JP5863087B2 - Exhaust gas treatment equipment for large displacement diesel engines using low quality fuels below heavy oil - Google Patents

Exhaust gas treatment equipment for large displacement diesel engines using low quality fuels below heavy oil Download PDF

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JP5863087B2
JP5863087B2 JP2010256160A JP2010256160A JP5863087B2 JP 5863087 B2 JP5863087 B2 JP 5863087B2 JP 2010256160 A JP2010256160 A JP 2010256160A JP 2010256160 A JP2010256160 A JP 2010256160A JP 5863087 B2 JP5863087 B2 JP 5863087B2
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exhaust gas
collecting
cyclone
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collection
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JP2012107556A (en
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宗勝 古堅
宗勝 古堅
義 牧野
義 牧野
滝川 一儀
一儀 滝川
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Usui Co Ltd
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Priority to CN201180055097.0A priority patent/CN103261596B/en
Priority to EP11842356.5A priority patent/EP2642095B1/en
Priority to KR1020137015397A priority patent/KR101423016B1/en
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N3/00Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
    • F01N3/02Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03CMAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/34Constructional details or accessories or operation thereof
    • B03C3/40Electrode constructions
    • B03C3/45Collecting-electrodes
    • B03C3/49Collecting-electrodes tubular
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03CMAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/02Plant or installations having external electricity supply
    • B03C3/04Plant or installations having external electricity supply dry type
    • B03C3/14Plant or installations having external electricity supply dry type characterised by the additional use of mechanical effects, e.g. gravity
    • B03C3/15Centrifugal forces
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03CMAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/34Constructional details or accessories or operation thereof
    • B03C3/36Controlling flow of gases or vapour
    • B03C3/368Controlling flow of gases or vapour by other than static mechanical means, e.g. internal ventilator or recycler
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03CMAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/34Constructional details or accessories or operation thereof
    • B03C3/40Electrode constructions
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03CMAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/34Constructional details or accessories or operation thereof
    • B03C3/40Electrode constructions
    • B03C3/41Ionising-electrodes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03CMAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C3/00Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
    • B03C3/34Constructional details or accessories or operation thereof
    • B03C3/86Electrode-carrying means
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04CAPPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C5/00Apparatus in which the axial direction of the vortex is reversed
    • B04C5/02Construction of inlets by which the vortex flow is generated, e.g. tangential admission, the fluid flow being forced to follow a downward path by spirally wound bulkheads, or with slightly downwardly-directed tangential admission
    • B04C5/04Tangential inlets
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N3/00Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
    • F01N3/01Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust by means of electric or electrostatic separators
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N3/00Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
    • F01N3/02Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust
    • F01N3/021Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters
    • F01N3/023Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters using means for regenerating the filters, e.g. by burning trapped particles
    • F01N3/027Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters using means for regenerating the filters, e.g. by burning trapped particles using electric or magnetic heating means
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N3/00Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
    • F01N3/02Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust
    • F01N3/021Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters
    • F01N3/023Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters using means for regenerating the filters, e.g. by burning trapped particles
    • F01N3/027Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters using means for regenerating the filters, e.g. by burning trapped particles using electric or magnetic heating means
    • F01N3/0275Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters using means for regenerating the filters, e.g. by burning trapped particles using electric or magnetic heating means using electric discharge means
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N3/00Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
    • F01N3/02Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust
    • F01N3/037Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of inertial or centrifugal separators, e.g. of cyclone type, optionally combined or associated with agglomerators
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03CMAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C2201/00Details of magnetic or electrostatic separation
    • B03C2201/08Ionising electrode being a rod
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03CMAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C2201/00Details of magnetic or electrostatic separation
    • B03C2201/10Ionising electrode has multiple serrated ends or parts
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03CMAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C2201/00Details of magnetic or electrostatic separation
    • B03C2201/30Details of magnetic or electrostatic separation for use in or with vehicles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04CAPPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C9/00Combinations with other devices, e.g. fans, expansion chambers, diffusors, water locks
    • B04C2009/001Combinations with other devices, e.g. fans, expansion chambers, diffusors, water locks with means for electrostatic separation

Description

本発明は、ディーゼルエンジンの排気ガスに含まれるカーボンを主体とする粒状物質(Particulate Matter:以下「PM」と称する)や有害ガスを除去し、浄化する船舶用、発電用、産業用などの特に重油以下の低質燃料を使用する大排気量ディーゼルエンジンの排気ガス処理技術に係り、より詳しくは高い温度の排気ガスを排出する重油以下の低質燃料を使用する大排気量ディーゼルエンジンにおけるコロナ放電を利用した排気ガス処理装置に関する。 The present invention removes particulate matter (Particulate Matter: hereinafter referred to as “PM”) and harmful gas mainly contained in exhaust gas of a diesel engine and removes and purifies, particularly for ships, power generation, industrial use, etc. The present invention relates to exhaust gas processing technology for large-displacement diesel engines that use low-quality fuel below heavy oil, and more specifically, corona discharge in large-displacement diesel engines that use low-quality fuel below heavy oil that discharges high-temperature exhaust gas. The present invention relates to a used exhaust gas treatment device.

