CN105820943A - Multistage gas-liquid combined stirring Venturi tube-CSTR reactor - Google Patents

Multistage gas-liquid combined stirring Venturi tube-CSTR reactor Download PDF

Info

Publication number
CN105820943A
CN105820943A CN201510285452.3A CN201510285452A CN105820943A CN 105820943 A CN105820943 A CN 105820943A CN 201510285452 A CN201510285452 A CN 201510285452A CN 105820943 A CN105820943 A CN 105820943A
Authority
CN
China
Prior art keywords
stirring
venturi tube
fermentation
liquid
gas
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CN201510285452.3A
Other languages
Chinese (zh)
Other versions
CN105820943B (en
Inventor
张无敌
刘健峰
尹芳
赵兴玲
田光亮
杨斌
柳静
王昌梅
杨红
刘士清
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Yunnan Normal University
Original Assignee
Yunnan Normal University
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Yunnan Normal University filed Critical Yunnan Normal University
Priority to CN201510285452.3A priority Critical patent/CN105820943B/en
Publication of CN105820943A publication Critical patent/CN105820943A/en
Application granted granted Critical
Publication of CN105820943B publication Critical patent/CN105820943B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • 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
    • C12M29/18External loop; Means for reintroduction of fermented biomass or liquid percolate
    • 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
    • C12M41/00Means for regulation, monitoring, measurement or control, e.g. flow regulation
    • C12M41/48Automatic or computerized control
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Organic Chemistry (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Zoology (AREA)
  • Wood Science & Technology (AREA)
  • Genetics & Genomics (AREA)
  • Sustainable Development (AREA)
  • Microbiology (AREA)
  • Biotechnology (AREA)
  • Biomedical Technology (AREA)
  • Biochemistry (AREA)
  • General Engineering & Computer Science (AREA)
  • General Health & Medical Sciences (AREA)
  • Molecular Biology (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Computer Hardware Design (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Apparatus Associated With Microorganisms And Enzymes (AREA)
  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)

Abstract

本发明公开了一种多级气液联合搅拌文丘里管—CSTR反应装置,其包括连续搅拌全混合厌氧反应器、文丘里管、多级外循环管路。本发明利用文丘里管实现了气液联合搅拌的效果,用泵把发酵液吸出,再通过文丘里管将其射入,沼气在射入位置的上部形成搅拌作用,而且可以达到防止发酵液上层结壳的效果,液体在射入位置的下部形成搅拌作用,可以根据发酵过程的不同情况,对发酵原料进行不同形式、不同程度的搅拌,缩短了水力滞留时间,大大提高了反应器的处理效率,另一方面该装置配备有自动化控制设备和变速器,实现定时自动进料、自动搅拌,并且可以根据发酵过程的不同情况,对发酵原料进行不同形式、不同程度的搅拌。

The invention discloses a multi-stage gas-liquid combined stirring Venturi tube-CSTR reaction device, which comprises a continuous stirring fully mixed anaerobic reactor, a Venturi tube, and a multi-stage external circulation pipeline. The present invention utilizes the Venturi tube to achieve the effect of gas-liquid combined stirring, sucks out the fermentation liquid with a pump, and then injects it through the Venturi tube, and the biogas forms a stirring effect at the upper part of the injection position, and can prevent the upper layer of the fermentation liquid from The effect of crusting, the liquid forms agitation at the lower part of the injection position, and the fermentation raw materials can be stirred in different forms and in different degrees according to the different conditions of the fermentation process, which shortens the hydraulic retention time and greatly improves the processing efficiency of the reactor. , On the other hand, the device is equipped with automatic control equipment and transmission to realize timing automatic feeding and automatic stirring, and can carry out different forms and different degrees of stirring on the fermentation raw materials according to different conditions of the fermentation process.

Description

一种多级气液联合搅拌文丘里管-CSTR反应装置A multi-stage gas-liquid combined stirring Venturi tube-CSTR reaction device

技术领域 technical field

本发明涉及一种基于文丘里管和CSTR全混合厌氧反应装置的多级气液联合搅拌系统,属于沼气发酵装备技术领域。 The invention relates to a multi-stage gas-liquid combined stirring system based on a venturi tube and a CSTR full-mix anaerobic reaction device, belonging to the technical field of biogas fermentation equipment.

