WO2020171594A1 - Appareil pour mesurer en continu et automatiquement des poussières fines dans des gaz d'échappement de cheminée - Google Patents

Appareil pour mesurer en continu et automatiquement des poussières fines dans des gaz d'échappement de cheminée Download PDF

Info

Publication number
WO2020171594A1
WO2020171594A1 PCT/KR2020/002409 KR2020002409W WO2020171594A1 WO 2020171594 A1 WO2020171594 A1 WO 2020171594A1 KR 2020002409 W KR2020002409 W KR 2020002409W WO 2020171594 A1 WO2020171594 A1 WO 2020171594A1
Authority
WO
WIPO (PCT)
Prior art keywords
flow rate
exhaust gas
sample
fine dust
particle size
Prior art date
Application number
PCT/KR2020/002409
Other languages
English (en)
Korean (ko)
Inventor
김근식
Original Assignee
주식회사 정엔지니어링
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 주식회사 정엔지니어링 filed Critical 주식회사 정엔지니어링
Publication of WO2020171594A1 publication Critical patent/WO2020171594A1/fr

Links

Images

Classifications

    • G—PHYSICS
    • G01—MEASURING; TESTING
    • G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N1/00—Sampling; Preparing specimens for investigation
    • G01N1/02—Devices for withdrawing samples
    • G01N1/22—Devices for withdrawing samples in the gaseous state
    • G01N1/2247—Sampling from a flowing stream of gas
    • G01N1/2258—Sampling from a flowing stream of gas in a stack or chimney
    • G—PHYSICS
    • G01—MEASURING; TESTING
    • G01F—MEASURING VOLUME, VOLUME FLOW, MASS FLOW OR LIQUID LEVEL; METERING BY VOLUME
    • G01F1/00—Measuring the volume flow or mass flow of fluid or fluent solid material wherein the fluid passes through a meter in a continuous flow
    • 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