各種船舶や発電機並びに大型建機、さらには各種自動車等の動力源としてディーゼルエンジンが広範囲に採用されているが、このディーゼルエンジンから排出される排気ガスに含まれるPMは、周知の通り大気汚染をきたすのみならず、人体に極めて有害な物質であるため、その排気ガスの浄化は極めて重要である。このため、ディーゼルエンジンの燃焼方式の改善や各種排気ガスフィルタの採用、そしてコロナ放電を利用して電気的に処理する方法等、既に数多くの提案がなされ、その一部は実用に供されている。   Diesel engines are widely used as power sources for various ships, generators, large construction machines, and various automobiles, but as is well known, PM contained in exhaust gas discharged from diesel engines is air pollution. In addition to toxic substances, it is a substance that is extremely harmful to the human body, so purification of the exhaust gas is extremely important. For this reason, many proposals have already been made, such as improvements in the combustion system of diesel engines, the use of various exhaust gas filters, and methods of electrical treatment using corona discharge, some of which have been put into practical use. .

ここで、ディーゼルエンジンの排気ガス中のPM(粒状物質)の成分は、有機溶剤可溶分(SOF:Soluble Organic Fractions、以下「SOF」と称す)と有機溶剤非可溶分(ISF:Insoluble Organic Fractions、以下「ISF」と称す)の2つに分けられるが、そのうちSOF分は、燃料や潤滑油の未燃分が主な成分で、発ガン作用のある多環芳香族等の有害物質が含まれる。一方、ISF分は、電気抵抗率の低いカーボン(すす)とサルフェート(Sulfate:硫酸塩)成分を主成分とするもので、このSOF分およびISF分は、その人体、環境に与える影響から、極力少ない排気ガスが望まれている。特に、生体におけるPMの悪影響の度合いは、その粒子径がnmサイズになる場合に特に問題であるとも言われている。   Here, components of PM (particulate matter) in exhaust gas of a diesel engine are organic solvent soluble (SOF: Soluble Organic Fractions, hereinafter referred to as “SOF”) and organic solvent insoluble (ISF: Insoluble Organic). Fractions (hereinafter referred to as “ISF”), of which SOF is mainly composed of unburned fuel and lubricating oil, and harmful substances such as polycyclic aromatics that have a carcinogenic effect. included. On the other hand, the ISF component is mainly composed of carbon (soot) and sulfate (sulfate) components having low electrical resistivity. The SOF component and the ISF component are affected as much as possible because of their effects on the human body and the environment. Less exhaust gas is desired. In particular, it is also said that the degree of adverse effects of PM in a living body is particularly problematic when the particle diameter is nm.

コロナ放電を利用して電気的に処理する方法としては、例えば以下に記載する方法及び装置(特許文献1〜5)が提案されている。   For example, methods and apparatuses described below (Patent Documents 1 to 5) have been proposed as a method of performing electrical treatment using corona discharge.

即ち、特許文献1には、図12にその概略を示すように、排気ガス通路21にコロナ放電部22−1と帯電部22−2とからなる放電帯電部22を連設して、コロナ放電された電子29を排気ガスG1中のカーボンを主体とするPM28に帯電させ、同排気ガス通路21に配置した捕集板23で前記帯電したPM28を捕集する方式であって、放電帯電部22における電極針24は排気ガス流の流れ方向長さが短く、かつ捕集板23は排気ガス流の流れ方向に対し直角方向に配設された構成となしたディーゼルエンジンの排気ガス用電気式処理方法及び装置が提案されている。図中、25はシールガス管、26は高圧電源装置、27は排気ガス誘導管である。   That is, in Patent Document 1, as schematically shown in FIG. 12, a discharge charging unit 22 including a corona discharge unit 22-1 and a charging unit 22-2 is connected to the exhaust gas passage 21 to corona discharge. The charged electrons 29 are charged to the PM 28 mainly composed of carbon in the exhaust gas G 1, and the charged PM 28 is collected by the collection plate 23 disposed in the exhaust gas passage 21. The electrode needle 24 has a short length in the flow direction of the exhaust gas flow, and the collecting plate 23 is arranged in a direction perpendicular to the flow direction of the exhaust gas flow. Methods and apparatus have been proposed. In the figure, 25 is a seal gas pipe, 26 is a high voltage power supply device, and 27 is an exhaust gas induction pipe.

又、特許文献2には、図13にその概略を示すように、針先31−1の周りにコロナ放電35を起こして排気ガス中のPM33を帯電させるためのニードル電極31と、帯電したPM33を捕集するための捕集電極32と、前記ニードル電極31と前記捕集電極32との間に所定の直流高電圧を印加するための高圧直流電源34とを備えたディーゼルエンジンの排気PM捕集装置が提案されている。図中、36は偏向電極である。   Further, in Patent Document 2, as schematically shown in FIG. 13, a needle electrode 31 for charging a PM 33 in exhaust gas by causing a corona discharge 35 around the needle tip 31-1 and a charged PM 33 are disclosed. Exhaust gas trapping of a diesel engine provided with a collecting electrode 32 for collecting the gas and a high-voltage DC power source 34 for applying a predetermined DC high voltage between the needle electrode 31 and the collecting electrode 32 A collecting device has been proposed. In the figure, 36 is a deflection electrode.

