CN108956922B - Monitor the device of water body methane wear rate - Google Patents

Monitor the device of water body methane wear rate Download PDF

Info

Publication number
CN108956922B
CN108956922B CN201810873520.1A CN201810873520A CN108956922B CN 108956922 B CN108956922 B CN 108956922B CN 201810873520 A CN201810873520 A CN 201810873520A CN 108956922 B CN108956922 B CN 108956922B
Authority
CN
China
Prior art keywords
reaction system
gas
methane
cylinder
outlet
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.)
Active
Application number
CN201810873520.1A
Other languages
Chinese (zh)
Other versions
CN108956922A (en
Inventor
罗怡君
肖尚斌
王炜
雷丹
胡芳方
李俊美
汪志江
严登华
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.)
China Three Gorges University CTGU
Original Assignee
China Three Gorges University CTGU
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 China Three Gorges University CTGU filed Critical China Three Gorges University CTGU
Priority to CN201810873520.1A priority Critical patent/CN108956922B/en
Publication of CN108956922A publication Critical patent/CN108956922A/en
Application granted granted Critical
Publication of CN108956922B publication Critical patent/CN108956922B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N33/00Investigating or analysing materials by specific methods not covered by groups G01N1/00 - G01N31/00
    • G01N33/18Water

Landscapes

  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Food Science & Technology (AREA)
  • Medicinal Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Analytical Chemistry (AREA)
  • Biochemistry (AREA)
  • General Health & Medical Sciences (AREA)
  • General Physics & Mathematics (AREA)
  • Immunology (AREA)
  • Pathology (AREA)
  • Sampling And Sample Adjustment (AREA)

Abstract

The invention discloses a kind of devices for monitoring water body methane wear rate, including greenhouse gases analyzer and at least a set of reaction system, connect into circulation loop by air inlet pipe and an air outlet pipe between greenhouse gases analyzer and reaction system;Reaction system includes the cylinder of sealing, is equipped with aeration pump above inner barrel, the exhaust outlet of aeration pump connect air stone by pipeline with air stone and is located at cylinder body bottom;It is additionally provided with fan in cylinder, the power supply line of aeration pump and fan is connected to cylinder external power supply.The device can be monitored the rate of its methane consumption to multiclass water body simultaneously, have the characteristics that easy to operate, stable and high treating effect, operating cost are cheap, can intelligent management, runing time is controllable, ensure that device stable operation and stable monitoring effect.

