WO2013094628A1 - Mist-containing gas analysis device - Google Patents

Mist-containing gas analysis device Download PDF

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Publication number
WO2013094628A1
WO2013094628A1 PCT/JP2012/082882 JP2012082882W WO2013094628A1 WO 2013094628 A1 WO2013094628 A1 WO 2013094628A1 JP 2012082882 W JP2012082882 W JP 2012082882W WO 2013094628 A1 WO2013094628 A1 WO 2013094628A1
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WIPO (PCT)
Prior art keywords
mist
gas
target gas
liquid
containing gas
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PCT/JP2012/082882
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French (fr)
Japanese (ja)
Inventor
岡本 真一
長安 弘貢
勝 千代丸
達也 辻内
琢也 平田
田中 裕士
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三菱重工業株式会社
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Publication of WO2013094628A1 publication Critical patent/WO2013094628A1/en

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    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N1/00Sampling; Preparing specimens for investigation
    • G01N1/28Preparing specimens for investigation including physical details of (bio-)chemical methods covered elsewhere, e.g. G01N33/50, C12Q
    • G01N1/40Concentrating samples
    • G01N1/4055Concentrating samples by solubility techniques
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/14Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
    • B01D53/1412Controlling the absorption process
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/14Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
    • B01D53/1456Removing acid components
    • B01D53/1475Removing carbon dioxide
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/14Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
    • B01D53/18Absorbing units; Liquid distributors therefor
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N1/00Sampling; Preparing specimens for investigation
    • G01N1/02Devices for withdrawing samples
    • G01N1/22Devices for withdrawing samples in the gaseous state
    • G01N1/2247Sampling from a flowing stream of gas
    • G01N2001/2267Sampling from a flowing stream of gas separating gas from liquid, e.g. bubbles
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N1/00Sampling; Preparing specimens for investigation
    • G01N1/28Preparing specimens for investigation including physical details of (bio-)chemical methods covered elsewhere, e.g. G01N33/50, C12Q
    • G01N1/40Concentrating samples
    • G01N1/4055Concentrating samples by solubility techniques
    • G01N2001/4066Concentrating samples by solubility techniques using difference of solubility between liquid and gas, e.g. bubbling, scrubbing or sparging
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N33/00Investigating or analysing materials by specific methods not covered by groups G01N1/00 - G01N31/00
    • G01N33/0004Gaseous mixtures, e.g. polluted air
    • G01N33/0009General constructional details of gas analysers, e.g. portable test equipment
    • G01N33/0027General constructional details of gas analysers, e.g. portable test equipment concerning the detector
    • G01N33/0036Specially adapted to detect a particular component
    • G01N33/0054Specially adapted to detect a particular component for ammonia
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters

Definitions

  • the present invention relates to a mist-containing gas analyzer for measuring the concentration of a substance to be measured in a target gas containing mist of the substance to be measured.
  • amines etc. concentrations of amines and ammonia contained in the combustion exhaust gas are measured.
  • the concentration of amines and the like contained in the combustion exhaust gas It is considered to measure.
  • an exhaust gas treatment device equipped with a carbon dioxide recovery device that makes combustion gas from a boiler or the like contact with an amine-containing absorption liquid and absorbs and recovers carbon dioxide in the combustion exhaust gas in the absorption liquid.
  • a carbon dioxide recovery device that makes combustion gas from a boiler or the like contact with an amine-containing absorption liquid and absorbs and recovers carbon dioxide in the combustion exhaust gas in the absorption liquid.
  • an object of the present invention is to provide a mist-containing gas analyzer that can easily and accurately measure the concentration of a substance to be measured in a target gas containing a mist of the substance to be measured. .
  • the mist-containing gas analyzer according to the first invention for solving the above-described problem is a mist-containing gas analyzer that measures the concentration of the substance to be measured in the target gas containing the mist of the substance to be measured.
  • a collection container in which a collection liquid for dissolving the substance to be measured is placed; a target gas sampling means for sampling the target gas; and the target substance sampled by the target gas sampling means is vaporized.
  • the substance to be measured is attached to the target gas feeding means by supplying a cleaning liquid for dissolving the substance to be measured to the target gas feeding means.
  • a cleaning liquid supply means for feeding the cleaning liquid together with the cleaning gas from the target gas supply means to the inside of the collection container, a liquid sorting means for sorting the liquid inside the collection container, and the liquid sorting means And measuring means for measuring the concentration of the substance to be measured in the liquid separated in step (b).
  • the mist-containing gas analyzer according to a second aspect of the present invention is the mist-containing gas analyzer according to the first aspect, wherein the target gas fed from the target gas feeding means into the collection liquid inside the collection container is finely divided. It is characterized by having a fine bubble forming means for forming bubbles.
  • the mist-containing gas analyzer is characterized in that, in the second aspect, the microbubble generation means is a filter having a maximum pore in a range of 5 to 120 ⁇ m.
  • a mist-containing gas analyzer is characterized in that, in any one of the first to third inventions, the substance to be measured is an amine and ammonia.
  • a mist-containing gas analyzer is characterized in that, in the fourth invention, the heating means heats the target gas sampling means in a range of 150 to 200 ° C.
  • a mist-containing gas analyzer is characterized in that, in the fifth invention, the target gas is a combustion exhaust gas from which carbon dioxide has been absorbed and removed by an absorbing solution containing amines. .
  • the mist-containing gas analyzer according to a seventh invention is the mist-containing gas analyzer according to any one of the first to sixth inventions, wherein the target gas sampling means includes a sampling pipe for sampling the target gas, A temperature detecting means is provided on the tip side.
  • the heating unit heats the target gas sampling unit so as to vaporize the substance to be measured sampled by the target gas sampling unit, and the clean liquid supply unit includes the clean liquid. Can be sent to the inside of the collection container from the target gas supply means together with the cleaning liquid. Even if the target gas is not only contained in the shape but also in the mist form, the concentration of the substance to be measured in the target gas can be measured easily and accurately.
  • a flue gas 1 that is a target gas from which carbon dioxide has been absorbed and removed through contact with an absorbing solution containing amines circulates in the duct 10.
  • the substances to be measured and ammonia hereinafter referred to as “amines”.
  • a sampling tube 111 is attached to the circumferential surface of the duct 10 so that the tip side is positioned inside the duct 10.
  • One end side of the guide tube 112 is connected to the proximal end side of the sampling tube 111 through the valve 101.
  • Connected to the other end side of the guide tube 112 is one end side (upper end side) of the introduction tube 114 oriented so as to face the axial direction in the vertical direction.
  • the sampling tube 111, the guide tube 112, and the introduction tube 114 are provided with an electric heater 113 serving as a heating means.
  • the electric heater 113 passes through the inside of the tubes 111, 112, 114 with the amines. Etc. can be heated at a temperature (about 150 to 200 ° C.) for vaporizing the like.
  • the other end side (lower end side) of the introduction pipe 114 is connected to one end side of the feed pipe 115 via the valve 102.
  • the feed pipe 115 is attached to the collection container 116 so that the other end side is positioned below the inside of the collection container 116.
  • a filter (maximum pore: 5 to 120 ⁇ m, particularly preferably 100 to 120 ⁇ m) 117 is attached to the other end side of the feeding pipe 115 as fine bubble forming means by sintering glass.
  • the collection container 116 is connected to one end side of a delivery pipe 118 having a valve 103 and a feed pump 119 in the middle thereof.
  • the other end of the delivery pipe 118 is connected to the bottom of the liquid storage tank 120.
  • a collection liquid 2 for dissolving and collecting the amines and the like.
  • the collected liquid 2 in the liquid storage tank 120 can be supplied from the delivery pipe 118 into the collection container 116. It has become.
  • the base end side of the exhaust pipe 121 having the valve 104 and the suction blower 122 in the middle is connected to the upper part of the collection container 116.
  • a gas flow meter 123 which is a gas flow rate detecting means for detecting the flow rate of gas flowing through the exhaust pipe 121.
  • a cooler 124 and a gas-liquid separator 125 are interposed between the valve 104 of the exhaust pipe 121 and the gas flow meter 123.
  • a buffer tank 126 is interposed between the gas flow meter 123 of the exhaust pipe 121 and the suction blower 122.
  • the bottom of the collection container 116 is connected to one end of a liquid feeding pipe 127 having a valve 105 in the middle.
  • the other end side of the liquid feeding pipe 127 is connected to a receiving port of the feeding pump 128.
  • the delivery port of the feed pump 128 communicates with a reception port of a constant volume / dilution device 129 that performs constant volume and dilution.
  • the outlet of the constant volume / dilution device 129 communicates with an inlet of a measuring device 130 which is a measuring means such as an ion exchange chromatography or an electric conductivity measuring device for measuring the concentration of the amines.
  • a drain pipe 131 having a valve 106 in the middle is connected between the valve 105 of the liquid feed pipe 127 and the feed pump 128, one end side of a drain pipe 131 having a valve 106 in the middle is connected.
  • the other end side of the drainage pipe 131 communicates outside the system.
  • a cleaning liquid introduction pipe 132 having a valve 107 in the middle In the vicinity of the valve 102 on the other end side (lower end side) of the introduction pipe 114, one end side of a cleaning liquid introduction pipe 132 having a valve 107 in the middle is connected, and the cleaning liquid introduction pipe 132 has one end side.
  • the axial direction is inclined and oriented so as to be positioned below the other end side.
  • the other end of the cleaning liquid introduction pipe 132 communicates with a cleaning liquid tank (not shown) that supplies the cleaning liquid 3 such as pure water.
  • the nitrogen gas introduction pipe 133 is The axial direction is inclined and oriented so that one end side is positioned below the other end side.
