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CN103243020A - Water pressure type clean water methane tank hulling method and device - Google Patents

Water pressure type clean water methane tank hulling method and device Download PDF

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CN103243020A
CN103243020A CN2013101378516A CN201310137851A CN103243020A CN 103243020 A CN103243020 A CN 103243020A CN 2013101378516 A CN2013101378516 A CN 2013101378516A CN 201310137851 A CN201310137851 A CN 201310137851A CN 103243020 A CN103243020 A CN 103243020A
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water
biogas
crust layer
raw materials
shaped pipe
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曾广宇
李勇江
李金怀
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Hunan Academy of Forestry
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    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M21/00Bioreactors or fermenters specially adapted for specific uses
    • C12M21/04Bioreactors or fermenters specially adapted for specific uses for producing gas, e.g. biogas
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M29/00Means for introduction, extraction or recirculation of materials, e.g. pumps
    • C12M29/06Nozzles; Sprayers; Spargers; Diffusers
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

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Abstract

本发明公开了一种水压式沼气池清水破壳方法及采用的装置,在沼气池内的上方安装雾化喷头,连接雾化喷头的管道在池外形成U型管然后连接水阀,U型管的进水一端高度高于水压间储水最高度,U型管的底部弯折部位低于喷头底部。结壳后,通过定时将清水均匀喷在沼气池内的结壳层顶部,使结壳层部分位置打湿,重新让原料发酵,原料通过打湿及降解,减少原料横向张力,让结壳层下面产生的沼气及沼液通过这些部位溢出来,从而打破结壳层,完成破壳。本发明装置简单,成本低,操作简便,可提高池内原料利用率,实现发酵原料的多样化,提高沼气池的产气量,减少因结壳问题。

Figure 201310137851

The invention discloses a water pressure type biogas tank clear water shell breaking method and the device used. An atomizing nozzle is installed above the biogas tank, and the pipe connecting the atomizing nozzle forms a U-shaped pipe outside the pool and then connects a water valve. The U-shaped The height of the water inlet end of the pipe is higher than the highest water storage height in the water pressure room, and the bent part of the bottom of the U-shaped pipe is lower than the bottom of the nozzle. After incrustation, spray clean water evenly on the top of the crust layer in the biogas digester at regular intervals to wet part of the crust layer and ferment the raw materials again. The raw materials are wetted and degraded to reduce the lateral tension of the raw materials and let the crust layer below The generated biogas and biogas slurry overflow through these parts, thereby breaking the crust layer and completing the crust breaking. The invention has the advantages of simple device, low cost and easy operation, can increase the utilization rate of raw materials in the pond, realize the diversification of fermentation raw materials, increase the gas production of the biogas pit, and reduce the problem of crusting.

Figure 201310137851

Description

水压式沼气池清水破壳方法及采用的装置Water pressure biogas digester clear water shell breaking method and the device used

技术领域technical field

本发明涉及一种水压式沼气池清水破壳方法以及采用的装置。The invention relates to a method for breaking shells of a water pressure biogas digester with clear water and a device used.