背景技术 Background technique

沼气发酵是一种处理有机废弃物,实现废弃物的资源化利用的有效途径。通过沼气发酵过程,可以将有机物经过微生物的分解作用,产生清洁能源沼气,实现有机废弃物的资源化利用,沼气发酵已经成为农业循环经济发展模式的重要纽带。厌氧消化过程中,混合搅拌技术的应用,可以有效地解决因微生物和可降解有机物无法实际接触而造成的传质困难以及物理、化学和生物学性状不均匀等问题,从而改善反应器的性能并提高厌氧消化的产气速率。 Biogas fermentation is an effective way to treat organic waste and realize resource utilization of waste. Through the biogas fermentation process, organic matter can be decomposed by microorganisms to produce clean energy biogas and realize the resource utilization of organic waste. Biogas fermentation has become an important link in the development model of agricultural circular economy. In the process of anaerobic digestion, the application of mixing and stirring technology can effectively solve the problems of mass transfer difficulties and uneven physical, chemical and biological properties caused by the inability of microorganisms and degradable organic matter to actually contact, thereby improving the performance of the reactor And increase the gas production rate of anaerobic digestion.

现行的沼气发酵工艺中的搅拌方式有人工搅拌、机械搅拌、气体搅拌、液体搅拌等,但这些搅拌方式都存在一定的问题:1)人工搅拌:多用于实验室中,发酵装置容积较小,通过定时摇晃发酵瓶,达到搅拌混合发酵液的目的。但是,对于秸秆性原料和高浓度的发酵,人工搅拌达不到混合的目的,同时发酵表面浮渣硬化,阻碍沼气收集;2)机械搅拌:机械搅拌是使用各种安装形式的机械装置,通过各种形式的机械运动使物料达到混合状态的一种搅拌方式。此种搅拌方式可以产生强大的剪切作用,可以借助搅拌叶片的转动来打碎消化原料,有利于高粘度物料混合,主要用于实验室发酵装置和沼气工程。但是,由于发酵时间过长,搅拌装置需要长期运转,特别是在沼气工程中,机械搅拌装置长期浸泡在发酵液中,容易造成装置的腐蚀,在腐蚀后,需要更换搅拌装置,在更换的同时,需要开启发酵装置,此时容易造成发酵罐体漏气,影响沼气发酵的正常运行,同时此种方式能耗大,成本高,操作复杂且不利于产气;3)液体搅拌:液体搅拌一般利用泵运转所产生的液体流动来完成对物料的搅拌,利用发酵液本身,通过泵抽取发酵液,再通过其冲击作用,打破发酵液表面结壳,实现发酵液搅拌,是一种能耗低,操作简单,保证罐体密封性的搅拌方式,但是液体搅拌会引起压力或发酵器内局部压力的增加,不利于发酵;4)气体搅拌:气体搅拌就是通过气泡在物料中的运动来实现对物料搅拌的目的,在沼气发酵中,气体搅拌主要指沼气循环搅拌,沼气经压缩加压后经各类分布器进入沼气发酵罐,罐内原料在沼气的推动下形成循环,该搅拌方式对于装置的气密性要求很高,难以被利用到工程中。 The current stirring methods in the biogas fermentation process include manual stirring, mechanical stirring, gas stirring, liquid stirring, etc., but there are certain problems in these stirring methods: 1) Manual stirring: it is mostly used in laboratories, and the volume of the fermentation device is small. The purpose of stirring and mixing the fermentation liquid is achieved by shaking the fermentation bottle regularly. However, for straw-based raw materials and high-concentration fermentation, manual stirring cannot achieve the purpose of mixing, and at the same time, the scum on the fermentation surface hardens, hindering the collection of biogas; 2) Mechanical stirring: Mechanical stirring is a mechanical device that uses various installation forms. A stirring method in which various forms of mechanical movement make materials reach a mixed state. This kind of stirring method can produce a strong shearing effect, and can use the rotation of the stirring blade to break up the digested raw materials, which is beneficial to the mixing of high-viscosity materials, and is mainly used in laboratory fermentation devices and biogas projects. However, due to the long fermentation time, the stirring device needs to run for a long time, especially in biogas projects, the mechanical stirring device is soaked in the fermentation liquid for a long time, which is easy to cause corrosion of the device. After corrosion, the stirring device needs to be replaced. , it is necessary to open the fermentation device. At this time, it is easy to cause air leakage in the fermentation tank, which affects the normal operation of biogas fermentation. At the same time, this method consumes a lot of energy, costs high, and is complicated to operate and is not conducive to gas production; 3) Liquid stirring: liquid stirring is general The liquid flow generated by the pump operation is used to complete the stirring of the materials, and the fermentation liquid itself is used to extract the fermentation liquid through the pump, and then through its impact, the crust on the surface of the fermentation liquid is broken, and the fermentation liquid is stirred. It is a low energy consumption. , easy to operate, and a stirring method that ensures the tightness of the tank, but liquid stirring will cause an increase in pressure or local pressure in the fermenter, which is not conducive to fermentation; 4) Gas stirring: Gas stirring is achieved by the movement of air bubbles in the material. The purpose of material agitation, in biogas fermentation, gas agitation mainly refers to the biogas circulation agitation, the biogas enters the biogas fermentation tank through various distributors after being compressed and pressurized, and the raw materials in the tank are circulated under the promotion of biogas. The airtightness requirements of the air-tightness are very high, and it is difficult to be used in engineering.

