JP2003083949A - System for measuring floating substance in fine particle shape for ship, and exhaust gas dilution equipment - Google Patents

System for measuring floating substance in fine particle shape for ship, and exhaust gas dilution equipment

Info

Publication number
JP2003083949A
JP2003083949A JP2001273332A JP2001273332A JP2003083949A JP 2003083949 A JP2003083949 A JP 2003083949A JP 2001273332 A JP2001273332 A JP 2001273332A JP 2001273332 A JP2001273332 A JP 2001273332A JP 2003083949 A JP2003083949 A JP 2003083949A
Authority
JP
Japan
Prior art keywords
exhaust gas
dilution
carbon dioxide
measuring
particulate matter
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP2001273332A
Other languages
Japanese (ja)
Other versions
JP3709434B2 (en
Inventor
Atsuto Ohashi
厚人 大橋
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
National Maritime Research Institute
Original Assignee
National Maritime Research Institute
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by National Maritime Research Institute filed Critical National Maritime Research Institute
Priority to JP2001273332A priority Critical patent/JP3709434B2/en
Publication of JP2003083949A publication Critical patent/JP2003083949A/en
Application granted granted Critical
Publication of JP3709434B2 publication Critical patent/JP3709434B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • 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

Landscapes

  • Analysing Materials By The Use Of Radiation (AREA)
  • Sampling And Sample Adjustment (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a measurement system of a floating substance in a fine particle shape for ships that can measure the floating substance in a fine particle shape in an exhaust gas easily even on a ship that oscillates conforming to the regulation of the International Standardization Organization. SOLUTION: The system comprises a dilution air supply apparatus 3 having a dry cleaning apparatus 31 and an amount-of-supply adjustment valve 32, exhaust gas dilution equipment 4 for mixing clean air that is transmitted from the dilution air supply apparatus 3 and the exhaust gas in an engine, a carbon gas-measuring instrument 10 for measuring a carbon dioxide gas contained in the exhaust gas in the engine or a diluted exhaust gas that is transmitted from the exhaust gas dilution equipment 4 via a switching cock 8 and a pretreating apparatus 9, and a beta ray absorption type floating fine particle-like substance measuring instrument 5 for measuring floating substances in a fine particle shape in the diluted exhaust gas that is transmitted from the exhaust gas dilution equipment 4. A dilution coefficient is obtained from the carbon dioxide gas measurement value of the exhaust gas of the engine and the diluted exhaust gas by the carbon dioxide gas-measuring instrument 10, and the amount of transmission of clean air in the dilution air supply apparatus 3 is adjusted so that the dilution coefficient becomes an appropriate one.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、船舶エンジンの排
ガス中の浮遊性微粒子状物質の測定システムと、その測
定システムに用いる排ガス希釈器に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a measuring system for airborne particulate matter in exhaust gas of a marine engine and an exhaust gas diluter used in the measuring system.

【0002】[0002]

【従来の技術】浮遊性微粒子状物質は地球環境あるいは
人体に悪影響を及ぼすものとされている。船舶は、その
多くがディーゼル機関で運行されており、しかも浮遊性
微粒子状物質の発生が多いといわれる低質燃料が使用さ
れる場合が多いが、その排出実態は明らかにされていな
い。これは船舶での計測に適合した計測機器の開発がな
されていないことが要因の一つである。
2. Description of the Related Art Floating particulate matter is said to adversely affect the global environment or the human body. Most of the ships are operated by diesel engines, and low-quality fuel, which is said to generate a lot of airborne particulate matter, is used in many cases, but their actual emissions have not been clarified. This is partly due to the fact that measuring instruments suitable for measurement on ships have not been developed.

【0003】船舶上で浮遊性微粒子状物質を測定した例
は少ないが、国際標準化機構の規定に沿ったダイリュー
ショントンネルを船舶に搭載して測定した例、あるいは
エゼクタ式希釈器とフィルタ振動式浮遊性微粒子状物質
測定器を組み合わせた船舶粒子濃度自動計測システムを
搭載して測定した例がある。
There are few examples of measurement of airborne particulate matter on a ship, but an example of measurement by mounting a dilution tunnel in accordance with the regulations of the International Organization for Standardization on a ship, or an ejector type diluter and filter vibration type. There is an example of measurement by mounting an automatic measurement system for ship particle concentration, which is a combination of measuring instruments for airborne particulate matter.

【0004】しかし、ダイリューショントンネルによる
浮遊性微粒子状物質の測定は、陸上用の機関を想定して
いるため、船舶に搭載して計測するには装置が大掛かり
であり、搬入搬出あるいは設置場所で制約を受ける。ま
た、浮遊性微粒子状物質の捕集に使用されるフィルタの
使用前後に恒温恒湿器で一定の温度と湿度を保った後、
精密天秤で秤量する必要があるため、船舶上では計測結
果を瞬時に求めることができない。
However, since the measurement of airborne particulate matter by a dilution tunnel is presumed to be a land-based engine, it requires a large-scale device to be mounted on a vessel for measurement, and the loading / unloading or installation location. Be restricted by. In addition, after maintaining a constant temperature and humidity with a thermo-hygrostat before and after using the filter used to collect airborne particulate matter,
Since it is necessary to weigh with a precision balance, the measurement result cannot be instantaneously obtained on the ship.