  • the other end side of the nitrogen gas introduction pipe 133 communicates with a nitrogen gas cylinder (not shown) that feeds nitrogen gas 4 that is an inert gas.
  • bypass pipe 134 having a valve 109 in the middle is connected between a connection part of the introduction pipe 114 to the cleaning liquid introduction pipe 132 and a connection part to the nitrogen gas introduction pipe 133.
  • the other end side of the bypass pipe 134 is connected between the valve 104 of the exhaust pipe 121 and the cooler 124.
  • the guide pipe 112 is connected to one end of a leak pipe 135 having a valve 110a in the middle.
  • the other end of the leak pipe 135 communicates outside the system.
  • One end of a leak pipe 136 having a valve 110b in the middle is connected to the upper portion of the collection container 116.
  • the other end of the leak pipe 136 communicates outside the system.
  • a temperature sensor 141 serving as a temperature detecting means is provided on the distal end side of the sampling tube 111.
  • a float type liquid quantity detector 142 is provided as a liquid quantity detection means for detecting the quantity of the collection liquid 2 in the collection container 116.
  • the gas flow meter 123, the temperature sensor 141, and the liquid amount detector 142 are electrically connected to an input unit of a calculation control device 140 that is a calculation control means incorporating a timer. .
  • the measuring device 130 is further electrically connected to the input unit of the arithmetic control device 140.
  • the output unit of the arithmetic and control unit 140 includes the valves 101 to 109, 110a and 110b, the electric heater 113, the feed pumps 119 and 128, the suction blower 122, the constant volume / dilution device 129, and the measuring device 130.
  • the arithmetic and control unit 140 includes the gas flow meter 123, the temperature sensor 141, the liquid amount detector 142, and the timer. Based on the information from the above, the operation of the valves 101 to 109, 110a, 110b, the electric heater 113, the feed pumps 119, 128, the suction blower 122, the constant volume / dilution device 129, and the measuring device 130 is performed. And controlling the operation of the constant volume / dilution device 129 based on information from the measuring device 130 and And it is capable of displaying various information on the monitor 143 (details will be described later).
  • the suction blower 122, the gas flow meter 123, the cooler 124, the gas-liquid separator 125, the buffer tank 126, and the like constitute a target gas sampling means, and the valves 102 and 104, the introduction pipe 114, and the feed pipe.
  • the liquid feeding pipe 127, the feeding pump 128, the constant volume / dilution device 129, and the like constitute liquid sorting means, and the valve 103, the feeding pipe 118, the feeding pump 119, the liquid storage
  • the tank 120 or the like constitutes a collected liquid supply means, and the valve 106, the drainage pipe 131, or the like constitutes a liquid discharge means, and the valve 108, the nitrogen gas introduction pipe, the nitrogen gas cylinder, etc.
  • the active gas supply means is configured, and the valve 109, the bypass pipe 134 and the like constitute bypass means.
  • valves 101 to 109 are all in a closed state, and when the arithmetic control device 140 is operated, the arithmetic control device 140 first determines the amine based on information from the temperature sensor 141.
  • the operation of the electric heater 113 is controlled so that the tubes 111, 112, 114 are heated at a temperature (about 150 to 200 ° C.) for vaporizing the like.
  • the arithmetic and control unit 140 opens and closes the valves 103 and 110b based on the information from the liquid amount detector 142 so as to store a predetermined amount of the collected liquid 2 in the collection container 116.
  • the collection liquid 2 in the storage tank 120 is discharged from the leak pipe 136 while the gas in the collection container 116 is discharged out of the system by controlling the operation and the operation of the feed pump 119. It is fed from 118 into the collection container 116.
  • the control device 140 When a specified amount of the collected liquid 2 is stored in the collection container 116, the control device 140, based on information from the liquid amount detector 142, the combustion exhaust gas that circulates in the duct 10. 1, the valves 101 and 109 are controlled to be opened so that the inside of the sampling pipe 111 and the guide pipe 112 is purged, and the suction blower 122 is operated and controlled so that the combustion exhaust gas 1 in the duct 10 is The sample is taken into the sampling pipe 111 and discharged from the guide pipe 112 through the bypass pipe 134 and the exhaust pipe 121 to the outside of the system.
  • the control device 140 removes the flue gas 1 based on the information from the timer.
  • the valve 109 is controlled to be closed (the valve 101 is maintained in an open state) so as to come into contact with the collected liquid 2 in 116, and the valves 102 and 104 are controlled to open, whereby the feeding pipe 115 is controlled.
  • the combustion exhaust gas 1 is fed into the collection liquid 2 in the collection container 116 through the filter 117 and the amines and the like in the combustion exhaust gas 1 are dissolved in the collection liquid 2.
  • the combustion exhaust gas 1 in which the amines and the like are collected is fed from the exhaust pipe 121 to the cooler 124 to be cooled, and moisture in the combustion exhaust gas 1 is removed.
  • condensation separated by the gas-liquid separator 125 and discharges the combustion exhaust gas 1 which is removing water from the gas flow meter 123 the suction blower 122 through the buffer tank 126 while the flow rates were measured by the outside of the system.
  • the pipes 111, 112, 114 are heated and held up to a temperature (about 150 to 200 ° C.) for vaporizing the amines and the like by the electric heater 113, so that the combustion exhaust gas taken in from the duct 10 1 can be fed in a state of being vaporized up to the feed pipe 115 without condensing and adhering the gaseous and mist amines contained in 1 to the inner wall surface.
  • the flue gas 1 from the feed pipe 115 is fed into the collected liquid 2 via the filter 117, the flue gas 1 is made into fine bubbles and the collected liquid 2 is mixed with the collected liquid 2.
  • the contact area can be increased, and the amines and the like in the combustion exhaust gas 1 can be efficiently collected.
  • the arithmetic and control unit 140 is based on information from the gas flow meter 123.
  • the valve 101, 102, 104 is controlled to be closed so that the supply of the flue gas 1 into the collected liquid 2 is stopped, and the suction blower 122 is controlled to stop, and then the information from the timer
  • the cleaning liquid 3 is fed from the cleaning liquid introduction pipe 132 into the introduction pipe 114 for a prescribed time (a prescribed amount) so that the introduction pipe 114 is filled with the cleaning liquid 3. 110a is controlled to open and close.
  • the arithmetic and control unit 140 is configured to control the valve based on information from the timer so as to send the amines and the like adhering to the inner wall surface of the feed pipe 115 into the collection container 116.
  • the opening / closing control of the 102, 108, 110b is performed at a prescribed timing, and the cleaning liquid 3 in the introduction pipe 114 is pushed out by the nitrogen gas 4 from the nitrogen gas introduction pipe 133, and the inside of the supply pipe 115
  • the cleaning liquid 3 is caused to flow down while being in contact with the inner wall surface of the feed pipe 115 so that the cleaning liquid 3 is brought into contact with all the amines and the like adhering to the wall surface.
  • the combustion exhaust gas 1 is allowed to flow into the collection liquid 2 in the collection container 116 while being discharged out of the system from the leak pipe 136.
  • the arithmetic and control unit 140 sorts the liquids 2 and 3 in the collection container 116 into the constant volume / dilution unit 129.
  • the opening / closing control of the valves 102, 105, and 108 and the operation control of the feed pump 128 are performed at a prescribed timing, and the nitrogen gas 4 is supplied from the nitrogen gas introduction pipe 133 through the introduction pipe 114 and the feed pipe 115.
  • the liquids 2 and 3 in the collection container 116 are mixed and fed from the liquid feed pipe 127 to the constant volume / dilution device 129 through the feed pump 128.
  • the arithmetic and control unit 140 controls the operation of the constant volume / dilution unit 129 so as to send the mixed specified amount of the liquids 2 and 3 to the measuring unit 130.
  • the arithmetic control device 140 can calibrate the measurement result based on information from the measurement device 130. It is determined whether or not it is within the range, and if it is within the range that can be calibrated, the concentration of the amines and the like in the combustion exhaust gas 1 is calculated, and the result is displayed on the monitor 143.
  • the arithmetic and control unit 140 may determine the amines and the like in the liquids 2 and 3 fed to the measurement device 130.
  • the dilution rate is calculated so that the concentration is within the calibratable range, and the constant volume / dilution device 129 is controlled to dilute the liquids 2 and 3 with a diluted solution such as pure water at the calculated magnification.
  • the arithmetic and control unit 140 again sends the diluted liquids 2 and 3 to the measuring device 130 in a specified amount.
  • the operation of the constant volume / dilution device 129 is controlled, and the measuring device 130 measures the concentration of the amines and the like in the liquids 2 and 3 again. Then, the arithmetic and control unit 140 calculates the concentration of the amines and the like in the combustion exhaust gas 1 based on the information from the measuring device 130 and displays the result on the monitor 143.
  • the arithmetic and control unit 140 removes the liquids 2 and 3 in the collection container 116 based on information from the measuring unit 130.
  • the valves 102, 105, 106, and 108 are controlled so as to be discharged out of the system, and the nitrogen gas 4 is captured from the nitrogen gas introduction pipe 133 through the introduction pipe 114 and the supply pipe 115. All the liquids 2 and 3 in the collection container 116 are discharged out of the system through the liquid supply pipe 127 and the drainage pipe 131 while being fed into the collection container 116.
  • the arithmetic and control unit 140 determines that the inside of the collection container 116 is based on information from the timer.
  • the valve 105, 106, 108 is controlled to be closed so as to be filled with the cleaning liquid 3 (the valve 102 is kept open), and the valves 107, 110b are controlled to open so that the cleaning liquid 3 is
  • the cleaning liquid 3 is supplied from the cleaning liquid introduction pipe 132 through the feeding pipe 115 to the inside of the collection container 116 for a specified time, and the gas in the collection container 116 is expelled from the leak pipe 136 to the outside of the system. To the inside of the collection container 116 to such an extent that it overflows from the leak pipe 136.