Definitions

  • the present invention relates to a continuous automatic measurement device for fine dust of a chimney exhaust gas, and more specifically, when collecting particulate matter such as fine dust from a flue exhaust gas, by sucking a constant velocity suction flow rate equal to the flow rate of the exhaust gas.
  • a constant constant velocity suction flow required for the particle size separation device is introduced into the measurement line.
  • the present invention relates to a continuous automatic measurement device for fine dust of chimney exhaust gas that enables continuous and automatic measurement of fine dust in exhaust gas.
  • harmful substances may include particulate matter, halogenated gas, and combustion gases such as nitrogen oxide, sulfurous acid gas, carbon monoxide, hydrogen chloride, ammonia, and the like.
  • harmful substances When such harmful substances are absorbed and accumulated in the human body, they not only cause various diseases, but also adversely affect the natural environment, which has been proven through various investigations and experiments.
  • TSP Total Suspended Particles
  • the concentration of fine dust must be collected for a long time due to the characteristics of the collection, but due to the characteristics of the flow velocity of the exhaust gas that changes frequently during such a long time, the constant velocity flow condition in the gas sampling step and the constant velocity flow condition in the particle size separation stage are simultaneously A method, apparatus, or system to meet has so far been very poorly developed in the related field.
  • constant velocity suction In order to measure fine dust, constant velocity suction is essential, and in order to separate and measure fine dust in the constant velocity suction process, particles must be separated by passing through a particle size separation device, but in a particle size separation device, a constant velocity suction flow rate must be sucked. It exists in this one process.
  • the present invention is to solve the above problems, the present invention is a chimney exhaust gas that minimizes the error in the measurement of fine dust by sucking through a suction nozzle at a constant flow rate equal to the flow rate of the exhaust gas when collecting a sample of the exhaust gas It is an object to provide a continuous automatic measuring device for fine dust.
  • the present invention controls the opening and closing of the first control valve provided in the control line in branching the sucked exhaust gas sample into the measurement line and the control line so that a constant speed flow rate is supplied to the particle diameter separation device provided in the measurement line. It is an object of the present invention to provide a continuous automatic measurement device for fine dust of flue gas, which enables precise separation of fine dust and continuous automatic measurement accordingly.
  • a continuous automatic measuring device for fine dust of a chimney exhaust gas for solving the above technical problem includes: a sample collecting unit configured to collect a sample of exhaust gas in the chimney; And branching the exhaust gas samples collected from the sample collection unit at one end in the traveling direction of the exhaust gas sample into a plurality of lines, and combining the exhaust gas samples from the plurality of lines at the other end in the traveling direction of the exhaust gas sample. It may include a sample branch / coupling portion configured.
  • the plurality of lines of the sample branching/combining unit may include a measurement line in which a particle size separation device is provided in at least one area, and a control line in which a first control valve is provided in at least one area.
  • the sample collection unit includes a suction pipe configured to suck an exhaust gas sample and transfer it to the sample branch/combination unit, and at one end of the suction pipe, a suction nozzle disposed in the chimney is provided, and of the suction nozzle
  • the cross-sectional area may be dimensionally designed to suck the exhaust gas sample at a flow rate exceeding the constant flow rate required for the particle size separation device.
  • the particle size separation device is implemented as a cascade impactor consisting of a PM10 impactor and a PM2.5 impactor, and accordingly, the constant flow rate required for the particle size separation device may be 16.67 l/min. .
  • the sample branching/combining unit includes: a dividing flow manifold configured to branch the exhaust gas sample collected from the sample collecting unit into the measurement line and the control line; And a combining flow manifold configured to combine the flow rate of the sample from the measurement line and the control line and transmit it to a constant velocity suction control unit at a rear stage.
  • the measurement line further includes a first flow meter configured to measure the flow rate of the exhaust gas sample flowing through the measurement line, and the constant velocity suction control unit has a constant velocity of the exhaust gas sample output from the coupling manifold.
  • a second flow meter configured to measure the suction flow rate may be provided.
  • the first control valve so that the flow rate measured by the first flow meter corresponds to the constant speed flow rate required for the particle size separation device. It may further include a controller configured to control the opening and closing of.
  • the controller is configured to open the first control valve when the flow rate measured by the first flow meter exceeds the constant speed flow rate required for the particle size separation device, and by the first flow meter It may be configured to close the first control valve when the measured flow rate is less than the constant velocity flow rate required for the particle size separation device.
  • the distance between the separation manifold and the first control valve may be adjustable based on the pressure loss in the measurement line and the pressure loss in the control line.
  • the error in the measurement of fine dust is minimized by suctioning at a constant velocity through a suction nozzle equal to the flow rate of the exhaust gas. can do.
  • the continuous automatic measurement device for fine dust of the chimney exhaust gas in branching the sucked exhaust gas sample into the measurement line and the control line, opening and closing of the first control valve provided in the control line By controlling the flow rate to be supplied to the particle size separation device provided in the measurement line, it is possible to precisely separate fine dust and continuous automatic measurement accordingly.
  • FIG. 1 is a schematic block diagram of an apparatus 10 for continuously measuring fine dust of a chimney exhaust gas according to an embodiment of the present invention.
  • FIG. 2 is a detailed configuration diagram of a continuous automatic measurement device 10 for fine dust of a chimney exhaust gas according to an embodiment of the present invention.
