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JP2011095229A - Dilution air refining device - Google Patents

Dilution air refining device Download PDF

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JP2011095229A
JP2011095229A JP2009252365A JP2009252365A JP2011095229A JP 2011095229 A JP2011095229 A JP 2011095229A JP 2009252365 A JP2009252365 A JP 2009252365A JP 2009252365 A JP2009252365 A JP 2009252365A JP 2011095229 A JP2011095229 A JP 2011095229A
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exhaust gas
dilution air
concentration
dilution
diluted
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Shigeru Nakatani
茂 中谷
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Horiba Ltd
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Horiba Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To reduce to the utmost, the ratio of an N<SB>2</SB>O concentration in dilution air to an N<SB>2</SB>O concentration in exhaust gas diluted by the dilution air by removing N<SB>2</SB>O in the dilution air, and to thereby improve measurement accuracy of the N<SB>2</SB>O concentration in the exhaust gas. <P>SOLUTION: This dilution air refining device 3 used in an exhaust gas sampling analysis system 100 for measuring components included in the diluted exhaust gas acquired by diluting engine exhaust gas by the dilution air includes: a heating part 33 for heating the dilution air collected from the atmosphere; a catalyst part 34 for converting N<SB>2</SB>O included in the heated dilution air into N<SB>2</SB>or NO<SB>X</SB>; and an NO<SB>X</SB>removal part 38 provided on the downstream of the catalyst part, for removing NO<SB>X</SB>included in the dilution air. <P>COPYRIGHT: (C)2011,JPO&amp;INPIT

Description

本発明は、排ガスサンプリング分析システムに用いられる希釈用空気精製装置に関するものである。   The present invention relates to an air purification apparatus for dilution used in an exhaust gas sampling analysis system.

従来、排ガスサンプリング分析システムに用いられる希釈用空気精製装置としては、特許文献1又は2に示すように、酸化触媒(Pd系、Pt系等)を用いて、CO、HC、NO等を酸化させるとともに、NO除去剤によりNOを吸着除去するものである。 Conventionally, as an air purification apparatus for dilution used in an exhaust gas sampling analysis system, as shown in Patent Document 1 or 2, an oxidation catalyst (Pd system, Pt system, etc.) is used to oxidize CO, HC, NO X, etc. together is, it is to adsorb and remove the NO X by NO X removal agent.

近年、一酸化二窒素(NO)が温室効果ガスとして注目されてきており、排ガス中に含まれるNOも例外ではなく、排ガス中に含まれるNOの濃度を分析する必要が生じてきている。 In recent years, dinitrogen monoxide (N 2 O) has attracted attention as a greenhouse gas, and N 2 O contained in exhaust gas is no exception, and it is necessary to analyze the concentration of N 2 O contained in exhaust gas. It is happening.

そして、排ガスサンプリング分析システムにおける希釈サンプリング方式を用いた排ガス分析においては、希釈用空気中の成分濃度を測定すると共に、希釈された排ガス中の成分濃度を測定して、それら測定結果の差分を取ることによってバックグラウンド補正をし、排ガス中の成分濃度を算出するものである。そして、排ガス中のNO濃度を測定する場合においても同様の手法が用いられる。 In the exhaust gas analysis using the dilution sampling method in the exhaust gas sampling analysis system, the component concentration in the dilution air is measured, the component concentration in the diluted exhaust gas is measured, and the difference between the measurement results is obtained. Thus, the background is corrected and the component concentration in the exhaust gas is calculated. The same technique is used when measuring the N 2 O concentration in the exhaust gas.

しかしながら、大気から採取される希釈用空気中には、既に約300ppb程度のNOが含まれており、排ガス中に含まれるNO濃度がそれに近い値又はそれ以下の場合には特に、希釈用空気のNO濃度の測定誤差が、バックグラウンド補正後の排ガス中のNO濃度に大きく影響してしまい、その結果、排ガス中のNO濃度の測定精度が悪くなるという問題がある。つまり、希釈された排ガス中のNO濃度に対する希釈用空気のNO濃度の割合が大きいという問題がある。 However, the dilution air collected from the atmosphere already contains about 300 ppb of N 2 O, and especially when the concentration of N 2 O contained in the exhaust gas is close to or lower than that, The measurement error of the N 2 O concentration in the dilution air greatly affects the N 2 O concentration in the exhaust gas after background correction, and as a result, the measurement accuracy of the N 2 O concentration in the exhaust gas is deteriorated. There is. That is, there is a problem that the ratio of the N 2 O concentration of the dilution air to the N 2 O concentration in the diluted exhaust gas is large.

