CN103991955B - Dynamic monitoring method and dynamic monitoring device for gas generation in anaerobic digestion process - Google Patents
Dynamic monitoring method and dynamic monitoring device for gas generation in anaerobic digestion process Download PDFInfo
- Publication number
- CN103991955B CN103991955B CN201310053258.3A CN201310053258A CN103991955B CN 103991955 B CN103991955 B CN 103991955B CN 201310053258 A CN201310053258 A CN 201310053258A CN 103991955 B CN103991955 B CN 103991955B
- Authority
- CN
- China
- Prior art keywords
- gas
- anaerobic digestion
- unit
- dynamic monitoring
- valveless
- 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.)
- Expired - Fee Related
Links
- 230000029087 digestion Effects 0.000 title claims abstract description 62
- 238000000034 method Methods 0.000 title claims abstract description 48
- 238000012544 monitoring process Methods 0.000 title claims abstract description 23
- 238000012806 monitoring device Methods 0.000 title claims description 11
- 239000007788 liquid Substances 0.000 claims abstract description 52
- 238000004519 manufacturing process Methods 0.000 claims abstract description 25
- 230000007797 corrosion Effects 0.000 claims abstract description 12
- 238000005260 corrosion Methods 0.000 claims abstract description 12
- 239000007789 gas Substances 0.000 claims description 135
- 239000000523 sample Substances 0.000 claims description 26
- 229910000365 copper sulfate Inorganic materials 0.000 claims description 10
- ARUVKPQLZAKDPS-UHFFFAOYSA-L copper(II) sulfate Chemical compound [Cu+2].[O-][S+2]([O-])([O-])[O-] ARUVKPQLZAKDPS-UHFFFAOYSA-L 0.000 claims description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 8
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 6
- 230000002159 abnormal effect Effects 0.000 claims description 3
- 229910052757 nitrogen Inorganic materials 0.000 claims description 3
- 238000012795 verification Methods 0.000 claims description 3
- 238000011160 research Methods 0.000 abstract description 4
- 239000000243 solution Substances 0.000 description 7
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- 229920001296 polysiloxane Polymers 0.000 description 4
- 230000035945 sensitivity Effects 0.000 description 3
- 239000010802 sludge Substances 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 2
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 2
- 230000002411 adverse Effects 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 238000001514 detection method Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 239000008103 glucose Substances 0.000 description 2
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 2
- 230000007774 longterm Effects 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 239000006228 supernatant Substances 0.000 description 2
- 238000005904 alkaline hydrolysis reaction Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003034 coal gas Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000003915 liquefied petroleum gas Substances 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
Classifications
-
- Y02W10/12—
Landscapes
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
- Treatment Of Sludge (AREA)
Abstract
本发明涉及一种厌氧消化过程中气体产生的动态监测方法及其装置。装置包括厌氧消化体系、气相压力变化范围控制单元、无阀式气体外排单元、外排气体有害组分去除单元和气体排放时间点记录单元;其中气相压力变化范围控制单元包活U型液管和液位控制器;厌氧消化体系的气相部分通过耐腐蚀软管分别与U型液管一端和无阀式气体外排单元相连通;U型液管的另一端通过导线与液位控制器连接,所述液位控制器通过导线分别与无阀式气体外排单元和气体排放时间点记录单元相连;无阀式气体外排单元再通过耐腐蚀软管与外排气体有害组分去除单元相连。本发明方法与装置应用于厌氧消化体系气体产生的动态监测,适用于室内外厌氧消化过程气体产生的动态监测研究。The invention relates to a dynamic monitoring method and device for gas generation in an anaerobic digestion process. The device includes an anaerobic digestion system, a gas phase pressure range control unit, a valveless gas discharge unit, a gas discharge harmful component removal unit, and a gas discharge time point recording unit; the gas phase pressure range control unit includes a U-shaped Liquid pipe and liquid level controller; the gas phase part of the anaerobic digestion system is connected to one end of the U-shaped liquid pipe and the valveless gas discharge unit through a corrosion-resistant hose; the other end of the U-shaped liquid pipe is connected to the liquid level through a wire. The liquid level controller is connected to the valveless gas discharge unit and the gas discharge time point recording unit respectively through wires; connected to the sub-removal unit. The method and device of the invention are applied to the dynamic monitoring of gas production in an anaerobic digestion system, and are suitable for the dynamic monitoring research of gas production in indoor and outdoor anaerobic digestion processes.
