CN112730164A - Real-time online measurement system for volatilization characteristics and mixing state of aerosol - Google Patents
Real-time online measurement system for volatilization characteristics and mixing state of aerosol Download PDFInfo
- Publication number
- CN112730164A CN112730164A CN202011584800.4A CN202011584800A CN112730164A CN 112730164 A CN112730164 A CN 112730164A CN 202011584800 A CN202011584800 A CN 202011584800A CN 112730164 A CN112730164 A CN 112730164A
- Authority
- CN
- China
- Prior art keywords
- tube
- aerosol particles
- subsystem
- real
- aerosol
- 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.)
- Pending
Links
- 239000000443 aerosol Substances 0.000 title claims abstract description 137
- 238000005259 measurement Methods 0.000 title claims abstract description 53
- 238000002156 mixing Methods 0.000 title claims abstract description 40
- 239000002245 particle Substances 0.000 claims abstract description 131
- 238000009792 diffusion process Methods 0.000 claims abstract description 95
- 238000012216 screening Methods 0.000 claims abstract description 6
- 238000010438 heat treatment Methods 0.000 claims description 86
- 238000001816 cooling Methods 0.000 claims description 48
- 238000001179 sorption measurement Methods 0.000 claims description 19
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 8
- 239000002594 sorbent Substances 0.000 claims description 4
- 239000003570 air Substances 0.000 description 25
- 239000007789 gas Substances 0.000 description 20
- 239000000112 cooling gas Substances 0.000 description 9
- 238000000034 method Methods 0.000 description 9
- 239000013618 particulate matter Substances 0.000 description 9
- 230000008569 process Effects 0.000 description 8
- 230000032683 aging Effects 0.000 description 7
- 238000001035 drying Methods 0.000 description 7
- 239000010419 fine particle Substances 0.000 description 7
- 238000011160 research Methods 0.000 description 6
- 230000001276 controlling effect Effects 0.000 description 5
- 238000005520 cutting process Methods 0.000 description 5
- 239000004071 soot Substances 0.000 description 5
- OKTJSMMVPCPJKN-NJFSPNSNSA-N Carbon-14 Chemical class [14C] OKTJSMMVPCPJKN-NJFSPNSNSA-N 0.000 description 4
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 4
- 230000008901 benefit Effects 0.000 description 4
- 150000001875 compounds Chemical class 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 238000007789 sealing Methods 0.000 description 4
- 229910001220 stainless steel Inorganic materials 0.000 description 4
- 239000010935 stainless steel Substances 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 238000004458 analytical method Methods 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 3
- 230000008859 change Effects 0.000 description 3
- 239000003638 chemical reducing agent Substances 0.000 description 3
- 230000007547 defect Effects 0.000 description 3
- 238000009826 distribution Methods 0.000 description 3
- 238000002474 experimental method Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 230000007246 mechanism Effects 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- 229910002651 NO3 Inorganic materials 0.000 description 2
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 2
- 238000003915 air pollution Methods 0.000 description 2
- 230000005540 biological transmission Effects 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 229910052802 copper Inorganic materials 0.000 description 2
- 239000010949 copper Substances 0.000 description 2
- 239000011258 core-shell material Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005538 encapsulation Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 230000036541 health Effects 0.000 description 2
- 238000004949 mass spectrometry Methods 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 238000005070 sampling Methods 0.000 description 2
- 238000004627 transmission electron microscopy Methods 0.000 description 2
- 238000012795 verification Methods 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 239000012080 ambient air Substances 0.000 description 1
- 150000003863 ammonium salts Chemical class 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000009529 body temperature measurement Methods 0.000 description 1
- 238000001311 chemical methods and process Methods 0.000 description 1
- 239000013626 chemical specie Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 230000031700 light absorption Effects 0.000 description 1
- 210000004072 lung Anatomy 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- 239000002923 metal particle Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 230000000877 morphologic effect Effects 0.000 description 1
- 239000002105 nanoparticle Substances 0.000 description 1
- 230000003287 optical effect Effects 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000000741 silica gel Substances 0.000 description 1
- 229910002027 silica gel Inorganic materials 0.000 description 1
- 238000004088 simulation Methods 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Images
Classifications
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N15/00—Investigating characteristics of particles; Investigating permeability, pore-volume, or surface-area of porous materials
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N15/00—Investigating characteristics of particles; Investigating permeability, pore-volume, or surface-area of porous materials
- G01N15/02—Investigating particle size or size distribution
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N15/00—Investigating characteristics of particles; Investigating permeability, pore-volume, or surface-area of porous materials
- G01N15/02—Investigating particle size or size distribution
- G01N15/0266—Investigating particle size or size distribution with electrical classification
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N15/00—Investigating characteristics of particles; Investigating permeability, pore-volume, or surface-area of porous materials
- G01N15/02—Investigating particle size or size distribution
- G01N15/0272—Investigating particle size or size distribution with screening; with classification by filtering
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N15/00—Investigating characteristics of particles; Investigating permeability, pore-volume, or surface-area of porous materials
- G01N15/10—Investigating individual particles
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N27/00—Investigating or analysing materials by the use of electric, electrochemical, or magnetic means
- G01N27/62—Investigating or analysing materials by the use of electric, electrochemical, or magnetic means by investigating the ionisation of gases, e.g. aerosols; by investigating electric discharges, e.g. emission of cathode
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N15/00—Investigating characteristics of particles; Investigating permeability, pore-volume, or surface-area of porous materials
- G01N2015/0042—Investigating dispersion of solids
- G01N2015/0046—Investigating dispersion of solids in gas, e.g. smoke
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N15/00—Investigating characteristics of particles; Investigating permeability, pore-volume, or surface-area of porous materials
- G01N15/02—Investigating particle size or size distribution
- G01N2015/0288—Sorting the particles
-
- G01N2015/1028—
-
- G01N2015/1029—
Abstract
The invention discloses a real-time online measurement system for volatile characteristics and mixing state of aerosol, which comprises: the system comprises an acquisition subsystem (100) for acquiring sample gas at room temperature and screening aerosol particles with target particle size from the sample gas; a thermal diffusion subsystem (200) for sequentially applying a plurality of ramping operations to the aerosol particles over an observation period to volatilize volatile components of the aerosol particles; a measurement subsystem (300) for sequentially measuring parameters of the aerosol particles at room temperature and after a plurality of said ramping operations; and the control subsystem (400) is used for controlling the collection subsystem (100), the thermal diffusion subsystem (200) and the measurement subsystem (300) to work and obtaining the aerosol volatilization characteristics and the mixing state according to the parameters.