更に、特許文献3には、図14にその概略を示すように、排気経路中に設けたPM捕集用の収集電極対の一方を構成する固定円筒体41と、該固定円筒体41の中心部に軸方向に延設されて収集電極対の他方を構成する電極棒42と、前記収集電極対間に静電界を形成して排気ガス中のPMを前記固定円筒体41の内面に集積させる高電圧電源部43と、前記固定円筒体41の内面に沿って当該固定円筒体に対し相対回動して該固定円筒体内面に堆積したPMを掻き落とす掻き落とし部44を備えた排気ガス浄化装置が提案されている。図中、45は排気管、46は回転円筒部である。   Further, in Patent Document 3, as schematically shown in FIG. 14, a fixed cylindrical body 41 that constitutes one of a collection electrode pair for collecting PM provided in an exhaust path, and a center of the fixed cylindrical body 41. The electrode rod 42 extending in the axial direction at the portion and constituting the other of the collection electrode pair, and an electrostatic field is formed between the collection electrode pair to accumulate PM in the exhaust gas on the inner surface of the fixed cylindrical body 41. Exhaust gas purification provided with a high voltage power supply unit 43 and a scraping unit 44 that rotates relative to the fixed cylindrical body along the inner surface of the fixed cylindrical body 41 to scrape PM accumulated on the inner surface of the fixed cylindrical body. A device has been proposed. In the figure, 45 is an exhaust pipe, and 46 is a rotating cylindrical part.

一方、特許文献4には、ディーゼルエンジンの排ガス中に含まれるPMを帯電させる放電電極、及び帯電されたPMを捕集する集塵電極を有する電気集塵手段と、集塵電極に捕集されて滞留するPMを当該集塵電極から剥離させる手段と、集塵電極から剥離されたPMを分別して捕集するサイクロン方式の分別捕集手段とを備えたディーゼルエンジン排ガス浄化装置が提案されている。
この装置は、図15にその一例を示すように、排ガスを横方向に流しながら処理するように構成されたもので、PMを捕集するための電気集塵部51と、分別捕集部としてのサイクロン52を備え、電気集塵部51は筒状ハウジング56の内周面に取付けた筒状金属体57と該筒状金属体の内周面に形成した凹凸部58とによって構成された集塵電極54と、この集塵電極54の軸線に沿って延びる主電極59と、この主電極59の長手方向に所定の間隔で配設された放射状に突出する電極針60の群とによって構成された放電電極55とを備え、サイクロン52は電気集塵部51を通過したガス流53の流れを旋回流に変換するガイドベーン61より下流側の部位に構成され、このサイクロン52の下流に該サイクロン内のガスを排出するための排気管62と、遠心分離されたPMを捕集するホッパー63が設けられている。64は集塵電極54に捕集されて滞留するPMを当該集塵電極から剥離させる剥離機構であり、例えば偏心による振動を発生する偏心モータ65で構成されている。66は排気管62内の排ガスをホッパー63の上部空間にリターンさせるための抽気管である。
即ち、上記構成の排ガス浄化装置は、電気集塵部51に流入した排ガス中のPMは、集塵電極54と放電電極55との間における放電によって帯電されてクーロン力によって集塵電極54に捕集され、捕集されたPMはガス流と共にガイドベーン61に流入し、ガイドベーン61より下流側の部位に構成されるサイクロン52によりPMが遠心分離され、遠心分離されたPMはホッパー63内に降下して捕集され、一方、浄化された排ガスは排気管62を介して外部に放出される仕組みとなしたものである。
On the other hand, Patent Document 4 discloses a discharge electrode for charging PM contained in exhaust gas of a diesel engine, an electric dust collection means having a dust collection electrode for collecting charged PM, and a dust collection electrode. Engine exhaust gas purification device provided with means for separating the PM accumulated from the dust collecting electrode and a cyclone-type separation collecting means for separating and collecting the PM peeled from the dust collecting electrode has been proposed .
As shown in FIG. 15, this apparatus is configured to process exhaust gas while flowing in the lateral direction, and serves as an electric dust collector 51 for collecting PM and a separate collector. The electrostatic dust collecting portion 51 is a collection of a cylindrical metal body 57 attached to the inner peripheral surface of the cylindrical housing 56 and an uneven portion 58 formed on the inner peripheral surface of the cylindrical metal body. The dust electrode 54, a main electrode 59 extending along the axis of the dust collection electrode 54, and a group of radially projecting electrode needles 60 disposed at predetermined intervals in the longitudinal direction of the main electrode 59. The cyclone 52 is configured at a downstream side of the guide vane 61 that converts the flow of the gas flow 53 that has passed through the electrostatic precipitator 51 into a swirl flow, and the cyclone is disposed downstream of the cyclone 52. The gas inside An exhaust pipe 62 of the eye, a hopper 63 for collecting PM, which is centrifuged is provided. A separation mechanism 64 separates the PM collected and collected by the dust collection electrode 54 from the dust collection electrode 54, and includes, for example, an eccentric motor 65 that generates vibration due to eccentricity. Reference numeral 66 denotes an extraction pipe for returning the exhaust gas in the exhaust pipe 62 to the upper space of the hopper 63.
That is, in the exhaust gas purification apparatus having the above-described configuration, PM in the exhaust gas flowing into the electric dust collector 51 is charged by the discharge between the dust collection electrode 54 and the discharge electrode 55 and captured by the dust collection electrode 54 by the Coulomb force. The collected and collected PM flows into the guide vane 61 together with the gas flow, and the PM is centrifuged by the cyclone 52 formed at the downstream side of the guide vane 61. The centrifuged PM is put into the hopper 63. On the other hand, the exhaust gas that has fallen and was collected and purified is discharged to the outside through the exhaust pipe 62.