【0005】また、エゼクタ式希釈器とフィルタ振動方
式浮遊性微粒子状物質測定器を組み合わせた船舶粒子濃
度自動計測システムは、コンパクトで搬入搬出あるいは
設置場所で有利である。その上、測定結果を瞬時に指示
するため、浮遊性微粒子状物質の排出状態の経過を把握
する上で有利である。
An automatic particle concentration measuring system for ships, which is a combination of an ejector diluter and a filter vibration type floating particulate matter measuring instrument, is compact and is advantageous at the loading / unloading or installation site. In addition, the measurement result is instantly indicated, which is advantageous for grasping the progress of the discharge state of the airborne particulate matter.

【0006】しかし、フィルタ振動式浮遊性微粒子状物
質測定器では、捕集フィルタに取付けたテーパエレメン
トの固有振動数が浮遊性微粒子状物質の捕集により変化
することを利用してその重量を求めるものであるため、
指示値は船体の動揺の影響を大きく受けるので、動揺を
伴なう場合の計測は不可能である。
However, in the filter vibration type floating particulate matter measuring device, the weight is obtained by utilizing the fact that the natural frequency of the taper element attached to the collection filter changes due to the collection of the floating particulate matter. Because it is
Since the indicated value is greatly affected by the shaking of the hull, it is impossible to measure it when shaking is involved.

【0007】また、船舶粒子濃度自動計測システムのエ
ゼクタ式希釈器は、エゼクタノズルの管径を小さくする
ことにより、常温常圧下で、ある範囲の希釈空気流用で
あることを条件に希釈係数が一定になるように造られて
いる。しかし、ディーゼル機関の排ガスは、上記条件と
異なる時に管径の細いエゼクタノズル内に多くの浮遊性
微粒子状物質の沈殿をもたらし、正確な計測ができない
という欠点がある。
Further, the ejector type diluter of the ship particle automatic concentration measuring system has a constant diluting coefficient under the condition that it is used for a certain range of diluting air flow under normal temperature and pressure by reducing the diameter of the ejector nozzle. Is designed to be. However, the exhaust gas of a diesel engine has a drawback in that, when the conditions are different from those described above, a large amount of airborne particulate matter is precipitated in the ejector nozzle having a small pipe diameter, and accurate measurement cannot be performed.

【0008】更に国際標準化機構の規定では排ガスと同
じ速度で吸引する等速吸引を行うことが定められている
が、船舶粒子濃度自動計測システムのエゼクタ式希釈器
ではディーゼル機関の排気管を流れる排ガスを吸引する
場合、その能力が足りず国際標準化機構の規定である等
速吸引が行えない。
Further, the International Organization for Standardization stipulates that the suction is performed at the same speed as the exhaust gas, but in the ejector diluter of the ship particle automatic concentration measurement system, the exhaust gas flowing through the exhaust pipe of the diesel engine is When suctioning, the ability is not sufficient to perform constant-speed suction as defined by the International Organization for Standardization.

【0009】[0009]

【発明が解決しようとする課題】そこで本発明は、動揺
を伴なう船舶上でも手軽に排ガス中の浮遊性微粒子状物
質を国際標準化機構の規定に準じた測定ができる船舶用
浮遊性微粒子状物質測定システムとそのシステムの実施
に有用な排ガス希釈器を提供することを課題とするもの
である。
SUMMARY OF THE INVENTION Therefore, the present invention is capable of easily measuring the floating particulate matter in the exhaust gas according to the provisions of the International Organization for Standardization even on a ship accompanied by shaking. An object of the present invention is to provide a substance measurement system and an exhaust gas diluter useful for implementing the system.

【0010】[0010]

【課題を解決するための手段】本発明は、上記の課題を
解決するためになされたもので、第1の発明はドライク
リーニング装置と供給量調整装置を備えた希釈空気供給
装置と、この希釈空気供給装置から送出される清浄空気
とエンジンの排ガスを混合する排ガス希釈器と、前記エ
ンジンの排ガス又は前記排ガス希釈器から送出される希
釈排ガス中に含まれる炭酸ガスを切替コックと前処理装
置を介して測定する炭酸ガス測定器と、前記排ガス希釈
器から送出される希釈排ガス中の浮遊性微粒子状物質を
測定するベータ線吸収式浮遊性微粒子状物質測定器とを
備え、前記炭酸ガス測定器によって測定したエンジンの
排ガスと希釈排ガスの炭酸ガス測定値から、希釈係数を
求め、その希釈係数が適正希釈係数となるように前記希
釈空気供給装置の清浄空気送出量を調整することを特徴
とする船舶用浮遊性微粒子状物質測定システムである。
SUMMARY OF THE INVENTION The present invention has been made to solve the above-mentioned problems. The first invention is a dilution air supply device having a dry cleaning device and a supply amount adjusting device, and this dilution air supply device. An exhaust gas diluter that mixes clean air sent from the air supply device and engine exhaust gas, a carbon dioxide gas contained in the exhaust gas of the engine or the diluted exhaust gas sent from the exhaust gas diluter, and a switching cock and a pretreatment device. A carbon dioxide gas measuring device for measuring via a carbon dioxide gas measuring device, and a beta ray absorption type floating fine particle measuring device for measuring floating fine particles in the diluted exhaust gas sent from the exhaust gas diluter. From the measured values of carbon dioxide gas of the engine exhaust gas and diluted exhaust gas measured by, the dilution coefficient is obtained, and the dilution air supply device is adjusted so that the dilution coefficient becomes an appropriate dilution coefficient. A floating particulate matter measurement system for vessels, which comprises adjusting the purification air delivery quantity.