Description
Technical Field
The invention relates to the technical field of atmospheric measurement, in particular to a real-time online measurement system for aerosol volatilization characteristics and mixing state.
Background
From the beginning of the century, the air pollution in China gradually evolves into regional and compound air pollution, which is mainly characterized in that the concentration of fine particulate matters (PM2.5) is seriously exceeded, the atmospheric visibility is rapidly deteriorated, and further, the disastrous weather such as city fog/haze is obviously increased, the air quality and the human health are endangered, and the normal production, traffic and daily life are seriously influenced. The PM2.5 has complex components and mainly comprises organic matters, element carbon, sulfate, nitrate, ammonium salt, trace metals, crust elements and the like. Generally, these different types of components do not exist individually in the atmosphere but exist in various mixed states due to complicated atmospheric physical and chemical processes (such as adsorption and agglomeration, mutual encapsulation of particles, heterogeneous reaction, cloud process, etc.). Current research mainly classifies the mixing regime of PM2.5 into two categories, external mixing and internal mixing: the external mixing means that a single compound is only distributed on a single particle, and the internal mixing means that different compounds are mixed and distributed on the single particle; the internal mixing state particulate matter is divided into homogeneous internal mixing and heterogeneous internal mixing, wherein the homogeneous internal mixing means that different compounds are uniformly distributed in a single particle, and the heterogeneous internal mixing can be called as the core-shell distribution state of the particle. The mixed particles have great changes in various aspects of properties and environmental effects. First, the optical properties of the aerosol can change, for example, when soot and sulfate are mixed in a "core-shell" form, the light absorption capacity of the soot can be increased by a factor of two by the encapsulation of the sulfate. Second, the mixing regime directly affects the hygroscopic characteristics of the aerosol. For example, fresh soot particles are typically non-hygroscopic, but they undergo various aging processes, such as condensation, oxidation, and cloud processes, after entering the atmosphere. In these processes, soot particles can intermix with a variety of organic or inorganic substances, thereby significantly altering their hygroscopicity in the atmosphere. Furthermore, toxic components in the particles, such as nano-sized soot, organic matter and metal particles, are present mainly in an intermixed form with the sulfate and nitrate aerosols. By internal mixing, the acid salt reacts with the metal to convert the insoluble metal oxide to metal ions which can readily enter the lung fluid. Moreover, the intermixing of the same chemical species increases the overall redox activity of the particulate matter, thereby creating a more serious hazard to human health. The influence of the mixed state on the properties of the particles is also reflected in various reaction processes in the atmosphere, the formation of cloud and the like. It can be seen that the mixing state is one of the important parameters for evaluating the various types of effects of the particulate matter. However, the information obtained by the prior art is still very insufficient, and can not meet the requirements of laboratory research and model simulation.
At present, the measurement of the aerosol mixing state at home and abroad is mainly based on two types of instruments, the first type is a Transmission Electron microscope (Transmission Electron microscope), the particle form can be measured, and the morphological characteristics of the particles can be displayed visually. The second is some online high time resolution devices, such as SP2(single particle photo meter), VTDMA (volume resolution mobility analyzer), PALM (particle analysis by mass spectrometer), ATOFMS (atomic time-of-thin mass spectrometer), SPAMS (single particle analysis mass spectrometer), and NanoSIMS (nanometer-scale collection mass spectrometer).
The research in this area is relatively late in China, but relatively rich research results are obtained currently, wherein two widely applied methods comprise single particle aerosol mass spectrometry (SPAMS or ATOFMS) and Transmission Electron Microscopy (TEM). SPAMS is single-particle aerosol mass spectrometry observation equipment independently developed by scientific research teams in China, and has been widely applied and obtained abundant achievements in China.
The existing aerosol volatilization characteristic and mixing state technology has the following defects:
(1) although TEM can observe the appearance of the aerosol and conjecture the aerosol mixing state, the device is based on a film sampling sample, has low time resolution (more than 24 hours), is difficult to realize long-time and high-frequency sampling observation, is not beneficial to the research of the aerosol aging mechanism, and has weak measuring capability on semi-volatile components;
(3) the online observation instrument represented by SPAMS cannot visually display the features of the particles of different types, such as appearance, structure and the like, so that the analysis depth is limited;
(1) the initial applications of the above-mentioned online observation instruments and devices are not directed to the observation of the aerosol mixture state, but to the online measurement of the physicochemical properties of the aerosol, and are therefore expensive (in millions).
Therefore, there is a need in the art to develop a real-time online measurement system for aerosol volatilization characteristics and mixing status, which can be monitored at high frequency, is easy to operate and maintain, and is inexpensive.
Disclosure of Invention
In view of the above, the present invention has been developed to provide a real-time online measurement system for aerosol volatility characteristics and mixing status that overcomes, or at least partially solves, the above-mentioned problems.