  • the arithmetic and control unit 140 based on the information from the timer, the valves 107 and 110b are controlled to be closed (the valve 102 is kept open) and the valves 105, 106 and 108 are controlled to be opened so that the cleaning liquid 3 is discharged out of the system. Is fed from the nitrogen gas introduction pipe 133 to the inside of the collection container 116 through the introduction pipe 114 and the supply pipe 115, and all the cleaning liquid 3 in the collection container 116 is fed to the liquid. The liquid is discharged from the pipe 127 through the drain pipe 131.
  • the arithmetic and control unit 140 cleans the filter 117 based on the information from the timer.
  • the valve 108 is controlled to be closed (the valves 102, 105, and 106 are kept open), the valve 107 is controlled to be opened, and the cleaning liquid 3 is supplied from the cleaning liquid introduction pipe 132 to the feeding pipe 115.
  • the filter 117 is supplied to the filter 117 for a specified time to clean the filter 117, and the cleaning liquid 3 is discharged from the liquid supply pipe 127 to the outside of the system through the drainage pipe 131.
  • the arithmetic and control unit 140 controls the valves 102, 105, 106, and 107 to be in an initial state based on information from the timer. return.
  • the concentration of the amines and the like in the combustion exhaust gas 1 flowing through the duct 10 can be automatically and continuously measured.
  • the mist-containing gas analyzer 100 even if the exhaust gas 1 contains not only amines and the like but also mist, The concentration of the amines in 1 can be measured easily and accurately.
  • the flue gas 1 from the feed pipe 115 is fed into the collected liquid 2 via the filter 117, the flue gas 1 is made into fine bubbles and the collected liquid 2 is mixed with the collected liquid 2.
  • the contact area can be increased, and the amines and the like in the combustion exhaust gas 1 can be efficiently collected.
  • a carbon dioxide recovery device in which combustion exhaust gas from a boiler or the like is brought into contact with an amine-containing absorption liquid and carbon dioxide in the combustion exhaust gas is absorbed and recovered in the absorption liquid.
  • concentration of the said amines in the said combustion exhaust gas 1 in the said waste gas treatment apparatus was measured, this invention is not restricted to this, For example, in the exit gas (for example, moisture saturation gas) of a gas-liquid contact apparatus As in the case of measuring the concentration of the substance to be measured in the target gas containing the mist of the substance to be measured, such as when measuring the liquid component concentration, the same as in the case of the above-described embodiment. Can be applied.
  • the mist-containing gas analyzer according to the present invention not only contains the substance to be measured in a gaseous state, but also the concentration of the substance to be measured in the target gas, even if it is a target gas that also contains the mist. Can be measured easily and accurately, and can be used extremely beneficially in various industries.

Abstract

A mist-containing gas analysis device is provided with: a collection container (116) in which a collection solution (2) is stored; a sampling tube (111), a guide tube (112), an introduction tube (114), and the like for sampling combustion exhaust gas (1); an electric heater (113) for heating the tubes (111, 112, 114) such that amines and the like sampled by the tubes (111, 112, 114) are vaporized; a feed tube (115) and the like for feeding the gas (1) sampled by the tubes (111, 112, 114) into the collection solution (2) in the collection container (116); a cleaning solution introduction tube (132) and the like for supplying a cleaning solution (3) to the tube (115) to thereby send, together with the cleaning solution (3), the amines and the like adhering to the tube (115) into the collection container (116) from the tube (115); and a measurement unit (130) for measuring the concentration of the amines and the like in the solutions (2, 3).

Description

ミスト含有ガス分析装置Mist-containing gas analyzer
 本発明は、被測定物質のミストを含有する対象ガス中の当該被測定物質の濃度を計測するミスト含有ガス分析装置に関する。 The present invention relates to a mist-containing gas analyzer for measuring the concentration of a substance to be measured in a target gas containing mist of the substance to be measured.
 例えば、ボイラ等からの燃焼排ガスをアミン類含有の吸収液に接触させて当該燃焼排ガス中の二酸化炭素を吸収液中に吸収して回収する二酸化炭素回収装置を備えた排ガス処理装置においては、二酸化炭素回収装置で二酸化炭素を吸収除去された燃焼排ガスに微量のアミン類やアンモニアが随伴して当該燃焼排ガスと共に外部に排出されてしまうことから、二酸化炭素回収装置で二酸化炭素を吸収除去されて排出される上記燃焼排ガスを作業員がサンプリングして当該燃焼排ガス中に含有されているアミン類及びアンモニア(以下「アミン類等」という。)の濃度を計測するようにしている。 For example, in an exhaust gas treatment apparatus equipped with a carbon dioxide recovery device that contacts a combustion exhaust gas from a boiler or the like with an amine-containing absorption liquid and absorbs and recovers carbon dioxide in the combustion exhaust gas in the absorption liquid. Since trace amounts of amines and ammonia accompany the combustion exhaust gas from which carbon dioxide has been absorbed and removed by the carbon recovery device and are discharged to the outside together with the combustion exhaust gas, carbon dioxide is absorbed and removed by the carbon dioxide recovery device. The above-mentioned combustion exhaust gas is sampled by an operator, and the concentrations of amines and ammonia (hereinafter referred to as “amines etc.”) contained in the combustion exhaust gas are measured.
特開昭62-106367号公報JP-A-62-106367 特開昭62-119496号公報JP-A-62-119496 特開2010-156592号公報JP 2010-156592 A
 しかしながら、前述したように作業員が燃焼排ガスをサンプリングしてアミン類等の濃度を計測するようにすると、計測を行うごとに作業員がサンプリングして分析しなければならず、非常に手間がかかってしまっていた。 However, as described above, if the worker samples the combustion exhaust gas and measures the concentration of amines, etc., the worker must sample and analyze every measurement, which is very laborious. It was.
 そこで、例えば、二酸化炭素回収装置で二酸化炭素を吸収除去されて排出される上記燃焼排ガスをFT-IR等で直接的に分析することにより、当該燃焼排ガス中に含有されているアミン類等の濃度を計測することが考えられている。 Therefore, for example, by directly analyzing the combustion exhaust gas discharged by absorbing and removing carbon dioxide with a carbon dioxide recovery device by FT-IR or the like, the concentration of amines and the like contained in the combustion exhaust gas It is considered to measure.
 ところが、このようにして燃焼排ガス中のアミン類等を計測すると、当該燃焼排ガス中でガス状となっているアミン類等を計測することはできるものの、当該燃焼排ガス中でミスト状になっているアミン類等を計測することはできず、当該燃焼排ガス中に含有されているアミン類等の濃度を正確に求めることができない。 However, when amines and the like in the combustion exhaust gas are measured in this way, the amines and the like that are in a gaseous state in the combustion exhaust gas can be measured, but the mist is in the combustion exhaust gas. The amines and the like cannot be measured, and the concentration of the amines and the like contained in the combustion exhaust gas cannot be accurately determined.
 このような問題は、ボイラ等からの燃焼排ガスをアミン類含有の吸収液に接触させて当該燃焼排ガス中の二酸化炭素を吸収液中に吸収して回収する二酸化炭素回収装置を備えた排ガス処理装置における当該燃焼排ガス中のアミン類等の濃度を計測する場合に限らず、例えば、気液接触装置の出口ガス(例えば水分飽和ガス)中の液体成分濃度を計測する場合等のように、被測定物質のミストを含有する対象ガス中の当該被測定物質の濃度を計測するような場合であれば、上述した場合と同様にして生じ得ることである。 Such a problem is that an exhaust gas treatment device equipped with a carbon dioxide recovery device that makes combustion gas from a boiler or the like contact with an amine-containing absorption liquid and absorbs and recovers carbon dioxide in the combustion exhaust gas in the absorption liquid. Not only when measuring the concentration of amines and the like in the combustion exhaust gas at, but also when measuring the concentration of liquid components in the exit gas (for example, water saturated gas) of the gas-liquid contact device If the concentration of the substance to be measured in the target gas containing the substance mist is measured, it can occur in the same manner as described above.
 このようなことから、本発明は、被測定物質のミストを含有する対象ガス中の被測定物質の濃度を簡単かつ正確に計測することができるミスト含有ガス分析装置を提供することを目的とする。 In view of the above, an object of the present invention is to provide a mist-containing gas analyzer that can easily and accurately measure the concentration of a substance to be measured in a target gas containing a mist of the substance to be measured. .
 前述した課題を解決するための、第一番目の発明に係るミスト含有ガス分析装置は、被測定物質のミストを含有する対象ガス中の当該被測定物質の濃度を計測するミスト含有ガス分析装置であって、前記被測定物質を溶解させる捕集液を内部に入れられる捕集容器と、前記対象ガスをサンプリングする対象ガスサンプリング手段と、前記対象ガスサンプリング手段でサンプリングされた前記被測定物質を気化させるように当該対象ガスサンプリング手段を加熱する加熱手段と、前記対象ガスサンプリング手段でサンプリングされた前記対象ガスを前記捕集容器の内部の前記捕集液中に送給する対象ガス送給手段と、前記被測定物質を溶解させる清浄液を前記対象ガス送給手段に供給して当該対象ガス送給手段に付着している前記被測定物質を当該清浄液と共に当該対象ガス送給手段から前記捕集容器の内部へ送り込ませる清浄液供給手段と、前記捕集容器の内部の前記液を分取する液分取手段と、前記液分取手段で分取された前記液中の前記被測定物質の濃度を計測する計測手段とを備えていることを特徴とする。 The mist-containing gas analyzer according to the first invention for solving the above-described problem is a mist-containing gas analyzer that measures the concentration of the substance to be measured in the target gas containing the mist of the substance to be measured. A collection container in which a collection liquid for dissolving the substance to be measured is placed; a target gas sampling means for sampling the target gas; and the target substance sampled by the target gas sampling means is vaporized. Heating means for heating the target gas sampling means, and target gas feeding means for feeding the target gas sampled by the target gas sampling means into the collection liquid inside the collection container; The substance to be measured is attached to the target gas feeding means by supplying a cleaning liquid for dissolving the substance to be measured to the target gas feeding means. A cleaning liquid supply means for feeding the cleaning liquid together with the cleaning gas from the target gas supply means to the inside of the collection container, a liquid sorting means for sorting the liquid inside the collection container, and the liquid sorting means And measuring means for measuring the concentration of the substance to be measured in the liquid separated in step (b).