【0011】第2の発明は第1の発明の実施に有用な排
ガス希釈器であって、混合チャンバーを備えた本体の一
端に、周囲数ヶ所から排ガス流入路へその噴出口側に向
って斜に清浄空気を噴出するノズルを備えたエヤガンを
設け、反対側に混合チャンバー内に向って分離管を突出
させた出口ノズルを設け、その分離管の側方の本体に炭
酸ガス測定用採取口と、オーバーフロー排出口を設けた
ことを特徴とする排ガス希釈器である。
A second aspect of the present invention is an exhaust gas diluter useful for carrying out the first aspect of the present invention, in which one end of a main body provided with a mixing chamber is inclined from several places around the exhaust gas inflow path toward the jet outlet side thereof. An air gun equipped with a nozzle for ejecting clean air is installed on the opposite side, and an outlet nozzle is provided on the opposite side with the separation tube protruding toward the inside of the mixing chamber. An exhaust gas diluter having an overflow discharge port.

【0012】第1の発明の船舶用浮遊微粒子状物質測定
システムは、船舶上でディーゼル機関の排気管を流れる
排ガスを採取し、排ガス中の浮遊微粒子状物質を計測す
ることを目的とするものであり、測定器としては大気中
の浮遊微粒子物質(ダスト)を測定するために用いられ
ているベータ線吸収式浮遊性微粒子物質測定器を選定し
使用した。この測定器の主要部は浮遊微粒子状物質捕集
機構、ろ紙供給機構、ベータ線源及び検出部並びに演算
制御器からなり、これらは計測中はいずれも固定され、
また、可動部もなく、動揺の影響を受け難いものであ
る。しかもフィルタ振動式浮遊微粒子状物質測定器と同
程度の大きさで搬入搬出及び設置場所の選定が容易であ
る。また、ベータ線吸収式浮遊微粒子状物質測定器は連
続測定が可能であるので、これをシステムの構成要素と
した。
The floating particulate matter measuring system for a ship according to the first aspect of the invention is intended to collect the exhaust gas flowing through the exhaust pipe of a diesel engine on a ship and measure the floating particulate matter in the exhaust gas. As a measuring instrument, a beta ray absorption type floating particulate matter measuring instrument used for measuring airborne particulate matter (dust) was selected and used. The main part of this measuring instrument consists of a suspended particulate matter trapping mechanism, a filter paper feeding mechanism, a beta ray source and detector, and an arithmetic controller, all of which are fixed during measurement.
Moreover, since there are no movable parts, it is not easily affected by shaking. Moreover, the size of the filter vibrating particulate matter measuring device is comparable to that of the filter vibrating type particulate matter measuring device, and it is easy to carry in / out and select the installation place. In addition, the beta ray absorption type suspended particulate matter measuring device is capable of continuous measurement, so this was made a component of the system.

【0013】しかし乍ら、このベータ線吸収式浮遊性微
粒子状物質測定器は、大気中のダストを測定するもので
あるから船舶用エンジンの排気ガス用としてはそのまヽ
使用することは出来ない。
However, since this beta ray absorption type buoyant particulate matter measuring instrument measures dust in the atmosphere, it cannot be used as it is for exhaust gas of a marine engine. .

【0014】船舶用エンジンの排気ガス用とする場合
は、排気ガスが大気中に拡散した状態、つまり希釈され
た状態のものを測定するようにしなければならない。そ
のため本発明計測システムでは、排ガス希釈器を用いる
ことにした。
When the exhaust gas of a marine engine is used, it is necessary to measure the exhaust gas in a diffused state in the atmosphere, that is, in a diluted state. Therefore, the exhaust gas diluter is used in the measurement system of the present invention.