发明内容 Contents of the invention

本发明主要针对上述问题,提供一种罐内设备少、结构简单、施工维修简便、搅拌效果好、效率高、运转设备费用低的厌氧反应装置。 The present invention mainly aims at the above problems, and provides an anaerobic reaction device with less equipment in the tank, simple structure, convenient construction and maintenance, good stirring effect, high efficiency and low operation equipment cost.

为实现上述目的,本发明采取下述技术方案:一种多级气液联合搅拌文丘里管——CSTR反应装置,在全混合厌氧反应器(5)的外部安装含有文丘里管(1)的多级外循环管路(2),在发酵过程中,可以通过循环泵(6)将发酵液从Ax(其中x=1,2,3···N,N由反应器的搅拌级数来确定)吸出,通过文丘里管(1)和外循环管路(2),再从Bx射入,沼气在射入位置的上部形成搅拌作用,而且可以达到防止发酵液上层结壳的效果,液体则在射入位置的下部形成搅拌作用,其中沼液出口的最下端一级应高于活性污泥层,另一方面配备有自动化控制设备和变速器,实现定时自动进料、自动搅拌,并且可以根据发酵过程的不同情况,对发酵原料进行不同形式、不同程度的搅拌。 In order to achieve the above object, the present invention adopts the following technical scheme: a multi-stage gas-liquid combined stirring venturi tube - CSTR reaction device, which is installed outside the fully mixed anaerobic reactor (5) containing a venturi tube (1) The multi-stage external circulation pipeline (2), during the fermentation process, the fermentation broth can be transferred from A x (where x=1, 2, 3···N, N by the stirring stage of the reactor through the circulation pump (6) (determined by the number) sucked out, through the Venturi tube (1) and the external circulation pipeline (2), and then injected from B x , the biogas forms agitation at the upper part of the injection position, and can prevent the upper layer of the fermentation broth from crusting As a result, the liquid forms a stirring effect at the lower part of the injection position, and the bottom level of the biogas slurry outlet should be higher than the activated sludge layer. On the other hand, it is equipped with automatic control equipment and transmission to realize automatic feeding and stirring at regular intervals. , and according to the different conditions of the fermentation process, the fermentation raw materials can be stirred in different forms and in different degrees.

所述的多级气液联合搅拌文丘里管——CSTR反应装置进一步是循环泵(6)安装在出水端的最下面一级,沼液由于重力作用,可以自行流到泵处,为泵提高足够的沼液,可使泵更好的工作,而且方便安装和维修。 The multi-stage gas-liquid combined stirring Venturi tube - CSTR reaction device is further equipped with a circulating pump (6) installed at the bottom of the water outlet, and the biogas slurry can flow to the pump by itself due to gravity, which is enough for the pump. The biogas slurry can make the pump work better, and it is convenient for installation and maintenance.

所述的多级气液联合搅拌文丘里管——CSTR反应装置进一步是循环泵(6)安装在出水端的最下面一级,沼液由于重力作用,可以自行流到泵处,为泵提高足够的沼液,可使泵更好的工作,而且方便安装和维修。 The multi-stage gas-liquid combined stirring Venturi tube - CSTR reaction device is further equipped with a circulating pump (6) installed at the bottom of the water outlet, and the biogas slurry can flow to the pump by itself due to gravity, which is enough for the pump. The biogas slurry can make the pump work better, and it is convenient for installation and maintenance.

所述的多级气液联合搅拌文丘里管——CSTR反应装置进一步是在文丘里管(1)的进气口段加一个沼气开关,可以有效的控制沼气的进气量,从而控制气体搅拌的程度。 The multi-stage gas-liquid combined stirring Venturi tube - CSTR reaction device further adds a biogas switch at the inlet section of the Venturi tube (1), which can effectively control the intake of biogas, thereby controlling gas stirring Degree.