 第二番目の発明に係るミスト含有ガス分析装置は、第一番目の発明において、前記対象ガス送給手段から前記捕集容器の内部の前記捕集液中へ送給される前記対象ガスを微細気泡化する微細気泡化手段を備えていることを特徴とする。 The mist-containing gas analyzer according to a second aspect of the present invention is the mist-containing gas analyzer according to the first aspect, wherein the target gas fed from the target gas feeding means into the collection liquid inside the collection container is finely divided. It is characterized by having a fine bubble forming means for forming bubbles.
 第三番目の発明に係るミスト含有ガス分析装置は、第二番目の発明において、前記微細気泡化手段が、5~120μmの範囲内の最大細孔を有するフィルタであることを特徴とする。 The mist-containing gas analyzer according to a third aspect is characterized in that, in the second aspect, the microbubble generation means is a filter having a maximum pore in a range of 5 to 120 μm.
 第四番目の発明に係るミスト含有ガス分析装置は、第一番目から第三番目の発明のいずれかにおいて、前記被測定物質が、アミン類及びアンモニアであることを特徴とする。 A mist-containing gas analyzer according to a fourth invention is characterized in that, in any one of the first to third inventions, the substance to be measured is an amine and ammonia.
 第五番目の発明に係るミスト含有ガス分析装置は、第四番目の発明において、前記加熱手段が、前記対象ガスサンプリング手段を150~200℃の範囲で加熱するものであることを特徴とする。 A mist-containing gas analyzer according to a fifth invention is characterized in that, in the fourth invention, the heating means heats the target gas sampling means in a range of 150 to 200 ° C.
 第六番目の発明に係るミスト含有ガス分析装置は、第五番目の発明において、前記対象ガスが、アミン類を含有する吸収液により二酸化炭素を吸収除去された燃焼排ガスであることを特徴とする。 A mist-containing gas analyzer according to a sixth invention is characterized in that, in the fifth invention, the target gas is a combustion exhaust gas from which carbon dioxide has been absorbed and removed by an absorbing solution containing amines. .
 第七番目の発明に係るミスト含有ガス分析装置は、第一番目から第六番目の発明のいずれかにおいて、前記対象ガスサンプリング手段が、前記対象ガスをサンプリングするサンプリング管を備え、前記サンプリング管の先端側に温度検出手段が設けられていることを特徴とする。 The mist-containing gas analyzer according to a seventh invention is the mist-containing gas analyzer according to any one of the first to sixth inventions, wherein the target gas sampling means includes a sampling pipe for sampling the target gas, A temperature detecting means is provided on the tip side.
 本発明に係るミスト含有ガス分析装置によれば、加熱手段が、対象ガスサンプリング手段でサンプリングされた被測定物質を気化させるように対象ガスサンプリング手段を加熱すると共に、清浄液供給手段が、清浄液を対象ガス送給手段に供給して対象ガス送給手段に付着している被測定物質を清浄液と共に対象ガス送給手段から捕集容器の内部へ送り込むことができるので、被測定物質をガス状に含有しているだけでなく、ミスト状でも含有している対象ガスであっても、当該対象ガス中の被測定物質の濃度を簡単かつ正確に計測することができる。 According to the mist-containing gas analyzer according to the present invention, the heating unit heats the target gas sampling unit so as to vaporize the substance to be measured sampled by the target gas sampling unit, and the clean liquid supply unit includes the clean liquid. Can be sent to the inside of the collection container from the target gas supply means together with the cleaning liquid. Even if the target gas is not only contained in the shape but also in the mist form, the concentration of the substance to be measured in the target gas can be measured easily and accurately.
本発明に係るミスト含有ガス分析装置の主な実施形態の全体概略構成図である。It is a whole schematic block diagram of main embodiment of the mist containing gas analyzer which concerns on this invention. 図1のミスト含有ガス分析装置の制御系のブロック図である。It is a block diagram of the control system of the mist containing gas analyzer of FIG.
 本発明に係るミスト含有ガス分析装置の実施形態を図面に基づいて説明するが、本発明は、図面に基づいて説明する以下の実施形態の場合のみに限定されるものではない。 Embodiments of a mist-containing gas analyzer according to the present invention will be described with reference to the drawings. However, the present invention is not limited only to the following embodiments described with reference to the drawings.
〈主な実施形態〉
 本発明に係るミスト含有ガス分析装置の主な実施形態を図1,2に基づいて説明する。
<Main embodiment>
A main embodiment of the mist-containing gas analyzer according to the present invention will be described with reference to FIGS.
 図1に示すように、ダクト10の内部には、アミン類を含有する吸収液と接触して二酸化炭素を吸収除去された対象ガスである燃焼排ガス1が流通しており、当該燃焼排ガス1は、被測定物質であるアミン類及びアンモニア(以下「アミン類等」という。)をガス状に含有しているだけでなく、ミスト状でも含有している。 As shown in FIG. 1, a flue gas 1 that is a target gas from which carbon dioxide has been absorbed and removed through contact with an absorbing solution containing amines circulates in the duct 10. In addition to gaseous substances, the substances to be measured and ammonia (hereinafter referred to as “amines”) are contained in a mist form.
 前記ダクト10の周面には、サンプリング管111が当該ダクト10の内部に先端側を位置させるようにして取り付けられている。前記サンプリング管111の基端側には、案内管112の一端側がバルブ101を介して接続されている。前記案内管112の他端側には、上下方向に軸方向を向けるように配向された導入管114の一端側(上端側)が接続されている。前記サンプリング管111及び前記案内管112並びに前記導入管114には、加熱手段である電熱ヒータ113が設けられており、当該電熱ヒータ113は、当該管111,112,114の内部を、前記アミン類等を気化させる温度(約150~200℃)で加熱することができるようになっている。 A sampling tube 111 is attached to the circumferential surface of the duct 10 so that the tip side is positioned inside the duct 10. One end side of the guide tube 112 is connected to the proximal end side of the sampling tube 111 through the valve 101. Connected to the other end side of the guide tube 112 is one end side (upper end side) of the introduction tube 114 oriented so as to face the axial direction in the vertical direction. The sampling tube 111, the guide tube 112, and the introduction tube 114 are provided with an electric heater 113 serving as a heating means. The electric heater 113 passes through the inside of the tubes 111, 112, 114 with the amines. Etc. can be heated at a temperature (about 150 to 200 ° C.) for vaporizing the like.
 前記導入管114の他端側(下端側)には、送給管115の一端側がバルブ102を介して接続している。前記送給管115は、他端側を捕集容器116の内部下方に位置させるように当該捕集容器116に取り付けられている。前記送給管115の他端側には、ガラスを焼結させた微細気泡化手段であるフィルタ(最大細孔:5~120μm、特に100~120μmが好適)117が取り付けられている。 The other end side (lower end side) of the introduction pipe 114 is connected to one end side of the feed pipe 115 via the valve 102. The feed pipe 115 is attached to the collection container 116 so that the other end side is positioned below the inside of the collection container 116. A filter (maximum pore: 5 to 120 μm, particularly preferably 100 to 120 μm) 117 is attached to the other end side of the feeding pipe 115 as fine bubble forming means by sintering glass.
 前記捕集容器116には、バルブ103及び送給ポンプ119を途中に有する送出管118の一端側が接続されている。前記送出管118の他端側は、貯液タンク120の底部に接続している。前記貯液タンク120の内部には、前記アミン類等を溶解させて捕集する捕集液2が貯留されている。 The collection container 116 is connected to one end side of a delivery pipe 118 having a valve 103 and a feed pump 119 in the middle thereof. The other end of the delivery pipe 118 is connected to the bottom of the liquid storage tank 120. Inside the liquid storage tank 120 is stored a collection liquid 2 for dissolving and collecting the amines and the like.
 つまり、前記バルブ103を開放して前記送給ポンプ119を作動させると、前記貯液タンク120内の捕集液2を前記送出管118から前記捕集容器116の内部に供給することができるようになっているのである。 That is, when the valve 103 is opened and the feed pump 119 is operated, the collected liquid 2 in the liquid storage tank 120 can be supplied from the delivery pipe 118 into the collection container 116. It has become.
 前記捕集容器116の上部には、バルブ104及び吸引ブロア122を途中に有する排気管121の基端側が接続されている。前記排気管121の前記バルブ104と前記吸引ブロア122との間には、当該排気管121内を流通するガス流量を検出するガス流量検出手段であるガス流量計123が設けられている。前記排気管121の前記バルブ104と前記ガス流量計123との間には、冷却器124及び気液分離器125が介在している。前記排気管121の前記ガス流量計123と前記吸引ブロア122との間には、バッファタンク126が介在している。 The base end side of the exhaust pipe 121 having the valve 104 and the suction blower 122 in the middle is connected to the upper part of the collection container 116. Between the valve 104 of the exhaust pipe 121 and the suction blower 122, a gas flow meter 123, which is a gas flow rate detecting means for detecting the flow rate of gas flowing through the exhaust pipe 121, is provided. A cooler 124 and a gas-liquid separator 125 are interposed between the valve 104 of the exhaust pipe 121 and the gas flow meter 123. A buffer tank 126 is interposed between the gas flow meter 123 of the exhaust pipe 121 and the suction blower 122.