Description
技术领域technical field
本发明涉及厌氧处理过程监测,具体是一种厌氧消化过程中气体产生的动态监测方法及其装置。The invention relates to anaerobic treatment process monitoring, in particular to a dynamic monitoring method and device for gas generation in anaerobic digestion process.
背景技术Background technique
在厌氧消化过程研究中,厌氧消化体系气体产生的测定一般采用排水法,这种方法的原理是先将气室中充满水,当气体产生进入气室的同时将等体积的水排出,从而测定气体体积。对于很小规模的厌氧消化体系,其总产气量不大,可以使用较大的气室一次性收集所有气体,此时采用排水法也较方便、简捷。但是,对于规模较大的厌氧消化体系,因产气量较多,如果使用排水法监测产气量,要么用很大的气室一次性收集所有气体;要么用常规大小的气室多次收集产生的气体。其中,采用很大的气室的办法在实验室研究中一般并不可行,采用常规气室收集则需要实验人员适时将气室内部气体排出,从而耗费很多时间和精力用于维护。排水法的另一个缺点是该法收集的气体一般为溶解度较低的甲烷、氢气等,而溶解度较大的二氧化碳和硫化氢等则在会在气体收集过程中通过被动扩散和主动排水过程而有较大程度的流失,不但污染室内环境,也只能近似地反映厌氧气体的产生总量,更不易反映厌氧气体排放速率的动态变化。In the research of anaerobic digestion process, the determination of gas production in anaerobic digestion system generally adopts the drainage method. The principle of this method is to fill the air chamber with water first, and discharge an equal volume of water when the gas is generated into the air chamber. The gas volume is thus determined. For a small-scale anaerobic digestion system, the total gas production is not large, and a larger gas chamber can be used to collect all the gas at one time. At this time, it is more convenient and simple to use the drainage method. However, for a large-scale anaerobic digestion system, due to the large amount of gas production, if the drainage method is used to monitor the gas production, either a large gas chamber is used to collect all the gas at one time; gas. Among them, the method of using a large gas chamber is generally not feasible in laboratory research, and the use of conventional gas chamber collection requires experimenters to discharge the gas inside the gas chamber in a timely manner, which consumes a lot of time and energy for maintenance. Another disadvantage of the drainage method is that the gas collected by this method is generally low-soluble methane, hydrogen, etc., while carbon dioxide and hydrogen sulfide with high solubility will pass through passive diffusion and active drainage during the gas collection process. A large degree of loss not only pollutes the indoor environment, but also can only approximately reflect the total amount of anaerobic gas produced, and it is not easy to reflect the dynamic change of anaerobic gas emission rate.
厌氧消化体系产气的特点是产气速率相对较低且波动幅度较大,目前市场上已有的各种气体流量计的测定范围往往高于一般厌氧过程的产气速率,而且要求的工作压力较大,一般适用于工业生产环境中天然气、煤气、液化气等气体流量的测定,不适用于产气速率相对较小且变化不定的厌氧消化体系的监测。The gas production of the anaerobic digestion system is characterized by a relatively low gas production rate and large fluctuations. The measurement ranges of various gas flowmeters currently on the market are often higher than the gas production rate of the general anaerobic process, and the required The working pressure is relatively high, and it is generally suitable for the measurement of gas flow rates such as natural gas, coal gas, and liquefied petroleum gas in industrial production environments. It is not suitable for the monitoring of anaerobic digestion systems with relatively small and variable gas production rates.
发明内容Contents of the invention
为了克服现有排水法的不足,本发明目的在于提供一种厌氧消化过程的气体产生的动态监测方法及其装置。In order to overcome the deficiencies of the existing drainage methods, the purpose of the present invention is to provide a dynamic monitoring method and device for gas production in an anaerobic digestion process.