In order to achieve the above object, the present invention provides a real-time online measurement system for volatile characteristics and mixing status of aerosol, comprising:
the system comprises an acquisition subsystem, a data processing subsystem and a data processing subsystem, wherein the acquisition subsystem is used for acquiring sample gas at room temperature and screening aerosol particles with target particle size from the sample gas; a thermal diffusion subsystem for sequentially applying a plurality of temperature ramping operations to the aerosol particles during an observation period to volatilize volatile components of the aerosol particles; the measurement subsystem is used for sequentially measuring the parameters of the aerosol particles at room temperature and after a plurality of temperature raising and lowering operations; and the control subsystem is used for controlling the collection subsystem, the thermal diffusion subsystem and the measurement subsystem to work and obtaining the volatilization characteristic and the mixing state of the aerosol according to the parameters.
In some examples, the cooling and warming operation includes: sequentially heating aerosol particles at room temperature to a plurality of observation temperatures and maintaining the temperature for a preset observation time, and then cooling the aerosol particles to the room temperature.
In some examples, the thermal diffusion subsystem and the control subsystem constitute a third order heating system.
In some examples, under the control of the control subsystem, the thermal diffusion subsystem may sequentially heat aerosol particles to N observation temperatures and maintain for T/(N +1) minutes, and cool the aerosol particles to room temperature, and the measurement subsystem may sequentially measure the aerosol particles at room temperature and after the ramping operation for T/(N +1) minutes, respectively, during an observation period T.
In some examples, the thermal diffusion subsystem comprises: room temperature diffusion, which is used for conveying the aerosol particles at room temperature to at least two thermal diffusion tubes of the measurement subsystem, sequentially heating the aerosol particles at room temperature to a plurality of observation temperatures in turn and maintaining the predetermined observation time, and then cooling the aerosol particles to room temperature; and the electromagnetic valve assembly is used for switching the gas circuit to control the flow direction of the aerosol particles so that the aerosol particles sequentially flow into the room temperature diffusion tube 7 and the at least two thermal diffusion tubes in the observation period.
In some examples, the solenoid valve assembly comprises: a first solenoid valve and a second solenoid valve; the at least two heat diffusion tubes include: a first thermal diffusion tube and a second thermal diffusion tube; the first heat diffusion tube includes: the first heating pipe and first cooling adsorption tube, the second heat diffusion pipe includes: a second heating pipe and a second cooling adsorption pipe.
In some examples, the first and second heating tubes each include: heating band, gradual flow fan, inner tube, outer tube and thermocouple.
In some examples, the inner tube is used to heat aerosol particles to volatilize volatile components; the outer tube is located outside the inner tube and the heating band for supporting and protecting the inner tube.
In some examples, the heating tape covers the outer wall of the inner tube for heating the inner tube.
In some examples, the thermocouple is configured to measure a real-time temperature of the inner tube and send the real-time temperature to the control subsystem.
In some examples, the flow-by-flow fan is mounted on the outer tube for cooling the inner tube.
In some examples, the first cooling sorbent tube and the second cooling sorbent tube each comprise: outer tube, inner tube, active carbon and cooling tube.
In some examples, the inner tube is for passage of heated aerosol particles; the outer pipe is arranged outside the inner pipe, and a space is formed between the outer pipe and the inner pipe.
In some examples, the cooling tube is located within the outer tube and is helically coiled around the inner tube for cooling the aerosol particles in the inner tube; the active filling is filled between the inner pipe and the outer pipe and is used for adsorbing volatile components.
In some examples, the control subsystem includes: the relay assembly is used for controlling the electromagnetic valve assembly and the flow-by-flow fan so as to switch a gas circuit, control the flow direction of aerosol particles and reduce the temperature of the first heating pipe and the second heating pipe; the temperature control meter assembly is used for increasing the temperatures of the first thermal diffusion pipe and the second thermal diffusion pipe in turn so as to heat aerosol particles at room temperature to a plurality of observation temperatures in sequence; and the computer is used for controlling the operation of the relay assembly and the temperature control meter assembly and determining the volatilization characteristic and the mixing state of the aerosol according to the parameters of the aerosol particles.
The real-time online measurement system improves the thermal diffusion subsystem, takes the actual temperature in the heating pipe as the reference, and adjusts the set temperature during heating, thereby overcoming the defect that the experimental temperature greatly deviates from the theoretical set temperature in the prior art, increasing the cooling device to realize rapid cooling, and improving the experimental precision and accuracy; the improved two thermal diffusion systems are combined with an aerosol mass spectrometer and an aerosol particle size spectrometer, the physicochemical characteristics of fine particles under different temperature gradients in the pollution process can be determined by switching between real atmosphere and a heating system, the advantage complementation and mutual verification of observation results can be realized, rich information about the characteristics of the mixing condition, the morphology, the structure and the like of the particles is obtained, and the initial source of the particles and a mixed aging mechanism are facilitated to be revealed; the effective use of the double-thermal diffusion tube can greatly save the experimental time, more efficiently acquire the observation result and be beneficial to researching the aerosol aging process under the situation of 'burst growth' of fine particles.
Drawings
Other objects and advantages of the present invention will become apparent from the following description of the invention which refers to the accompanying drawings, and may assist in a comprehensive understanding of the invention.
Fig. 1 is a schematic diagram of a real-time online measurement system for aerosol volatilization characteristics and mixing status in accordance with an embodiment of the present invention.
Fig. 2 is a block diagram of a real-time on-line measurement system of aerosol volatilization characteristics and mixing status in accordance with an embodiment of the present invention.
FIG. 3 is a block diagram of a thermal diffusion subsystem of an embodiment of the present invention.
Fig. 4 is a structural view of a first heating pipe and a second heating pipe according to an embodiment of the present invention.
Fig. 5 is a structural view of a first cooling adsorption tube and a second cooling adsorption tube according to an embodiment of the present invention.