 前記捕集容器116の底部には、バルブ105を途中に有する送液管127の一端側が連結されている。前記送液管127の他端側は、送給ポンプ128の受入口に接続している。前記送給ポンプ128の送出口は、定容及び希釈を行う定容・希釈装置129の受入口に連絡している。前記定容・希釈装置129の送出口は、前記アミン類等の濃度を計測するイオン交換クロマトグラフィや電気伝導度測定装置等のような計測手段である計測装置130の受入口に連絡している。 The bottom of the collection container 116 is connected to one end of a liquid feeding pipe 127 having a valve 105 in the middle. The other end side of the liquid feeding pipe 127 is connected to a receiving port of the feeding pump 128. The delivery port of the feed pump 128 communicates with a reception port of a constant volume / dilution device 129 that performs constant volume and dilution. The outlet of the constant volume / dilution device 129 communicates with an inlet of a measuring device 130 which is a measuring means such as an ion exchange chromatography or an electric conductivity measuring device for measuring the concentration of the amines.
 前記送液管127の前記バルブ105と前記送給ポンプ128との間には、バルブ106を途中に有する排液管131の一端側が接続されている。前記排液管131の他端側は、系外へ連絡している。 Between the valve 105 of the liquid feed pipe 127 and the feed pump 128, one end side of a drain pipe 131 having a valve 106 in the middle is connected. The other end side of the drainage pipe 131 communicates outside the system.
 前記導入管114の他端側(下端側)の前記バルブ102の近傍には、バルブ107を途中に有する清浄液導入管132の一端側が接続されており、当該清浄液導入管132は、一端側が他端側よりも下方へ位置するように軸方向が傾斜配向されている。上記清浄液導入管132の他端側は、純水等の清浄液3を送給する図示しない清浄液タンクへ連絡している。 In the vicinity of the valve 102 on the other end side (lower end side) of the introduction pipe 114, one end side of a cleaning liquid introduction pipe 132 having a valve 107 in the middle is connected, and the cleaning liquid introduction pipe 132 has one end side. The axial direction is inclined and oriented so as to be positioned below the other end side. The other end of the cleaning liquid introduction pipe 132 communicates with a cleaning liquid tank (not shown) that supplies the cleaning liquid 3 such as pure water.
 前記導入管114の一端側(上端側)の前記案内管112との接続部分近傍には、バルブ108を途中に有する窒素ガス導入管133の一端側が接続されており、当該窒素ガス導入管133は、一端側が他端側よりも下方へ位置するように軸方向が傾斜配向されている。上記窒素ガス導入管133の他端側は、不活性ガスである窒素ガス4を送給する図示しない窒素ガスボンベへ連絡している。 Near one end side (upper end side) of the introduction pipe 114 in the vicinity of the connection portion with the guide pipe 112, one end side of a nitrogen gas introduction pipe 133 having a valve 108 in the middle is connected. The nitrogen gas introduction pipe 133 is The axial direction is inclined and oriented so that one end side is positioned below the other end side. The other end side of the nitrogen gas introduction pipe 133 communicates with a nitrogen gas cylinder (not shown) that feeds nitrogen gas 4 that is an inert gas.
 前記導入管114の前記清浄液導入管132との接続部分と前記窒素ガス導入管133との接続部分との間には、バルブ109を途中に有するバイパス管134の一端側が接続されている。前記排気管121の前記バルブ104と前記冷却器124との間には、上記バイパス管134の他端側が接続されている。 One end side of a bypass pipe 134 having a valve 109 in the middle is connected between a connection part of the introduction pipe 114 to the cleaning liquid introduction pipe 132 and a connection part to the nitrogen gas introduction pipe 133. The other end side of the bypass pipe 134 is connected between the valve 104 of the exhaust pipe 121 and the cooler 124.
 前記案内管112には、バルブ110aを途中に有するリーク管135の一端側が接続されている。前記リーク管135の他端側は、系外へ連絡している。前記捕集容器116の上部には、バルブ110bを途中に有するリーク管136の一端側が接続されている。前記リーク管136の他端側は、系外へ連絡している。 The guide pipe 112 is connected to one end of a leak pipe 135 having a valve 110a in the middle. The other end of the leak pipe 135 communicates outside the system. One end of a leak pipe 136 having a valve 110b in the middle is connected to the upper portion of the collection container 116. The other end of the leak pipe 136 communicates outside the system.
 前記サンプリング管111の先端側には、温度検出手段である温度センサ141が設けられている。前記捕集容器116の内部には、当該捕集容器116内の前記捕集液2の量を検知する液量検出手段であるフロート形式の液量検出器142が設けられている。 A temperature sensor 141 serving as a temperature detecting means is provided on the distal end side of the sampling tube 111. In the collection container 116, a float type liquid quantity detector 142 is provided as a liquid quantity detection means for detecting the quantity of the collection liquid 2 in the collection container 116.
 図2に示すように、前記ガス流量計123、前記温度センサ141、前記液量検出器142は、タイマを内蔵した演算制御手段である演算制御装置140の入力部に電気的に接続している。前記演算制御装置140の入力部には、さらに、前記計測装置130が電気的に接続されている。前記演算制御装置140の出力部は、前記バルブ101~109,110a,110b、前記電熱ヒータ113、前記送給ポンプ119,128、前記吸引ブロア122、前記定容・希釈装置129、前記計測装置130に電気的に接続すると共に、表示手段であるモニタ143に電気的に接続しており、当該演算制御装置140は、前記ガス流量計123、前記温度センサ141、前記液量検出器142、前記タイマからの情報に基づいて、前記バルブ101~109,110a,110b、前記電熱ヒータ113、前記送給ポンプ119,128、前記吸引ブロア122、前記定容・希釈装置129、前記計測装置130の作動を制御すると共に、前記計測装置130からの情報に基づいて、前記定容・希釈装置129の作動制御及び前記モニタ143に各種情報を表示することができるようになっている(詳細は後述する)。 As shown in FIG. 2, the gas flow meter 123, the temperature sensor 141, and the liquid amount detector 142 are electrically connected to an input unit of a calculation control device 140 that is a calculation control means incorporating a timer. . The measuring device 130 is further electrically connected to the input unit of the arithmetic control device 140. The output unit of the arithmetic and control unit 140 includes the valves 101 to 109, 110a and 110b, the electric heater 113, the feed pumps 119 and 128, the suction blower 122, the constant volume / dilution device 129, and the measuring device 130. Are connected electrically to a monitor 143 which is a display means, and the arithmetic and control unit 140 includes the gas flow meter 123, the temperature sensor 141, the liquid amount detector 142, and the timer. Based on the information from the above, the operation of the valves 101 to 109, 110a, 110b, the electric heater 113, the feed pumps 119, 128, the suction blower 122, the constant volume / dilution device 129, and the measuring device 130 is performed. And controlling the operation of the constant volume / dilution device 129 based on information from the measuring device 130 and And it is capable of displaying various information on the monitor 143 (details will be described later).
 このような本実施形態においては、前記バルブ101,102,104、前記サンプリング管111、前記案内管112、前記導入管114、前記送給管115、前記捕集容器116、前記排気管121、前記吸引ブロア122、前記ガス流量計123、前記冷却器124、前記気液分離器125、前記バッファタンク126等により、対象ガスサンプリング手段を構成し、前記バルブ102,104、前記導入管114、前記送給管115、前記排気管121、前記吸引ブロア122、前記ガス流量計123、前記冷却器124、前記気液分離器125、前記バッファタンク126等により、対象ガス送給手段を構成し、前記バルブ107、前記清浄液導入管132、前記清浄液タンク等により、清浄液供給手段を構成し、前記バルブ105、前記送液管127、前記送給ポンプ128、前記定容・希釈装置129等により、液分取手段を構成し、前記バルブ103、前記送出管118、前記送給ポンプ119、前記貯液タンク120等により、捕集液供給手段を構成し、前記バルブ106、前記排液管131等により、液排出手段を構成し、前記バルブ108、前記窒素ガス導入管、前記窒素ガスボンベ等により、不活性ガス供給手段を構成し、前記バルブ109、前記バイパス管134等により、バイパス手段を構成している。 In this embodiment, the valves 101, 102, 104, the sampling pipe 111, the guide pipe 112, the introduction pipe 114, the supply pipe 115, the collection container 116, the exhaust pipe 121, The suction blower 122, the gas flow meter 123, the cooler 124, the gas-liquid separator 125, the buffer tank 126, and the like constitute a target gas sampling means, and the valves 102 and 104, the introduction pipe 114, and the feed pipe. The supply pipe 115, the exhaust pipe 121, the suction blower 122, the gas flow meter 123, the cooler 124, the gas-liquid separator 125, the buffer tank 126, etc. constitute a target gas supply means, and the valve 107, the cleaning liquid supply pipe 132, the cleaning liquid tank, and the like constitute cleaning liquid supply means, and the valve 1 5. The liquid feeding pipe 127, the feeding pump 128, the constant volume / dilution device 129, and the like constitute liquid sorting means, and the valve 103, the feeding pipe 118, the feeding pump 119, the liquid storage The tank 120 or the like constitutes a collected liquid supply means, and the valve 106, the drainage pipe 131, or the like constitutes a liquid discharge means, and the valve 108, the nitrogen gas introduction pipe, the nitrogen gas cylinder, etc. The active gas supply means is configured, and the valve 109, the bypass pipe 134 and the like constitute bypass means.