为实现上述目的,本发明所采用的技术方案为:To achieve the above object, the technical solution adopted in the present invention is:
一种厌氧消化过程中气体产生的动态监测装置,其特征在于:包括厌氧消化体系、气相压力变化范围控制单元、无阀式气体外排单元、外排气体有害组分去除单元和气体排放时间点记录单元;A dynamic monitoring device for gas production during anaerobic digestion, characterized in that it includes an anaerobic digestion system, a gas phase pressure change range control unit, a valveless gas discharge unit, a harmful component removal unit for the discharge gas, and a gas Emission time point recording unit;
其中气相压力变化范围控制单元包活U型液管和液位控制器;厌氧消化体系的气相部分通过耐腐蚀软管分别与U型液管一端和无阀式气体外排单元相连通;The gas phase pressure change range control unit includes a U-shaped liquid pipe and a liquid level controller; the gas phase part of the anaerobic digestion system is respectively connected to one end of the U-shaped liquid pipe and the valveless gas discharge unit through a corrosion-resistant hose;
U型液管的另一端通过导线与液位控制器连接,所述液位控制器通过导线分别与无阀式气体外排单元和气体排放时间点记录单元相连;无阀式气体外排单元再通过耐腐蚀软管与外排气体有害组分去除单元相连。The other end of the U-shaped liquid pipe is connected to a liquid level controller through a wire, and the liquid level controller is respectively connected to a valveless gas discharge unit and a gas discharge time point recording unit through a wire; It is connected to the harmful component removal unit of the exhaust gas through a corrosion-resistant hose.
所述U型液管一端通过耐腐蚀软管与厌氧消化体系的气相部分联通,另一端内配有悬垂导电探头,悬垂导电探头通过导线与液位控制器连接。One end of the U-shaped liquid pipe communicates with the gas phase of the anaerobic digestion system through a corrosion-resistant hose, and the other end is equipped with a hanging conductive probe connected to the liquid level controller through a wire.
所述内配有悬垂导电探头的U型液管端联通有密封气袋,所述U型液管内配有3个悬垂导电探头,三个悬垂导电探头由同一水平高度向下悬垂。The end of the U-shaped liquid pipe equipped with a suspended conductive probe is connected with a sealed air bag, and the U-shaped liquid pipe is equipped with 3 suspended conductive probes, and the three suspended conductive probes are suspended from the same level.
所述三个悬垂导电探头具有高度差,其中,两个低位点的悬垂导电探头的相对高度相同。The three suspended conductive probes have height differences, wherein the relative heights of the suspended conductive probes at the two low points are the same.
所述厌氧消化体系的气相部分通过耐腐蚀软管与装水的容器相连,软管插入水面以下,用于非正常停电时以气泡形式被动排放厌氧消化体系产生的气体。The gas phase part of the anaerobic digestion system is connected to the container filled with water through a corrosion-resistant hose, and the hose is inserted below the water surface to passively discharge the gas generated by the anaerobic digestion system in the form of bubbles during an abnormal power failure.
所述无阀式气体外排单元通过耐腐蚀软管与设于外排气体有害组分去除单元上的倒置三角漏斗相连;外排气体经过倒置三角漏斗与承有硫酸铜溶液的外排气体有害组分去除单元的硫酸铜溶液液面接触。The valveless gas exhaust unit is connected to the inverted triangular funnel provided on the harmful component removal unit of the exhaust gas through a corrosion-resistant hose; The copper sulfate solution of the gas harmful component removal unit is in contact with the liquid surface.
利用厌氧消化过程中气体产生的动态监测装置的动态监测方法,厌氧消化过程中,在厌氧消化体系内进行厌氧消化过程,产生的气体改变气相压力,气相压力的升高与降低分别推动气相压力变化范围控制单元中U型液管的常压密闭端的液面上升接触高位点的悬垂导电探头,与液面降低至低位点的悬垂导电探头以下,将信号分别传递给无阀式气体外排单元和气体排放时间点记录单元,实现对厌氧消化处理过程中产生气体的定量的排放与记录,从而一定精度上实现气体产生的实时、动态监测。Using the dynamic monitoring method of the dynamic monitoring device for gas production in the anaerobic digestion process, during the anaerobic digestion process, the anaerobic digestion process is carried out in the anaerobic digestion system, the gas produced changes the gas phase pressure, and the increase and decrease of the gas phase pressure are respectively Push the gas phase pressure change range control unit. The liquid level at the normal pressure airtight end of the U-shaped liquid pipe rises and touches the hanging conductive probe at the high point, and the liquid level drops below the hanging conductive probe at the low point, and the signals are respectively transmitted to the valveless gas. The external discharge unit and the gas discharge time point recording unit realize the quantitative discharge and recording of the gas generated during the anaerobic digestion process, so as to realize the real-time and dynamic monitoring of the gas generation with a certain accuracy.