Description

Monitor the device of water body methane wear rate
Technical field
The present invention relates to aquatic monitoring field, especially a kind of device for monitoring water body methane wear rate.
Background technique
It is shown according to the 5th assessment report of IPCC, since the industrial revolution, carbon dioxide, methane in atmosphere, oxidation Sub- nitrogen isothermal chamber gas emissions significantly increase, and Global Temperature averagely rises 0.85 DEG C.Climate warming is to earth environment and people Class activity has produced significant impact, and such as glacier volume-diminished, sea level rise.Freshwater ecosystems are carbon dioxide With the important emission source of methane.However, the atmospheric heating potential due to equivalent methane is higher by more than 20 times than carbon dioxide.Therefore, The methane wear rate in water body is monitored to accurately assessment aquatic ecosystem to atmosphere CH4The influence of release iron, and adopt It takes corresponding measure to weaken greenhouse gases release of aquatic ecosystem etc. to be of great significance.
Summary of the invention
In order to solve the above technical problem, the present invention provides a kind of devices for monitoring water body methane wear rate, can be fast Fast accurate measurements water body methane wear rate;The apparatus structure is simple, and reliable performance is easy to carry about with one, moreover it is possible to realize intelligent control System.
The technical solution adopted by the present invention is that the device of monitoring water body methane wear rate, including greenhouse gases analysis Instrument and at least a set of reaction system, connect into circulation by air inlet pipe and an air outlet pipe between greenhouse gases analyzer and reaction system Circuit;Reaction system includes the cylinder of sealing, is equipped with aeration pump above inner barrel, exhaust outlet and the air stone of aeration pump pass through Pipeline connection, air stone are located at cylinder body bottom;It is additionally provided with fan in cylinder, the power supply line of aeration pump and fan is connected to outside cylinder Portion's power supply.
Further, the reaction system is 2-6 set, and air inlet pipe includes inlet manifold and air intake branch, and escape pipe includes Outlet general pipeline and going out gas branch pipe;The air inlet of greenhouse gases analyzer is connected with inlet manifold, and gas outlet is connected with outlet general pipeline, Every set reaction system is designed with air intake branch and going out gas branch pipe, and air intake branch is connected to inlet manifold, and going out gas branch pipe is all connected with To outlet general pipeline, and solenoid valve is mounted in each air intake branch and going out gas branch pipe, the air intake branch of every set reaction system and Solenoid valve in going out gas branch pipe connects a timer jointly.
Further, it is connected between the inlet manifold and outlet general pipeline by solenoid valve.
Further, the cylinder lower part is equipped with inlet and outlet pipe lines, is equipped with accurate constant flow pump on inlet and outlet pipe lines.
Further, the aeration pump and fan are respectively connected with timer.
Further, which further includes the seal box that can control temperature, illumination, its outside temperature removing chamber's gas analyzer He is respectively positioned in seal box component.
Using the method for described device monitoring water body methane wear rate, comprising the following steps:
Into the cylinder of reaction system, injection monitoring water body, is then turned on aeration pump and fan is handled, 10-20min Stop aeration, is obtained using the concentration of methane in gas in greenhouse gases analyzer monitoring cylinder, then by Henry's law analysis Water body methane wear rate.
Further, when setting covers reaction system more, Air Exposure and gas-monitoring in reaction system are successively carried out, and are made With same greenhouse gases analyzer, when in greenhouse gases analyzer without monitoring gas, by its inlet manifold and outlet general pipeline Connection carries out internal circulation.
The method have the advantages that:
1) present apparatus is treated survey water sample using aeration pump and air stone and is aerated, and micro- gas is covered on the air stone in water body Hole can make gas fast exchange in water-gas, and by fan the methane in cylinder internal upper part gas be isolated with water body The methane come quickly mixes to reach aqueous vapor balance;Different moments water body dissolved methane concentration can be monitored on-line, pass through exposure Gas can make methane concentration in aqueous vapor reach balance rapidly, when avoiding the artificial bring error of conventional method, while shortening experiment Between.And using the concentration of methane in greenhouse gases analyzer detection gas, can be intended online with computer after observing a period of time The data in greenhouse gases analyzer are closed, the device for obtaining monitoring water body methane wear rate can be analyzed by Henry's law, Also it is avoided that the error that the generation of Laboratory Monitoring off-line monitoring is taken back using conventional method.
2) automatic control system can also be arranged in the present apparatus, and solenoid valve is such as mounted in air inlet pipe and an air outlet pipe, And by solenoid valve connection timer, measurement duration is set by timer, effectively controls opening and closing for solenoid valve, solenoid valve and meter When device joint can automatically control the minute of water body dissolved methane concentration.Finally, aeration pump and fan are connected with timer, The aeration duration of automatic control water body may be implemented.By above-mentioned setting, manual operation process is reduced.
3) present apparatus can be monitored the rate of its methane consumption to multiclass water body simultaneously, have easy to operate, operation surely Fixed and high treating effect, the features such as operating cost is cheap, can intelligent management, runing time is controllable, ensure that the stabilization of device Operation and stable monitoring effect.
Detailed description of the invention
Fig. 1 is the structural diagram of the present invention.
Fig. 2 is continuously to supervise methane total amount variation diagram in Time Measurement Unit for the first time.