特開平6−3232号公報JP-A-6-3232 特開平10−19744号公報Japanese Patent Laid-Open No. 10-19744

そこで本発明は、希釈用空気中のNOを除去して、当該希釈用空気によって希釈された排ガス中のNO濃度に対する希釈用空気のNO濃度の割合を可及的に小さくし、排ガス中のNO濃度の測定精度を向上させることをその主たる所期課題とするものである。 The present invention removes the N 2 O in the dilution air, as much as possible the proportion of N 2 O concentration of the dilution air to N 2 O concentration in the exhaust gas diluted by the dilution air small Therefore, it is a main intended issue to improve the measurement accuracy of the N 2 O concentration in the exhaust gas.

すなわち本発明に係る希釈用空気精製装置は、エンジン排ガスを希釈用空気によって希釈し、その希釈排ガス中に含まれる成分を測定する排ガスサンプリング分析システムに用いられる希釈用空気精製装置であって、大気から採取した希釈用空気を加熱する加熱器と、前記加熱器により加熱された希釈用空気に含まれるNOをN又はNOに変換する触媒部と、前記NO触媒部の下流に設けられ、前記希釈用空気に含まれるNOを除去するNO除去部と、を備えることを特徴とする。 That is, the dilution air purifying apparatus according to the present invention is a dilution air purifying apparatus used in an exhaust gas sampling analysis system for diluting engine exhaust gas with dilution air and measuring components contained in the diluted exhaust gas. A heater for heating the dilution air collected from the catalyst, a catalyst part for converting N 2 O contained in the dilution air heated by the heater into N 2 or NO X , and downstream of the N 2 O catalyst part provided, characterized in that it comprises, a NO X removal unit for removing NO X contained in the dilution air.

このように構成した本発明によれば、希釈用空気中のNOを除去して、当該希釈用空気によって希釈された排ガス中のNO濃度に対する希釈用空気のNO濃度の割合を可及的に小さくし、排ガス中のNO濃度の測定精度を向上させることができる。 According to thus constituted present invention, the ratio of N 2 O concentration of the dilution air for removing the N 2 O in the dilution air, N 2 O concentration in the exhaust gas diluted by the dilution air Can be made as small as possible, and the measurement accuracy of the N 2 O concentration in the exhaust gas can be improved.

本発明の一実施形態に排ガスサンプリング分析システムの模式的斜視図である。1 is a schematic perspective view of an exhaust gas sampling analysis system according to an embodiment of the present invention. 同実施形態の希釈用空気精製装置の構成を示す図である。It is a figure which shows the structure of the air purification apparatus for dilution of the embodiment. 希釈用空気中のNO除去の有無における補正結果を示す模式図である。It is a schematic diagram showing a correction result in the presence of N 2 O removal dilution air.

以下に本発明に係る希釈用空気精製装置を用いた排ガスサンプリング分析システムの一実施形態について図面を参照して説明する。   Hereinafter, an embodiment of an exhaust gas sampling analysis system using a dilution air purifier according to the present invention will be described with reference to the drawings.

本実施形態に係る排ガスサンプリング分析システム100は、希釈サンプリング方式のものであり、自動車200から採取したエンジン排ガス(以下、「排ガス」という。)を大気から精製される希釈用空気で数倍に希釈して、濃度測定を行うものである。以下、本実施形態では、排ガス全量をサンプリングして、希釈用空気で希釈して一定の既知流量にする定容量定容量希釈サンプリング方式のものについて説明する。   The exhaust gas sampling analysis system 100 according to this embodiment is of a dilution sampling system, and engine exhaust gas (hereinafter referred to as “exhaust gas”) collected from the automobile 200 is diluted several times with dilution air purified from the atmosphere. Thus, the concentration is measured. Hereinafter, in the present embodiment, a description will be given of a constant volume, constant volume dilution sampling method in which the exhaust gas is sampled and diluted with dilution air to obtain a constant known flow rate.