所述的多级气液联合搅拌文丘里管——CSTR反应装置进一步是外循环管路(2)的沼液出口端到文丘里管(1)的管道直径应大于沼液进口端的管道直径,不但能保证文丘里管有够的压力,而且可以确保沼液射流进入反应器。 In the multi-stage gas-liquid combined stirring Venturi tube-CSTR reaction device, the diameter of the pipeline from the biogas slurry outlet end of the external circulation pipeline (2) to the Venturi tube (1) should be larger than the pipeline diameter of the biogas slurry inlet end, Not only can the Venturi tube have enough pressure, but also can ensure that the jet of biogas slurry enters the reactor.

所述的多级气液联合搅拌文丘里管——CSTR反应装置进一步是在沼液射入端口安装一个水力喷射器,来增强搅拌效果。 The multi-stage gas-liquid combined stirring Venturi tube-CSTR reaction device is further equipped with a hydraulic injector at the injection port of the biogas slurry to enhance the stirring effect.

所述的多级气液联合搅拌文丘里管——CSTR反应装置进一步是配备有自动化控制设备和变速器,实现定时自动进料、自动搅拌,并且可以根据发酵过程的不同情况,对发酵原料进行不同形式、不同程度的搅拌。 The multi-stage gas-liquid combined stirring Venturi tube-CSTR reaction device is further equipped with automatic control equipment and a transmission to realize automatic feeding and automatic stirring at regular intervals, and different fermentation raw materials can be processed according to different conditions of the fermentation process. forms, varying degrees of agitation.

本发明产生的有益效果有:实现了多级的气液联合搅拌,可以根据发酵过程的不同情况,对发酵原料进行不同形式、不同程度的搅拌,解决了液面结壳的现象,保证发酵完全、产气均匀,从而提高产气效率,提供了一种罐内设备少、结构简单、施工维修简便、搅拌效果好、效率高、运转设备费用低的厌氧反应装置。 The beneficial effects produced by the present invention are as follows: multi-stage gas-liquid combined stirring is realized, and the fermentation raw materials can be stirred in different forms and in different degrees according to different conditions of the fermentation process, which solves the phenomenon of crusting on the liquid surface and ensures complete fermentation , Uniform gas production, thereby improving gas production efficiency, providing an anaerobic reaction device with less equipment in the tank, simple structure, easy construction and maintenance, good stirring effect, high efficiency, and low operating equipment costs.

附图说明:Description of drawings:

图1是本发明结构示意图。 Fig. 1 is a schematic diagram of the structure of the present invention.

图2是本发明结构示意图。 Fig. 2 is a schematic diagram of the structure of the present invention.

符号说明: Symbol Description:

1.文丘里管、2.多级外循环管路、3.出气口、4.水封出料口、5.CSTR反应器、6.沼液循环泵、7.进料口、8.排污口、9.发酵液进口、10.沼气进口、11.发酵液出口、Ax为发酵液出口开关、Bx为发酵液进口开关。 1. Venturi tube, 2. Multi-stage external circulation pipeline, 3. Gas outlet, 4. Water seal outlet, 5. CSTR reactor, 6. Biogas slurry circulation pump, 7. Feed inlet, 8. Sewage discharge 9. Fermentation liquid import, 10. Biogas import, 11. Fermentation liquid export, Ax is the switch of fermentation liquid export, Bx is the switch of fermentation liquid import.

具体实施方式:detailed description:

下面结合附图和实例对本发明作进一步说明: Below in conjunction with accompanying drawing and example the present invention will be further described:

如图1所示,一种多级气液联合搅拌文丘里管—CSTR反应装置,在连续搅拌全混合厌氧反应器5的外部安装含有文丘里管1的多级外循环管路2,在发酵过程中,可以通过循环泵6将发酵液从Ax(其中x=1,2,3···N,N由反应器的搅拌级数来确定)吸出,通过文丘里管1和外循环管路2,再从Bx射入,沼气在射入位置的上部形成搅拌作用,而且可以达到防止发酵液上层结壳的作用,液体则在射入位置的下部形成搅拌作用,其中沼液出口的最下端一级应高于活性污泥层,另一方面配备有自动化控制设备和变速器,实现定时自动进料、自动搅拌,并且可以根据发酵过程的不同情况,对发酵原料进行不同形式、不同程度的搅拌。 As shown in Figure 1, a multi-stage gas-liquid combined stirring Venturi tube-CSTR reaction device, a multi-stage external circulation pipeline 2 containing a Venturi tube 1 is installed outside the continuous stirring fully mixed anaerobic reactor 5. During the fermentation process, the fermentation broth can be sucked out from A x (where x=1, 2, 3···N, N is determined by the stirring stages of the reactor) through the circulation pump 6, through the Venturi tube 1 and the external circulation Pipeline 2, and then injected from B x , the biogas forms agitation at the upper part of the injection position, and can prevent the upper layer of the fermentation liquid from crusting, and the liquid forms agitation at the lower part of the injection position, in which the biogas slurry exits The bottom level of the tank should be higher than the activated sludge layer. On the other hand, it is equipped with automatic control equipment and transmission to realize automatic feeding and stirring at regular intervals, and the fermentation raw materials can be processed in different forms and in different ways according to different conditions of the fermentation process. degree of stirring.