Fig. 3 is methane total amount variation diagram in second of continuous prison Time Measurement Unit.
Specific embodiment
The present invention is further illustrated below with reference to examples and drawings, but the scope of protection of present invention is not limited to In the range of embodiment statement.
As shown in Figure 1, monitoring water body methane wear rate device, including greenhouse gases analyzer 1 and at least it is a set of instead System is answered, circulation loop is connected by air inlet pipe and an air outlet pipe between greenhouse gases analyzer and reaction system;Reaction system Cylinder 2 including sealing, inner barrel top are equipped with aeration pump 3, and the exhaust outlet of aeration pump is connect with air stone 4 by pipeline, Air stone 4 is located at cylinder body bottom;It is additionally provided with fan 5 in cylinder, the power supply line of aeration pump and fan is connected to cylinder external power supply.
Aeration pump is by overhead gas in cylinder, and the pipeline being connected by aeration pump with air stone is into bottom water body Air stone air inlet, air stone is located in water body to be measured, micro- stomata is covered on air stone, gas in water-gas can be made quick Exchange, and reach balance;The methane for finally by fan methane in cylinder internal upper part gas being separated with water body is fast Speed mixes to reach aqueous vapor balance.
Preferably, the reaction system is 2-6 set, and air inlet pipe includes inlet manifold 6 and air intake branch 7, and escape pipe includes Outlet general pipeline 8 and going out gas branch pipe 9;The air inlet of greenhouse gases analyzer is connected with inlet manifold, and it is total that gas outlet is connected with outlet Pipe, every set reaction system are designed with air intake branch and going out gas branch pipe, and air intake branch is connected to inlet manifold, and going out gas branch pipe connects It is connected to outlet general pipeline, and is mounted on solenoid valve, the air intake branch of every set reaction system in each air intake branch and going out gas branch pipe A timer 11 is connected jointly with the solenoid valve 10 in going out gas branch pipe.It is further preferable that reaction system is 4 sets.Solenoid valve can Effectively to control air inlet and outlet, the gas circuit of solenoid valve is opened when energized, and the gas circuit of solenoid valve is automatically closed when power-off, in conjunction with After time timing aeration pump and fan are in conjunction with timer, duration can also be aerated with intelligent control.
It is further preferred that the cylinder is organic glass material.Using glass material, sealing effect well can be played Fruit will not generate interference to gas therein or water body, and convenient for observation inner case.Settable rubber stopper at the top of cylinder It is sealed, air inlet, gas outlet and pipeline communication port is set on rubber stopper, wherein air inlet is for installing greenhouse gases analysis The outlet pipe of instrument, gas outlet is used to install the admission line of greenhouse gases analyzer, and pipeline communication port is for placing aeration The power supply line of pump and fan.Air inlet pipe is analyzed to greenhouse gases analyzer by the intracorporal gas of reaction system cylinder is defeated, is analyzed Entered in cylinder by escape pipe after the completion.Recycle under test gas in this way to ensure the stabilization of reaction system internal environment.Air inlet Pipe reserves a certain distance and difference in height in the intracorporal position of cylinder in the intracorporal position of cylinder and escape pipe, to ensure test result Accuracy.
In addition, the model of solenoid valve can choose that 2W200-20 of section sieve;The model of timer can select KG316T.Greenhouse The optional model G2301 greenhouse gases analyzer Picarro of gas analyzer, the U.S. or DLT-100 greenhouse gases analyzer LGR, the U.S..
It will be understood by those skilled in the art that the electronic components such as solenoid valve, timer belong to skill well known to those skilled in the art Art is not limited to the record of this specification, the connection and control of timer and conventional electrical component to the selection of their models Relationship belongs to the common knowledge of those skilled in the art, repeats no more in the present specification, and those skilled in the art can be according to existing Field actual conditions selection known approaches install each element.
Preferably, it is connected between the inlet manifold and outlet general pipeline by solenoid valve;In no monitoring gas, such as still It needs greenhouse gases analyzer to be run, will be connected between inlet manifold and outlet general pipeline, so that gas is carried out in instrument internal Circulation, prevents from blocking and damages to instrument.
Preferably, the cylinder lower part is equipped with inlet and outlet pipe lines, is equipped with accurate constant flow pump on inlet and outlet pipe lines.It can also be with Inlet and outlet are respectively set, and inlet and outlet are passed through into pipeline respectively and connect accurate constant flow pump, more accurately The intracorporal water level of application cylinder.
Preferably, the aeration pump and fan are respectively connected with timer, and the automatic control of aeration time may be implemented.
Preferably, which further includes the seal box that can control temperature, illumination, other outside temperature removing chamber's gas analyzer Component is respectively positioned in seal box.Constant temperature mode can be set in seal box, shading treatment or supplementary light can also be carried out, it can To be compared simultaneously using methane concentration of ordinary dissolution of multiple reaction systems to water bodys different at identical temperature.Screening can also be passed through Light processing is to water body whether the methane concentration of ordinary dissolution under illumination condition compares.
Using the method for described device monitoring water body methane wear rate, comprising the following steps:
Into the cylinder of reaction system, injection monitoring water body, is then turned on aeration pump and fan is handled, 10-20min Stop aeration, is obtained using the concentration of methane in gas in greenhouse gases analyzer monitoring cylinder, then by Henry's law analysis Water body methane wear rate.