背景技术Background technique

当前沼气发酵工艺有水压式工艺、全混合厌氧工艺(CSTR)、升流式厌氧污泥床反应器(UASB),IC反应器工艺等。在我国,水压式沼气工艺主要运用于户用沼气及中小型沼气工程中,水压式沼气池优点明显,建设及使用简单方便,成本也低,当前我国农村推广的沼气池95%以上都是水压式沼气池,但水压式沼气池也有其不足,其中不足之一就是没有防结壳及破壳功能。沼气池在发酵过程中,发酵原料浮于水面上,特别是牛粪及秸秆等易上浮物质,上浮物料由于高出水位而变干,导致不能进行降解发酵,就形成了一硬壳层,随着发酵原料的不断上浮,把上面原料顶起,结壳层越来越厚,有的甚至可以在其上站一个人。沼气池一旦结壳,就会使沼气池发酵的空间越来越少,顶部储气空间也越来越少,产气效果将会慢慢下降,久之则成为病池废池。由于当前农村沼气结壳现象普遍,结壳严重阻碍了农村沼气事业的发展,因而必须解决破壳难题。现有的水压式沼气池新增的破壳方法主要有出料口手动搅动发酵液破壳、沼液回流破壳、满池发酵破壳等,这些方法有其优点,但更多是局限性,不能完成破壳。如出料口手动搅动发酵液破壳方法,由于只能从下面搅动发酵原料,对上层发酵原料搅动不大,因而只能在预防结壳及刚结壳时才有些效果,如已结壳则不能破壳。沼液回流破壳方法想法非常好,但由于沼液很容易沉淀并堵塞回流管及出液孔,而且由于沼液需要通过手动或机械设施抽出池外再反喷到发酵间原料表面,常常有沼液溢出在池外面,导致池外又臭又脏,同时沼液抽取设施也容易生锈腐烂,因而不受农户欢迎,很难推广。满池发酵破壳有一定效果,但满池发酵需要另外建一个储气室,建池复杂,成本也更高,而且也很难解决顶部出气孔处不被封死、堵住。The current biogas fermentation process includes hydraulic process, fully mixed anaerobic process (CSTR), upflow anaerobic sludge bed reactor (UASB), IC reactor process, etc. In my country, the hydraulic biogas process is mainly used in household biogas and small and medium-sized biogas projects. The hydraulic biogas digester has obvious advantages, simple and convenient construction and use, and low cost. At present, more than 95% of the biogas digesters promoted in rural areas in my country are It is a hydraulic biogas digester, but the hydraulic biogas digester also has its shortcomings, one of which is that it does not have the functions of anti-crust and broken shells. During the fermentation process of the biogas digester, the fermentation raw materials float on the water surface, especially the easily floating substances such as cow dung and straw. The floating materials become dry because they are higher than the water level, so that they cannot be degraded and fermented, and a hard shell layer is formed. As the fermented raw materials continue to float up, the upper raw materials are lifted up, and the crust layer becomes thicker and thicker, and some can even stand on it. Once the biogas digester is encrusted, there will be less and less space for fermentation in the biogas digester, as well as less and less gas storage space at the top, and the effect of gas production will gradually decline, and over time it will become a sick pond and a waste pond. Due to the widespread phenomenon of crusting of biogas in rural areas, the crusting has seriously hindered the development of rural biogas industry, so the problem of shell breaking must be solved. The newly added shell breaking methods of the existing hydraulic biogas digesters mainly include manually stirring the fermentation liquid shell breaking at the outlet, biogas slurry backflow breaking shells, and full tank fermentation shell breaking. These methods have their advantages, but more are limitations Sex, cannot complete shell breaking. For example, the method of manually stirring the fermentation liquid at the discharge port to break the shell, because the fermentation raw materials can only be stirred from the bottom, and the upper layer of the fermentation raw materials is not stirred much, so it can only be effective in preventing crusting and just crusting. Can't break the shell. The idea of biogas slurry backflow to break the shell is very good, but because the biogas slurry is easy to settle and block the return pipe and liquid outlet hole, and because the biogas slurry needs to be pumped out of the tank by manual or mechanical means and then sprayed back to the surface of the raw material in the fermentation room, there are often problems The biogas slurry overflows outside the pond, causing the outside of the pond to be smelly and dirty. At the same time, the biogas slurry extraction facilities are also prone to rust and rot, so they are not welcomed by farmers and are difficult to promote. Fermentation in a full tank has a certain effect, but fermentation in a full tank requires an additional gas storage chamber, which is complicated to build and more expensive, and it is also difficult to prevent the air outlet at the top from being sealed or blocked.

发明内容Contents of the invention

本发明所要解决的技术问题是提供一种有效防止沼气池结壳、并有效处理沼气池结壳问题的水压式沼气池清水破壳方法以及采用的装置。The technical problem to be solved by the present invention is to provide a water pressure type biogas digester clear water shell breaking method and the device used to effectively prevent the biogas digester from encrusting and effectively deal with the biogas digester's encrustation problem.