 このようにして構成された本実施形態に係るミスト含有ガス分析装置100の作動を次に説明する。 Next, the operation of the mist-containing gas analyzer 100 according to this embodiment configured as described above will be described.
 当初、前記バルブ101~109は、すべて閉鎖した状態となっており、前記演算制御装置140を作動させると、当該演算制御装置140は、まず、前記温度センサ141からの情報に基づいて、前記アミン類等を気化させる温度(約150~200℃)で前記管111,112,114を加熱するように、前記電熱ヒータ113の作動を制御する。 Initially, the valves 101 to 109 are all in a closed state, and when the arithmetic control device 140 is operated, the arithmetic control device 140 first determines the amine based on information from the temperature sensor 141. The operation of the electric heater 113 is controlled so that the tubes 111, 112, 114 are heated at a temperature (about 150 to 200 ° C.) for vaporizing the like.
 続いて、前記演算制御装置140は、前記液量検出器142からの情報に基づいて、前記捕集容器116の内部に規定量の捕集液2を溜めるように、前記バルブ103,110bの開閉制御及び前記送給ポンプ119の作動制御を行って、前記捕集容器116内のガスを前記リーク管136から系外へ排出しながら前記貯液タンク120内の前記捕集液2を前記送出管118から当該捕集容器116内へ送給する。 Subsequently, the arithmetic and control unit 140 opens and closes the valves 103 and 110b based on the information from the liquid amount detector 142 so as to store a predetermined amount of the collected liquid 2 in the collection container 116. The collection liquid 2 in the storage tank 120 is discharged from the leak pipe 136 while the gas in the collection container 116 is discharged out of the system by controlling the operation and the operation of the feed pump 119. It is fed from 118 into the collection container 116.
 前記捕集容器116の内部に規定量の捕集液2が貯留されると、前記制御装置140は、前記液量検出器142からの情報に基づいて、前記ダクト10内を流通する前記燃焼排ガス1で前記サンプリング管111及び前記案内管112の内部をパージするように、前記バルブ101,109を開放制御すると共に、前記吸引ブロア122を作動制御し、前記ダクト10内の前記燃焼排ガス1を前記サンプリング管111内に取り込んで、前記案内管112から前記バイパス管134及び前記排気管121を経由させて系外へ排出する。 When a specified amount of the collected liquid 2 is stored in the collection container 116, the control device 140, based on information from the liquid amount detector 142, the combustion exhaust gas that circulates in the duct 10. 1, the valves 101 and 109 are controlled to be opened so that the inside of the sampling pipe 111 and the guide pipe 112 is purged, and the suction blower 122 is operated and controlled so that the combustion exhaust gas 1 in the duct 10 is The sample is taken into the sampling pipe 111 and discharged from the guide pipe 112 through the bypass pipe 134 and the exhaust pipe 121 to the outside of the system.
 このようにして前記サンプリング管111及び前記案内管112の内部を前記燃焼排ガス1で所定時間パージすると、前記制御装置140は、前記タイマからの情報に基づいて、前記燃焼排ガス1を前記捕集容器116内の前記捕集液2と接触させるように、前記バルブ109を閉鎖制御(前記バルブ101は開放状態を維持)すると共に、前記バルブ102,104を開放制御することにより、前記送給管115から前記フィルタ117を介して前記燃焼排ガス1を前記捕集容器116内の前記捕集液2中に送給して当該燃焼排ガス1中の前記アミン類等を当該捕集液2に溶解させて捕集する一方、当該アミン類等を捕集された上記燃焼排ガス1を前記排気管121から前記冷却器124に送給して冷却し、当該燃焼排ガス1中の水分を凝縮させて気液分離器125で分離し、水分を除去された当該燃焼排ガス1を前記ガス流量計123で流量計測しながら前記バッファタンク126を介して前記吸引ブロア122から系外へ排出する。 Thus, when the inside of the sampling pipe 111 and the guide pipe 112 is purged with the flue gas 1 for a predetermined time, the control device 140 removes the flue gas 1 based on the information from the timer. The valve 109 is controlled to be closed (the valve 101 is maintained in an open state) so as to come into contact with the collected liquid 2 in 116, and the valves 102 and 104 are controlled to open, whereby the feeding pipe 115 is controlled. The combustion exhaust gas 1 is fed into the collection liquid 2 in the collection container 116 through the filter 117 and the amines and the like in the combustion exhaust gas 1 are dissolved in the collection liquid 2. On the other hand, the combustion exhaust gas 1 in which the amines and the like are collected is fed from the exhaust pipe 121 to the cooler 124 to be cooled, and moisture in the combustion exhaust gas 1 is removed. By condensation separated by the gas-liquid separator 125, and discharges the combustion exhaust gas 1 which is removing water from the gas flow meter 123 the suction blower 122 through the buffer tank 126 while the flow rates were measured by the outside of the system.
 このとき、前記管111,112,114は、前記電熱ヒータ113で前記アミン類等を気化させる温度(約150~200℃)にまで加熱保持されているので、前記ダクト10から取り込んだ前記燃焼排ガス1中に含有されるガス状及びミスト状の上記アミン類等を内壁面に凝縮付着させることなく前記送給管115にまで気化させた状態で送給することができる。 At this time, the pipes 111, 112, 114 are heated and held up to a temperature (about 150 to 200 ° C.) for vaporizing the amines and the like by the electric heater 113, so that the combustion exhaust gas taken in from the duct 10 1 can be fed in a state of being vaporized up to the feed pipe 115 without condensing and adhering the gaseous and mist amines contained in 1 to the inner wall surface.
 また、前記送給管115からの前記燃焼排ガス1を前記捕集液2中に前記フィルタ117を介して送給しているので、当該燃焼排ガス1を微細気泡化して当該捕集液2との接触面積を大きくすることができ、当該燃焼排ガス1中の前記アミン類等を効率よく捕集することができる。 Further, since the flue gas 1 from the feed pipe 115 is fed into the collected liquid 2 via the filter 117, the flue gas 1 is made into fine bubbles and the collected liquid 2 is mixed with the collected liquid 2. The contact area can be increased, and the amines and the like in the combustion exhaust gas 1 can be efficiently collected.
 このようにして前記捕集容器116内の前記捕集液2中に規定の積算流量の前記燃焼排ガス1を流通させると、前記演算制御装置140は、前記ガス流量計123からの情報に基づいて、当該捕集液2中への当該燃焼排ガス1の供給を停止するように、前記バルブ101,102,104を閉鎖制御すると共に、前記吸引ブロア122を作動停止制御した後、前記タイマからの情報に基づいて、前記清浄液3を前記清浄液導入管132から前記導入管114内に規定時間(規定量)送給して当該導入管114内を当該清浄液3で満たすように前記バルブ107,110aを開閉制御する。 When the combustion exhaust gas 1 having a prescribed integrated flow rate is circulated in the collected liquid 2 in the collection container 116 in this way, the arithmetic and control unit 140 is based on information from the gas flow meter 123. The valve 101, 102, 104 is controlled to be closed so that the supply of the flue gas 1 into the collected liquid 2 is stopped, and the suction blower 122 is controlled to stop, and then the information from the timer The cleaning liquid 3 is fed from the cleaning liquid introduction pipe 132 into the introduction pipe 114 for a prescribed time (a prescribed amount) so that the introduction pipe 114 is filled with the cleaning liquid 3. 110a is controlled to open and close.
 次に、前記演算制御装置140は、前記送給管115の内壁面に付着している前記アミン類等を前記捕集容器116内に送り込むように、前記タイマからの情報に基づいて、前記バルブ102,108,110bの開閉制御を規定のタイミングで行って、前記導入管114内の前記清浄液3を前記窒素ガス導入管133からの前記窒素ガス4で押し出して、前記送給管115の内壁面に付着してしまっているすべての前記アミン類等に当該清浄液3を接触させるように当該送給管115の内壁面に接触させながら流下させて、前記捕集容器116内に存在する前記燃焼排ガス1を前記リーク管136から系外へ排出しながら当該捕集容器116内の当該捕集液2中に流入させる。 Next, the arithmetic and control unit 140 is configured to control the valve based on information from the timer so as to send the amines and the like adhering to the inner wall surface of the feed pipe 115 into the collection container 116. The opening / closing control of the 102, 108, 110b is performed at a prescribed timing, and the cleaning liquid 3 in the introduction pipe 114 is pushed out by the nitrogen gas 4 from the nitrogen gas introduction pipe 133, and the inside of the supply pipe 115 The cleaning liquid 3 is caused to flow down while being in contact with the inner wall surface of the feed pipe 115 so that the cleaning liquid 3 is brought into contact with all the amines and the like adhering to the wall surface. The combustion exhaust gas 1 is allowed to flow into the collection liquid 2 in the collection container 116 while being discharged out of the system from the leak pipe 136.
 これにより、前記送給管115の内壁面に付着したすべての前記アミン類等を前記捕集容器116内に捕集することができる。 Thereby, all the amines and the like adhering to the inner wall surface of the feed pipe 115 can be collected in the collection container 116.
 続いて、前記演算制御装置140は、前記捕集容器116内の前記液2,3の一部を前記定容・希釈装置129に分取するように、前記タイマからの情報に基づいて、前記バルブ102,105,108の開閉制御及び前記送給ポンプ128の作動制御を規定のタイミングで行い、前記窒素ガス4を前記窒素ガス導入管133から前記導入管114及び前記送給管115を介して前記捕集容器116内に供給しながら当該捕集容器116内の前記液2,3を前記送液管127から前記送給ポンプ128を介して前記定容・希釈装置129に混合送給する。 Subsequently, based on the information from the timer, the arithmetic and control unit 140 sorts the liquids 2 and 3 in the collection container 116 into the constant volume / dilution unit 129. The opening / closing control of the valves 102, 105, and 108 and the operation control of the feed pump 128 are performed at a prescribed timing, and the nitrogen gas 4 is supplied from the nitrogen gas introduction pipe 133 through the introduction pipe 114 and the feed pipe 115. While being supplied into the collection container 116, the liquids 2 and 3 in the collection container 116 are mixed and fed from the liquid feed pipe 127 to the constant volume / dilution device 129 through the feed pump 128.