Preferably, when setting covers reaction system more, Air Exposure and gas-monitoring in reaction system are successively carried out, and are used Same greenhouse gases analyzer connects its inlet manifold and outlet general pipeline when in greenhouse gases analyzer without monitoring gas It is logical, carry out internal circulation.
When 4 sets of reaction systems are arranged such as apparatus of the present invention, structure chart is as shown in Figure 1.
Specific operation process is as follows, and the timer of first reaction system is opened using timer setting 9:00-9:15, Aeration pump is controlled, water body is aerated by air stone, timer is concurrently set and opens fan, set 9:15-9:25 timing Device opens two solenoid valves of control gas analyzer disengaging gas, the two solenoid valves are controlled with a timer, greenhouse gases Analyzer monitors the concentration of methane gas of first set reaction system at this time, collects data.9:15-9:30 opens second set of reaction The aeration pump of system is aerated, and the solenoid valve of first set reaction system control disengaging gas has closed when 9:30 after aeration It closing, setting 9:30-9:40 opens two solenoid valves of disengaging gas of control second set of reaction system of gas analyzer, and so on, Sequence is monitored the methane concentration of other a few set reaction systems, can every 3 hours companies in order to obtain accurate methane wear rate Continuous monitoring, which repeats to test primary data of collecting, to be analyzed, and can analyze to consume in water-outlet body the speed of methane by Henry's law Rate.In this device using upper, we can monitor the water body methane wear rates in more set reaction systems simultaneously, can also lead to The impact factor of control differential responses system is crossed to carry out check experiment, as first set and second set of reaction system carry out at shading Reason, third set and the 4th set of reaction system carry out lighting process or four sets of reaction systems use different water bodys;It can also incite somebody to action Four sets of reaction systems are handled with same way, are compared to result accuracy.
Pass through each device of injection of water inlet siphon successively equivalent after the Surface water sample for being derived from pond being shaken up when experiment In (transparent organic glass cylinder, internal diameter 22cm, height 30cm) (height for accounting for about one third), all connect then is sealed Mouthful.When observing gas concentration in certain device, the power supply of air pump and fan in the device is connected by automatic control system, is cut simultaneously It changes DLT-100 greenhouse gases analyzer to be connected with its gas circuit, CH in measurement pipe headspace gas4Concentration, observe 15 points (i.e. pipe inner top air CH after clock4With the CH dissolved in water body4Basically reach balance) it is switched to next device.So circulation.Often 3 hours circulation primaries.DLT-100 greenhouse gases analyzer power supply is always in an ON state during all experimentss.According to henry Sharp law, the amount of dissolved gas is directly proportional to gaseous phase partial pressure in solution;The CH above device4It is dense that partial pressure is higher than water body dissolved methane When spending, air pump blasts the overhead gas in reactor in water, and portion of methane can be absorbed by water body.Conversely, the methane in water body It can be come out with the bubble back-diffusion that air pump generates.In this way, the gas in water constantly exists with the gas in device (reactor) It swaps, so that the concentration of methane in device be made to be in dynamic change state.
The present apparatus is by the CH in observation system used in experiment with computing4Gross mass changes with time to estimate water CH in body4Wear rate.Methane total amount includes with part existing for gas phase state and the part being dissolved in water sample, Qian Zheyou The CH of pipe headspace after the water of LGR measurement-gas balance4Concentration (Cg) is directly calculated multiplied by the gas volume of observation system It obtains, the latter is then calculated according to Henry's law.
According to Henry's law: Hcc=Ca/Cg
Hcc=HcpR T
H in formulaccFor dimensionless Henry solubility;HcpFor Henry solubility (unit: mol/m3/Pa);T is temperature (K);R For gas constant (8.314J/mol/K;For Ca aqueous-phase concentration (μm ol/L);Cg is gas phase concentration (μm ol/L).
The H chosen during present apparatus experimental calculationcpIt is 1.4 × 10-5mol/m3/Pa。
Choosing calorstat temperature in this experiment is 15 degrees Celsius, the initial methane total amount of injection or various concentration in two devices Water body, after continuously monitoring, the data that wherein device one is measured according to LGR after treatment, obtain 1 data of table, according to In acquired continuous time in device methane molal weight variation, carry out exponential fitting obtain Fig. 2.Wherein T-CH4According to Methane total amount in the device of detection.Sometime the variation of methane total amount is methane wear rate in water body, device in section apparatus One water body methane wear rate is 0.0265 μm of ol/min.
Methane total amount changes in table 1 first time continuous monitoring device
Device two after treatment according to the data of LGR measurement, obtains 2 data of table, according to acquired after continuous monitoring In continuous time in device methane molal weight variation, carry out exponential fitting and obtain Fig. 3, the water body methane of device two consumes speed Rate is 0.0453 μm of ol/min.
Time/min T-CH4/μmol Time/min T-CH4/μmol Time/min T-CH4/μmol
0.000 124.370 899.845 46.359 1800.031 19.306
179.951 100.588 1079.784 38.847 1979.989 16.303
360.020 82.920 1259.725 32.457 2159.946 13.718
539.963 67.887 1440.005 27.237 2339.904 11.692
719.901 56.461 1619.961 23.011 2519.864 10.125
Methane total amount changes in second of the continuous monitoring device of table 2
This observation shows in experimentation that the methane content in device is presented index pattern and reduces, although in experimental provision Setting initial methane total amount or concentration it is inconsistent, but two device monitorings with calculating after obtained methane wear rate in phase It is very close under synthermal and dark conditions, matched curve also very close to.The result shows that this experimental provision is for monitoring In water body methane wear rate it is relatively simple with it is quick.