所述无阀式气体外排单元通过耐腐蚀软管与设于外排气体有害组分去除单元上的倒置三角漏斗相连;外排气体经过倒置三角漏斗与承有硫酸铜溶液的外排气体有害组分去除单元的硫酸铜溶液液面接触。所述硫酸铜溶液浓度为0.1-0.8N。The valveless gas exhaust unit is connected to the inverted triangular funnel provided on the harmful component removal unit of the exhaust gas through a corrosion-resistant hose; The copper sulfate solution of the gas harmful component removal unit is in contact with the liquid surface. The concentration of the copper sulfate solution is 0.1-0.8N.
本发明所具有的优点是:The advantage that the present invention has is:
1.本发明装置实现动态监测厌氧消化体系的气体产生过程,大大降低实验人员的现场维护要求;1. The device of the present invention realizes the dynamic monitoring of the gas generation process of the anaerobic digestion system, greatly reducing the on-site maintenance requirements of the experimenters;
2.本发明装置与方法能够适合动态监测在较大范围内变动的厌氧气体产生过程,监测灵敏度可以根据实验的具体要求进行调节,适用范围广泛;2. The device and method of the present invention can be suitable for dynamic monitoring of the anaerobic gas production process that changes in a large range, and the monitoring sensitivity can be adjusted according to the specific requirements of the experiment, and has a wide range of applications;
3.本发明装置中采用无阀式的气体外排单元与外排气体有害组分去除单元的联合使用,大大降低来自厌氧消化产生的有害气体组分对监测设备长期运行和实验实验室环境的不利影响,适用于室内外厌氧消化过程研究。3. In the device of the present invention, the combined use of the valveless gas exhaust unit and the harmful component removal unit of the exhaust gas greatly reduces the impact of the harmful gas components produced by anaerobic digestion on the long-term operation of the monitoring equipment and the experimental laboratory. Adverse effects of the environment, suitable for indoor and outdoor anaerobic digestion process research.
4.本发明装置适用于产气速率不定、持续时间较长的厌氧消化体系的气体产生的动态监测。4. The device of the present invention is suitable for dynamic monitoring of gas production in an anaerobic digestion system with variable gas production rate and long duration.
5.本发明既可以测定厌氧过程中气体产生的动态变化,又可以更准确地测定厌氧气体的总体积,并采用无阀式气体外排单元和外排气体有害组分去除单元,有效避免厌氧消化所产生的有害气体组分对监测装置和实验室环境的不利影响,确保长期运行。5. The present invention can not only measure the dynamic change of gas production in the anaerobic process, but also more accurately measure the total volume of anaerobic gas, and adopts a valveless gas exhaust unit and an exhaust gas harmful component removal unit, Effectively avoid the adverse effects of harmful gas components produced by anaerobic digestion on the monitoring device and laboratory environment, ensuring long-term operation.
附图说明Description of drawings
图1是本发明实施例提供的厌氧消化体系气体产生的动态监测装置图。Fig. 1 is a diagram of a dynamic monitoring device for gas production in an anaerobic digestion system provided by an embodiment of the present invention.
图2是本发明实施例中3天之内厌氧消化体系内气体产生的状况。Fig. 2 is the status of gas production in the anaerobic digestion system within 3 days in the embodiment of the present invention.
图3是本发明实施例中10天之内厌氧消化体系内气体产生的状况。Fig. 3 is the status of gas production in the anaerobic digestion system within 10 days in the embodiment of the present invention.