 そして、前記演算制御装置140は、混合された規定量の前記液2,3を前記計測装置130に送給するように前記定容・希釈装置129の作動を制御する。前記計測装置130が、定容された前記液2,3中の前記アミン類等の濃度を計測すると、前記演算制御装置140は、当該計測装置130からの情報に基づき、計測結果が検量可能な範囲内であるか否か判断し、検量可能な範囲内である場合には、前記燃焼排ガス1中の前記アミン類等の濃度を算出し、その結果を前記モニタ143に表示する。 Then, the arithmetic and control unit 140 controls the operation of the constant volume / dilution unit 129 so as to send the mixed specified amount of the liquids 2 and 3 to the measuring unit 130. When the measurement device 130 measures the concentration of the amines or the like in the liquids 2 and 3 in a constant volume, the arithmetic control device 140 can calibrate the measurement result based on information from the measurement device 130. It is determined whether or not it is within the range, and if it is within the range that can be calibrated, the concentration of the amines and the like in the combustion exhaust gas 1 is calculated, and the result is displayed on the monitor 143.
 他方、前記計測装置130での計測結果が検量可能な範囲外である場合には、前記演算制御装置140は、前記計測装置130に送給される前記液2,3中の前記アミン類等の濃度が検量可能な範囲内となる希釈倍率を算出し、算出された倍率で前記液2,3を純水等の希釈液で希釈するように前記定容・希釈装置129を作動制御する。前記定容・希釈装置129が前記液2,3を算出倍率で希釈すると、前記演算制御装置140は、希釈された上記液2,3を前記計測装置130に規定量で改めて送給するように前記定容・希釈装置129の作動を制御し、前記計測装置130が、当該液2,3中の前記アミン類等の濃度を改めて計測する。そして、前記演算制御装置140は、前記計測装置130からの情報に基づき、上記燃焼排ガス1中の前記アミン類等の濃度を算出して、その結果を前記モニタ143に表示する。 On the other hand, when the measurement result of the measurement device 130 is outside the range that can be calibrated, the arithmetic and control unit 140 may determine the amines and the like in the liquids 2 and 3 fed to the measurement device 130. The dilution rate is calculated so that the concentration is within the calibratable range, and the constant volume / dilution device 129 is controlled to dilute the liquids 2 and 3 with a diluted solution such as pure water at the calculated magnification. When the constant volume / dilution device 129 dilutes the liquids 2 and 3 at the calculated magnification, the arithmetic and control unit 140 again sends the diluted liquids 2 and 3 to the measuring device 130 in a specified amount. The operation of the constant volume / dilution device 129 is controlled, and the measuring device 130 measures the concentration of the amines and the like in the liquids 2 and 3 again. Then, the arithmetic and control unit 140 calculates the concentration of the amines and the like in the combustion exhaust gas 1 based on the information from the measuring device 130 and displays the result on the monitor 143.
 このようにして前記燃焼排ガス1中のアミン類等の濃度を求めたら、前記演算制御装置140は、前記計測装置130からの情報に基づいて、前記捕集容器116内の前記液2,3を系外へ排出するように、前記バルブ102,105,106,108を開放制御して、前記窒素ガス4を前記窒素ガス導入管133から前記導入管114及び前記送給管115を介して前記捕集容器116の内部に送給しながら当該捕集容器116内のすべての前記液2,3を前記送液管127から前記排液管131を介して系外へ排出する。 When the concentration of amines and the like in the combustion exhaust gas 1 is obtained in this way, the arithmetic and control unit 140 removes the liquids 2 and 3 in the collection container 116 based on information from the measuring unit 130. The valves 102, 105, 106, and 108 are controlled so as to be discharged out of the system, and the nitrogen gas 4 is captured from the nitrogen gas introduction pipe 133 through the introduction pipe 114 and the supply pipe 115. All the liquids 2 and 3 in the collection container 116 are discharged out of the system through the liquid supply pipe 127 and the drainage pipe 131 while being fed into the collection container 116.
 このようにして前記捕集容器116内から系外への前記液2,3の排出を規定時間行うと、前記演算制御装置140は、前記タイマからの情報に基づいて、前記捕集容器116内を前記清浄液3で満たすように、前記バルブ105,106,108を閉鎖制御(前記バルブ102は開放状態を維持)すると共に、前記バルブ107,110bを開放制御して、前記清浄液3を前記清浄液導入管132から前記送給管115を介して前記捕集容器116の内部に規定時間供給し、当該捕集容器116内のガスを前記リーク管136から系外へ追い出しつつ上記清浄液3を当該リーク管136からオーバフローさせる程度にまで当該捕集容器116の内部に供給する。 When the liquids 2 and 3 are discharged from the collection container 116 to the outside of the system in a specified time in this way, the arithmetic and control unit 140 determines that the inside of the collection container 116 is based on information from the timer. The valve 105, 106, 108 is controlled to be closed so as to be filled with the cleaning liquid 3 (the valve 102 is kept open), and the valves 107, 110b are controlled to open so that the cleaning liquid 3 is The cleaning liquid 3 is supplied from the cleaning liquid introduction pipe 132 through the feeding pipe 115 to the inside of the collection container 116 for a specified time, and the gas in the collection container 116 is expelled from the leak pipe 136 to the outside of the system. To the inside of the collection container 116 to such an extent that it overflows from the leak pipe 136.
 このようにして前記捕集容器116の内部に前記清浄液3を規定時間(規定量)供給すると、前記演算制御装置140は、前記タイマからの情報に基づいて、前記捕集容器116内の前記清浄液3を系外へ排出するように、前記バルブ107,110bを閉鎖制御(前記バルブ102は開放状態を維持)すると共に、前記バルブ105,106,108を開放制御して、前記窒素ガス4を前記窒素ガス導入管133から前記導入管114及び前記送給管115を介して前記捕集容器116の内部に送給しながら当該捕集容器116内のすべての前記清浄液3を前記送液管127から前記排液管131を介して系外へ排出する。 In this way, when the cleaning liquid 3 is supplied to the inside of the collection container 116 for a specified time (a specified amount), the arithmetic and control unit 140, based on the information from the timer, The valves 107 and 110b are controlled to be closed (the valve 102 is kept open) and the valves 105, 106 and 108 are controlled to be opened so that the cleaning liquid 3 is discharged out of the system. Is fed from the nitrogen gas introduction pipe 133 to the inside of the collection container 116 through the introduction pipe 114 and the supply pipe 115, and all the cleaning liquid 3 in the collection container 116 is fed to the liquid. The liquid is discharged from the pipe 127 through the drain pipe 131.
 このようにして前記捕集容器116内から系外への前記清浄液3の排出を規定時間行うと、前記演算制御装置140は、前記タイマからの情報に基づいて、前記フィルタ117を洗浄するように、前記バルブ108を閉鎖制御(前記バルブ102,105,106は開放状態を維持)すると共に、前記バルブ107を開放制御し、前記清浄液3を前記清浄液導入管132から前記送給管115を介して前記フィルタ117に規定時間送給して当該フィルタ117を洗浄し、当該清浄液3を前記送液管127から前記排液管131を介して系外へ排出する。 In this way, when the cleaning liquid 3 is discharged from the collection container 116 to the outside of the system for a specified time, the arithmetic and control unit 140 cleans the filter 117 based on the information from the timer. In addition, the valve 108 is controlled to be closed (the valves 102, 105, and 106 are kept open), the valve 107 is controlled to be opened, and the cleaning liquid 3 is supplied from the cleaning liquid introduction pipe 132 to the feeding pipe 115. Then, the filter 117 is supplied to the filter 117 for a specified time to clean the filter 117, and the cleaning liquid 3 is discharged from the liquid supply pipe 127 to the outside of the system through the drainage pipe 131.
 このような上記清浄液3による清浄化を規定時間行うと、前記演算制御装置140は、前記タイマからの情報に基づいて、前記バルブ102,105,106,107を閉鎖制御して、初期状態に戻す。 When such cleaning with the cleaning liquid 3 is performed for a specified time, the arithmetic and control unit 140 controls the valves 102, 105, 106, and 107 to be in an initial state based on information from the timer. return.
 以下、上述した作動を繰り返すことにより、前記ダクト10内を流通する前記燃焼排ガス1中の前記アミン類等の濃度を自動で継続的に計測することができる。 Hereinafter, by repeating the above-described operation, the concentration of the amines and the like in the combustion exhaust gas 1 flowing through the duct 10 can be automatically and continuously measured.
 したがって、本実施形態に係るミスト含有ガス分析装置100によれば、アミン類等をガス状に含有しているだけでなく、ミスト状でも含有している燃焼排ガス1であっても、当該燃焼排ガス1中の当該アミン類等の濃度を簡単かつ正確に計測することができる。 Therefore, according to the mist-containing gas analyzer 100 according to the present embodiment, even if the exhaust gas 1 contains not only amines and the like but also mist, The concentration of the amines in 1 can be measured easily and accurately.
 また、前記送給管115からの前記燃焼排ガス1を前記捕集液2中に前記フィルタ117を介して送給しているので、当該燃焼排ガス1を微細気泡化して当該捕集液2との接触面積を大きくすることができ、当該燃焼排ガス1中の前記アミン類等を効率よく捕集することができる。 Further, since the flue gas 1 from the feed pipe 115 is fed into the collected liquid 2 via the filter 117, the flue gas 1 is made into fine bubbles and the collected liquid 2 is mixed with the collected liquid 2. The contact area can be increased, and the amines and the like in the combustion exhaust gas 1 can be efficiently collected.