FIG. 6 is a block diagram of a control subsystem of an embodiment of the present invention.
It is noted that the drawings are not necessarily to scale and are merely illustrative in nature and not intended to obscure the reader.
Description of reference numerals:
100-an acquisition subsystem; 200-a thermal diffusion subsystem; 300-a measurement subsystem; 400-a control subsystem; 1-a drying tube; 2-a vacuum pump; 3-a computer; 4-a first electrostatic separator; 5-a solenoid valve assembly; 6-a first heat diffusion tube; 7-room temperature diffusion tube; 8-a second heat diffusion tube; 9-a second electrostatic separator; 10-aerosol mass spectrometer; 11-a particle counter; 12-a heating belt; 13-a flow-by-flow fan; 14-activated carbon; 15-PM2.5 cutting head; 16-an air inlet; 17-air outlet; 18-a first heating tube; 19-a first cooling adsorption tube; 20-a second heating pipe; 21-a second cooling adsorption tube; 22-a first solenoid valve; 23-a second solenoid valve; 24. 28-inner tube; 25. 29-outer tube; 26-a thermocouple; 27-equivalent reducer pipe; 30-a cooling tube; 31-an intake pipe; 32-an air outlet pipe; 33-cooling gas inlet pipe; 34-a cooling gas outlet pipe; 35-a first relay; 36-a second relay; 37-a first temperature control meter; 38-second temperature control gauge.
Detailed Description
In order to make the objects, technical solutions and advantages of the present invention more apparent, the technical solutions of the present invention will be described clearly and completely with reference to the accompanying drawings of the embodiments of the present invention. It should be apparent that the described embodiment is one embodiment of the invention, and not all embodiments. All other embodiments, which can be derived by a person skilled in the art from the described embodiments of the invention without any inventive step, are within the scope of protection of the invention.
Unless defined otherwise, technical or scientific terms used herein shall have the ordinary meaning as understood by one of ordinary skill in the art to which this invention belongs.
The real-time online measurement system for the volatile characteristic and the mixing state of the aerosol can invert the mass concentration and the particle size distribution of the volatile components of the aerosol at different temperatures and invert the mixing state of the aerosol based on the mass concentration and the particle size distribution, so that the real-time online measurement of the volatile characteristic and the mixing state of the aerosol is realized, the time resolution and the representativeness of the measurement result are improved, and the technical problem that the aging process and the environmental influence of the aerosol are difficult to accurately characterize in the field observation at present is solved.
As shown in fig. 1, the system for real-time online measurement of aerosol volatilization characteristics and mixing state of the present embodiment includes:
the collection subsystem 100 is used for collecting sample gas at room temperature and screening aerosol particles with target particle size from the sample gas;
a thermal diffusion subsystem 200 for sequentially applying a plurality of temperature raising and lowering operations to the aerosol particles during an observation period;
a measurement subsystem 300 for sequentially measuring parameters of the aerosol particles at room temperature and after a plurality of temperature raising and lowering operations;
and the control subsystem 400 is used for controlling the collection subsystem 100, the thermal diffusion subsystem 200 and the measurement subsystem 300 to work, and obtaining the volatilization characteristics and the mixing state of the aerosol according to the parameters.
As shown in fig. 2, the acquisition subsystem 100 includes: collection unit and screening unit.
The acquisition unit includes: PM2.5 cutting head 15, drying tube 1 and vacuum pump 2. The PM2.5 cutting head 15 is connected with the vacuum pump 2 through a pipeline. The vacuum pump 2 may form a negative pressure, and under the negative pressure, the PM2.5 cutting head 15 collects the atmosphere at room temperature and screens the target particulate matter, i.e., fine particulate matter, from the atmosphere. The pipeline is provided with the drying pipe 1, and the drying pipe 1 can reduce the humidity of fine particulate matters screened by PM 2.5. In some examples, the drying tube 1 may be a silica gel drying tube; the humidity of the fine particles can be reduced to be below 40%, so that the influence of water vapor on a measurement result is reduced, and the measurement precision and accuracy are improved.
The screening unit comprises a first electrostatic separator 4. The first electrostatic separator 4 is controlled by a control subsystem 400, and the first electrostatic separator 4 may be regulated by the control subsystem 400. The dried fine particulate matter passes through the first electrostatic separator 4, and aerosol particles of a target particle size can be screened out by adjusting the first electrostatic separator 4.
The thermal diffusion subsystem 200 of the present embodiment is connected to the collection subsystem 100, which includes: a solenoid valve assembly 5, a room temperature diffuser 7, and at least two thermal diffusers. The room temperature diffusion pipe 7 and the thermal diffusion pipe are connected with the first electrostatic separator 4 through pipelines, and the electromagnetic valve assembly 5 is installed on the pipeline between the first electrostatic separator 4 and the room temperature diffusion pipe 7 and the thermal diffusion pipe.
The solenoid valve assembly 5 may include a plurality of solenoid valves, and specifically, the number of solenoid valves is the same as the number of heat diffusion pipes. The solenoid valve assembly 5 is used for switching the gas circuit to control the flow direction of the aerosol particles, so that the aerosol particles sequentially flow into the room temperature diffusion tube 7 and the at least two thermal diffusion tubes in the observation period.
The room temperature diffuser 7 is used to transport aerosol particles at room temperature to the measurement subsystem 300. The at least two thermal diffusers may sequentially heat the aerosol particles at room temperature to a plurality of observation temperatures under the control of the control subsystem 400 and deliver the heated aerosol particles to the measurement subsystem 300.