优选地,循环泵6安装在出水端的最下面一级,沼液由于重力作用,可以自行流到泵处,为泵提高足够的沼液,可使泵更好的工作,而且方便安装和维修。 Preferably, the circulation pump 6 is installed at the bottom stage of the water outlet, and the biogas slurry can flow to the pump by itself due to gravity, so as to increase enough biogas slurry for the pump, which can make the pump work better, and is convenient for installation and maintenance.

优选地,在外循环管路2上安装文丘里管1,文丘里管1的进气口10与气柜相连,利用文丘里管的原理来达到气液搅拌和破壳的效果。 Preferably, a Venturi tube 1 is installed on the external circulation pipeline 2, and the inlet 10 of the Venturi tube 1 is connected to the gas cabinet, and the principle of the Venturi tube is used to achieve the effects of gas-liquid stirring and shell breaking.

优选地,在文丘里管1的进气口段加一个沼气开关,可以有效的控制沼气的进气量,从而控制气体搅拌的程度。 Preferably, a biogas switch is added to the inlet section of the Venturi tube 1, which can effectively control the intake amount of the biogas, thereby controlling the degree of gas stirring.

优选地,外循环管路2的沼液出口端到文丘里管1的管道直径应大于沼液进口端的管道直径,不但能保证文丘里管有够的压力,而且可以确保沼液射流进入反应器。 Preferably, the diameter of the pipeline from the biogas slurry outlet end of the external circulation pipeline 2 to the Venturi tube 1 should be larger than the pipeline diameter of the biogas slurry inlet end, not only to ensure that the venturi tube has sufficient pressure, but also to ensure that the biogas slurry jet flows into the reactor .

优选地,在沼液射入端口安装一个水力喷射器,来增强搅拌效果。 Preferably, a hydro jet is installed at the biogas slurry injection port to enhance the stirring effect.

优选地,该多级气液联合搅拌文丘里管—CSTR反应装置配备有自动化控制设备和变速器,实现定时自动进料、自动搅拌,并且可以根据发酵过程的不同情况,对发酵原料进行不同形式、不同程度的搅拌。 Preferably, the multi-stage gas-liquid combined stirring Venturi tube-CSTR reaction device is equipped with automatic control equipment and a transmission to realize automatic feeding and stirring at regular intervals, and different forms, varying degrees of agitation.

本发明实现了多级的气液联合搅拌,可以根据发酵过程的不同情况,对发酵原料进行不同形式、不同程度的搅拌,解决了液面结壳的现象,保证发酵完全、产气均匀,从而提高产气效率,提供了一种罐内设备少、结构简单、施工维修简便、搅拌效果好、效率高、运转设备费用低的厌氧反应装置。 The invention realizes multi-stage gas-liquid combined stirring, and can carry out different forms and different degrees of stirring on the fermentation raw materials according to different conditions of the fermentation process, solves the phenomenon of crusting on the liquid surface, ensures complete fermentation and uniform gas production, and thus The gas production efficiency is improved, and an anaerobic reaction device with less equipment in the tank, simple structure, convenient construction and maintenance, good stirring effect, high efficiency and low operation equipment cost is provided.

上面以举例的方式对本发明进行了说明,但本发明不限于上述具体实施例,凡基于本发明所做的任何改动或变型均属于本发明要求保护的范围。 The present invention has been described above by way of examples, but the present invention is not limited to the above-mentioned specific embodiments, and any changes or variations made based on the present invention fall within the scope of protection of the present invention.