本发明以如下技术方案解决上述技术问题:The present invention solves the above technical problems with the following technical solutions:

本发明水压式沼气池清水破壳方法,在沼气池内的顶部设置至少一个置于结壳层上方的雾化喷头,连接雾化喷头的管道在池外形成U型管,U型管连接水阀,通过定时将清水均匀喷在沼气池内的结壳层顶部,使结壳层部分位置打湿,重新让原料发酵,原料通过打湿及降解,减少原料横向张力,让结壳层下面产生的沼气及沼液通过这些部位溢出来,从而打破结壳层,完成破壳。The water pressure type biogas tank clear water shell breaking method of the present invention, at least one atomizing nozzle placed above the crust layer is arranged on the top of the biogas tank, the pipeline connecting the atomizing nozzle forms a U-shaped pipe outside the pool, and the U-shaped pipe connects the water Valve, by regularly spraying clean water evenly on the top of the crust layer in the biogas digester, so that part of the crust layer is wetted, and the raw materials are fermented again. The raw materials are wetted and degraded to reduce the lateral tension of the raw materials, and let the crust layer generated below Biogas and biogas slurry overflow through these parts, thereby breaking the crust layer and completing the crust breaking.

本发明水压式沼气池清水破壳采用的装置,在沼气池内的上方安装雾化喷头,连接雾化喷头的管道在池外形成U型管,U型管的另一端接通池外清水,U型管的进水一端高度高于水压间储水最高度,在不放水时起到水封防漏气作用,U型管的底部弯折部位低于喷头底部,以防止虹吸现象,导致U型管水全部从喷头流出。The device adopted by the water pressure biogas tank of the present invention is to install an atomizing nozzle above the biogas tank, and the pipe connecting the atomizing nozzle forms a U-shaped pipe outside the pool, and the other end of the U-shaped tube is connected to the clear water outside the pool. The height of the water inlet end of the U-shaped tube is higher than the highest water storage height in the water pressure room, and it acts as a water seal to prevent air leakage when the water is not released. U-shaped pipe water all flows out from the nozzle.

本发明具有如下有益效果:设施简单,成本低,不需要很多或很复杂的设备;操作简便,每次只需打开水龙头开关十多分钟就行;提高池内原料利用率,实现发酵原料的多样化,提高沼气池的产气量;减少因结壳问题导致的病池废池数,提高沼气使用率,产生能源,减少污染、提高生态效应。The invention has the following beneficial effects: simple facilities, low cost, no need for many or very complicated equipment; easy operation, only need to turn on the tap switch for more than ten minutes each time; improve the utilization rate of raw materials in the pool, realize the diversification of fermentation raw materials, Increase the gas production of biogas digesters; reduce the number of sick ponds and waste ponds caused by crusting problems, increase the utilization rate of biogas, generate energy, reduce pollution, and improve ecological effects.

附图说明Description of drawings

图1是本发明水压式沼气池清水破壳方法采用的装置的结构示意图。Fig. 1 is a structural schematic diagram of the device used in the water pressure biogas digester shell breaking method of the present invention.

图中:1—沼气池,2—发酵液,3—结壳层,4—水雾,5—导气口,6—雾化喷头,7—水封盖,8—PE管,9—水阀,10—U型管。In the figure: 1—digester, 2—fermentation liquid, 3—crust layer, 4—water mist, 5—air guide port, 6—atomizing nozzle, 7—water seal, 8—PE pipe, 9—water valve , 10-U-shaped tube.

具体实施方式Detailed ways

下面结合附图对本发明作进一步的描述。The present invention will be further described below in conjunction with the accompanying drawings.

如图1所示,在沼气池1内的顶部设置一个置于结壳层3上方的折射式雾化喷头6,折射式雾化喷头6安装在带有导气口5的水封盖7上,并使雾化喷头垂直向下20厘米左右,连接折射式雾化喷头6的PE管8在池外形成U型管10,U型管10的另一端接通池外清水并设有水阀9,U型管10的进水一端高度高于水压间11储水最高度,在不放水时可起到水封防漏气作用,U型管10的底部弯折部位低于折射式雾化喷头6的底部,以防止虹吸现象,导致U型管水全部从喷头流出;水压间11的水与沼气池1内的发酵液2相通。As shown in Figure 1, a refraction atomization nozzle 6 placed above the crust layer 3 is arranged on the top of the biogas digester 1, and the refraction atomization nozzle 6 is installed on a water seal 7 with an air guide port 5, Make the atomizing nozzle vertically downward about 20 cm, connect the PE pipe 8 of the refracting atomizing nozzle 6 to form a U-shaped pipe 10 outside the pool, and the other end of the U-shaped pipe 10 is connected to the clear water outside the pool and is provided with a water valve 9 , the height of the water inlet end of the U-shaped tube 10 is higher than the highest water storage height of the water pressure room 11, and can play a role of water seal and air leakage prevention when no water is released. The bottom of the nozzle 6 is to prevent the siphon phenomenon, causing the water in the U-shaped pipe to flow out from the nozzle;