In some examples, as shown in fig. 2 and 3, the solenoid valve assembly 5 includes: a first solenoid valve 22 and a second solenoid valve 23. The at least two heat diffusion tubes include: a first heat diffusion tube 6 and a second heat diffusion tube 8. Under the control of the control subsystem 400, the first electromagnetic valve 22 may open the air path of the room temperature diffusion tube and close the air path of the thermal diffusion tube, or close the air path of the room temperature diffusion tube and open the air path of the thermal diffusion tube, so that the aerosol particles flow to the room temperature diffusion tube 7 or the thermal diffusion tube. The second electromagnetic valve 23 can open the first thermal diffusion tube gas path and close the second thermal diffusion tube gas path, or close the first thermal diffusion tube gas path and open the second thermal diffusion tube gas path, so that the aerosol particles flow to the first thermal diffusion tube 6 or the second thermal diffusion tube 8.
The first heat diffusion tube 6 and the second heat diffusion tube 8 have the same structure. The first heat diffusion tube 6 includes: the first heating pipe 18 and the first cooling adsorption pipe 19, the second heat diffusion pipe 8 includes: a second heating pipe 20 and a second cooling adsorption pipe 21. As shown in fig. 2, each heating tube has a heating belt 12 and a flow-by-flow fan 13, and each cooling adsorption tube has activated carbon 14.
The first heating pipe 18 and the second heating pipe 20 have the same structure, and the structure thereof will be described below by taking the first heating pipe 18 as an example. As shown in fig. 4, the first heating pipe 18 includes: heating belt 12, gradual flow fan 13, equivalent reducer 27, inner tube 24, outer tube 25 and thermocouple 26.
An inner tube 24 for heating the aerosol particles to volatilize the volatile components. The inner tube 24 may be any material that conducts heat well, and in some examples a stainless steel tube may be used. The inner tube diameter may be larger than the tube diameter, thereby increasing the residence time of the aerosol particles in the heating tube. The air inlet end and the air outlet end of the inner pipe 24 are connected with the pipeline through an equivalent reducer pipe 27. As the aerosol particles pass through the inner tube 24, the aerosol particles are heated as the inner tube 24 is heated by the heating belt 12 to maintain a predetermined temperature, causing the volatile components of the aerosol particles to volatilize due to the heating.
And the heating belt 12 is covered on the outer wall of the inner pipe 24 and used for heating the inner pipe 24. The heating belt 12, under the control of the control subsystem 400, heats the inner tube 24 and maintains the inner tube 24 at the observed temperature for a predetermined time.
The outer tube 25, which is located outside the inner tube 24 and the heating belt 12, functions to support and protect the inner tube 24. In some examples, the outer tube 25 may be stainless steel tubing and the outer tube 25 may be wrapped with a sponge to prevent scalding of the experimenter.
A thermocouple 26 for measuring the real-time temperature of the inner tube 24 and sending the real-time temperature measurement to the control subsystem 400 to determine whether the inner tube 24 has reached a set temperature. Because the temperature in the cavity of the inner tube 24 is different from the temperature measured by the thermocouple 26, the thermocouple 26 measures the real-time temperature of the central axis of the inner tube 24, and the control subsystem 400 adjusts the observed temperature of the inner tube 24 with reference to the real-time temperature.
The gradual-flow fan 13 is mounted on the outer tube 25 and comprises: a flow-by-flow fan 13 at the air inlet 16 and a flow-by-flow fan 13 at the air outlet 17. When it is desired to cool down the first heating duct 18, the free-flow fan 13 is switched on. The flow-by-flow fan 13 of the air inlet 16 sucks in external cold air, and the flow-by-flow fan 13 of the air outlet 17 blows out hot air in the outer pipe 25, so that the inner pipe 24 is accelerated to cool through air flow.
The first cooling adsorption tube 19 and the second cooling adsorption tube 21 have the same structure, and the structure of the first cooling adsorption tube 19 will be described below as an example. As shown in fig. 5, the first cooling adsorption tube 19 includes: including an outer tube 29, an inner tube 28, the activated carbon 14, and a cooling tube 30.
An inner tube 28 for passing the heated aerosol particles. The inner tube 28 may be a stainless steel mesh tube.
The outer tube 29, which is located outside the inner tube 28, forms a space with the inner tube 28. The outer tube 29 may be made of any material having good sealing properties, and in some examples, a stainless steel tube may be used. The ends of the inner tube 28 and the outer tube 29 are secured and sealed with plastic O-rings. Both ends of the outer tube 29 are provided with external threads, respectively, and sealing caps, the inner sides of which are provided with internal threads, are matched with the external threads at both ends of the outer tube 29 to seal and fix the inner tube 28, the outer tube 29 and the O-ring as a whole. The O-rings at the two ends of the outer tube 29 are respectively provided with an air inlet tube 31 and an air outlet tube 32, and the air inlet tube 31 and the air outlet tube 32 are respectively connected with the first heating tube 18 and the measurement subsystem 300. The pipe wall of the outer pipe 29 near both ends is provided with a cooling gas inlet pipe 33 and a cooling gas outlet pipe 34 respectively.
And the cooling pipe 30 is positioned in the outer pipe 29 and spirally wound on the inner pipe 28, and two ends of the cooling pipe are respectively connected with a cooling gas inlet pipe 33 and a cooling gas outlet pipe 34 for rapidly cooling aerosol particles passing through the inner pipe 28. The cooling tube 30 may be made of a material having good heat conductivity and sealing property, and in some examples, a metal copper tube may be used, and a cooling gas is introduced into the copper tube to reduce the temperature of the aerosol particles in the cooling adsorption tube through the flow of the cooling gas. The cooling adsorption tube of the present embodiment has high sealing performance, aerosol particles only enter from the inlet tube 31 and exit from the outlet tube 32, and cooling gas only flows in the cooling tube 30.
The space between the inner tube 28 and the outer tube 29 is filled with activated carbon 14. After the aerosol particles are heated, the volatile components of the aerosol particles are volatilized into gas, and the gaseous volatile components are adsorbed by the activated carbon 14, so that the volatile components are prevented from being re-condensed to the surfaces of the aerosol particles in the cooling process.