具体的にこのものは、図1に示すように、排ガス全量及び希釈用空気を装置に導入して、それらを合わせた総流量が常に一定となるように制御して、希釈された排ガス(以下、「希釈排ガス」という。)の一部を一定流量で採取バッグに採取する定容量サンプリング装置2と、大気中の不純物を除去して精製された希釈用空気を前記定容量サンプリング装置2に供給する希釈用空気精製装置3と、前記定容量サンプリング装置2の採取バッグにより採取された希釈排ガス中の所定成分(例えば、HC、COなど)の濃度を分析するガス分析計4と、を備えている。   Specifically, as shown in FIG. 1, the exhaust gas is diluted with exhaust gas (hereinafter referred to as “diluted exhaust gas”) by introducing a total amount of exhaust gas and dilution air into the apparatus and controlling the combined total flow rate to be always constant. , "Diluted exhaust gas") is supplied to the constant volume sampling device 2 with a constant volume sampling device 2 that collects a part of the exhaust gas in a collection bag at a constant flow rate, and dilution air purified by removing impurities in the atmosphere. And a gas analyzer 4 for analyzing the concentration of a predetermined component (for example, HC, CO, etc.) in the diluted exhaust gas collected by the collection bag of the constant volume sampling device 2. Yes.

定容量サンプリング装置2は、シャシダイナモ300に乗載された自動車200の排気管200Hに接続されるとともに、希釈用空気精製装置3の希釈用空気供給管3Hが導入接続された排ガス導入ライン21と、排ガス導入ライン21の下流に設けられ、排ガス及び希釈用空気を攪拌混合させるサイクロン22と、当該サイクロン22により攪拌混合された希釈排ガスを一定流量で流す定流量機構231を有する希釈排ガス流通ライン23と、この希釈排ガス流通ライン23から希釈された排ガスを分取するための希釈排ガス採取ライン24と、希釈用空気精製装置3の希釈用空気供給管3Hから希釈用空気を分取するための希釈用空気採取ライン25と、を備えている。   The constant volume sampling device 2 is connected to the exhaust pipe 200H of the automobile 200 mounted on the chassis dynamo 300, and the exhaust gas introduction line 21 to which the dilution air supply pipe 3H of the dilution air purification device 3 is introduced and connected. The diluted exhaust gas distribution line 23 provided downstream of the exhaust gas introduction line 21 and having a constant flow mechanism 231 for flowing the diluted exhaust gas stirred and mixed by the cyclone 22 at a constant flow rate. The dilution exhaust gas collecting line 24 for separating the diluted exhaust gas from the diluted exhaust gas distribution line 23 and the dilution for separating the dilution air from the dilution air supply pipe 3H of the dilution air purifier 3 Air sampling line 25.

定流量機構231は、希釈排ガス流通ライン23上に設けられたベンチュリ管231aと当該ベンチュリ管231aの下流に設けられたターボブロア231bとから構成される。   The constant flow rate mechanism 231 includes a venturi pipe 231a provided on the diluted exhaust gas distribution line 23 and a turbo blower 231b provided downstream of the venturi pipe 231a.

希釈排ガス採取ライン24は、一端が希釈排ガス流通ライン23内に設けられた希釈排ガス採取管241と、この希釈排ガス採取管241上に設けられた希釈排ガス採取ポンプ242と、この希釈排ガス採取ポンプ242により採取された希釈排ガスを収納する希釈排ガスバッグ243とを備えている。なお、希釈排ガス採取管241は、定流量機構231よりも上流側に設けられている。   The diluted exhaust gas collection line 24 has one end provided in the diluted exhaust gas distribution line 23, a diluted exhaust gas collection pipe 241 provided on the diluted exhaust gas collection pipe 241, and the diluted exhaust gas collection pump 242. And a diluted exhaust gas bag 243 for storing the diluted exhaust gas collected by the above. The diluted exhaust gas sampling pipe 241 is provided on the upstream side of the constant flow rate mechanism 231.

また、希釈用空気採取ライン25は、一端が希釈用空気供給管3H内に設けられた希釈用空気採取管251と、この希釈用空気採取管251上に設けられた希釈用空気採取ポンプ252と、この希釈用空気採取ポンプ252により採取された希釈用空気を収納する希釈用空気バッグ253とを備えている。   The dilution air sampling line 25 has a dilution air sampling pipe 251 provided at one end in the dilution air supply pipe 3H, and a dilution air sampling pump 252 provided on the dilution air sampling pipe 251. And a dilution air bag 253 for storing the dilution air collected by the dilution air sampling pump 252.