【0015】しかし乍ら、排ガス希釈器として公知のエ
ゼクタ式希釈器を用いた場合、ディーゼル機関の排気管
内の排ガス圧力が負荷状態により変化するので、それに
伴いエゼクタ式希釈器の希釈係数が変わるという問題が
生じる。そこで本発明ではこの問題に対しディーゼル機
関の排ガス中の炭酸ガス濃度xを測定すると共に、エゼ
クタ式希釈器の胴に炭酸ガス測定用採取口を新たに設
け、希釈された排ガス中の炭酸ガス濃度x’を測定し、
この両者の炭酸ガス濃度から計算により希釈係数x/
x’を求め、その希釈係数が適正値(規則により4以上
とされている)となるように希釈空気の供給量を設定す
ることにより問題を解決したものである。
However, when a known ejector type diluter is used as the exhaust gas diluter, the exhaust gas pressure in the exhaust pipe of the diesel engine changes depending on the load state, and accordingly, the dilution coefficient of the ejector diluter changes. The problem arises. Therefore, in the present invention, in order to solve this problem, the present invention measures the carbon dioxide concentration x in the exhaust gas of a diesel engine, and additionally provides a sampling port for measuring carbon dioxide in the body of the ejector diluter to measure the carbon dioxide concentration in the diluted exhaust gas. x'is measured,
Dilution coefficient x /
The problem is solved by finding x ′ and setting the supply amount of the dilution air so that the dilution coefficient becomes an appropriate value (set to 4 or more according to the rule).

【0016】また、デイーゼル機関の排気管内を流れる
排ガス速度に対し、エゼクタ式希釈器では能力が足りず
等速吸引ができないという問題に対して、本発明ではエ
ヤガン式排ガス希釈器を開発し使用した。
Further, with respect to the speed of the exhaust gas flowing through the exhaust pipe of the diesel engine, the problem that the ejector type diluter does not have sufficient capacity to perform constant velocity suction, and in the present invention, the air gun type exhaust gas diluter was developed and used. .

【0017】この排ガス希釈器の胴はエゼクタ式希釈器
の同じ大きさのものであり、胴の一端に市販のこのエヤ
ガンを装着したものである。このエヤガンは本来、粉
体、粒体、煙等の清掃、移送あるいは噴射に使用するも
のである。
The cylinder of this exhaust gas diluter is the same size as the ejector diluter, and one end of the cylinder is equipped with this commercially available air gun. This air gun is originally used for cleaning, transporting or spraying powder, particles, smoke and the like.

【0018】従って、ディーゼル機関の排ガス速度に適
合した吸引能力をもつエヤガンを使用すれば容易に等速
吸引が可能になり、さらに排ガスの流量調整は希釈空気
供給装置から送出される清浄空気量を調節して変化させ
れば、吸引する排ガス量が加減でき等速吸引することが
できることになる。
Therefore, if an air gun having a suction capacity adapted to the exhaust gas velocity of the diesel engine is used, uniform velocity suction can be easily performed, and the flow rate of the exhaust gas can be adjusted by adjusting the amount of clean air sent from the dilution air supply device. By adjusting and changing the amount, the amount of exhaust gas to be sucked can be adjusted, and it is possible to suck at a constant speed.

【0019】また、最小内径が他の配管とくらべて大き
いので浮遊微粒子状物質の沈着が少ない。これにより希
釈係数は変化するが、前述のように炭酸ガス濃度から希
釈係数を求めるため、補正は容易である。
Further, since the minimum inner diameter is larger than that of other pipes, the deposition of suspended particulate matter is small. Although the dilution coefficient changes due to this, the correction is easy because the dilution coefficient is obtained from the carbon dioxide gas concentration as described above.

【0020】[0020]

【発明の実施の形態】図1は、本発明の実施例の全体の
構成を示すブロック図で、1はディーゼル機関の排気
管、2は浮遊性微粒子状物質用の測定用プローブ、3は
ドライクリーニングユニット31とバルブ32(供給量
調整装置)とを備えた希釈空気供給装置である。
1 is a block diagram showing the overall construction of an embodiment of the present invention. 1 is an exhaust pipe of a diesel engine, 2 is a measurement probe for buoyant particulate matter, and 3 is a dry probe. The dilution air supply device includes a cleaning unit 31 and a valve 32 (supply amount adjusting device).

【0021】4は排ガス希釈器、5は浮遊微粒子状物質
捕集機構、ろ紙供給機構、ベータ線源及び検出部並びに
演算制御器から成るベータ線吸収式浮遊性微粒子状物質
測定器、6は前記演算制御器によって制御される吸引ポ
ンプ、7は炭酸ガス測定用のプローブ、8は切換コッ
ク、9は前処理装置、10は炭酸ガス測定器である。
Reference numeral 4 is an exhaust gas diluter, 5 is a beta-ray absorption type floating particulate matter measuring instrument comprising a suspended particulate matter trapping mechanism, a filter paper supply mechanism, a beta ray source and a detector, and an arithmetic controller, and 6 is the above-mentioned. A suction pump controlled by an arithmetic controller, 7 is a probe for measuring carbon dioxide gas, 8 is a switching cock, 9 is a pretreatment device, and 10 is a carbon dioxide measuring device.