  • FIG 3 is a conceptual diagram for explaining an embodiment of implementing a constant flow rate of the measurement line 220 by the opening and closing operation of the first control valve 231 according to an embodiment of the present invention.
  • FIG. 4 is a conceptual diagram illustrating a variable distance adjustment between the separation manifold 210 and the first control valve 231 according to an embodiment of the present invention.
  • the apparatus 10 for continuous automatic measurement of fine dust of the flue gas according to an embodiment of the present invention includes a sample collection unit 100, a sample branch/combination unit 200, and a pretreatment unit. It may be composed of 300, a gas measurement unit 400, a constant velocity suction control unit 500, a controller 600, and the like.
  • the elements 100, 200, 300, 400, 500, 600 shown in FIG. 1 are the operation, function, etc. of the continuous automatic measurement device 10 for fine dust of the flue gas according to an embodiment of the present invention. It will be apparent that it corresponds to an exemplary element for explaining, and therefore additional elements (eg, a power supply unit, an alarm unit, a monitoring unit, etc.) not shown in FIG. 1 may be further provided.
  • At least a portion of the sample collection unit 100 is disposed in the chimney 1 to collect a sample of exhaust gas in the chimney 1.
  • constant velocity suction is very important, because when the exhaust gas is sucked at a faster rate than the exhaust gas flow rate, the surrounding fine particles are first sucked. This is because when is shown at a lower concentration than the actual concentration, and when suction is performed at a lower velocity than the exhaust gas flow rate, large particles are first sucked by the inertial force, and the result is measured at a higher concentration than the actual value.
  • This constant velocity suction flow condition in the sample collection unit 100 may be implemented by the constant velocity suction control unit 500 according to the control signals i 520 and/or i 530 output from the controller 600, and for this It will be described in more detail in the following.
  • the remaining elements that is, the sample branch/combination unit 200, and the pretreatment unit ( 300), the gas measuring unit 400, the constant velocity suction control unit 500, the controller 600, and the like may be disposed outside the chimney 1.
  • the sample branch/couple 200 provided with the particle diameter separation device 221 is disposed outside the chimney 1 to enable continuous measurement of fine dust, which will be described in more detail below. .
  • the sample branching/combining unit 200 divides the exhaust gas sample collected from the sample collection unit 100 at one end in the traveling direction of the exhaust gas sample into a plurality of lines, and from a plurality of lines at the other end in the traveling direction of the exhaust gas sample.
  • the exhaust gas samples of can be combined.
  • the plurality of lines provided in the sample branching/combining unit 200 may include at least a measurement line 220 (see FIG. 2 below) and a control line 230 (see FIG. 2 below), and the control line 230 ) By controlling the opening and closing of the first control valve 231 (refer to FIG. 2 below) disposed in the particle diameter separation device 221 (refer to FIG. 2 below) disposed in the measurement line 220.
  • 16.67 l/min, etc. may be supplied, and opening and closing of the first control valve 231 may be implemented by a control signal i 231 output from the controller 600.
  • a control signal i 231 output from the controller 600 16.67 l/min, etc.
  • the pretreatment unit 300 may perform a function of removing moisture contained in the exhaust gas output from the sample branch/combination unit 200, and accordingly, the gas measurement unit 400 disposed at the rear end of the exhaust gas progress direction It is possible to protect the constant velocity suction control unit 500. A more detailed description of the operation, function, and the like of the preprocessor 300 will be described later.
  • the gas measuring unit 400 may measure a gas, for example, a gas such as oxygen (O 2 ), carbon dioxide (CO 2 ), and the like.
  • a gas such as oxygen (O 2 ), carbon dioxide (CO 2 ), and the like.
  • the gas measurement unit 400 may include an oxygen sensor, a carbon dioxide sensor, and the like, and a more detailed description of the operation, function, and the like of the gas measurement unit 400 will be described again below.
  • the constant velocity suction control unit 500 may control the opening and closing of the valve and/or the pressure of the pump to satisfy the constant velocity flow suction condition in the sample collection unit 100, which is a control signal output from the controller 600 (i 520 And/or i 530 ). A more detailed description of the operation, function, and the like of the constant velocity suction control unit 500 will be described again below.
  • the controller 600 includes a first control valve 231 in the sample branch/coupler 200 so that the constant velocity suction flow condition in the sample collection unit 100 and the constant velocity suction flow condition in the particle size separation device 221 are satisfied.
  • Open/close control for example, by a control signal (i 231 )
  • valve open/close control and/or pump pressure control in the constant velocity suction control unit 500 for example, control signals (i 520 and/or i 530)
  • the controller 600 may be implemented in other device types such as a micro-controller, a processor, or a micro-processor according to various embodiments or embodiments.
  • the apparatus 10 for continuously measuring fine dust of flue gas includes at least a part of a sample collecting unit disposed inside the chimney 1 ( 100) and a sample branch/combination unit 200 disposed outside the chimney 1, a pretreatment unit 300, a gas measurement unit 400, a constant velocity suction control unit 500, and a controller 600. .
  • the sample collection unit 100 may be configured to collect a sample of exhaust gas in the chimney, and as shown in FIG. 2, the sample collection unit 100 includes a suction tube 110, a Pitot tube 120, and a thermometer 130. Wow, it may be composed of a heating device 140, and the like.
  • the exhaust gas in order to analyze and measure particulate matter such as fine dust in the exhaust gas, it is desirable to collect the exhaust gas from the discharge origin, such as a chimney.This is because the fine dust density condition of the exhaust gas in the chimney is uniform. This is because it is very different from a normal atmosphere. Therefore, since the exhaust gas that deviates from the emission origin such as the chimney is mixed with the general atmosphere and the density is lowered, it is preferable to perform sampling at the emission origin such as the chimney before the exhaust gas is mixed with the general atmosphere.
  • the discharge origin such as a chimney.
  • a pitot tube 120 meeting the standards of the domestic process test method is illustrated as an example.