Claims (8)

1.一种多级气液联合搅拌文丘里管—CSTR反应装置,其特征是:在连续搅拌全混合厌氧反应器(5)的外部安装含有文丘里管(1)的多级外循环管路(2),在发酵过程中,可以通过循环泵(6)将发酵液从Ax(其中x=1,2,3···N,N由反应器的搅拌级数来确定)吸出,通过文丘里管(1)和外循环管路(2),再从Bx射入,沼气在射入位置的上部形成搅拌作用,而且可以达到防止发酵液上层结壳的效果,液体在射入位置的下部形成搅拌作用,其中沼液出口的最下端一级应高于活性污泥层,另一方面该装置配备有自动化控制设备和变速器,实现定时自动进料、自动搅拌,并且可以根据发酵过程的不同情况,对发酵原料进行不同形式、不同程度的搅拌。 1. A multi-stage gas-liquid combined stirring Venturi tube-CSTR reaction device is characterized in that: a multi-stage external circulation tube containing a Venturi tube (1) is installed outside the continuous stirring fully mixed anaerobic reactor (5) Road (2), during the fermentation process, the fermentation broth can be sucked out from A x (where x=1, 2, 3···N, N is determined by the stirring stages of the reactor) through the circulation pump (6), Through the Venturi tube (1) and the external circulation pipeline (2), and then injected from B x , the biogas forms agitation at the upper part of the injection position, and can achieve the effect of preventing the upper layer of the fermentation broth from crusting, and the liquid is injected The lower part of the position forms the stirring effect, and the bottom level of the biogas slurry outlet should be higher than the activated sludge layer. On the other hand, the device is equipped with automatic control equipment and transmission to realize automatic feeding and stirring at regular intervals, and can be based on fermentation According to the different conditions of the process, the fermentation raw materials are stirred in different forms and in different degrees. 2.根据权利要求1所述的多级气液联合搅拌文丘里管—CSTR反应装置,其特征是:在CSTR反应器(5)的侧面安装多级外循环管路(2),各级之间相互连通,只需通过开关来控制循环的级数,且通过一个循环泵(6)便可实现多级循环,以达到低耗能、低成本的目的。 2. The multi-stage gas-liquid combined stirring venturi tube-CSTR reaction device according to claim 1, characterized in that: a multi-stage external circulation pipeline (2) is installed on the side of the CSTR reactor (5), and the They are connected with each other, only need to control the number of stages of circulation through a switch, and realize multi-stage circulation through a circulation pump (6), so as to achieve the purpose of low energy consumption and low cost. 3.根据权利要求1或2所述的多级气液联合搅拌文丘里管—CSTR反应装置,其特征是:把循环泵(6)安装在出水端的最下面一级,沼液由于重力作用,可以自行流到泵处,为泵提供足够的沼液,可使泵更好的工作,而且方便安装和维修。 3. The multi-stage gas-liquid combined stirring Venturi tube-CSTR reaction device according to claim 1 or 2, characterized in that: the circulating pump (6) is installed at the bottom stage of the water outlet, and the biogas slurry due to gravity, It can flow to the pump by itself, provide enough biogas slurry for the pump, make the pump work better, and facilitate installation and maintenance. 4.根据权利要求1或2所述的多级气液联合搅拌文丘里管—CSTR反应装置,其特征是:在外循环管路(2)上安装文丘里管(1),文丘里管(1)的进气口与气柜相连,利用文丘里管的原理来达到气液搅拌和破壳的效果。 4. The multi-stage gas-liquid combined stirring Venturi tube-CSTR reaction device according to claim 1 or 2, characterized in that: a Venturi tube (1) is installed on the external circulation pipeline (2), and the Venturi tube (1 ) The air inlet is connected to the gas cabinet, and the principle of the Venturi tube is used to achieve the effect of gas-liquid stirring and shell breaking. 5.根据权利要求4所述的多级气液联合搅拌文丘里管—CSTR反应装置,其特征是:在文丘里管(1)的进气口端加一个沼气开关,可以有效的控制沼气的进气量,从而控制气体搅拌的程度。 5. The multi-stage gas-liquid combined stirring Venturi tube-CSTR reaction device according to claim 4, characterized in that: a biogas switch is added at the inlet end of the Venturi tube (1), which can effectively control the flow of biogas The amount of air intake, thereby controlling the degree of gas stirring. 6.根据权利要求1或2所述的多级气液联合搅拌文丘里管—CSTR反应装置,其特征是:外循环管路(2)的沼液出口端到文丘里管(1)的管道直径应大于沼液进口端的管道直径,不但能保证文丘里管有足够的压力,而且可以确保沼液射流进入反应器。 6. The multi-stage gas-liquid combined stirring venturi tube-CSTR reaction device according to claim 1 or 2, characterized in that: the pipeline from the biogas slurry outlet end of the external circulation pipeline (2) to the venturi tube (1) The diameter should be larger than the diameter of the pipeline at the biogas slurry inlet, not only to ensure sufficient pressure in the Venturi tube, but also to ensure that the biogas slurry jet flows into the reactor. 7.根据权利要求6所述的多级气液联合搅拌文丘里管—CSTR反应装置,其特征是:在沼液进口端安装一个水力喷射器,来增强搅拌效果。 7. The multi-stage gas-liquid combined stirring Venturi tube-CSTR reaction device according to claim 6, characterized in that: a hydraulic injector is installed at the inlet end of the biogas slurry to enhance the stirring effect. 8.根据权利要求1所述的多级气液联合搅拌文丘里管—CSTR反应装置,其特征是:该装置配备有自动化控制设备和变速器,实现定时自动进料、自动搅拌,并且可以根据发酵过程的不同情况,对发酵原料进行不同形式、不同程度的搅拌。 8. The multi-stage gas-liquid combined stirring Venturi tube-CSTR reaction device according to claim 1 is characterized in that: the device is equipped with automatic control equipment and a speed changer to realize automatic feeding and automatic stirring at regular intervals, and can be based on fermentation According to the different conditions of the process, the fermentation raw materials are stirred in different forms and in different degrees.
CN201510285452.3A 2015-05-29 2015-05-29 A kind of multi-stage gas-liquid joint stirring Venturi tube-CSTR reaction units Expired - Fee Related CN105820943B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510285452.3A CN105820943B (en) 2015-05-29 2015-05-29 A kind of multi-stage gas-liquid joint stirring Venturi tube-CSTR reaction units