具体实施方式Detailed ways
实施例1Example 1
容积为6.36L厌氧消化体系1内装有厌氧消化活性污泥,溶液体积为5.4L,添加易降解碳源葡萄糖,TOC负荷为380mg/L,进行厌氧消化实验。厌氧消化体系1设有两个出气口,分别通过硅胶管与U型液管6一端和无阀式气体外排单元4联通。U型液管6另一端内配有3个悬垂导电探头9,其中两个低位点的探头的空间相对高度相同;向U型液管6内注水至接近低位点悬垂导电探头9,U型液管配有悬垂导电探头9的一端与密封气袋8联通形成常压密闭环境,悬垂导电探头9通过导线11与液位控制器7连接。The anaerobic digestion system 1 with a volume of 6.36L is equipped with anaerobic digestion activated sludge, the volume of the solution is 5.4L, and the easily degradable carbon source glucose is added, and the TOC load is 380mg/L, and the anaerobic digestion experiment is carried out. The anaerobic digestion system 1 is provided with two gas outlets, which communicate with one end of the U-shaped liquid pipe 6 and the valveless gas discharge unit 4 respectively through silicone tubes. The other end of the U-shaped liquid pipe 6 is equipped with three hanging conductive probes 9, wherein the relative heights of the probes at the two low points are the same; water is injected into the U-shaped liquid pipe 6 to close to the low point hanging conductive probes 9, and the U-shaped liquid One end of the pipe equipped with a suspended conductive probe 9 is connected to the sealed air bag 8 to form a closed environment at normal pressure, and the suspended conductive probe 9 is connected to the liquid level controller 7 through a wire 11 .
U型液管内高低位点悬垂导电探头9的垂直距离决定监测的灵敏度,决定每一次的排气量。本实施例中,多次调节高低位点悬垂导电探头的间距,并经多次向反应器内缓慢注射氮气验证,最终确定每次排气的体积为36mL。The vertical distance of the suspended conductive probe 9 at the high and low points in the U-shaped liquid pipe determines the sensitivity of monitoring and the exhaust volume each time. In this example, the distance between the suspended conductive probes at the high and low points was adjusted several times, and after several slow injections of nitrogen into the reactor for verification, the volume of each exhaust was finally determined to be 36 mL.
无阀式气体外排单元3通过硅胶管10与外排气体有害组分去除单元4连接。The valveless gas exhaust unit 3 is connected to the exhaust gas harmful component removal unit 4 through a silicone tube 10 .
外排气体有害组分去除单元5由倒置三角漏斗与容置有0.2N硫酸铜溶液的容器组成,外排气体经过倒置三角漏斗并与0.2N硫酸铜溶液的液面接触,去除硫化氢等有害组分。The harmful component removal unit 5 of the exhaust gas is composed of an inverted triangular funnel and a container containing a 0.2N copper sulfate solution. The exhaust gas passes through the inverted triangular funnel and contacts the liquid surface of the 0.2N copper sulfate solution to remove hydrogen sulfide and other harmful components.
气体排放时间点记录单元4通过继电器将厌氧消化体系气相压力变化范围控制单元2的输出信号转化为开关、电阻、电流或电压变化信号,并通过开关/电阻/电流/电压记录仪,实时记录厌氧消化体系气体排放的启动与停止时间点。The gas discharge time point recording unit 4 converts the output signal of the anaerobic digestion system gas phase pressure change range control unit 2 into a switch, resistance, current or voltage change signal through a relay, and records it in real time through a switch/resistance/current/voltage recorder The start and stop time points of the gas emission of the anaerobic digestion system.
在非正常的停电状况下,厌氧反应体系1内产生的气体达到一定压力后,通过插入于装水的容器12底部硅胶管10将产生气体以气泡形式被动排出。Under abnormal power failure conditions, after the gas generated in the anaerobic reaction system 1 reaches a certain pressure, the generated gas is passively discharged in the form of bubbles through the silicone tube 10 inserted at the bottom of the water-filled container 12 .
本实施例中,装置正常运转检测过程为:In this embodiment, the normal operation detection process of the device is as follows:
厌氧消化体系1内产生的气体,不断提高厌氧消化体系1的气相压力,并通过硅胶管10,推动U型液管6的液体向常压密闭一段上移,当常压端液面接触高位点的悬垂探头9时,触发液位控制器7通过导线11将信号发送给无阀式气体外排单元4和气体排放记录单元5,启动无阀式气体外排单元4的开关,排出厌氧消化反应器1内的气体,同时记录单元5通过继电器将排气外排信号转化为开关的打开信号,并将这一时刻记录下来,作为气体排放的启动时间点。The gas generated in the anaerobic digestion system 1 continuously increases the gas phase pressure of the anaerobic digestion system 1, and through the silicone tube 10, pushes the liquid in the U-shaped liquid pipe 6 to move up to the airtight section at normal pressure. When the pendant probe 9 at the high point triggers the liquid level controller 7 to send the signal to the valveless gas discharge unit 4 and the gas discharge recording unit 5 through the wire 11, the switch of the valveless gas discharge unit 4 is activated to discharge the exhaust gas. Oxygen digests the gas in the reactor 1, and the recording unit 5 converts the exhaust signal into a switch opening signal through the relay, and records this moment as the start time point of the gas discharge.