  • the Pitot tube 120 is a device installed inside the flowing fluid and configured to measure the velocity of the fluid, and a law in which the pressure difference inside/outside the Pitot tube 120 is proportional to the square of the fluid velocity, that is, Bernoulli's law ( The velocity of the fluid can be obtained according to Bernoulli's equation.
  • the suction pipe 110 is provided with a suction nozzle 111 disposed in at least a portion of the chimney 1 at one end thereof, and the other end thereof is a sample branch/combination part 200 and, more specifically, a separation manifold 210 ) And the exhaust gas sample in the chimney may be delivered to the sample branch/coupler 200 through the suction pipe 110.
  • the cross-sectional area of the suction nozzle 111 is characterized in that it is dimensionally designed to suck the exhaust gas sample at a flow rate exceeding the constant flow rate required for the particle size separation device 221.
  • the exhaust gas sample at a flow rate exceeding the constant flow rate required by the particle size separation device 221 may be determined so that the suction nozzle 111 can be sucked at a constant velocity, and the particle diameter separation device 221 is a cascade impactor composed of a PM10 impactor 221a and a PM2.5 impactor 221b.
  • the constant flow rate required for such a cascade-impacter may be 16.67 l/min.
  • the particle size separation device 221 in which the PM10 impactor 221a and the PM2.5 impactor 221b are connected in series is described, but in another embodiment of the present invention, the particle size separation device 221 is Only one of the PM10 impactor 221a and the PM2.5 impactor 221b may be provided, or an additional impactor, for example, a PM1.0 impactor may be further provided.
  • the cross-sectional area of the suction nozzle 111 can be determined to suck the exhaust gas sample at a constant velocity at a flow rate exceeding the constant velocity flow rate required by the particle size separation device 221 based on the design capacity of the chimney 1, etc. Accordingly, a constant flow rate required for particle size separation can be stably supplied to the particle size separation device 221 by a branching operation in the separation manifold 210.
  • the constant velocity suction flow rate (for reference, process test method According to the permissible range of 95% to 110%) can be set to 17.5 l/min to 34 l/min, under these conditions, if the outlet flow rate is 8.5 m/sec and the discharge temperature is 150°C, the constant velocity suction flow rate is 29.2 It can be calculated as l/min.
  • the total flow rate (Q Total ) measured by the second flow meter 510 due to various causes within the chimney is a constant flow rate required for the particle size separation device 221 (eg, 16.67 l/min). May be less than. If the constant velocity flow condition required for the particle size separation device 221 is not satisfied, the particle separation and measurement by the particle size separation device 221 may be regarded as a virtually meaningless operation, so the total flow rate measured by the second flow meter 510 When (Q Total ) falls below a constant flow rate (for example, 16.67 l/min) required for the particle size separation device 221, the controller 600 according to a further embodiment of the present invention is an alarm unit (not shown).
  • the diameter of the suction nozzle 111 may be increased by one level, for example, a suction nozzle 111 having a diameter of 12 mm may be replaced and used.
  • the heating device 140 may be implemented while surrounding at least a portion of the outer circumferential surface of the suction pipe 110, and to prevent condensation of moisture during the transport of the exhaust gas sample, heat from a heat source (not shown) is absorbed by the suction pipe 110. Can be delivered to the sample of exhaust gas inside.
  • thermometer 130 may be additionally disposed in at least a partial region along the longitudinal direction of the suction pipe 110, more preferably near the boundary between the inner region and the outer region of the chimney 1, and the thermometer 130 May measure the temperature of the suction pipe 110 and transmit the measured temperature value to another element, for example, to the controller 600 wirelessly or by wire.
  • the sample collection unit 100 is more specifically configured to measure fine dust by sucking the exhaust gas sample at a constant flow rate equal to the flow rate of the exhaust gas through the suction nozzle 111.
  • the error can be minimized, and the constant velocity flow rate here supplies a flow rate exceeding the constant velocity flow rate required for the particle size separation device 221, and the constant velocity suction flow rate condition in the suction nozzle 111 is provided in the constant velocity suction control unit 500
  • It may be implemented by opening and closing of the second control valve 520 and/or controlling the pressure of the suction pump 530, which is based on the control signals i 520 and/or i 530 output from the controller 600. I can.
  • the suction pump 530 provided in the constant velocity suction control unit 500 generates a constant power.
  • the second control valve 520 By controlling the opening and closing of the second control valve 520 while outputting, or by adjusting the power of the suction pump 530 itself provided in the constant velocity suction control unit 500 (in this case, the second control valve 520 will be omitted. May) It is possible to implement a constant velocity flow rate collection in the sample collection unit 100.
  • a method of simultaneously controlling the pressure of the pump may be used.
  • the sample branching/combining unit 200 diverges the exhaust gas sample retaken from the sample collection unit 100 at one end in the traveling direction of the exhaust gas sample into a plurality of lines, and a plurality of the exhaust gas samples at the other end in the traveling direction of the exhaust gas sample It can be configured to combine the sample of exhaust gas from the line of.
  • the measurement line 220 and the control line 230 are exemplary as a plurality of lines implemented in the sample branch/combination unit 200 in the following specification. Although described, the number of lines constituting a plurality of lines may be different according to various embodiments or implementations.
  • the plurality of lines of the sample branching/combining unit 200 include a measurement line 220 having a particle size separation device 221 in at least one area, It may include a control line 230 in which the first control valve 231 is provided in at least one area, and the sample branching/combining unit 200 is a measurement line for measuring the exhaust gas sample collected from the sample collecting unit 100. It may further include a separation manifold 210 branching to 220 and the control line 230.
  • FIG. 2 exemplarily shows a configuration in which the first control valve 231 is spaced apart from the separation manifold 210 by a predetermined distance. do.
  • FIG. 4 corresponds to a conceptual diagram for explaining the variable distance adjustment between the separation manifold 210 and the first control valve 231 according to an embodiment of the present invention.