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510285452.3A CN105820943B (en) 2015-05-29 2015-05-29 A kind of multi-stage gas-liquid joint stirring Venturi tube-CSTR reaction units

Publications (2)

Publication Number Publication Date
CN105820943A true CN105820943A (en) 2016-08-03
CN105820943B CN105820943B (en) 2018-07-17

Family

ID=56514949

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510285452.3A Expired - Fee Related CN105820943B (en) 2015-05-29 2015-05-29 A kind of multi-stage gas-liquid joint stirring Venturi tube-CSTR reaction units

Country Status (1)

Country Link
CN (1) CN105820943B (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109289713A (en) * 2018-10-18 2019-02-01 辽宁石油化工大学 A kind of mosquito coil isothermal reactor and using method
CN110791412A (en) * 2019-12-10 2020-02-14 云南师范大学 Complementary stirring full-mixing anaerobic reactor
CN111701561A (en) * 2020-07-31 2020-09-25 中国石油化工股份有限公司 Multi-stage variable speed rotating packed tower and extraction method
CN112452224A (en) * 2020-09-29 2021-03-09 开能康德威健康科技(北京)有限责任公司 Stirring device and centralized liquid supply system
CN112481106A (en) * 2020-12-02 2021-03-12 通化县东明农牧业发展(集团)有限公司 Straw anaerobic digester material mixing system
CN113817582A (en) * 2021-10-21 2021-12-21 四川省天惠能源科技有限公司 Circulating multiphase flow biogas reaction system
CN114350480A (en) * 2022-01-12 2022-04-15 万华化学(四川)有限公司 Double-circulation bubbling fermentation tank and method for preparing lactic acid through fermentation
CN114794442A (en) * 2022-05-23 2022-07-29 福建胜美鲜生物科技有限公司 Method and device for brewing fish sauce by microbial fermentation
CN117123078A (en) * 2023-08-24 2023-11-28 成都瑞耘环境科技有限公司 Hydraulic stirring mechanism, high-performance anaerobic reactor and anaerobic reaction process

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101182454A (en) * 2007-11-05 2008-05-21 程龙 External-internal double-cycling bioreactor
CN102154372A (en) * 2010-12-20 2011-08-17 昆明理工大学 Method for producing methane by means of fermentation with jet mixing technology
CN102502960A (en) * 2011-12-26 2012-06-20 陕西清源环境实业有限公司 Gas-liquid blending and stirring device of sewage-sludge complete mixing type anaerobic fermentation tank and treatment method thereof
CN202786235U (en) * 2012-09-28 2013-03-13 云南师范大学 Circulation biogas slurry pipeline for biogas slurry stirring and hull breaking of anaerobic reactor
CN202953832U (en) * 2012-11-08 2013-05-29 广西华纳新材料科技有限公司 Venturi tube reactor