そして、希釈排ガス採取ライン24の希釈排ガスバッグ243及び希釈用空気採取ライン25の希釈用空気バッグ253を用いてガス分析計4によりいわゆるバッグ測定が行われる。   Then, so-called bag measurement is performed by the gas analyzer 4 using the diluted exhaust gas bag 243 of the diluted exhaust gas sampling line 24 and the diluted air bag 253 of the dilution air sampling line 25.

希釈用空気精製装置3は、排ガス分析におけるバックグラウンドの低濃度安定化を図るために、希釈用空気中のCO、HC、NO等を除去するものである。この希釈用空気精製装置3において、CO、HC、NOを除去する方法としては、希釈用空気中のCO、HC、NOをCOとHOとNOに変換する触媒酸化法を採用し、また、NOが酸化されて生じたNOをNO吸着剤を用いて吸着処理するものである。また、NO吸着剤にも酸化剤が含まれており、未変換のNOをNOに酸化させて吸着処理する。 The dilution air purifying apparatus 3 removes CO, HC, NO x and the like in the dilution air in order to stabilize the low concentration of the background in the exhaust gas analysis. In this dilution air purifier 3, CO, HC, as a method for removing NO is, CO in the diluted air, HC, the catalytic oxidation method to convert the NO to CO 2 and H 2 O and NO 2 adopted In addition, NO 2 produced by oxidation of NO is adsorbed using a NO X adsorbent. Further, the NO X adsorbent also contains an oxidant, and the unconverted NO is oxidized to NO X and adsorbed.

希釈用空気精製装置3の具体的な構成としては、図2に示すように、吸気フィルタ31を介して外部から希釈用空気を装置内部に導入する吸引ポンプ32と、当該吸引ポンプ32により導入された希釈用空気を約400度に加熱する加熱器33と、当該加熱器33により加熱された希釈用空気中のHC、COを燃焼させるPt、Pd系又はCu、Mn系を用いた触媒部34と、当該触媒部34及びその下流に設けられた熱交換器35及び三方電磁弁36を通過した希釈用空気を冷却する冷却器37と、当該冷却器37により例えば25度に冷却された希釈用空気中のNOを吸着除去するNO吸着器38と、を備えている。そして、NO吸着器38を通過した希釈用空気が希釈用空気供給管3Hにより定容量サンプリング装置2に供給される。 As shown in FIG. 2, the specific configuration of the dilution air purifying device 3 includes a suction pump 32 that introduces dilution air from the outside through the intake filter 31 and the suction pump 32. The heater 33 for heating the diluted air to about 400 degrees, and the catalyst unit 34 using Pt, Pd system or Cu, Mn system for burning HC and CO in the dilution air heated by the heater 33 A cooling unit 37 that cools the dilution air that has passed through the catalyst unit 34 and the heat exchanger 35 and the three-way solenoid valve 36 that are provided downstream of the catalyst unit 34, and a dilution unit that is cooled to, for example, 25 degrees by the cooling unit 37. And an NO X adsorber 38 that adsorbs and removes NO 2 in the air. The dilution air that has passed through the NO X adsorber 38 is supplied to the constant volume sampling device 2 through the dilution air supply pipe 3H.

しかして、本実施形態のガス分析計4は、希釈排ガス中のNO成分の濃度を分析するものであり、希釈用空気精製装置3は、希釈用空気中のNOを除去するNO除去部3Aを備えている。このNO除去部3Aは、NOを還元又は酸化によりN又はNOに変換するNO触媒部と、当該NO触媒部によって生じるNOを除去するNO除去部と、からなる。 Therefore, the gas analyzer 4 of the present embodiment analyzes the concentration of the N 2 O component in the diluted exhaust gas, and the dilution air purifier 3 removes N 2 O in the dilution air. 2 O removal part 3A is provided. The N 2 O removal section 3A, and N 2 O catalyst unit for converting the N 2 or NO X by reduction or oxidation of N 2 O, and NO X removal unit for removing the NO X produced by the N 2 O catalytic unit It consists of.

O触媒部は、前記の触媒部34に含まれており、例えばPtやPdをゼオライトに担持して構成されている。また、NO除去部3Aを構成するNO除去部は、前記のNO吸着器38を用いて構成される。 The N 2 O catalyst portion is included in the catalyst portion 34, and is configured by, for example, supporting Pt or Pd on zeolite. Further, the NO X removing unit constituting the N 2 O removing unit 3A is configured by using the NO X adsorber 38.