  • the separation manifold is based on the actual pressure loss in the measurement line 220 and/or the actual pressure loss in the control line 230, more preferably based on the difference in pressure loss.
  • the distance between the 210 and the first control valve 231 may be adjustable, and in (a) of FIG. 4, the first control valve 231 is approximately equal to the separation manifold 210 and the coupling manifold 240.
  • An example of a configuration disposed in the middle region is shown, and (b) of FIG. 4 exemplarily shows a configuration in which the first control valve 231 is disposed close to the separation manifold 210 side.
  • (c) exemplarily shows a configuration in which the first control valve 231 is disposed distal to the separation manifold 210.
  • the inlet inner diameter of the measurement line 220 is controlled based on the pressure loss in the measurement line 220 and/or the pressure loss in the control line 230. It may be implemented differently from the inner diameter of the inlet portion of the line 230, or an orifice may be installed therein.
  • the measurement line 220 is a line (or path) for separating and measuring fine dust, and may be composed of a particle size separation device 221, a fine dust measurement sensor 222, a first flow meter 223, and the like. have.
  • the particle size separation device 221 may be appropriately selected according to the particulate matter to be measured. For example, when measuring fine dust, the particle size separation device 221 uses the inertial force of the particles and A cyclone using centrifugal force can be used. In addition, it is possible to select PM10, PM2.5, etc. according to the size of the particle diameter to be measured, and in the following specification, the particle diameter separation device 221 is a PM10 impactor (221a) and PM2. An example implemented as a cascade-impacter composed of 5 impactors 221b will be described.
  • the impactor uses the law of inertial collision of particles to rapidly change the direction of fluid flow, the principle that heavy particles go straight to the collection tube and are collected by gravity and inertial force, whereas light particles proceed with the fluid. Because of the use of the fluid inlet speed, device structure, dimensional design, etc. are very important.
  • the fine dust measuring sensor 222 is a device for measuring fine dust, and, for example, a filter for a gravimetric method, a beta-ray sensor, a light scattering sensor, and the like may be applied.
  • the first flow meter 223 is a device for measuring the flow rate in the measurement line 220, for example, a mass flow meter (MFM) may be used.
  • MFM mass flow meter
  • mass is a standard for measurement in which the unit of measurement is not derived from other physical quantities, and forms the basis of all physical measurements along with units such as length, time, etc., and mass flowmeters measure the mass of such an invariant. It has the advantage of being linear without calculation and no correction for fluid properties.
  • the mass flow meter is a flow meter that measures the mass flow rate rather than the volume flow rate of a fluid.
  • direct mass flow meters include thermal mass flow meters, differential pressure mass flow meters, Coriolis mass flow meters, angular momentum mass flow meters, gyro mass flow meters, turbine mass flow meters, and the like.
  • mass flowmeter may be implemented to operate in a digital mode or an analog mode, and an operation mode may be switched between a digital mode and an analog mode, and the switching of such an operation mode is performed by the controller 600 ) Can be implemented by
  • the device 10 for continuous automatic measurement of fine dust of the flue gas is characterized in that a constant flow rate is supplied to the particle size separation device 221, whereby the particle size separation device 221
  • the first flow meter 223 always detects a value of 16.67 L/min as a constant speed flow rate, and when the flow rate value of the first flow meter 223 exceeds or falls below 16.67 L/min, the control line
  • the opening and closing of the first control valve 231 provided in 230 the flow rate value of the first flow meter 223 can be corrected by 16.67 l/min, and this correction/control operation implemented by the controller 600 It will be described in more detail with reference to FIG. 3 below.
  • the control line 230 corresponds to the remaining lines excluding the measurement line 220 from the plurality of lines provided in the sample branch/combination unit 200, and in FIG. 2, one line is illustratively used as the control line 230. Although shown, according to a further embodiment of the present invention, the control line 230 may be implemented as a plurality of lines (eg, two lines, three lines, etc.).
  • the control line 230 may be provided with a first control valve 231, and the distance between the first control valve 231 and the separation manifold 210 is a pressure loss in the measurement line 220 and/or It is already described that it is variably adjustable based on the pressure loss in the control line 230.
  • the first control valve 231 provided in the control line 230, the constant speed flow rate condition of the particle size separation device 221 provided in the measurement line 220 can be satisfied, and the first control valve
  • the opening and closing control control of the 231 may be possible by a control signal i 231 output from the controller 600.
  • FIG. 3 is a conceptual diagram for explaining an embodiment of implementing a constant flow rate of the measurement line 220 by the opening and closing operation of the first control valve 231 according to an embodiment of the present invention.
  • the constant flow rate required for the particle size separation device 221 is 16.67 l/min, and for accurate detection and measurement of fine dust, the constant flow rate condition in the particle size separation device 221 ( 16.67 l/min) must be observed.
  • the summation flow rate (Q Total ) is measured at 20 l/min by the second flow meter 510 provided in the constant velocity suction control unit 500, and the measurement line 220
  • the controller 60 determines that there is a flow rate of 5 L/min in the control line 230. I can.
  • the controller 600 controls 1.67 L/min at the 5 L/min flow rate of the control line 230.
  • the first control valve 231 may be further closed.
  • the summation flow rate (Q Total ) is measured as 20 l/min by the second flow meter 510 provided in the constant velocity suction control unit 500, and the measurement line (
  • the controller 60 has a flow rate of 2 L/min in the control line 230 You can judge that there is.
  • the controller 600 controls 1.33 L/min at the 2 L/min flow rate of the control line 230.
  • the first control valve 231 may be controlled to be further opened.
  • the controller 600 is based on the flow rate measured by the first flow meter 223 and the second flow meter 510 (ie, Q 220 , Q Total ), the first flow meter ( Opening and closing of the first control valve 231 may be controlled so that the flow rate measured by 223 corresponds to a constant speed flow rate (eg, 16.67 L/min) required for the particle size separation device 221.