As shown in fig. 2, the measurement subsystem 300 of the present embodiment includes: a second electrostatic separator 9, an aerosol mass spectrometer 10 and a particle counter 11.
The second electrostatic separator 9 is used to measure the particle size of the aerosol particles passing through the thermal diffusion subsystem 200. After the particle size is measured by the second electrostatic separator 9, the aerosol particles enter the aerosol mass spectrometer 10 and the particle counter 11, respectively. The aerosol mass spectrometer 10 is used to analyze the chemical composition of aerosol particles and the particle counter 11 is used to measure the concentration of aerosol particles.
The control subsystem 400 of the present embodiment includes: computer 3, relay assembly and temperature control table subassembly. The relay assembly is used for controlling the electromagnetic valve assembly 5 and the flow-by-flow fan 13 so as to switch the air path and control the flow direction of aerosol particles and reduce the temperature of each heat diffusion tube. The temperature control meter component is used for increasing the temperature of each thermal diffusion tube in turn so as to heat aerosol particles at room temperature to a plurality of observation temperatures in sequence. The computer 3 is used to control the operation of the relay assembly, the temperature control gauge assembly and the first electrostatic separator 4. The computer 3 is also connected with the measurement subsystem 300, receives the particle size of the aerosol particles measured by the second electrostatic separator 9, the chemical composition of the aerosol particles analyzed by the aerosol mass spectrometer 10 and the concentration of the aerosol particles measured by the particle counter 11, and determines the volatilization characteristic and the mixing state of the aerosol according to the parameters of the aerosol particles.
In some examples, as shown in fig. 6, a relay assembly includes: a first relay 35 and a second relay 36. The first relay 35 is connected with the first solenoid valve 22 and the second solenoid valve 23, and each solenoid valve corresponds to two switching values. The first relay 35 controls the first electromagnetic valve 22 to switch the air path between the air path of the room temperature diffusion tube 7 and the air path of the thermal diffusion tube. The first relay 35 controls the second solenoid valve 23 to switch the gas path between the gas path of the first heat diffusion pipe 6 and the gas path of the second heat diffusion pipe 8. The second relay 36 is connected with the four flow-by-flow fans 13 of the first heating pipe 18 and the second heating pipe 20, and when the heating pipes need to be cooled, the second relay 36 turns on the flow-by-flow fans 13 to cool the heating pipes.
The temperature control gauge assembly comprises: a first temperature control gauge 37 and a second temperature control gauge 38. The first temperature control gauge 37 is connected to the heating zone 12 of the first heating tube 18 and the thermocouple 26, and the second temperature control gauge 38 is connected to the heating zone 12 of the second heating tube 20 and the thermocouple 26. Each temperature control meter comprises a thermocouple input module and a relay output module, the thermocouple input module measures the temperature of the heating pipe in real time and feeds the temperature back to the relay output module, and meanwhile the relay output module controls the heating temperature of the heating belt 12. When the temperature of the current heating pipe is lower than the set temperature, the relay output module controls the heating belt 12 to heat the heating pipe, and when the temperature of the current heating pipe is higher than the set temperature, the relay output module controls the heating belt 12 to be closed. The first relay 35, the second relay 36, the first temperature control meter 37 and the second temperature control meter 38 are all connected with the computer 3 through an RS485 bus, the state of the valve assembly and the temperature of the heating pipe are transmitted to the computer 3, and the computer 3 sends instructions to the relay assembly and the temperature control meter assembly, so that the switching of the valve assembly and the change of the temperature of the heating pipe are controlled to start and close the flow-by-flow fan 13.
The real-time on-line measuring system of this embodiment, a plurality of processes of going up and down to warm include: sequentially heating aerosol particles at room temperature to a plurality of observation temperatures and maintaining the temperature for a preset observation time, and then cooling the aerosol particles to the room temperature.
In the real-time online measurement system of the present embodiment, when the thermal diffusion subsystem 200 includes one room temperature diffusion tube 7 and two thermal diffusion tubes, the thermal diffusion subsystem 200 and the control subsystem 400 constitute a third-order heating system. Under the control of the control subsystem 400, the thermal diffusion subsystem 200 may sequentially heat the aerosol particles to N observation temperatures for T/(N +1) minutes and then cool the aerosol particles to room temperature during the observation period T, so that the measurement subsystem 300 sequentially measures the aerosol particles at room temperature and after the temperature increase and decrease operations for T/(N +1) minutes, respectively. In some examples, the observation period T is 60 minutes and N has a value of 5, and the operation of the real-time online measurement system is described in detail below.