次に、このように構成した排ガスサンプリング分析システム100を用いたNOの濃度測定について図3を参照して説明する。 Next, N 2 O concentration measurement using the thus configured exhaust gas sampling analysis system 100 will be described with reference to FIG.

希釈用空気精製装置3にNO除去部3Aが無い場合、希釈用空気バッグ253により得られた希釈用空気中のNO濃度は約300[ppb](大気中に含まれるNO濃度の平均値)である。このとき希釈排ガスバッグ243により得られる希釈排ガス中のNO濃度が約560[ppb]であるとすると、バックグラウンド補正の結果、排ガス中に含まれるNO濃度は、約260[ppb]となる。しかしながら、希釈排ガス中のNO濃度に対する希釈用空気中のNO濃度の割合が大きく、希釈用空気中のNO濃度の測定誤差が排ガス中のNO濃度に与える影響が大きくなってしまい、その結果、バックグラウンド補正により得られた排ガス中のNO濃度の測定精度が低下してしまう。 When the dilution air purifier 3 does not have the N 2 O removing unit 3A, the N 2 O concentration in the dilution air obtained by the dilution air bag 253 is about 300 [ppb] (N 2 O contained in the atmosphere). Density average value). When N 2 O concentration in the dilution in the exhaust gas obtained by diluting the exhaust gas bag 243 at this time it is assumed to be approximately 560 [ppb], the results of background correction, N 2 O concentration in the exhaust gas, about 260 [ppb] It becomes. However, large proportions of N 2 O concentration in the dilution air for N 2 O concentration in the diluted exhaust gas is greatly affected the measurement error of the N 2 O concentration in the dilution air is applied to the N 2 O concentration in the exhaust gas As a result, the measurement accuracy of the N 2 O concentration in the exhaust gas obtained by the background correction is lowered.

一方で、本実施形態のようにNO除去部3Aを設けることによって、希釈用空気バッグ253により得られた希釈用空気中のNO濃度が例えば約30[ppb]に低減されると、希釈排ガスバッグ243により得られる希釈排ガス中のNO濃度が約290[ppb]となり、バックグラウンド補正の結果、排ガス中に含まれるNO濃度は、約260[ppb]となる。このとき、希釈排ガス中のNO濃度に対する希釈用空気中のNO濃度の割合を小さくすることができ、希釈用空気中のNO濃度の測定誤差が排ガス中のNO濃度に与える影響を小さくすることができ、その結果、バックグラウンド補正により得られた排ガス中のNO濃度の測定精度を向上させることができる。 On the other hand, when the N 2 O removing unit 3A is provided as in the present embodiment, the N 2 O concentration in the dilution air obtained by the dilution air bag 253 is reduced to, for example, about 30 [ppb]. The N 2 O concentration in the diluted exhaust gas obtained by the diluted exhaust gas bag 243 is about 290 [ppb], and as a result of background correction, the N 2 O concentration contained in the exhaust gas is about 260 [ppb]. At this time, N 2 O concentration ratio can be reduced in, N 2 O concentration of the measurement error in the exhaust gas of the N 2 O concentration in the dilution air dilution air for N 2 O concentration in the diluted exhaust gas As a result, the measurement accuracy of the N 2 O concentration in the exhaust gas obtained by background correction can be improved.

このように構成した本実施形態に係る排ガスサンプリング分析システム100によれば、排ガスを希釈用空気で希釈させる前に、当該希釈用空気からNOを除去させることによって、希釈排ガス中のNO濃度に対する希釈用空気のNO濃度の割合を可及的に小さくすることができ、NO濃度のバックグラウンド変動を小さくして、排ガス中のNO濃度の測定精度を向上することができる。 According to the exhaust gas sampling analysis system 100 of the present embodiment configured as described above, prior to diluting the exhaust gas with dilution air, by removal of N 2 O from the dilution air, in the diluted exhaust gas N 2 the ratio of N 2 O concentration in the dilution air to O concentration as much as possible can be made small, to reduce the background variation of the N 2 O concentration, to improve the measurement accuracy of the N 2 O concentration in the exhaust gas be able to.

なお、本発明は前記実施形態に限られるものではない。
例えば、前記実施形態では、定容量サンプリング装置を用いているが、その他、排ガスの一部を採取して一定比率で希釈する、バックミニダイリュータ装置を用いても良い。
その他、本発明は前記実施形態に限られず、その趣旨を逸脱しない範囲で種々の変形が可能であるのは言うまでもない。
The present invention is not limited to the above embodiment.
For example, the constant volume sampling device is used in the embodiment, but a back mini-diluter device that collects a part of the exhaust gas and dilutes it at a constant ratio may be used.
In addition, it goes without saying that the present invention is not limited to the above-described embodiment, and various modifications can be made without departing from the spirit of the present invention.