U型液管6常压密封一端液面随着厌氧消化体系内气体的排出而下降,液面离开低位点悬垂探头9时,液位传感器7再次通过导线11将信号发送给无阀式气体外排单元4,使其停止排气,液面恢复初始状况,同时记录单元5通过继电器将排气外排的停止信号转化为开关的关闭信号,并将这一时刻记录下来,作为气体排放的停止时间点。因所加碳源为易降解的葡萄糖,厌氧消化体系1内气体产生迅速,1天之内产生大量气体,3天之内厌氧消化体系内气体产生的状况如图2所示,实现了厌氧消化过程气体产生的动态监测。The liquid level at one end of the U-shaped liquid pipe 6 is sealed at normal pressure and drops with the discharge of gas in the anaerobic digestion system. When the liquid level leaves the low point hanging probe 9, the liquid level sensor 7 sends a signal to the valveless gas again through the wire 11. The exhaust unit 4 makes it stop the exhaust, and the liquid level returns to the initial state. At the same time, the recording unit 5 converts the stop signal of the exhaust exhaust into the closing signal of the switch through the relay, and records this moment as the gas discharge. stop time point. Because the added carbon source is easily degradable glucose, the gas in the anaerobic digestion system 1 is generated rapidly, and a large amount of gas is generated within 1 day, and the gas generation in the anaerobic digestion system within 3 days is shown in Figure 2. Dynamic monitoring of gas production during anaerobic digestion.
实施例2Example 2
实施例2与实施例1运行过程基本一样,其不同点主要有:Embodiment 2 is basically the same with embodiment 1 operation process, and its difference mainly contains:
1.厌氧消化系统内添加剩余活性污泥碱性水解上清液2.5L,水解上清液的TOC浓度为1.76g/L。1. Add 2.5L of alkaline hydrolysis supernatant of residual activated sludge to the anaerobic digestion system, and the TOC concentration of the hydrolysis supernatant is 1.76g/L.
2.缩短U型液体管内高低位点的间距,增大监测敏感度,经反复多次向反应器内缓慢注射氮气验证,最终确定每次排气的体积为20mL。2. Shorten the distance between the high and low points in the U-shaped liquid tube, increase the monitoring sensitivity, and repeatedly inject nitrogen into the reactor for verification, and finally determine the volume of each exhaust to be 20mL.
本实施例装置正常运转检测过程与实施例1相同。来自于污泥碱性水解液中的TOC具有较高的厌氧可降解性,特别是前3天之内的气体排放速率明显高于后7天内的气体排放速率,10天之内气体产生的状况见图3,实现了厌氧消化过程气体产生的动态监测。The normal operation detection process of the device in this embodiment is the same as that in Embodiment 1. TOC from sludge alkaline hydrolyzate has high anaerobic degradability, especially the gas emission rate in the first 3 days is significantly higher than that in the next 7 days, and the gas emission rate in 10 days The status is shown in Figure 3, which realizes the dynamic monitoring of gas production in the anaerobic digestion process.