本发明水压式沼气池清水破壳方法,是利用外来清水通过PE管8、U型管10进入折射式雾化喷头6,形成水雾4以大面积喷洒在结壳层3上。由于结壳层3本身是有机物,而且自身携带及在浮上来过程中携带了一些发酵微生物,因而在被打湿后,原料重新开始发酵降解,而且由于被打湿部位原料横向张力也明显下降,底层产生的沼气及沼液将从这里冒出,从而打破结壳,实现破壳。The clear water cracking method of the hydraulic biogas digester of the present invention is to use external clear water to enter the refraction atomizing nozzle 6 through the PE pipe 8 and the U-shaped pipe 10, and form a water mist 4 to spray on the crust layer 3 in a large area. Since the crust layer 3 itself is an organic matter, and carries some fermenting microorganisms in itself and during the process of floating up, after being wetted, the raw material starts to ferment and degrade again, and because the transverse tension of the raw material in the wetted part is also significantly reduced, The biogas and biogas slurry generated at the bottom will emerge from here, thereby breaking the crust and achieving shell breaking.

使用者在发现沼气池结壳后,打开水阀9十多分钟,让水通过雾化喷头6喷到结壳层3顶部,使结壳层3顶部一定面积原料被打湿,每天打开水阀开关一次,防止打湿原料重新变干,连续几天,开水时间逐渐缩短。原料被打湿后,原料横向张力将逐渐变小,同时原料也会重新开始降解,几天后结壳层下面产生的沼气及水压间水的压力会使底层沼气及发酵液从此口溢出,从而完成破壳,破壳后,水压间水位将会有明显降低。由于打湿结壳层原料所需水量相对发酵间水量微乎其微,因而新加得水对发酵间发酵微生物几乎没有影响。外来清水可以是自来水、农户自己抽到水箱使用的水及其它任何与沼气池有高差的清水。如果发酵间容积大于20立方米,建议安装2个以上喷头,安装位置根据喷雾距离,尽量使所有喷头喷出的水雾能尽量覆盖结壳层。After discovering the encrustation in the biogas digester, the user opens the water valve 9 for more than ten minutes, allowing water to be sprayed to the top of the encrustation layer 3 through the atomizing nozzle 6, so that a certain area of raw materials on the top of the encrustation layer 3 is wetted, and the water valve is opened every day Turn it on and off once to prevent the wet ingredients from drying out again. For several days, the boiling time will gradually shorten. After the raw material is wetted, the lateral tension of the raw material will gradually decrease, and the raw material will start to degrade again at the same time. After a few days, the pressure of the water between the biogas and water pressure generated under the crust layer will cause the bottom biogas and fermentation liquid to overflow from the mouth. Thereby completing shell breaking, after shell breaking, the water level in the water pressure room will be significantly reduced. Since the amount of water needed to wet the raw material of the crust layer is negligible relative to the amount of water in the fermentation room, the newly added water has almost no effect on the fermentation microorganisms in the fermentation room. External clean water can be tap water, water pumped by the farmers themselves to the water tank and any other clean water that has a height difference from the biogas digester. If the volume of the fermentation room is greater than 20 cubic meters, it is recommended to install more than 2 nozzles. The installation position is based on the spraying distance, so that the water mist sprayed by all the nozzles can cover the crust layer as much as possible.