100・・・排ガスサンプリング測定システム
2 ・・・定容量サンプリング装置
3 ・・・希釈用空気精製装置
3A ・・・NO除去部
33 ・・・加熱器
34 ・・・触媒部
38 ・・・NO除去部
100 ... exhaust gas sampling measurement system 2 ... constant volume sampling device 3 ... dilution air purifier 3A ... N 2 O removal unit 33 ... heater 34 ... catalyst 38 ... NO X removal section

Claims (1)

エンジン排ガスを希釈用空気によって希釈し、その希釈排ガス中に含まれる成分を測定する排ガスサンプリング分析システムに用いられる希釈用空気精製装置であって、
大気から採取した希釈用空気を加熱する加熱器と、
前記加熱器により加熱された希釈用空気に含まれるNOをN又はNOに変換するNO触媒部と、
前記NO触媒部の下流に設けられ、前記希釈用空気に含まれるNOを除去するNO除去部と、を備える希釈用空気精製装置。
An air purification device for dilution used in an exhaust gas sampling analysis system for diluting engine exhaust gas with dilution air and measuring components contained in the diluted exhaust gas,
A heater for heating dilution air collected from the atmosphere;
An N 2 O catalyst unit for converting N 2 O contained in the dilution air heated by the heater into N 2 or NO X ;
A dilution air purification apparatus, comprising: a NO X removal section that is provided downstream of the N 2 O catalyst section and removes NO X contained in the dilution air.
JP2009252365A 2009-11-02 2009-11-02 Dilution air refining device Pending JP2011095229A (en)

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JPS637826A (en) * 1986-06-30 1988-01-13 Ebara Res Co Ltd Removing method for nitrous oxide in gas mixture
JPH063232A (en) * 1992-06-20 1994-01-11 Horiba Ltd Overflow supervision monitoring method for diluent air fed from diluent air purifier and constant volume sampling device with its monitoring function
JPH08323143A (en) * 1995-06-06 1996-12-10 Dainippon Ink & Chem Inc How to remove nitrous oxide
JPH1019744A (en) * 1996-07-09 1998-01-23 Mitsubishi Motors Corp Exhaust gas measurement device
WO1999025461A1 (en) * 1997-11-18 1999-05-27 Asahi Kasei Kogyo Kabushiki Kaisha Method and device for global warming prevention
JPH11230871A (en) * 1998-02-09 1999-08-27 Tsukasa Sokken:Kk Exhaust gas dilution sampling apparatus
JPH11344425A (en) * 1998-06-02 1999-12-14 Horiba Ltd Device for analyzing exhaust gas of internal combustion engine using gas trace method
JP2001165827A (en) * 1999-12-06 2001-06-22 Horiba Ltd Exhaust gas analysis system
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS637826A (en) * 1986-06-30 1988-01-13 Ebara Res Co Ltd Removing method for nitrous oxide in gas mixture
JPH063232A (en) * 1992-06-20 1994-01-11 Horiba Ltd Overflow supervision monitoring method for diluent air fed from diluent air purifier and constant volume sampling device with its monitoring function
JPH08323143A (en) * 1995-06-06 1996-12-10 Dainippon Ink & Chem Inc How to remove nitrous oxide
JPH1019744A (en) * 1996-07-09 1998-01-23 Mitsubishi Motors Corp Exhaust gas measurement device
WO1999025461A1 (en) * 1997-11-18 1999-05-27 Asahi Kasei Kogyo Kabushiki Kaisha Method and device for global warming prevention
JPH11230871A (en) * 1998-02-09 1999-08-27 Tsukasa Sokken:Kk Exhaust gas dilution sampling apparatus
JPH11344425A (en) * 1998-06-02 1999-12-14 Horiba Ltd Device for analyzing exhaust gas of internal combustion engine using gas trace method
JP2001165827A (en) * 1999-12-06 2001-06-22 Horiba Ltd Exhaust gas analysis system
JP2005062056A (en) * 2003-08-18 2005-03-10 Horiba Ltd Measuring device of exhaust gas flow rate and exhaust gas measuring system using the same

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