Claims (7)

1. monitoring the device of water body methane wear rate, it is characterised in that: including greenhouse gases analyzer and at least a set of reaction System connects into circulation loop by air inlet pipe and an air outlet pipe between greenhouse gases analyzer and reaction system;Reaction system packet The cylinder of sealing is included, is equipped with aeration pump above inner barrel, the exhaust outlet of aeration pump is connect with air stone by pipeline, air stone Positioned at cylinder body bottom;It is additionally provided with fan in cylinder, the power supply line of aeration pump and fan is connected to cylinder external power supply;The reaction System is 2-6 set, and air inlet pipe includes inlet manifold and air intake branch, and escape pipe includes outlet general pipeline and going out gas branch pipe;Greenhouse gas The air inlet of body analyzer is connected with inlet manifold, and gas outlet is connected with outlet general pipeline, and every set reaction system is designed with air inlet branch Pipe and going out gas branch pipe, air intake branch are connected to inlet manifold, and going out gas branch pipe is connected to outlet general pipeline, and each air intake branch With solenoid valve is mounted in going out gas branch pipe, the solenoid valve on the air intake branch and going out gas branch pipe of every set reaction system connects jointly One timer.
2. the apparatus according to claim 1, it is characterised in that: pass through solenoid valve between the inlet manifold and outlet general pipeline Connection.
3. the apparatus according to claim 1, it is characterised in that: the cylinder lower part is equipped with inlet and outlet pipe lines, inlet and outlet pipes Accurate constant flow pump is installed on road.
4. the apparatus according to claim 1, it is characterised in that: the aeration pump and fan are respectively connected with timer.
5. device according to any one of claims 1-4, it is characterised in that: the device further include can control temperature, The seal box of illumination, the other component outside temperature removing chamber's gas analyzer are respectively positioned in seal box.
6. using the method for claim 5 described device monitoring water body methane wear rate, which is characterized in that including following step It is rapid:
Into the cylinder of reaction system, injection monitoring water body, is then turned on aeration pump and fan is handled, and 10-20min stops Aeration analyzes to obtain water-outlet body using the concentration of methane in gas in greenhouse gases analyzer monitoring cylinder, then by Henry's law Methane wear rate.
7. according to the method described in claim 6, it is characterized by: aeration when the more set reaction system of setting, in reaction system Processing and gas-monitoring successively carry out, using same greenhouse gases analyzer, when monitoring gas no in greenhouse gases analyzer When, its inlet manifold is connected to outlet general pipeline, carries out internal circulation.
CN201810873520.1A 2018-08-02 2018-08-02 Monitor the device of water body methane wear rate Active CN108956922B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201810873520.1A CN108956922B (en) 2018-08-02 2018-08-02 Monitor the device of water body methane wear rate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201810873520.1A CN108956922B (en) 2018-08-02 2018-08-02 Monitor the device of water body methane wear rate

Publications (2)

Publication Number Publication Date
CN108956922A CN108956922A (en) 2018-12-07
CN108956922B true CN108956922B (en) 2019-05-28

Family

ID=64467343

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201810873520.1A Active CN108956922B (en) 2018-08-02 2018-08-02 Monitor the device of water body methane wear rate

Country Status (1)

Country Link
CN (1) CN108956922B (en)