First, the atmosphere screens out the target particulate matter, i.e., fine particulate matter, by the PM2.5 cutting head 15. After the fine particles pass through the drying tube 1, the humidity of the fine particles can be reduced to below 40%. The electrostatic separator screens aerosol particles with a target particle size from the dried fine particulate matter, and the flow direction of the aerosol particles is regulated by the electromagnetic valve assembly 5. The temperature dependence of the volatile components was established by preliminary experiments, setting 5 different observed temperatures, for example: room temperature (atmospheric temperature) is 50 ℃ (the first thermal diffusion tube 6) to 100 ℃ (the second thermal diffusion tube 8) to 150 ℃ (the first thermal diffusion tube 6) to 220 ℃ (the second thermal diffusion tube 8) to 280 ℃ (the first thermal diffusion tube 6). Specifically, when the experiment starts, the control subsystem 400 controls the first electromagnetic valve 22 to switch the gas path to the room temperature diffusion tube 7, the measurement subsystem 300 measures the parameters of the aerosol particles at room temperature, and simultaneously controls the first heating tube 18 to be heated to 50 ℃; after 10 minutes, the first electromagnetic valve 22 switches the gas circuit to the thermal diffusion tube, the second electromagnetic valve 23 switches the gas circuit to the first thermal diffusion tube 6, the aerosol particles are heated to 50 ℃ in the first heating tube 18, then the aerosol particles are cooled to room temperature through the first cooling adsorption tube 19 and adsorb volatile components, the measurement subsystem 300 measures parameters of the aerosol particles which are cooled to the room temperature after being heated to 50 ℃, and meanwhile the second heating tube 20 is controlled to be heated to 100 ℃; after 10 minutes, the second electromagnetic valve 23 switches the gas circuit to the second heat diffusion pipe 8, the first heating pipe 18 is heated to 150 ℃, and the observation period of room temperature (atmospheric temperature) -50 ℃ (the first heating pipe 18) -100 ℃ (the second heating pipe 20) -150 ℃ (the first heating pipe 18) -220 ℃ (the second heating pipe 20) -280 ℃ (the first heating pipe 18) is realized in a circulating manner. The time is considered to be short enough within an observation period of 1 hour that the aerosol particles of ambient air do not change significantly under most conditions, and therefore the observations at different temperature gradients within this observation period are considered to be comparable. After an observation period is completed, the first electromagnetic valve 22 switches the gas path to the room temperature diffusion tube 7, the flow-by-flow fan 13 of the heating tube is started, the first heating tube 18 is cooled to 50 ℃, and the second heating tube 20 is cooled to 100 ℃, and the experiment of the next observation period is started. The computer 3 determines the volatilization characteristics and the mixing state of the aerosol according to the particle size, the chemical composition and the concentration of the aerosol particles at room temperature and after each temperature rise and drop process.
The real-time online measurement system of the embodiment improves the thermal diffusion subsystem, and adjusts the set temperature during heating by taking the actual temperature in the heating pipe as a reference, so that the defect that the experimental temperature greatly deviates from the theoretical set temperature in the prior art is overcome, a cooling device is added to realize rapid cooling, and the experimental precision and accuracy are improved; the improved two thermal diffusion systems are combined with an aerosol mass spectrometer and an aerosol particle size spectrometer, the physicochemical characteristics of fine particles under different temperature gradients in the pollution process can be determined by switching between real atmosphere and a heating system, the advantage complementation and mutual verification of observation results can be realized, rich information about the characteristics of the mixing condition, the morphology, the structure and the like of the particles is obtained, and the initial source of the particles and a mixed aging mechanism are facilitated to be revealed; the effective use of the double-thermal diffusion tube can greatly save the experimental time, more efficiently acquire the observation result and be beneficial to researching the aerosol aging process under the situation of 'burst growth' of fine particles.
It should also be noted that, in the case of the embodiments of the present invention, features of the embodiments and examples may be combined with each other to obtain a new embodiment without conflict.
The above description is only an embodiment of the present invention, but the scope of the present invention is not limited thereto, and the scope of the present invention is subject to the scope of the claims.
Claims (15)
1. Real-time online measurement system of aerosol volatility characteristic and mixing state, its characterized in that includes:
the system comprises an acquisition subsystem (100) for acquiring sample gas at room temperature and screening aerosol particles with target particle size from the sample gas;
a thermal diffusion subsystem (200) for sequentially applying a plurality of ramping operations to the aerosol particles over an observation period to volatilize volatile components of the aerosol particles;
a measurement subsystem (300) for sequentially measuring parameters of the aerosol particles at room temperature and after a plurality of said ramping operations;
and the control subsystem (400) is used for controlling the collection subsystem (100), the thermal diffusion subsystem (200) and the measurement subsystem (300) to work and obtaining the aerosol volatilization characteristics and the mixing state according to the parameters.
2. The real-time online measurement system of claim 1, wherein the ramping operation comprises: sequentially heating aerosol particles at room temperature to a plurality of observation temperatures and maintaining the temperature for a preset observation time, and then cooling the aerosol particles to the room temperature.
3. The real-time on-line measurement system of claim 1, wherein the thermal diffusion subsystem (200) and the control subsystem (400) constitute a third order heating system.
4. The real-time on-line measurement system of claim 3, wherein under the control of the control subsystem (400), the thermal diffusion subsystem (200) sequentially heats aerosol particles to N observation temperatures and maintains T/(N +1) minutes, and lowers the aerosol particles to room temperature, and the measurement subsystem (300) sequentially measures the aerosol particles at room temperature and after the temperature raising and lowering operations for T/(N +1) minutes.
5. The real-time on-line measurement system of claim 1, wherein the thermal diffusion subsystem (200) comprises:
a room temperature diffuser tube (7) for transporting aerosol particles at room temperature to the measurement subsystem (300);
the thermal diffusion pipes are used for sequentially heating aerosol particles at room temperature to a plurality of observation temperatures in turn and maintaining the predetermined observation time, and then cooling the aerosol particles to the room temperature;
and the electromagnetic valve assembly (5) is used for switching the gas circuit to control the flow direction of the aerosol particles so that the aerosol particles sequentially flow into the room-temperature diffusion tube (7) and the at least two thermal diffusion tubes in an observation period.
6. The real-time on-line measurement system of claim 5,
the solenoid valve assembly (5) comprises: a first solenoid valve (22) and a second solenoid valve (23);
the at least two heat diffusion tubes include: a first thermal diffusion tube (6) and a second thermal diffusion tube (8);
the first heat diffusion tube (6) comprises: a first heating pipe (18) and a first cooling adsorption pipe (19), the second heat diffusion pipe (8) comprising: a second heating pipe (20) and a second cooling adsorption pipe (21).