  • a constant speed flow rate eg, 16.67 L/min
  • the controller 600 opens the first control valve 231 when the flow rate measured by the first flow meter 223 exceeds the constant speed flow rate required for the particle size separation device 221, and the first flow meter When the flow rate measured by 223 is less than the constant speed flow rate required for the particle size separation device 221, the first control valve 231 may be closed.
  • the coupling manifold 240 combines the sample flow rate from the measurement line 220 and the control line 230 and transmits it to the pretreatment unit 300, the gas measurement unit 400, the constant velocity suction control unit 500, etc. Can be configured.
  • the pretreatment unit 300 may be composed of a cooler 310 and a discharge pump 320.
  • the pretreatment unit 300 may perform pretreatment for normal measurement and/or control operation in the gas measurement unit 400 and/or the constant velocity suction control unit 500.
  • the pretreatment unit 300 removes moisture Can be implemented.
  • a gas sensor is used to measure an exhaust gas component in the gas measurement unit 400, and in general, the gas sensor is greatly affected by moisture. Accordingly, in order to reduce measurement errors and failures of the gas sensor due to moisture, the pretreatment unit 300 may remove moisture from the exhaust gas output through the coupling manifold 240. When the exhaust gas containing a large number of moisture passes through the cooler 310, moisture is condensed and converted into water, and the converted water is discharged to the outside through the discharge pump 320, thereby removing moisture from the exhaust gas.
  • the gas measurement unit 400 may include various types of gas sensors, and in this specification, the oxygen sensor 410 and the carbon dioxide sensor 420 are exemplarily described to correct air density in relation to the calculation of the constant velocity suction flow rate. I will do it.
  • the oxygen sensor 410 corresponds to a device for measuring oxygen in the exhaust gas
  • the carbon dioxide sensor 420 corresponds to a device for measuring carbon dioxide in the exhaust gas.
  • sensors such as the oxygen sensor 410 and the carbon dioxide sensor 420 may be removed even if the moisture of the target gas is removed. It can be implemented as a sensor device that conforms to the characteristics of a gas that does not cause overmeasurement errors.
  • the constant velocity suction control unit 500 may control the operation of the second control valve 520 and/or the suction pump 530 in order to satisfy the constant velocity flow rate condition in the sample collection unit 100. For example, based on the flow rate (Q Total ) measured by the second flow meter 510 provided in the constant velocity suction control unit 500, the suction pump 530 provided in the constant velocity suction control unit 500 generates a constant power. By controlling the opening and closing of the second control valve 520 while outputting, or by adjusting the power of the suction pump 530 itself provided in the constant velocity suction control unit 500 (in this case, the second control valve 520 will be omitted. May) It is possible to implement a constant velocity flow rate collection in the sample collection unit 100.
  • the flow rate measured by the second flow meter 510 provided in the constant velocity suction control unit 500 (Q Total ) Based on the method of controlling the opening and closing of the second control valve 520 and simultaneously controlling the pressure of the pump.
  • the second flow meter 510 may be a mass flow meter, or a dry flow meter, which is relatively inexpensive, may be used in general since moisture from the gas is removed from the pretreatment unit 300.
  • the continuous automatic measuring device for fine dust of the flue gas when collecting a sample of the flue gas, fine dust is sucked at a constant velocity through a suction nozzle equal to the flow rate of the exhaust gas. Measurement errors can be minimized.
  • the continuous automatic measurement device for fine dust of the chimney exhaust gas in branching the sucked exhaust gas sample into the measurement line and the control line, opening and closing of the first control valve provided in the control line By controlling the flow rate to be supplied to the particle size separation device provided in the measurement line, it is possible to precisely separate fine dust and continuous automatic measurement accordingly.
  • various embodiments described in the present specification may be implemented by hardware, middleware, microcode, software, and/or a combination thereof.
  • various embodiments include one or more application specific semiconductors (ASICs), digital signal processors (DSPs), digital signal processing devices (DSPDs), programmable logic devices (PLDs), field programmable gate arrays (FPGAs). ), processors, controllers, microcontrollers, microprocessors, other electronic units designed to perform the functions presented herein, or a combination thereof.
  • ASICs application specific semiconductors
  • DSPs digital signal processors
  • DSPDs digital signal processing devices
  • PLDs programmable logic devices
  • FPGAs field programmable gate arrays
  • processors controllers, microcontrollers, microprocessors, other electronic units designed to perform the functions presented herein, or a combination thereof.
  • various embodiments may be embodied or encoded on a computer-readable medium containing instructions. Instructions embodied or encoded on a computer-readable medium may cause a programmable processor or other processor to perform a method, for example, when the instructions are executed.
  • Computer-readable media includes computer storage media, and computer storage media may be any available media that can be accessed by a computer.
  • such computer-readable media may include RAM, ROM, EEPROM, CD-ROM or other optical disk storage medium, magnetic disk storage medium, or other magnetic storage device.
  • Such hardware, software, firmware, and the like may be implemented within the same device or within separate devices to support the various operations and functions described herein. Additionally, components, units, modules, components, and the like described as "units" in the present invention may be implemented together or separately as interoperable logic devices. The description of different features for modules, units, etc. is intended to highlight different functional embodiments, and does not necessarily imply that they must be realized by separate hardware or software components. Rather, functionality associated with one or more modules or units may be performed by separate hardware or software components or may be integrated within common or separate hardware or software components.
  • sample collection unit 110 suction tube
  • suction nozzle 120 Pitot tube
  • thermometer 140 heating device
  • sample branch/couple 210 separation manifold
  • fine dust measurement sensor 223 first flow meter
  • control line 231 first control valve
  • cooler 320 discharge pump
  • gas measuring unit 410 O 2 sensor
  • suction pump 600 controller