【0022】図2は排ガス希釈器4の詳細図で、本体4
1の胴内には混合チャンバー42とこの混合チャンバー
42と連通する分離チャンバー43が設けられていて、
本体41の上端にはエヤガン11が取付けられている。
FIG. 2 is a detailed view of the exhaust gas diluter 4, which shows the main body 4
A mixing chamber 42 and a separation chamber 43 communicating with the mixing chamber 42 are provided in the body of No. 1.
The air gun 11 is attached to the upper end of the main body 41.

【0023】排気管1から取り出した排ガスは、エヤガ
ン11の吸引口11aから吸引され噴射口11bから混
合チャンバー42内へ噴出する。そして、希釈空気供給
装置3から供給された清浄空気はエヤガン11の吸気口
11cを通り、噴射口11b方向に斜に設けた4つのノ
ズルN1,N2,N3,N4(図示せず)から軸心に向
って噴出し、噴射口11bより混合チャンバー42内に
噴射され、排ガスと混合して、排ガスを希釈する。
The exhaust gas taken out from the exhaust pipe 1 is sucked from the suction port 11a of the air gun 11 and jetted into the mixing chamber 42 from the jet port 11b. Then, the clean air supplied from the dilution air supply device 3 passes through the intake port 11c of the air gun 11 and the axial center from four nozzles N1, N2, N3, N4 (not shown) obliquely provided in the injection port 11b direction. Toward the interior of the mixing chamber 42 and is mixed with the exhaust gas to dilute the exhaust gas.

【0024】本体41の下端には、混合チャンバー42
と連通する分離チャンバー42内に分離管44を突出さ
せた出口ノズル45が設けられ、この分離管44の側方
の本体41には炭酸ガス測定用採取口46とオーバフロ
ー排出口47が設けられてる。
At the lower end of the body 41, a mixing chamber 42
An outlet nozzle 45 having a separation pipe 44 protruding is provided in a separation chamber 42 communicating with the separation chamber 42, and a main body 41 on the side of the separation pipe 44 is provided with a carbon dioxide gas measurement collection port 46 and an overflow discharge port 47. .

【0025】このように構成したのは、水滴などを含ま
ない測定用希釈排ガスを出口ノズル45から排出させる
ためと、オーバフロー排出口47から希釈排気ガスの残
部を大気中に放出して分離チャンバー42内を大気圧と
し、出口ノズル45から取り出される希釈排ガスが、ベ
ータ線吸収式浮遊性微粒子状物質測定器5によって測定
可能とするためである。
The above-described structure is used for discharging the measurement diluted exhaust gas containing no water droplets from the outlet nozzle 45, and for discharging the remainder of the diluted exhaust gas into the atmosphere from the overflow outlet 47. This is because the inside is set to the atmospheric pressure and the diluted exhaust gas taken out from the outlet nozzle 45 can be measured by the beta ray absorption type floating particulate matter measuring device 5.

【0026】実施例に示した船舶用浮遊性微粒子状物質
測定システム全体の作用は、ディーゼル機関の排気管1
に取り付けた浮遊性徴粒子状物質測定用プローブ2から
排ガスの一部が排ガス稀釈器4へと導かれると、排ガス
稀釈器4で排ガスは清浄空気によって稀釈される。そし
て、この稀釈された排ガスは、排ガス稀釈器4の本体4
1の胴部に設けられた出口ノズル45からベータ線吸収
式浮遊性微粒子状物質測定器5に導かれ、ここで稀釈さ
れた排ガス中の浮遊粒子状物質の濃度が測定され、測定
に使用された稀釈された排ガスは吸引ポンプ6で大気中
へ放出される。
The operation of the whole floating particulate matter measurement system for a ship shown in the embodiment is performed by the exhaust pipe 1 of the diesel engine.
When part of the exhaust gas is guided to the exhaust gas diluter 4 from the buoyant particulate matter measuring probe 2 attached to the exhaust gas diluter 4, the exhaust gas is diluted with clean air. Then, the diluted exhaust gas is supplied to the main body 4 of the exhaust gas diluter 4.
From the outlet nozzle 45 provided in the body of No. 1 to the beta ray absorption type floating particulate matter measuring instrument 5, the concentration of the floating particulate matter in the exhaust gas diluted here is measured and used for the measurement. The diluted exhaust gas is discharged into the atmosphere by the suction pump 6.

【0027】次に、ディーゼル機関の排ガス及び稀釈さ
れた排ガス中の炭酸ガス濃度の測定について述べる。
Next, the measurement of the carbon dioxide concentration in the exhaust gas of the diesel engine and the diluted exhaust gas will be described.

【0028】排ガスの一部は排気管1に取り付けた炭酸
ガス測定用プローブ7から切替えコック8、前処理装置
9を経て炭酸ガス測定器10に至り、ここで炭酸ガス濃
度Xが測定される。
A part of the exhaust gas reaches the carbon dioxide measuring instrument 10 from the carbon dioxide measuring probe 7 attached to the exhaust pipe 1 through the switching cock 8 and the pretreatment device 9, and the carbon dioxide concentration X is measured there.