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101182454A (en) * 2007-11-05 2008-05-21 程龙 External-internal double-cycling bioreactor
CN102154372A (en) * 2010-12-20 2011-08-17 昆明理工大学 Method for producing methane by means of fermentation with jet mixing technology
CN102502960A (en) * 2011-12-26 2012-06-20 陕西清源环境实业有限公司 Gas-liquid blending and stirring device of sewage-sludge complete mixing type anaerobic fermentation tank and treatment method thereof
CN202786235U (en) * 2012-09-28 2013-03-13 云南师范大学 Circulation biogas slurry pipeline for biogas slurry stirring and hull breaking of anaerobic reactor
CN202953832U (en) * 2012-11-08 2013-05-29 广西华纳新材料科技有限公司 Venturi tube reactor

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109289713A (en) * 2018-10-18 2019-02-01 辽宁石油化工大学 A kind of mosquito coil isothermal reactor and using method
CN110791412A (en) * 2019-12-10 2020-02-14 云南师范大学 Complementary stirring full-mixing anaerobic reactor
CN111701561A (en) * 2020-07-31 2020-09-25 中国石油化工股份有限公司 Multi-stage variable speed rotating packed tower and extraction method
CN112452224A (en) * 2020-09-29 2021-03-09 开能康德威健康科技(北京)有限责任公司 Stirring device and centralized liquid supply system
CN112481106A (en) * 2020-12-02 2021-03-12 通化县东明农牧业发展(集团)有限公司 Straw anaerobic digester material mixing system
CN112481106B (en) * 2020-12-02 2021-07-30 通化县东明农牧业发展(集团)有限公司 A straw anaerobic digester material mixing system
CN113817582A (en) * 2021-10-21 2021-12-21 四川省天惠能源科技有限公司 Circulating multiphase flow biogas reaction system
CN114350480A (en) * 2022-01-12 2022-04-15 万华化学(四川)有限公司 Double-circulation bubbling fermentation tank and method for preparing lactic acid through fermentation
CN114350480B (en) * 2022-01-12 2023-12-19 万华化学(四川)有限公司 A double-circulation bubbling fermentation tank and a method for producing lactic acid through fermentation
CN114794442A (en) * 2022-05-23 2022-07-29 福建胜美鲜生物科技有限公司 Method and device for brewing fish sauce by microbial fermentation
CN117123078A (en) * 2023-08-24 2023-11-28 成都瑞耘环境科技有限公司 Hydraulic stirring mechanism, high-performance anaerobic reactor and anaerobic reaction process

Also Published As

Publication number Publication date
CN105820943B (en) 2018-07-17

Similar Documents

Publication Publication Date Title
CN105820943B (en) A kind of multi-stage gas-liquid joint stirring Venturi tube-CSTR reaction units
CN204058476U (en) A kind of biogas fermentation device
CN106222074B (en) Continous way wet-and-dry two-stage dynamic anaerobic fermentation equipment
CN204824868U (en) Anaerobic jar marsh gas agitating unit
CN105152508B (en) Enhance sludge anaerobic installation for fermenting
CN104277968A (en) Large-scale biogas hydraulic-circulating even mixing device
CN203333655U (en) Overflow type double-circulation anaerobic reactor
CN105036505A (en) Dry fermentation device for dewatering sludge treatment
CN204281750U (en) Rural area high efficient marsh gas tank
CN205062077U (en) Gas -liquid jointly stirs venturi - entirely and mixes anaerobic digestion reactor
CN102010113A (en) Anaerobic solid reactor
CN203754718U (en) Solid-state anaerobic reactor
CN206428237U (en) Helical feed stirs sludge gas dry fermentation anaerobic reactor
CN207671861U (en) A kind of underground integrated sewage treating equipment
CN201678671U (en) Biogas recycling mixing equipment
CN202116383U (en) Cultivating and augmenting device for effective solid microorganism microbial inoculum
CN204918160U (en) A pulse play water system for anaerobic reactor
CN107720957B (en) Reaction device and method for anaerobic treatment of high-concentration organic wastewater and solid waste at constant temperature in sequencing batch
CN105062870A (en) Rural biogas tank
CN215799554U (en) Dry-type anaerobic system for stirring by utilizing gas pressure
CN204619874U (en) Gas push formula is from stirring combination purification groove
CN204675885U (en) Aerobic biological process pond
CN209778349U (en) Air stripping adds medicine reflux unit
CN209322551U (en) Urban wastewater treatment aerobic tank
CN201825781U (en) Anaerobic solid reactor

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20180717

Termination date: 20210529

CF01 Termination of patent right due to non-payment of annual fee