Landscapes

  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • General Physics & Mathematics (AREA)
  • Health & Medical Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Biochemistry (AREA)
  • Analytical Chemistry (AREA)
  • General Health & Medical Sciences (AREA)
  • Immunology (AREA)
  • Pathology (AREA)
  • Fluid Mechanics (AREA)
  • Biomedical Technology (AREA)
  • Engineering & Computer Science (AREA)
  • Molecular Biology (AREA)
  • Dispersion Chemistry (AREA)
  • Sampling And Sample Adjustment (AREA)

Abstract

L'invention concerne un appareil (10) pour mesurer en continu et automatiquement des poussières fines dans des gaz d'échappement de cheminée. Cet appareil (10) pour mesurer en continu et automatiquement des poussières fines dans des gaz d'échappement de cheminée peut comprendre : une partie de collecte d'échantillons (100) conçue pour collecter des échantillons de gaz d'échappement dans une cheminée ; et une partie de séparation/combinaison des échantillons (200) qui est conçue, à une extrémité dans le sens de déplacement des échantillons de gaz d'échappement, pour séparer les échantillons de gaz d'échappement collectés par la partie de collecte d'échantillons (100) en une pluralité de lignes et, à l'autre extrémité dans le sens de déplacement des échantillons de gaz d'échappement, pour combiner les échantillons de gaz d'échappement à partir de la pluralité de lignes.
PCT/KR2020/002409 2019-02-22 2020-02-19 Appareil pour mesurer en continu et automatiquement des poussières fines dans des gaz d'échappement de cheminée WO2020171594A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
KR10-2019-0020923 2019-02-22
KR1020190020923A KR102060651B1 (ko) 2019-02-22 2019-02-22 굴뚝 배출가스의 미세먼지 연속자동측정장치

Publications (1)

Publication Number Publication Date
WO2020171594A1 true WO2020171594A1 (fr) 2020-08-27

Family

ID=69051538

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/KR2020/002409 WO2020171594A1 (fr) 2019-02-22 2020-02-19 Appareil pour mesurer en continu et automatiquement des poussières fines dans des gaz d'échappement de cheminée

Country Status (2)

Country Link
KR (1) KR102060651B1 (fr)
WO (1) WO2020171594A1 (fr)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR102060651B1 (ko) * 2019-02-22 2019-12-31 주식회사 정엔지니어링 굴뚝 배출가스의 미세먼지 연속자동측정장치
KR102179129B1 (ko) * 2019-12-24 2020-11-18 주식회사 정엔지니어링 굴뚝 배출가스의 고정오염원 통합측정장치
KR102199628B1 (ko) * 2020-01-23 2021-01-08 주식회사 정엔지니어링 응축성 미세먼지를 포함하는 굴뚝 미세먼지의 연속측정장치 및 유해중금속을 포함하는 다이옥신 연속포집장치
KR102332142B1 (ko) * 2020-02-06 2021-11-30 (주)켄텍 확산관을 구비한 베타레이방식 굴뚝 미세 먼지 측정장치
KR102440408B1 (ko) * 2020-12-10 2022-09-06 주식회사 제스와이테크 산업용 굴뚝의 유해가스 채취장치
KR102451787B1 (ko) * 2020-12-24 2022-10-12 주식회사 정엔지니어링 굴뚝 내 미세먼지 측정 장치
KR102260692B1 (ko) * 2021-01-26 2021-06-07 한국표준과학연구원 굴뚝 배출 미세먼지 실시간 측정 장치
KR102556940B1 (ko) * 2021-03-10 2023-07-20 주식회사 전진엠에스 선박 내 블랙카본 측정 장치