又、特許文献5には、自動車に搭載したディーゼルエンジンの排気ガス中の捕集対象成分をコロナ放電により帯電させて凝集する帯電凝集部と、凝集させた成分を捕集するフィルタ部とを備えたガス処理装置として、図16、図17に示すように帯電凝集部70を上流側に、フィルタ部80を下流側に配設して構成すると共に、帯電凝集部70のガス通路壁を筒状体71、71a等で形成し、又、ガス通路壁の表面近傍に配置された導電性の筒状体71fで低電圧電極の集塵電極を形成し、これらの筒状体の内部に配置した線状体の高電圧電極でコロナ電極を形成すると共に、前記ガス通路壁の筒状体を自然対流と熱放射による自然によりガスを冷却するガス冷却部として形成し、更に、前記ガス通路壁の筒状体、又は前記導電性の筒状体の内側表面近傍を流れるガス流に対して、乱流を促進する乱流促進手段71eを、前記筒状体の表面又は表面近傍に設けて構成するガス処理装置が示されている。図中、71cはガス入口室、71bはコロナ電極、71dはガス出口室である。   Further, Patent Document 5 includes a charge aggregation portion that collects and aggregates the components to be collected in the exhaust gas of a diesel engine mounted on an automobile by corona discharge, and a filter portion that collects the aggregated components. As shown in FIGS. 16 and 17, the gas aggregating unit 70 is arranged on the upstream side and the filter unit 80 is arranged on the downstream side as shown in FIGS. The dust collecting electrode of the low voltage electrode is formed by the conductive cylindrical body 71f formed by the bodies 71, 71a, etc., and disposed in the vicinity of the surface of the gas passage wall, and is disposed inside these cylindrical bodies. A corona electrode is formed by a high-voltage electrode of a linear body, and a cylindrical body of the gas passage wall is formed as a gas cooling portion that cools the gas by natural convection and heat radiation, and further, the gas passage wall Of the cylindrical body or the conductive cylindrical body To gas flow through the vicinity of the back surface, the means for accelerating turbulence 71e to promote turbulence, the gas processing devices constituting provided on the surface or near the surface of the tubular body is shown. In the figure, 71c is a gas inlet chamber, 71b is a corona electrode, and 71d is a gas outlet chamber.

WO2006/064805B号公報WO2006 / 064805B 特開平9−112246号公報JP-A-9-112246 特開平6−173637号公報Japanese Patent Laid-Open No. 6-173637 特開2006−136766号公報JP 2006-136766 A 特許第4529013号Japanese Patent No. 4529013

しかしながら、上記した従来のディーゼルエンジン排ガス浄化装置には、以下に記載する欠点がある。
即ち、前記特許文献1に記載されたディーゼルエンジンの排気ガス用電気式処理方法及び装置は、放電帯電部22における電極針24は排気ガス流の流れ方向長さが短くかつ捕集板23は排気ガス流の流れ方向に対し直角方向に配設され、又、排気ガス流が捕集板23に対し直接当接するので流過抵抗(圧力損失;圧損)が大きいこと、捕集板23が薄く排気ガス流の流れ方向長さが短いのでPMの素通りが危惧され、PM捕集効率を十分に高めることができない恐れがあること、一旦捕集板23を通過したPMは再度コロナ放電により帯電させて捕集されることがなくそのまま排出されてしまうことが危惧される、といった問題を有する。
なお、前記特許文献1には、捕集板を排気ガス流の流れ方向に長尺な管状とすると共に、管状捕集部の管軸方向に電極針を設け、PM粒子を排気ガス流の流れ方向に流しながら堆積・剥離を繰返すジャンピング現象を発現させて成長させ、この成長現象により排気ガス流の管状捕集部内面付近のPMの粒径をサイクロンで捕集し易いように粗大化させると共にPMの濃度を上昇させ、さらにこのPMの粒径が大径でかつ濃度が高濃度に濃縮した排気ガス流を選択的に抽出してサイクロンで捕集するという技術思想は開示も示唆もしていない。
However, the above-described conventional diesel engine exhaust gas purification apparatus has the following drawbacks.
That is, in the electric processing method and apparatus for exhaust gas of a diesel engine described in Patent Document 1, the electrode needle 24 in the discharge charging unit 22 is short in the flow direction of the exhaust gas flow, and the collection plate 23 is exhausted. It is arranged in a direction perpendicular to the flow direction of the gas flow, and the exhaust gas flow is in direct contact with the collection plate 23, so that the flow resistance (pressure loss; pressure loss) is large, the collection plate 23 is thin and exhausted. Since the flow direction length of the gas flow is short, there is a concern that the PM may pass through, and there is a possibility that the PM collection efficiency cannot be sufficiently increased. The PM once passed through the collection plate 23 is charged again by corona discharge. There is a problem that it is feared that it will be collected without being collected.
In Patent Document 1, the collecting plate has a long tube shape in the flow direction of the exhaust gas flow, and an electrode needle is provided in the tube axis direction of the tubular collection portion, so that the PM particles flow in the flow of the exhaust gas flow. In addition to increasing the particle size of PM in the vicinity of the inner surface of the tubular collection part of the exhaust gas flow so that it can be easily collected by a cyclone. The technical idea of increasing the concentration of PM and selectively extracting the exhaust gas stream having a large PM particle size and concentrated to a high concentration and collecting them with a cyclone is not disclosed or suggested. .