〈他の実施形態〉
 なお、前述した実施形態においては、ボイラ等からの燃焼排ガスをアミン類含有の吸収液に接触させて当該燃焼排ガス中の二酸化炭素を吸収液中に吸収して回収する二酸化炭素回収装置を備えた排ガス処理装置における当該燃焼排ガス1中の上記アミン類等の濃度を計測する場合について説明したが、本発明はこれに限らず、例えば、気液接触装置の出口ガス(例えば水分飽和ガス)中の液体成分濃度を計測する場合等のように、被測定物質のミストを含有する対象ガス中の当該被測定物質の濃度を計測するような場合であれば、前述した実施形態の場合と同様にして適用することができる。
<Other embodiments>
In the embodiment described above, a carbon dioxide recovery device is provided in which combustion exhaust gas from a boiler or the like is brought into contact with an amine-containing absorption liquid and carbon dioxide in the combustion exhaust gas is absorbed and recovered in the absorption liquid. Although the case where the density | concentration of the said amines in the said combustion exhaust gas 1 in the said waste gas treatment apparatus was measured was demonstrated, this invention is not restricted to this, For example, in the exit gas (for example, moisture saturation gas) of a gas-liquid contact apparatus As in the case of measuring the concentration of the substance to be measured in the target gas containing the mist of the substance to be measured, such as when measuring the liquid component concentration, the same as in the case of the above-described embodiment. Can be applied.
 本発明に係るミスト含有ガス分析装置は、被測定物質をガス状に含有しているだけでなく、ミスト状でも含有している対象ガスであっても、当該対象ガス中の被測定物質の濃度を簡単かつ正確に計測することができるので、各種産業において、極めて有益に利用することができる。 The mist-containing gas analyzer according to the present invention not only contains the substance to be measured in a gaseous state, but also the concentration of the substance to be measured in the target gas, even if it is a target gas that also contains the mist. Can be measured easily and accurately, and can be used extremely beneficially in various industries.
 1 燃焼排ガス
 2 捕集液
 3 清浄液
 4 窒素ガス
 10 ダクト
 100 ミスト含有ガス分析装置
 101~109,110a,110b バルブ
 111 サンプリング管
 112 案内管
 113 電熱ヒータ
 114 導入管
 115 送給管
 116 捕集容器
 117 フィルタ
 118 送出管
 119 送給ポンプ
 120 貯液タンク
 121 排気管
 122 吸引ブロア
 123 ガス流量計
 124 冷却器
 125 気液分離器
 126 バッファタンク
 127 送液管
 128 送給ポンプ
 129 定容・希釈装置
 130 計測装置
 131 排液管
 132 清浄液導入管
 133 窒素ガス導入管
 134 バイパス管
 135,136 リーク管
 140 演算制御装置
 141 温度センサ
 142 液量検出器
 143 モニタ
DESCRIPTION OF SYMBOLS 1 Combustion exhaust gas 2 Collected liquid 3 Cleaning liquid 4 Nitrogen gas 10 Duct 100 Mist containing gas analyzer 101-109, 110a, 110b Valve 111 Sampling pipe 112 Guide pipe 113 Electric heating heater 114 Introduction pipe 115 Feed pipe 116 Collection container 117 Filter 118 Delivery pipe 119 Feed pump 120 Storage tank 121 Exhaust pipe 122 Suction blower 123 Gas flow meter 124 Cooler 125 Gas-liquid separator 126 Buffer tank 127 Feed pipe 128 Feed pump 129 Constant volume / dilution device 130 Measuring device 131 Drainage pipe 132 Clean liquid introduction pipe 133 Nitrogen gas introduction pipe 134 Bypass pipe 135, 136 Leak pipe 140 Arithmetic controller 141 Temperature sensor 142 Liquid quantity detector 143 Monitor

Claims (7)

  1.  被測定物質のミストを含有する対象ガス中の当該被測定物質の濃度を計測するミスト含有ガス分析装置であって、
     前記被測定物質を溶解させる捕集液を内部に入れられる捕集容器と、
     前記対象ガスをサンプリングする対象ガスサンプリング手段と、
     前記対象ガスサンプリング手段でサンプリングされた前記被測定物質を気化させるように当該対象ガスサンプリング手段を加熱する加熱手段と、
     前記対象ガスサンプリング手段でサンプリングされた前記対象ガスを前記捕集容器の内部の前記捕集液中に送給する対象ガス送給手段と、
     前記被測定物質を溶解させる清浄液を前記対象ガス送給手段に供給して当該対象ガス送給手段に付着している前記被測定物質を当該清浄液と共に当該対象ガス送給手段から前記捕集容器の内部へ送り込ませる清浄液供給手段と、
     前記捕集容器の内部の前記液を分取する液分取手段と、
     前記液分取手段で分取された前記液中の前記被測定物質の濃度を計測する計測手段と
     を備えていることを特徴とするミスト含有ガス分析装置。
    A mist-containing gas analyzer for measuring the concentration of a substance to be measured in a target gas containing a mist of the substance to be measured,
    A collection container into which a collection solution for dissolving the substance to be measured can be placed;
    A target gas sampling means for sampling the target gas;
    Heating means for heating the target gas sampling means so as to vaporize the substance to be measured sampled by the target gas sampling means;
    Target gas feeding means for feeding the target gas sampled by the target gas sampling means into the collected liquid inside the collection container;
    A cleaning liquid for dissolving the substance to be measured is supplied to the target gas feeding means, and the substance to be measured attached to the target gas feeding means is collected from the target gas feeding means together with the cleaning liquid. Cleaning liquid supply means for feeding into the container;
    A liquid fractionating means for fractionating the liquid inside the collection container;
    A mist-containing gas analyzer comprising: a measuring unit that measures the concentration of the substance to be measured in the liquid sorted by the liquid sorting unit.
  2.  請求項1に記載のミスト含有ガス分析装置において、
     前記対象ガス送給手段から前記捕集容器の内部の前記捕集液中へ送給される前記対象ガスを微細気泡化する微細気泡化手段を備えている
     ことを特徴とするミスト含有ガス分析装置。
    The mist-containing gas analyzer according to claim 1,
    A mist-containing gas analyzer characterized by comprising microbubble generation means for microbubbles the target gas fed from the target gas feeding means into the collection liquid inside the collection container. .
  3.  請求項2に記載のミスト含有ガス分析装置において、
     前記微細気泡化手段が、5~120μmの範囲内の最大細孔を有するフィルタである
     ことを特徴とするミスト含有ガス分析装置。
    The mist-containing gas analyzer according to claim 2,
    The mist-containing gas analyzer, wherein the microbubble generation means is a filter having a maximum pore in the range of 5 to 120 μm.
  4.  請求項1から請求項3のいずれか一項に記載のミスト含有ガス分析装置において、
     前記被測定物質が、アミン類及びアンモニアである
     ことを特徴とするミスト含有ガス分析装置。
    In the mist containing gas analyzer according to any one of claims 1 to 3,
    The mist-containing gas analyzer, wherein the substances to be measured are amines and ammonia.
  5.  請求項4に記載のミスト含有ガス分析装置において、
     前記加熱手段が、前記対象ガスサンプリング手段を150~200℃の範囲で加熱するものである
     ことを特徴とするミスト含有ガス分析装置。
    The mist-containing gas analyzer according to claim 4,
    The mist-containing gas analyzer characterized in that the heating means heats the target gas sampling means in the range of 150 to 200 ° C.
  6.  請求項5に記載のミスト含有ガス分析装置において、
     前記対象ガスが、アミン類を含有する吸収液により二酸化炭素を吸収除去された燃焼排ガスである
     ことを特徴とするミスト含有ガス分析装置。
    In the mist containing gas analyzer of Claim 5,
    The mist-containing gas analyzer, wherein the target gas is a combustion exhaust gas from which carbon dioxide has been absorbed and removed by an absorbing solution containing amines.
  7.  請求項1から請求項6のいずれか一項に記載のミスト含有ガス分析装置において、
     前記対象ガスサンプリング手段が、前記対象ガスをサンプリングするサンプリング管を備え、前記サンプリング管の先端側に温度検出手段が設けられている
     ことを特徴とするミスト含有ガス分析装置。
    In the mist containing gas analyzer according to any one of claims 1 to 6,
    The mist-containing gas analyzing apparatus, wherein the target gas sampling means includes a sampling pipe for sampling the target gas, and a temperature detecting means is provided on a tip side of the sampling pipe.
PCT/JP2012/082882 2011-12-21 2012-12-19 Mist-containing gas analysis device WO2013094628A1 (en)

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CN105004761A (en) * 2015-06-26 2015-10-28 华电电力科学研究院 Denitration system escaping ammonia on-line continuous monitoring device and method
CN106645977A (en) * 2017-03-07 2017-05-10 云南电网有限责任公司电力科学研究院 Fog conductivity detection device and use method
CN107305162A (en) * 2016-04-20 2017-10-31 中国石油天然气股份有限公司 Sour crude oil sampler and sampling method

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JP6575794B2 (en) * 2015-02-16 2019-09-18 中国電力株式会社 Analytical sample collection device and collected sample analysis device

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CN105004761A (en) * 2015-06-26 2015-10-28 华电电力科学研究院 Denitration system escaping ammonia on-line continuous monitoring device and method
CN107305162A (en) * 2016-04-20 2017-10-31 中国石油天然气股份有限公司 Sour crude oil sampler and sampling method
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