实施例Example

以8立方水压式户用沼气池为例,发酵原料主要为牛粪,如已结壳,且结壳厚度为20cm。打开雾化喷头的进水开关以及水阀15分钟将清水喷到结壳层顶部,喷进的水大约9升左右,水雾将结壳层中心一大块结壳层打湿,第二天打开开关10分钟左右,保持已打湿的结壳原料湿度,维持原料发酵,如此连续一周左右,停止喷水,如还没破壳,则每2天喷10分钟水,如此大约10天左右将破壳。结壳厚度越厚开水时间可以相应加长,破壳时间根据结壳厚度、结壳原料性质、喷水时间等不同有所变化。利用此装置,如每隔5-8天开一次水阀,则也可以避免结壳。Take the 8 cubic water pressure household biogas digester as an example, the fermentation raw material is mainly cow dung, if it has crusted, and the thickness of the crust is 20cm. Turn on the water inlet switch and water valve of the atomizing nozzle and spray clean water on the top of the crust layer for 15 minutes. The sprayed water is about 9 liters, and the water mist will wet a large crust layer in the center of the crust layer. The next day Turn on the switch for about 10 minutes, keep the humidity of the wet crusted raw materials, and keep the raw materials fermented. After about a week, stop spraying water. If the shell has not been broken, spray water for 10 minutes every 2 days, so about 10 days. Broken shell. The thicker the crust, the boiling water time can be lengthened accordingly, and the cracking time varies according to the thickness of the crust, the properties of the crust raw material, and the water spraying time. Using this device, if the water valve is opened once every 5-8 days, crusting can also be avoided.

Claims (2)

1. hydraulic type biomass pool clear water shell breaking method, it is characterized in that, top in methane-generating pit arranges at least one and places atomizer above the crust layer, the pipeline that connects atomizer forms U-shaped pipe and connects water valve then outside the pond, the crust back is by regularly evenly being sprayed on clear water the crust layer top in the methane-generating pit, crust layer segment position is drenched, again allow fermenting raw materials, raw material is by drenching and degrading, reduce the raw material horizontal tension, the biogas and the natural pond liquid that allow the crust layer produce below overflow by these positions, thereby break the crust layer, finish broken shell.
2. the device that adopts of hydraulic type biomass pool clear water broken shell, it is characterized in that, atomizer is installed above in methane-generating pit, the pipeline that connects atomizer forms U-shaped pipe outside the pond, the other end of U-shaped pipe is connected clear water outside the pond, and the water inlet one end height of U-shaped pipe is higher than water pressure house water storage topnotch, when not discharging water, play the effect of water seal anti-gas-leak, the bottom bending part of U-shaped pipe is lower than the shower nozzle bottom, to prevent siphonage, causes U-shaped pipe water all to flow out from shower nozzle.
CN2013101378516A 2013-04-19 2013-04-19 Water pressure type clean water methane tank hulling method and device Pending CN103243020A (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104877902A (en) * 2015-05-08 2015-09-02 张家港市天源机械制造有限公司 Biogas fermentation tank
CN113956956A (en) * 2021-08-19 2022-01-21 王兴旺 Fermentation vat is collected to marsh gas
CN115124197A (en) * 2022-07-21 2022-09-30 重庆大学 Tower type filter tank for treating macromolecular degradation-resistant pollutants and treatment method

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CN200985329Y (en) * 2006-12-19 2007-12-05 青岛天人环境工程有限公司 Device for preventing and eliminating scum from crusting in anaerobic reaction tank
CN201473535U (en) * 2009-07-06 2010-05-19 陈诗礼 Methane tank shell-crushing and stirring device
CN102212462A (en) * 2011-05-13 2011-10-12 沈阳农业大学 Solid phase and liquid phase integrated methane fermenting device

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CN200985329Y (en) * 2006-12-19 2007-12-05 青岛天人环境工程有限公司 Device for preventing and eliminating scum from crusting in anaerobic reaction tank
CN201473535U (en) * 2009-07-06 2010-05-19 陈诗礼 Methane tank shell-crushing and stirring device
CN102212462A (en) * 2011-05-13 2011-10-12 沈阳农业大学 Solid phase and liquid phase integrated methane fermenting device

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104877902A (en) * 2015-05-08 2015-09-02 张家港市天源机械制造有限公司 Biogas fermentation tank
CN104877902B (en) * 2015-05-08 2017-09-12 张家港市天源机械制造有限公司 Marsh-gas fermentation tank
CN113956956A (en) * 2021-08-19 2022-01-21 王兴旺 Fermentation vat is collected to marsh gas
CN115124197A (en) * 2022-07-21 2022-09-30 重庆大学 Tower type filter tank for treating macromolecular degradation-resistant pollutants and treatment method
CN115124197B (en) * 2022-07-21 2023-11-03 重庆大学 Tower filter and treatment method for treating macromolecular refractory pollutants

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Application publication date: 20130814