Claims (6)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201310053258.3A CN103991955B (en) | 2013-02-19 | 2013-02-19 | Dynamic monitoring method and dynamic monitoring device for gas generation in anaerobic digestion process |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201310053258.3A CN103991955B (en) | 2013-02-19 | 2013-02-19 | Dynamic monitoring method and dynamic monitoring device for gas generation in anaerobic digestion process |
Publications (2)
Publication Number | Publication Date |
---|---|
CN103991955A CN103991955A (en) | 2014-08-20 |
CN103991955B true CN103991955B (en) | 2015-06-10 |
Family
ID=51306334
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201310053258.3A Expired - Fee Related CN103991955B (en) | 2013-02-19 | 2013-02-19 | Dynamic monitoring method and dynamic monitoring device for gas generation in anaerobic digestion process |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN103991955B (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105890935A (en) * | 2016-05-31 | 2016-08-24 | 黑龙江省科学院科技孵化中心 | Simple fermentation gas collecting and measuring device and measuring method thereof |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1865865A (en) * | 2006-06-07 | 2006-11-22 | 李学哲 | Multifunctional gas release measuring instrument |
KR20100019774A (en) * | 2008-08-11 | 2010-02-19 | 주식회사 케이엔알 | Volume measuring device for gas produced by reaction of micro-organism in reaction tank and multi channel type automatic gas analyzing system comprising the same |
CN102515453A (en) * | 2011-11-22 | 2012-06-27 | 中国科学院沈阳应用生态研究所 | High-concentration anaerobic digestion treating device for urban sludge and use method |
CN203144175U (en) * | 2013-02-19 | 2013-08-21 | 中国科学院沈阳应用生态研究所 | Dynamic monitoring device for gas generation in anaerobic digestion process |
-
2013
- 2013-02-19 CN CN201310053258.3A patent/CN103991955B/en not_active Expired - Fee Related
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1865865A (en) * | 2006-06-07 | 2006-11-22 | 李学哲 | Multifunctional gas release measuring instrument |
KR20100019774A (en) * | 2008-08-11 | 2010-02-19 | 주식회사 케이엔알 | Volume measuring device for gas produced by reaction of micro-organism in reaction tank and multi channel type automatic gas analyzing system comprising the same |
CN102515453A (en) * | 2011-11-22 | 2012-06-27 | 中国科学院沈阳应用生态研究所 | High-concentration anaerobic digestion treating device for urban sludge and use method |
CN203144175U (en) * | 2013-02-19 | 2013-08-21 | 中国科学院沈阳应用生态研究所 | Dynamic monitoring device for gas generation in anaerobic digestion process |
Also Published As
Publication number | Publication date |
---|---|
CN103991955A (en) | 2014-08-20 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN103674156B (en) | A kind of metering method utilizing laboratory micro gas-metering device | |
CN106525710B (en) | An electrochemical test device for acoustic emission detection of corrosion performance of materials and its application method | |
CN106525709B (en) | A corrosion electrochemical test device and its application method | |
CN101520358B (en) | Roof system comprehensive physical property detection device | |
CN203144175U (en) | Dynamic monitoring device for gas generation in anaerobic digestion process | |
CN103991955B (en) | Dynamic monitoring method and dynamic monitoring device for gas generation in anaerobic digestion process | |
CN101980009B (en) | Solid oxide electrolytic cell testing bracket | |
CN206330874U (en) | A kind of electrochemical testing device of acoustic emission detection material corrosion performance | |
CN202767949U (en) | Wax removal through thermal wash monitoring system of oil well | |
CN106525711B (en) | Acoustic emission testing fixture for material corrosion performance and using method thereof | |
CN206311482U (en) | For the sample clamp of electrochemical corrosion test | |
CN107727564A (en) | The electrochemical testing device of metal microbiologic(al) corrosion under current system | |
CN106679768A (en) | Float switch type liquid leakage flow monitoring wireless acquisition terminal device | |
CN204007801U (en) | A kind of anti-fluctuation magnetic fluid level gauge | |
CN203642986U (en) | Metering device of laboratory trace gas | |
CN201378103Y (en) | Buried-type trigger for indoor dam-break experiments | |
CN205068181U (en) | Industry liquid -level monitoring device | |
CN204631558U (en) | An EDI pure water control system | |
CN204011594U (en) | A kind of environment-friendly type lead acid accumulator | |
CN203124380U (en) | External liquid level monitoring system for silicon solar battery cleaning machine | |
CN203132639U (en) | Liquid level measurement device | |
CN107631751B (en) | Gas flow measuring system and method based on circuit on-off | |
CN106706510B (en) | Sample holder for electrochemical corrosion testing and method of use thereof | |
CN207197574U (en) | Measuring gas flow rate system based on connecting and disconnecting of the circuit | |
CN206574798U (en) | A kind of integrated fuel storage device based on liquid hydrogen storage |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150610 Termination date: 20200219 |