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR200378620Y1 (ko) * 2004-12-31 2005-03-18 광주과학기술원 대기중 부유 입자상 물질의 실시간 측정 장치
KR100823947B1 (ko) * 2007-07-18 2008-04-22 구성테크닉스 주식회사 유량 조절이 가능한 습식 먼지 측정 시스템
KR101219527B1 (ko) * 2005-09-14 2013-01-11 고등기술연구원연구조합 고압배관의 분진농도 측정장치
KR101490328B1 (ko) * 2014-09-23 2015-02-16 대한민국 입자 개수 농도 측정 장치
KR20180076667A (ko) * 2016-12-28 2018-07-06 인하대학교 산학협력단 굴뚝 배출가스 중 미세먼지 시료 채취관
KR102060651B1 (ko) * 2019-02-22 2019-12-31 주식회사 정엔지니어링 굴뚝 배출가스의 미세먼지 연속자동측정장치

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR200378620Y1 (ko) * 2004-12-31 2005-03-18 광주과학기술원 대기중 부유 입자상 물질의 실시간 측정 장치
KR101219527B1 (ko) * 2005-09-14 2013-01-11 고등기술연구원연구조합 고압배관의 분진농도 측정장치
KR100823947B1 (ko) * 2007-07-18 2008-04-22 구성테크닉스 주식회사 유량 조절이 가능한 습식 먼지 측정 시스템
KR101490328B1 (ko) * 2014-09-23 2015-02-16 대한민국 입자 개수 농도 측정 장치
KR20180076667A (ko) * 2016-12-28 2018-07-06 인하대학교 산학협력단 굴뚝 배출가스 중 미세먼지 시료 채취관
KR102060651B1 (ko) * 2019-02-22 2019-12-31 주식회사 정엔지니어링 굴뚝 배출가스의 미세먼지 연속자동측정장치

Also Published As

Publication number Publication date
KR102060651B1 (ko) 2019-12-31

Similar Documents

Publication Publication Date Title
WO2020171594A1 (fr) Appareil pour mesurer en continu et automatiquement des poussières fines dans des gaz d'échappement de cheminée
JP3793947B2 (ja) リアルタイム水分モニタを備えた排ガス微粒子質量測定装置
CN102998233B (zh) 适用于高压气体管道内颗粒物在线检测的方法
CN102967541B (zh) 适用于高温气体管道内颗粒物在线检测的装置及方法
CN107917736B (zh) 一种民用炉具烟气污染物排放现场检测系统
JP2012529097A5 (fr)
US7343782B2 (en) System and method for performing quantifiable release spore testing on bioaerosol detection technologies
KR20180076667A (ko) 굴뚝 배출가스 중 미세먼지 시료 채취관
CN203011800U (zh) 适用于高温气体管道内颗粒物在线检测的装置
CN109164027A (zh) 空气过滤器性能测试系统
CN104764631A (zh) 一种便携式污染源稀释通道气溶胶采样装置及流化舱
KR20210100283A (ko) 확산관을 구비한 베타레이방식 굴뚝 미세 먼지 측정장치
CN110068526A (zh) 一种颗粒物在线稀释采样测量系统及方法
CN106248436A (zh) 全粒径在线取样装置
KR102290065B1 (ko) 확산관을 구비한 베타레이방식 굴뚝 미세 먼지 측정장치
CN107036950A (zh) 一种动态烟尘浓度仪检测系统及其检定方法
CN203011801U (zh) 适用于高压气体管道内颗粒物在线检测的装置
CN206038383U (zh) 一种用于多相流介质成分监测的网格多点取样系统
KR20030095482A (ko) 희석을 이용한 굴뚝가스시료 채취장치
CN205679426U (zh) 全粒径在线取样装置
CN102486440A (zh) 烟气可吸入颗粒物自动采样仪
CN104237090A (zh) 一种快速测定除尘器的烟气中烟尘浓度的方法及装置
CN114018776A (zh) 一种高压气体管道内颗粒物的检测装置
CN114018777A (zh) 一种高温气体内颗粒物浓度检测装置
KR102451787B1 (ko) 굴뚝 내 미세먼지 측정 장치

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 20760192

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 20760192

Country of ref document: EP

Kind code of ref document: A1