【0029】一方、稀釈された排ガスの一部は排ガス希
釈器4の胴に設けた炭酸ガス測定用採取口46から切替
えコック8、前処理装置9を経て炭酸ガス測定器10に
至り、ここで炭酸ガス濃度x’が測定され、前述のよう
に希釈係数x/x’を求め、その希釈係数が4以上とな
るようにバルブ32を調節する。
On the other hand, a part of the diluted exhaust gas reaches the carbon dioxide measuring instrument 10 through the carbon dioxide measuring sampling port 46 provided in the body of the exhaust gas diluter 4 through the switching cock 8 and the pretreatment device 9, and here. The carbon dioxide concentration x'is measured, the dilution coefficient x / x 'is obtained as described above, and the valve 32 is adjusted so that the dilution coefficient becomes 4 or more.

【0030】次に、排ガス稀釈器4の作用について述べ
ると、排ガスはエヤガン11の吸引口11aへ導びかれ
る。一方、ドライクリーニングユニット31で清浄空気
となった圧縮空気は、エヤガン11の給気口11cから
ノズルN1〜N4へと導かれ、排ガスを吸引すると同時
に、排ガスと混合しながら噴射口11bより混合チヤン
バー42へ噴出する。混合チャンバー42では送り込ま
れた排ガスと清浄空気はここで均一に混合し、稀釈され
た排ガスとなる。
Next, the operation of the exhaust gas diluter 4 will be described. The exhaust gas is guided to the suction port 11a of the air gun 11. On the other hand, the compressed air that has become clean air in the dry cleaning unit 31 is guided from the air supply port 11c of the air gun 11 to the nozzles N1 to N4 to suck the exhaust gas and at the same time mix it with the exhaust gas from the injection port 11b. Eject to 42. In the mixing chamber 42, the discharged exhaust gas and the clean air are uniformly mixed here, and become diluted exhaust gas.

【0031】そして稀釈された排ガスの一部は胴に設け
られたオーバフロー出口47より大気へと逃げる。同時
に混合チヤンバー42の圧力は大気圧に保たれ、ベータ
線吸収式浮遊性微粒子状物質測定器5の測定条件を整え
る。そして、稀釈された排ガスは胴の下部に設けらた出
口ノズル45よりベータ線吸収式浮遊性微粒子状物質測
定器5へと導かれ、浮遊性微粒子状物質が測定される。
Then, a part of the diluted exhaust gas escapes to the atmosphere through an overflow outlet 47 provided in the cylinder. At the same time, the pressure of the mixing chamber 42 is kept at atmospheric pressure, and the measurement conditions of the beta ray absorption type floating particulate matter measuring instrument 5 are adjusted. Then, the diluted exhaust gas is guided to the beta ray absorption type floating particulate matter measuring instrument 5 from an outlet nozzle 45 provided at the lower part of the body, and the floating particulate matter is measured.

【0032】[0032]

【発明の効果】実験用中型中速4サイクルディーゼル機
関に於いて、機関専用のダイリューショントンネルと本
発明にかヽる船舶用浮遊性微粒子状物質測定システムと
の比較を行ったところ、それぞれで浮遊性微粒子状物質
排出濃度を測定した結果は一致した。このことにより本
発明にかヽる船舶用浮遊性微粒子状物質測定システムの
測定結果は、国際標準化機構の規定に準じたといえる。
[Effects of the Invention] In an experimental medium-sized medium-speed 4-cycle diesel engine, a comparison was made between an engine-specific dilution tunnel and the ship floating particulate matter measurement system according to the present invention. The results of measurement of airborne particulate matter emission concentrations were in agreement. From this, it can be said that the measurement results of the floating particulate matter measurement system for ships according to the present invention comply with the regulations of the International Organization for Standardization.

【0033】フィルタ振動式浮遊性微粒子状物質測定器
とベータ線吸収式浮遊性微粒子状物質測定器を実際に船
舶に搭載して比較測定を行ったところ船体動揺に対し
て、フィルタ振動式浮遊性微組子状物質測定器ではテー
パエレメントの固有振動数が変化するが、ベータ線吸収
式浮遊性微粒子状物質測定器のゼロ点の変化はなく、船
体動揺下でも計測は可能であった。
A filter vibration type floating particulate matter measuring instrument and a beta ray absorption type floating particulate matter measuring instrument were actually mounted on a ship and comparative measurement was carried out. Although the natural frequency of the taper element changed with the fine particle measuring instrument, the zero point of the beta ray absorption type floating particulate matter measuring instrument did not change, and the measurement was possible even when the ship was swaying.

【0034】従って、ベータ線吸収式浮遊性微粒子状物
質測定器を構成要素の一つとした本発明にかヽる船舶用
浮遊性微徴粒子状物質測定システムは船舶での計側に適
応でき、船舶から排出される浮遊性微粒子状物質の排出
実態の調査が可能になり、排出実態が明らかになる。
Therefore, the buoyant microscopic particulate matter measuring system for a ship according to the present invention having the beta ray absorption type buoyant particulate matter measuring device as one of its constituent elements can be applied to the measuring side of a ship, It becomes possible to investigate the actual discharge of airborne particulate matter discharged from ships, and the actual discharge becomes clear.