又、前記特許文献2に記載の排気PM捕集装置及び特許文献3に記載の排気ガス浄化装置は、放電電圧と捕集偏向電圧が同電位であるため両電圧をそれぞれの適正条件に設定することが難しいこと、偏向電極と捕集電極間のスパーク発生を防止するためにその間隔を大きくとらざるを得ないこと、又そのために捕集されずに捕集区間を素通りするPMが多くなり、捕集効率が低下すること、更に、捕集効率を上げるためには捕集部の容量を大きくとる必要があり、装置の大型化を余儀なくされ、小型軽量化が望まれる舶用部品としては不適当である、といった欠点を有する。
なお、前記特許文献2には、捕集電極32は排気の通り道となるトンネル状の電極とされ、捕集電極32のトンネル内にニードル電極31と偏向電極36との電極結合体が、トンネルと軸心を略共通にして配設され、太く長尺の電極結合体が管状捕集部のほぼ全長にわたり内挿されて格子状に形成され、と記載され、又、前記特許文献3には、実施例6の段落[0033]に「……固定円筒体41の中心線に沿って放電電極対及び収集電極対の各一方を構成する電極棒42が垂下され、……固定円筒体41の下部側面には径大な排気口が設けられ、排気口には下流側排気管45が嵌入……。」と、段落[0035]には「回転円筒部46は下部が径小な切頭円錐形状を有し……回転円筒部46の内面から上方に長尺のバー(掻き落とし部)44が立設しており、バー44の外縁は固定円筒体41の径大部の内面に接している。」と、段落[0036]には「……ディーゼルパティキュレートは、放電空間で電極棒42と固定円筒体41……との間のコロナ放電により……帯電したディーゼルパティキュレートは、……静電界に引かれて固定円筒体41の径大部の内面に堆積する。」と、記載され、更に段落[0037]には「回転円筒部46の回転とともに、バー44は固定円筒体41の径大部の内面に接して低速で回転し、径大部の内面に堆積したディーゼルパティキュレート層を落下させ、……落下したディーゼルパティキュレートは収集箱に集め、……除去することができる。」と記載されて管状捕集部が形成されてはいるが、特許文献3に記載されているものは、捕集電極を排気ガス流の流れ方向に長尺な固定円筒部(管状)とすると共に、管状捕集部の管軸方向に間隔を保持して電極針を設け、PMを排気ガス流の流れ方向に流しながら堆積させ、堆積したPM粒子をバーにて掻き落とす技術であり、掻き落とされた時に飛散するPM粒子の一部は収集箱の手前に設けられた径大な排気口に嵌入された下流側排気管より排出されることが大いに危惧される技術である。
従って、特許文献2、3に記載された技術も、前記特許文献1に記載された技術と同様に、捕集板を排気ガス流の流れ方向に長尺な管状とすると共に、管状捕集部の管軸方向に電極針を設け、PM粒子を排気ガス流の流れ方向に流しながら堆積・剥離を繰返すジャンピング現象を発現させて成長させ、この成長現象により排気ガス流の管状捕集部内面付近のPMの粒径をサイクロンで捕集し易いように粗大化させると共にPMの濃度を上昇させ、さらにこのPMの粒径が大径でかつ濃度が高濃度に濃縮した排気ガス流を選択的に抽出してサイクロンで能率よく捕集する技術思想は開示も示唆もしていない。
In addition, the exhaust PM collection device described in Patent Document 2 and the exhaust gas purification device described in Patent Document 3 set both voltages to appropriate conditions because the discharge voltage and the collection deflection voltage are the same potential. In order to prevent the occurrence of sparks between the deflection electrode and the collection electrode, it is necessary to increase the distance between the deflection electrode and the collection electrode, and for this reason, the PM passing through the collection section without being collected increases. In order to reduce the collection efficiency, and to increase the collection efficiency, it is necessary to increase the capacity of the collection section. It has the disadvantage that it is.
In Patent Document 2, the collection electrode 32 is a tunnel-like electrode that serves as an exhaust passage, and an electrode assembly of the needle electrode 31 and the deflection electrode 36 is formed in the tunnel of the collection electrode 32. The shaft center is arranged in a substantially common manner, and a thick and long electrode assembly is inserted in almost the entire length of the tubular collecting portion to form a lattice shape. In the paragraph [0033] of the sixth embodiment, “...... the electrode rod 42 constituting one of the discharge electrode pair and the collection electrode pair is suspended along the center line of the fixed cylindrical body 41... A large-diameter exhaust port is provided on the side surface, and a downstream exhaust pipe 45 is fitted into the exhaust port .... "Paragraph [0035] states that" the rotating cylindrical portion 46 has a truncated conical shape with a small diameter at the bottom. ... A long bar (scraping part) 4 upward from the inner surface of the rotating cylindrical part 46 ”And the outer edge of the bar 44 is in contact with the inner surface of the large diameter portion of the fixed cylindrical body 41,” paragraph [0036] states that “...... diesel particulate is the electrode rod 42 in the discharge space. The charged diesel particulates are ... attracted by an electrostatic field and are deposited on the inner surface of the large diameter portion of the fixed cylinder 41. " Further, in paragraph [0037], “a diesel particulate layer deposited on the inner surface of the large-diameter portion as the bar 44 rotates at a low speed in contact with the inner surface of the large-diameter portion of the fixed cylindrical body 41 as the rotating cylindrical portion 46 rotates. The diesel particulates that fall are collected in a collection box and can be removed ... "and a tubular collection part is formed, but it is described in Patent Document 3. Things are collecting electrodes A fixed cylindrical portion (tubular) that is long in the flow direction of the exhaust gas flow is provided, and an electrode needle is provided while maintaining an interval in the tube axis direction of the tubular collection portion, so that PM flows in the flow direction of the exhaust gas flow. This is a technique for depositing and scraping the deposited PM particles with a bar, and a part of the PM particles scattered when scraped off is a downstream exhaust fitted into a large exhaust port provided in front of the collection box. It is a technology that is highly concerned about being discharged from the pipe.
Therefore, in the techniques described in Patent Documents 2 and 3, as in the technique described in Patent Document 1, the collecting plate has a tubular shape that is long in the flow direction of the exhaust gas flow. An electrode needle is provided in the direction of the tube axis of the tube, and the growth is caused by a jumping phenomenon that repeats deposition and separation while flowing PM particles in the flow direction of the exhaust gas flow. The particle size of PM is coarsened so that it can be easily collected by a cyclone, the concentration of PM is increased, and the exhaust gas stream having a large particle size and concentrated at a high concentration is selectively selected. The technical idea of extracting and collecting efficiently with a cyclone is neither disclosed nor suggested.

一方、前記特許文献4に記載のディーゼルエンジン排ガス浄化装置は、電気集塵部51の集塵電極54や排ガスの流れ方向に短寸の筒状ハウジング56の内周壁面(捕集管壁)に捕集されたPM粒子は大きな塊を形成し、このPM塊が自然剥離ないし機械的剥離機構により集塵電極54や捕集管壁を離脱して筒状ハウジング56内で混合され、この離脱して混合されたPM塊を排ガス中からサイクロン52において遠心分離してホッパー63に再捕集する方式であるが、この方式においては、筒状ハウジング56が排ガスの流れ方向に短寸であるためPM塊が十分な粒径には粗大化できず筒状ハウジング56内の後流側に配設した流過抵抗の増加によるエネルギーロスを犠牲にして全排ガス量の混合を伴うガイドベーン61によるサイクロン52に排ガスの全量を流してPMを遠心分離させるため、必然的に大型のガイドベーン61を配置した大型のサイクロン52が必要となり、設備コスト及びランニングコストが高くつくこと、又、構造的にサイクロン52を複数設置することができないため、運転エンジン台数の増減やエンジンの負荷率の大きな変動に伴う排気ガス流量の大幅な増減に対応できない上、サイクロン導入部の排ガス流速を適正に制御する手段を備えていないため高いPM捕集率を維持しかつサイクロンでの過大な圧損による燃費の悪化等の問題を解消することができない、といった欠点を有する。
なお、前記特許文献4においては、捕集板を排気ガス流の流れ方向に長尺な管状とすると共に、管状捕集部の管軸方向に電極針を設け、PM粒子を排気ガス流の流れ方向に流しながら管状捕集部内面付近に堆積させサイクロンで捕集してはいるが、該特許文献4に記載された技術も、前記特許文献1〜3に記載された技術と同様に、排気ガス流のPMの粒径をサイクロンで捕集し易いように粗大化させると共に排気ガス流の管状捕集部内面付近のPMの濃度を上昇させ、さらにこのPMの粒径が大径でかつ濃度が高濃度に濃縮した排気ガス流の管状捕集部内面付近の流れだけを選択的に抽出して集中的にサイクロンで捕集する技術思想は開示も示唆もしていない。
On the other hand, in the diesel engine exhaust gas purification device described in Patent Document 4, the dust collecting electrode 54 of the electric dust collector 51 and the inner peripheral wall surface (collecting tube wall) of the cylindrical housing 56 that is short in the flow direction of the exhaust gas. The collected PM particles form a large lump. The PM lump is separated from the dust collecting electrode 54 and the collecting tube wall by a natural peeling or mechanical peeling mechanism, and is mixed in the cylindrical housing 56. The PM lump mixed in this way is centrifuged in the cyclone 52 in the cyclone 52 and collected again in the hopper 63. In this method, the cylindrical housing 56 is short in the flow direction of the exhaust gas. cyclone by the guide vanes 61 in the mass sufficient particle size with the mixing of the total amount of exhaust gas at the expense of energy loss due to an increase in the flow-through resistance is disposed on the downstream side after the cylindrical housing 56 can not be coarsened In order to centrifuge the PM by flowing the entire amount of exhaust gas to No. 2, a large cyclone 52 having a large guide vane 61 is inevitably required, which increases the equipment cost and running cost, and is structurally cyclone. Since it is not possible to install a plurality of 52, it is not possible to cope with a large increase / decrease in the exhaust gas flow rate due to an increase or decrease in the number of operating engines or a large change in the engine load factor, and a means for appropriately controlling the exhaust gas flow rate at the cyclone introduction part Since it is not provided, it has the disadvantages of maintaining a high PM collection rate and not solving problems such as deterioration in fuel consumption due to excessive pressure loss in the cyclone.
In Patent Document 4, the collection plate has a long tubular shape in the flow direction of the exhaust gas flow, an electrode needle is provided in the tube axis direction of the tubular collection portion, and the PM particles are flowed in the exhaust gas flow. While flowing in the direction, it is deposited near the inner surface of the tubular collection part and collected by the cyclone. However, the technique described in Patent Document 4 is exhausted in the same manner as the techniques described in Patent Documents 1 to 3. The particle size of the gas flow PM is coarsened so that it can be easily collected by a cyclone, and the concentration of PM in the vicinity of the inner surface of the tubular collection portion of the exhaust gas flow is increased. However, there is no disclosure or suggestion of a technical idea of selectively extracting only the flow in the vicinity of the inner surface of the tubular collection portion of the exhaust gas flow concentrated to a high concentration and collecting it intensively with a cyclone.

更に、特許文献5に記載のガス処理装置は、車載用の小型のガス処理装置であって、帯電凝集部70を上流側に、フィルタ部80を下流側に配設して構成すると共に、帯電凝集部70に排気ガスを多数に分流するガス入口室71cを設けると共にガス通路壁を筒状体71fで形成しかつ該筒状体71fを外気に露出してガス通路壁である当該筒状体71fを自然対流と熱放射による自然放熱によりガスを冷却するガス冷却部として形成し、その後分流した排気ガスをガス出口室71dにて再混合させる装置に関する技術であり、管状捕集部から流出した排気ガスが、PM粒子の捕集工程以前に再混合されることのない技術(後述する本発明)とは異なる。この特許文献5に記載のガス処理装置は、筒状体71fの内表面又はその内表面の近傍にガス流れに対する乱流促進手段71eを設けて、特に筒状体の表面近傍にガスの乱流化を促進して、流路断面方向の攪拌作用を大きくしてしまう欠点を有する。
なお、この特許文献5に記載のものは、捕集壁を排気ガス流の流れ方向に長尺な管状の筒状体とすると共に該管状捕集部の管軸方向に電極針を設け、PM粒子を排気ガス流の流れ方向に流しながら該管状捕集部内面付近に堆積させて捕集しているものの、この特許文献5も、前記特許文献1〜4と同様に、排気ガス流のPMの粒径を下流側に設置されたサイクロンで捕集し易いように粗大化させると共に排気ガス流の管状捕集部内面付近のPMの濃度を上昇させ、更にこのPMの粒径が大径でかつPM濃度が高濃度の排気ガス流の管状捕集部内面付近の流れだけを選択的に抽出して集中的にサイクロンで捕集するという技術思想は開示も示唆もしていない。
Further, the gas processing apparatus described in Patent Document 5 is a small vehicle-mounted gas processing apparatus, which is configured by disposing the charging aggregation unit 70 on the upstream side and the filter unit 80 on the downstream side. A gas inlet chamber 71c that divides exhaust gas into a large number is provided in the agglomeration portion 70, a gas passage wall is formed of a cylindrical body 71f, and the cylindrical body 71f is exposed to the outside air to form the cylindrical body that is a gas passage wall 71f is a technology related to a device that forms a gas cooling part that cools a gas by natural convection and natural heat dissipation by heat radiation, and then remixes the separated exhaust gas in a gas outlet chamber 71d, and flows out from the tubular collecting part. This is different from a technique (the present invention described later) in which the exhaust gas is not remixed before the PM particle collecting step. The gas processing apparatus described in Patent Document 5 is provided with a turbulent flow promoting means 71e for the gas flow on the inner surface of the cylindrical body 71f or in the vicinity of the inner surface, and particularly the turbulent flow of gas near the surface of the cylindrical body. This has the disadvantage that the agitation action is promoted to increase the stirring action in the cross-sectional direction of the flow path.
In addition, the thing of this patent document 5 provides an electrode needle in the tube-axis direction of this tubular collection part while making a collection wall into the tubular cylindrical body long in the flow direction of exhaust gas flow, PM Although the particles are collected while being collected in the vicinity of the inner surface of the tubular collecting portion while flowing in the flow direction of the exhaust gas flow, this Patent Document 5 is also similar to Patent Documents 1 to 4 in the PM of the exhaust gas flow. The particle size of the exhaust gas is coarsened so as to be easily collected by a cyclone installed on the downstream side, and the concentration of PM in the vicinity of the inner surface of the tubular collection part of the exhaust gas flow is increased. In addition, the technical idea of selectively extracting only the flow in the vicinity of the inner surface of the tubular collecting portion of the exhaust gas flow having a high PM concentration and collecting it in a concentrated manner with a cyclone is not disclosed or suggested.

本発明は、上記した従来技術の欠点を解消するためになされたもので、特に全排ガス量が流れる通路内にガイドベーンを配設してサイクロンを構成する特許文献4に記載のディーゼルエンジン排ガス浄化装置の方式に替えて、サイクロン方式の分別捕集手段を管状捕集部内ではなく管状捕集部の下流側に配設し、かつ該サイクロン捕集手段を複数の接線式サイクロンで構成する方式を採用することにより、サイクロンを小型化することができる上、重油以下の低質燃料を使用する舶用大排気量ディーゼルエンジンにおける主機及び補機の並列運転や単独運転に伴う運転状況の変化やエンジンの負荷率の大きな変動などによる排気ガス流量の大幅な増減に応じてサイクロンを適正に選択使用することが可能であり、さらにサイクロン導入部の排ガス流速を適正に制御する手段を備えることにより、高いPM捕集率を維持しかつ当該排ガス浄化装置での過大な圧損による燃費の悪化等の問題を解消することができる重油以下の低質燃料を使用する大排気量ディーゼルエンジン排ガス処理装置を提供しようとするものである。 The present invention was made in order to eliminate the above-mentioned drawbacks of the prior art, and in particular, the diesel engine exhaust gas purification described in Patent Document 4 in which a guide vane is arranged in a passage through which the total exhaust gas amount flows to constitute a cyclone. Instead of the system of the apparatus, a system in which the cyclone type separation and collection means is arranged not in the tubular collection part but on the downstream side of the tubular collection part, and the cyclone collection means is constituted by a plurality of tangential cyclones. By adopting it, the cyclone can be reduced in size, and in the large-displacement marine diesel engine that uses low-quality fuel less than heavy oil , changes in the operating conditions and engine load due to the parallel operation and independent operation of the main engine and auxiliary machinery The cyclone can be selected and used appropriately according to the significant increase / decrease in the exhaust gas flow rate due to large fluctuations in the rate, etc. By providing a means for properly controlling the scan velocity, the oil following low quality fuel that can solve the problem of deterioration of fuel efficiency by excessive pressure loss in maintaining a high PM collection efficiency and the exhaust gas purifying device The present invention intends to provide an exhaust gas treatment device for a large displacement diesel engine to be used .