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103321616A (en) * 2013-07-06 2013-09-25 李贤明 Method and system for collecting seabed methane hydrate
CN105137020A (en) * 2015-08-20 2015-12-09 四川大学 Method for promoting release of supersaturated total dissolved gas by using aeration and experimental device thereof
CN204945129U (en) * 2015-09-18 2016-01-06 中国疾病预防控制中心辐射防护与核安全医学所 A kind of water radon rapid measurement device
CN106082430A (en) * 2016-07-26 2016-11-09 尚川(北京)水务有限公司 A kind of aeration control system and aeration control method
CN106277299A (en) * 2016-08-29 2017-01-04 尚川(北京)水务有限公司 A kind of aeration control system based on oxygen consumption rate analyzer and method
CN206057241U (en) * 2016-09-18 2017-03-29 东莞市东江水务有限公司 A kind of biomembrane oxygen consumption rate for being applied to water treatment filter material determines device
CN106980001A (en) * 2017-04-10 2017-07-25 济南大学 A kind of experimental rig for being used to determine solubilised state nitrous oxide in water body

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103321616A (en) * 2013-07-06 2013-09-25 李贤明 Method and system for collecting seabed methane hydrate
CN105137020A (en) * 2015-08-20 2015-12-09 四川大学 Method for promoting release of supersaturated total dissolved gas by using aeration and experimental device thereof
CN204945129U (en) * 2015-09-18 2016-01-06 中国疾病预防控制中心辐射防护与核安全医学所 A kind of water radon rapid measurement device
CN106082430A (en) * 2016-07-26 2016-11-09 尚川(北京)水务有限公司 A kind of aeration control system and aeration control method
CN106277299A (en) * 2016-08-29 2017-01-04 尚川(北京)水务有限公司 A kind of aeration control system based on oxygen consumption rate analyzer and method
CN206057241U (en) * 2016-09-18 2017-03-29 东莞市东江水务有限公司 A kind of biomembrane oxygen consumption rate for being applied to water treatment filter material determines device
CN106980001A (en) * 2017-04-10 2017-07-25 济南大学 A kind of experimental rig for being used to determine solubilised state nitrous oxide in water body

Also Published As

Publication number Publication date
CN108956922A (en) 2018-12-07

Similar Documents

Publication Publication Date Title
CN109668824A (en) Simulate the high speed humidity corrosion loop experimental provision of natural gas line internal corrosion environment
US6904815B2 (en) Configurable multi-point sampling method and system for representative gas composition measurements in a stratified gas flow stream
JP6380971B2 (en) Gas monitor device
CN109085316A (en) Measure the device of water body dissolved methane concentration
AU2009290420A1 (en) Method and device for detecting leaks in an underground liquid pipe, particularly a water pipe
CN209606292U (en) Simulate the high speed humidity corrosion loop experimental provision of natural gas line internal corrosion environment
CN103984938B (en) Remote sensing time series abnormity detection method
CN109212580B (en) Method for measuring radium concentration in water by open-loop type electrostatic collection two-stage method
US20090113988A1 (en) Mitigation of gas memory effects in gas analysis
CN108732329B (en) Coal seam gas pressure measurement simulation experiment device and method
Butnor et al. Soil properties differently influence estimates of soil CO 2 efflux from three chamber-based measurement systems
CN108956922B (en) Monitor the device of water body methane wear rate
KR20160075394A (en) Simultaneous real-time continuous monitoring system of emission gas concentrations in mutliple chambers
CN107389499B (en) Detection device and method
CN207730632U (en) A kind of experimental rig of simulation draining pipe culvert inside corrosive environment
CN203534928U (en) Experimental device for testing adsorption/desorption performance of adsorbing working substance pair
CN208588726U (en) Monitor the device of water body dissolved methane and nitrous oxide concentration
US20240102896A1 (en) Drone for measuring odor concentration
CN104656116A (en) Method and device for quickly measuring exhalation rate of radon in uranium tailings
CN210572192U (en) Water oxygen particle analysis and detection system
CN208109824U (en) A kind of device of synchronous detection different depth water body biodegradability
CN109188497B (en) Method for measuring radium concentration in water in open-loop mode by utilizing effective decay constant
CN209513524U (en) A kind of flue gas minimum discharge micronic dust detection system
CN103383317A (en) Sampling apparatus and method used for estimation of source intensity of non-point atmospheric pollution source
JP6066405B2 (en) Quantitative measurement system for oil-contaminated soil

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant