 10, and the tank body 8 The methane bacteria inside ferment at a certain temperature to produce methane gas, and part of the raw materials float on the liquid surface. The raw materials are crushed by the stirring blade 5 arranged on the stirring shaft 4, and at the same time, the pump body II14 is used to pass the biogas slurry extraction pipe 9 The biogas slurry from the lower part of the tank body 8 is pumped out. Before entering the tank body 8, the filter screen 15 filters the biogas slurry, and returns it to the tank body 8 through the biogas slurry return pipe 11, so that the upper material can also undergo fermentation reaction with methane bacteria. , continuously extracting and refluxing to form liquid reflux stirring, methane gas generated during the fermentation process is discharged and collected through the exhaust port 12 arranged on the upper part of the tank body 8, and the material after the reaction is completed is discharged through the discharge port 6.
本实用新型采用在发酵罐之前设置有预处理装置,对原料在发酵之前进行预处理,使得发酵效果更好,发酵更完全;在发酵罐内部设置桨式搅拌叶,其产生的径向作用力具有强剪切作用,促使原料的分散和原料与沼液的充分混合,避免物料产生结壳现象;同时,利用泵体Ⅱ使罐体内部的沼液循环流动,形成液体搅拌,将机械搅拌与液体搅拌共同作用,提高了搅拌效果,使反应进行的更彻底,有效降低搅拌消耗功率;沼液抽取管与泵体连接处设有过滤网,能够在沼液进入沼液抽取管之前进行过滤,避免沼液抽取管的堵塞;本实用新型结构简单,成本低廉,而且操作方便。 The utility model adopts that a pretreatment device is arranged in front of the fermentation tank, and the raw materials are pretreated before fermentation, so that the fermentation effect is better and the fermentation is more complete; a paddle-type stirring blade is arranged inside the fermentation tank, and the radial force generated by it It has a strong shearing effect, promotes the dispersion of raw materials and the full mixing of raw materials and biogas slurry, and avoids the phenomenon of crusting of materials; at the same time, the pump body II is used to circulate the biogas slurry inside the tank to form liquid agitation, and mechanical agitation and biogas slurry are combined. The combined effect of liquid stirring improves the stirring effect, makes the reaction more thorough, and effectively reduces the power consumption of stirring; a filter is installed at the connection between the biogas slurry extraction pipe and the pump body, which can filter the biogas slurry before entering the biogas slurry extraction pipe, The blockage of the biogas slurry extraction pipe is avoided; the utility model has the advantages of simple structure, low cost and convenient operation.
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 (5)
Publication number | Priority date | Publication date | Assignee | Title |
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CN107399993A (en) * | 2017-08-31 | 2017-11-28 | 北京沃尔夫斯科技有限公司 | A kind of kitchen garbage aerobic sigestion system |
CN107446817A (en) * | 2017-09-26 | 2017-12-08 | 天津农学院 | A kind of use for laboratory anaerobic fermentation tank and manufacture method |
CN108164300A (en) * | 2016-12-07 | 2018-06-15 | 深圳市祁科作物科技有限公司 | A kind of fermentation tank and its fermentation process and purposes |
CN108176129A (en) * | 2018-01-03 | 2018-06-19 | 陈瑾 | It is a kind of to be used to purify the equipment that biogas slurry organic matter is used as animal and fowl fodder |
CN112940911A (en) * | 2021-03-01 | 2021-06-11 | 王锐群 | Biomass natural gas fermentation tank |
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2016
- 2016-01-17 CN CN201620038783.7U patent/CN205528747U/en not_active Expired - Fee Related
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
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CN108164300A (en) * | 2016-12-07 | 2018-06-15 | 深圳市祁科作物科技有限公司 | A kind of fermentation tank and its fermentation process and purposes |
CN107399993A (en) * | 2017-08-31 | 2017-11-28 | 北京沃尔夫斯科技有限公司 | A kind of kitchen garbage aerobic sigestion system |
CN107446817A (en) * | 2017-09-26 | 2017-12-08 | 天津农学院 | A kind of use for laboratory anaerobic fermentation tank and manufacture method |
CN108176129A (en) * | 2018-01-03 | 2018-06-19 | 陈瑾 | It is a kind of to be used to purify the equipment that biogas slurry organic matter is used as animal and fowl fodder |
CN108176129B (en) * | 2018-01-03 | 2023-08-25 | 陈瑾 | Equipment for purifying biogas slurry organic matters to be used as livestock and poultry feed |
CN112940911A (en) * | 2021-03-01 | 2021-06-11 | 王锐群 | Biomass natural gas fermentation tank |
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