【図面の簡単な説明】[Brief description of drawings]

【図1】 本発明の実施例の全体の構成を示すブロック
図。
FIG. 1 is a block diagram showing the overall configuration of an embodiment of the present invention.

【図2】 排ガス希釈器の詳細を示す拡大断面図。FIG. 2 is an enlarged sectional view showing details of an exhaust gas diluter.

【符号の説明】[Explanation of symbols]

1 排気管 2 浮遊性微粒子状物質測定用プローブ 3 希釈空気供給装置 31 ドライクリーニングユニット 32 バルブ 4 排ガス希釈器 41 本体 42 混合チャンバー 43 分離チャンバー 44 分離管 45 出口ノズル 46 炭酸ガス測定用採取口 47 オーバフロー排出口 5 ベータ線吸収式浮遊性微粒子状物質測定器 6 吸引ポンプ 7 炭酸ガス測定用プローブ 8 切替コック 9 前処理装置 10 炭酸ガス測定器 11 エヤガン 11a 吸引口 11b 噴射口 11c 給気口 1 exhaust pipe 2 Probe for measuring airborne particulate matter 3 dilution air supply device 31 Dry Cleaning Unit 32 valves 4 Exhaust gas diluter 41 body 42 mixing chamber 43 Separation chamber 44 Separation tube 45 outlet nozzle 46 Sampling port for measuring carbon dioxide 47 Overflow outlet 5 Beta-ray absorption type floating particulate matter measuring instrument 6 suction pump 7 Carbon dioxide measurement probe 8 switching cock 9 Pretreatment equipment 10 Carbon dioxide measuring instrument 11 Air Gun 11a suction port 11b injection port 11c Air supply port

───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 2G001 AA03 BA11 CA03 KA01 MA04 PA11 RA08 2G052 AA02 AB22 AC19 AD04 AD24 AD44 BA05 BA14 CA03 CA04 CA11 DA22 EA03 FB02 FB09 GA09 GA19 HA15 HC02 HC09 HC24 HC43 JA04    ─────────────────────────────────────────────────── ─── Continued front page    F-term (reference) 2G001 AA03 BA11 CA03 KA01 MA04                       PA11 RA08                 2G052 AA02 AB22 AC19 AD04 AD24                       AD44 BA05 BA14 CA03 CA04                       CA11 DA22 EA03 FB02 FB09                       GA09 GA19 HA15 HC02 HC09                       HC24 HC43 JA04

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 ドライクリーニング装置と供給量調整装
置を備えた希釈空気供給装置と、この希釈空気供給装置
から送出される清浄空気とエンジンの排ガスを混合する
排ガス希釈器と、前記エンジンの排ガス又は前記排ガス
希釈器から送出される希釈排ガス中に含まれる炭酸ガス
を切替コックと前処理装置を介して測定する炭酸ガス測
定器と、前記排ガス希釈器から送出される希釈排ガス中
の浮遊性微粒子状物質を測定するベータ線吸収式浮遊性
微粒子状物質測定器とを備え、前記炭酸ガス測定器によ
って測定したエンジンの排ガスと希釈排ガスの炭酸ガス
測定値から希釈係数を求め、その希釈係数が適正希釈係
数となるように前記希釈空気供給装置の清浄空気送出量
を調整することを特徴とする船舶用浮遊性微粒子状物質
測定システム。
1. A dilution air supply device including a dry cleaning device and a supply amount adjustment device, an exhaust gas diluter for mixing clean air sent from the dilution air supply device and engine exhaust gas, and exhaust gas of the engine or A carbon dioxide gas measuring device for measuring carbon dioxide gas contained in the diluted exhaust gas sent from the exhaust gas diluter via a switching cock and a pretreatment device, and floating fine particles in the diluted exhaust gas sent from the exhaust gas diluter. Equipped with a beta ray absorption type floating particulate matter measuring device for measuring a substance, the dilution coefficient is obtained from the carbon dioxide measurement value of the engine exhaust gas and diluted exhaust gas measured by the carbon dioxide measuring device, and the dilution coefficient is an appropriate dilution. A floating airborne particulate matter measuring system for a ship, wherein the amount of clean air delivered from the dilution air supply device is adjusted so as to obtain a coefficient.
【請求項2】 混合チャンバーを備えた本体の一端に、
周囲数ヶ所から排ガス流入路へその噴出口側に向って斜
に清浄空気を噴出するノズルを備えたエヤガンを設け、
反対側に混合チャンバー内に向って分離管を突出させた
出口ノズルを設け、その分離管の側方の本体に炭酸ガス
測定用採取口と、オーバーフロー排出口を設けたことを
特徴とする排ガス希釈器。
2. At one end of the body with a mixing chamber,
An air gun equipped with a nozzle that jets clean air diagonally from several places around the exhaust gas inflow path toward the jet outlet side,
Exhaust gas dilution characterized in that an outlet nozzle with a separation pipe protruding toward the inside of the mixing chamber is provided on the opposite side, and a carbon dioxide gas measurement sampling port and an overflow discharge port are provided on the side body of the separation pipe. vessel.
JP2001273332A 2001-09-10 2001-09-10 Method for measuring suspended particulate matter for ships and its exhaust gas diluter Expired - Lifetime JP3709434B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001273332A JP3709434B2 (en) 2001-09-10 2001-09-10 Method for measuring suspended particulate matter for ships and its exhaust gas diluter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001273332A JP3709434B2 (en) 2001-09-10 2001-09-10 Method for measuring suspended particulate matter for ships and its exhaust gas diluter