7. The real-time on-line measuring system of claim 6, characterized in that the first and second heating pipes (18, 20) each comprise: a heating belt (12), a flow-by-flow fan (13), an inner tube (24), an outer tube (25) and a thermocouple (26).
8. The real-time on-line measurement system of claim 7, wherein the inner tube (24) is for heating aerosol particles to volatilize volatile components; the outer tube (25) is located outside the inner tube (24) and the heating belt (12) for supporting and protecting the inner tube (24).
9. The real-time on-line measuring system of claim 7, wherein the heating tape (12) covers the outer wall of the inner tube (24) for heating the inner tube (24).
10. The real-time on-line measurement system of claim 7 wherein the thermocouple (26) is configured to measure a real-time temperature of the inner tube (24) and transmit the real-time temperature to the control subsystem (400).
11. The real-time on-line measuring system according to claim 7, characterized in that the flow-by-flow fan (13) is mounted on the outer tube (25) for cooling the inner tube (24).
12. The real-time on-line measuring system of claim 6, wherein the first cooling sorbent tube (19) and the second cooling sorbent tube (21) each comprise: an outer tube (29), an inner tube (28), activated carbon (14) and a cooling tube (30).
13. The real-time on-line measurement system of claim 12, wherein the inner tube (28) is adapted for passage of heated aerosol particles; the outer pipe (29) is located outside the inner pipe (28), and a space is formed between the outer pipe and the inner pipe (28).
14. The real-time on-line measuring system of claim 12, wherein the cooling tube (30) is located within the outer tube (29) and is helically coiled around the inner tube (28) for cooling the aerosol particles in the inner tube (28); the activated carbon (14) is filled between the inner tube (28) and the outer tube (29) for adsorbing volatile components.
15. The real-time on-line measurement system of claim 7, wherein the control subsystem (400) comprises:
a relay assembly for controlling the solenoid valve assembly (5) and the flow-by-flow fan (13) to switch gas paths and control the flow direction of aerosol particles, and to reduce the temperature of the first and second heating tubes (18, 20);
the temperature control meter assembly is used for increasing the temperatures of the first thermal diffusion pipe and the second thermal diffusion pipe in turn so as to heat aerosol particles at room temperature to a plurality of observation temperatures in sequence;
and the computer (3) is used for controlling the operation of the relay assembly and the temperature control meter assembly and determining the volatilization characteristic and the mixing state of the aerosol according to the parameters of the aerosol particles.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202011584800.4A CN112730164A (en) | 2020-12-28 | 2020-12-28 | Real-time online measurement system for volatilization characteristics and mixing state of aerosol |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202011584800.4A CN112730164A (en) | 2020-12-28 | 2020-12-28 | Real-time online measurement system for volatilization characteristics and mixing state of aerosol |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN112730164A true CN112730164A (en) | 2021-04-30 |
Family
ID=75606848
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202011584800.4A Pending CN112730164A (en) | 2020-12-28 | 2020-12-28 | Real-time online measurement system for volatilization characteristics and mixing state of aerosol |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN112730164A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113504160A (en) * | 2021-07-09 | 2021-10-15 | 西南交通大学 | Efficient and accurate temperature control thermal diffusion tube heating system |
-
2020
- 2020-12-28 CN CN202011584800.4A patent/CN112730164A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113504160A (en) * | 2021-07-09 | 2021-10-15 | 西南交通大学 | Efficient and accurate temperature control thermal diffusion tube heating system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| Drewnick et al. | Intercomparison and evaluation of four semi-continuous PM2. 5 sulfate instruments | |
| CN214584711U (en) | Real-time online measurement system for volatilization characteristics and mixing state of aerosol | |
| JP6313609B2 (en) | Nitrate particle measuring apparatus and measuring method thereof | |
| Hodgson et al. | A multisorbent sampler for volatile organic compounds in indoor air | |
| CN112730164A (en) | Real-time online measurement system for volatilization characteristics and mixing state of aerosol | |
| Polidori et al. | Laboratory evaluation of low-cost air quality sensors | |
| Harshman et al. | Evaluation of a standardized collection device for exhaled breath sampling onto thermal desorption tubes | |
| KR20180106830A (en) | Experimental apparatus and experimental method for measuring indoor and outdoor penetration coefficient of airborne | |
| CN111781251A (en) | Device for measuring content of low-concentration gas in flue gas | |
| Trujillo et al. | Development of a multistage air sampler for mercury | |
| JP2003130860A (en) | Automatic volatile substance analyzer | |
| CN111982784A (en) | PM2.5 cutterbar characteristic calibrating device | |
| Qian et al. | A pre-concentration system design for electronic nose via finite element method | |
| WO2023093203A1 (en) | Monitoring device and monitoring method for atmospheric mercury in different states | |
| Swaans et al. | Laboratory and field validation of a combined NO 2–SO 2 Radiello passive sampler | |
| CN208427075U (en) | More sheath Atmospheric Chemistry laminar flow reaction systems | |
| JP2001159592A (en) | Heat generated gas evaluating device | |
| JP2002214116A (en) | Gas removal rate test method and testing device of chemical filter | |
| CN105738579A (en) | Treatment method for improving atmospheric particulate measurement precision | |
| Helsper et al. | On the influence of the vapour substance on the behaviour of an expansion-type condensation nucleus counter | |
| Su et al. | Development of aerosol sample introduction interface coupled with ICP-MS for direct introduction and quantitative online monitoring of environmental aerosol | |
| Misra et al. | Development and evaluation of a compact facility for exposing humans to concentrated ambient ultrafine particles | |
| CN212341122U (en) | Half open type dynamic box system for measuring plant BVOCs emission in outfield | |
| Ferlin et al. | A very simple and fast analytical method for atmospheric particulate-bound mercury determination | |
| TWM457175U (en) | Positive pressure gas supply device capable of controlling temperature and humidity |
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 |