Publications (2)

Publication Number Publication Date
JP2003083949A true JP2003083949A (en) 2003-03-19
JP3709434B2 JP3709434B2 (en) 2005-10-26

Family

ID=19098562

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001273332A Expired - Lifetime JP3709434B2 (en) 2001-09-10 2001-09-10 Method for measuring suspended particulate matter for ships and its exhaust gas diluter

Country Status (1)

Country Link
JP (1) JP3709434B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103636532A (en) * 2013-11-29 2014-03-19 浙江海洋学院 Carbon sink informationized marine ranch
JP2017053822A (en) * 2015-09-11 2017-03-16 株式会社東芝 Particle measurement apparatus and particle measurement method
CN113650769A (en) * 2021-07-21 2021-11-16 上海外高桥造船有限公司 Ship with exhaust carbon content measuring equipment

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104819919B (en) * 2015-05-20 2017-11-21 北京曼德克环境科技有限公司 A kind of granular material discharged content detection instrument
KR101592022B1 (en) * 2015-08-20 2016-03-07 (주)팀솔루션 Method and system for determining concentration of gas and Ship having the same, and method for detecting sulphur content of fuel oil for ship

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103636532A (en) * 2013-11-29 2014-03-19 浙江海洋学院 Carbon sink informationized marine ranch
JP2017053822A (en) * 2015-09-11 2017-03-16 株式会社東芝 Particle measurement apparatus and particle measurement method
CN113650769A (en) * 2021-07-21 2021-11-16 上海外高桥造船有限公司 Ship with exhaust carbon content measuring equipment

Also Published As

Publication number Publication date
JP3709434B2 (en) 2005-10-26

Similar Documents

Publication Publication Date Title
US5249561A (en) Hydrocarbon vapor sensor system for an internal combustion engine
JP2003083949A (en) System for measuring floating substance in fine particle shape for ship, and exhaust gas dilution equipment
US7798020B2 (en) Fast response proportional sampling system and method for exhaust gas analysis
CN101398368A (en) Aerated solids particle laser analyzer gas path system for aerated solids particle laser analyzer
CA2483964C (en) Monitoring medical gas xenon concentration using ultrasonic gas analyser
CN107860598A (en) A kind of portable cutter for particles fast calibration device and its calibration method
US5728927A (en) Controlled multi-purpose chemical agent vapor generator system
CN112345688A (en) Device and method for testing fire extinguishing efficiency of superfine dry powder extinguishing agent
Killough et al. A low-sample-consumption dry-particulate aerosol generator for use in nose-only inhalation exposures
EP3918301B1 (en) Diluting device for aerosol measurements
CN212621469U (en) Air pipeline system for nozzle and fuel oil main pipe performance tester
CN111649949A (en) Air pipeline system for nozzle and fuel oil main pipe performance tester
JPH11211631A (en) Apparatus for diluting sampling exhaust gas
GB2214449A (en) Exhaust gas particulate measurement
WO2023020582A1 (en) A coating system for coating a substrate and a process of coating the substrate with the same
JPS586903B2 (en) Sampling method
CN218240087U (en) Airflow field PIV test system and high-speed putting device of tracer particles
JPS59206741A (en) Method and apparatus for diluting mixed phase fluid of solid and gas
RU2681192C1 (en) Device for the selection of average for flight air samples from aircraft gas turbine engines while taking tests on flying laboratories
Weingartner et al. Pressure drop across fiber filters
CN1070477A (en) Adjustable flue gas dilution sampling device
JPS63214326A (en) Dilution device for solid-gas mixed phase fluid
GB2162647A (en) Apparatus for measuring total flow in pipes
JPS57102545A (en) Suction device for engine
JPS5887453A (en) Particle feeding method for running magnetic powder flaw detector

Legal Events

Date Code Title Description
A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20040622

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20040727

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20050405

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20050411

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20050712

R150 Certificate of patent or registration of utility model

Ref document number: 3709434

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

Free format text: JAPANESE INTERMEDIATE CODE: R150

S533 Written request for registration of change of name

Free format text: JAPANESE INTERMEDIATE CODE: R313533

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

S533 Written request for registration of change of name

Free format text: JAPANESE INTERMEDIATE CODE: R313533

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

EXPY Cancellation because of completion of term