本発明に係る重油以下の低質燃料を使用する大排気量ディーゼルエンジン排ガス処理装置は、重油以下の低質燃料を使用する大排気量ディーゼルエンジンの排ガス中に含まれるPMに帯電させる放電電極、及び帯電された前記PMを捕集する集塵電極を構成する所定長さの管状捕集部を有し、かつ前記放電電極は前記管状捕集部を構成する補集管内に管軸方向に配設された主電極と該主電極に間隔配設された放射状に突出する複数本の電極針とによって構成された電気集塵手段と、前記管状捕集部から剥離したPMを分別して捕集するサイクロン方式の分別捕集手段を備えた重油以下の低質燃料を使用する大排気量ディーゼルエンジン排ガス処理装置において、前記管状捕集部の下流側の軸心付近にPMの低濃度排ガス導出管を、同管状捕集部の下流側の内周面付近に高濃度排ガス導出部をそれぞれ設け、PMの高濃度排ガス導出部に前記PMを捕集するサイクロン捕集手段を連設するとともに、該サイクロン捕集手段を接線式サイクロンで構成し、前記低濃度排ガス導出管に配設したダンパーの開度を制御することにより前記接線式サイクロンへの排ガス流入速度を制御する仕組みとなし、さらに前記捕集管の長さをL、該捕集管の内径をDとした場合、その関係が5D≦L≦15Dの条件を満たすことを特徴とするものである。なお、低濃度排ガスとはPM含有量の少ない排ガス(浄化された排ガス)のことであり、高濃度排ガスとはPMを多く含む排ガスのことであることはいうまでもない。 An exhaust gas treatment apparatus for a large displacement diesel engine using heavy oil or less low quality fuel according to the present invention includes a discharge electrode for charging PM contained in exhaust gas of a large displacement diesel engine using heavy oil or less low quality fuel, and It has a predetermined length tubular collecting part of which constitutes a dust collecting electrode for collecting the charged the PM, and the discharge electrode arrangement in the tube axis direction to collecting tube constituting the tubular collecting part Electric dust collecting means composed of a main electrode provided and a plurality of radially projecting electrode needles spaced from the main electrode, and PM separated from the tubular collecting portion are separated and collected. In an exhaust gas treatment apparatus for a large displacement diesel engine using a low quality fuel less than heavy oil equipped with a cyclone separation and collection means, a low concentration exhaust gas exhaust pipe for PM is provided in the vicinity of the axial center downstream of the tubular collection part. The tube A high-concentration exhaust gas deriving part is provided in the vicinity of the inner peripheral surface on the downstream side of the collecting part, and a cyclone collecting means for collecting the PM is connected to the PM high-concentration exhaust gas deriving part, and the cyclone collecting means is provided. constituted by a tangential cyclone, said to such a mechanism for controlling the exhaust gas inflow rate to the tangential cyclone by controlling the damper opening which is arranged in a low concentration exhaust gas outlet pipe, a longer of the collecting tube When the thickness is L and the inner diameter of the collection tube is D, the relationship satisfies the condition of 5D ≦ L ≦ 15D . Needless to say, low-concentration exhaust gas is exhaust gas having a low PM content (purified exhaust gas), and high-concentration exhaust gas is exhaust gas containing a large amount of PM.

又、本発明装置は、前記サイクロン捕集手段を複数の接線式サイクロンで構成し、前記高濃度排ガス導出部より排出される高濃度排ガスを当該排ガスの流量に応じて選択的に前記接線式サイクロンへ導入する方式となすことを特徴とするものである。   Further, the apparatus of the present invention comprises the cyclone collecting means constituted by a plurality of tangential cyclones, and the high concentration exhaust gas discharged from the high concentration exhaust gas deriving section is selectively selected according to the flow rate of the exhaust gas. It is characterized in that it becomes a method to be introduced into.

本発明装置において、前記管状捕集部は、その下流側端部にテーパ状に拡径するテーパ管状部と該テーパ管状部に連なる大径管状部を有し、前記大径管状部の軸心付近に低濃度排ガス導出管と前記大径管状部の内周面付近に高濃度排ガス導出部が連設された構成となすことを好ましい態様とするものである。   In the device according to the present invention, the tubular collecting portion has a tapered tubular portion that expands in a tapered shape at a downstream end portion thereof, and a large-diameter tubular portion that is continuous with the tapered tubular portion, and an axial center of the large-diameter tubular portion It is a preferable aspect that a low concentration exhaust gas outlet pipe and a high concentration exhaust gas outlet portion are connected in the vicinity of the inner peripheral surface of the large diameter tubular portion.

更に、前記管状捕集部のテーパ管状部又は該テーパ管状部と該テーパ管状部に連なる大径管状部の領域にまで放電電極を延長して設けた構成となすことを好ましい態様とするものである。   Further, it is preferable that the discharge electrode is extended to the tapered tubular portion of the tubular collection portion or the region of the tapered tubular portion and the large-diameter tubular portion connected to the tapered tubular portion. is there.

本発明装置は又、前記サイクロン捕集手段を、処理能力の異なる複数の接線式サイクロンで構成するとともに、各接線式サイクロンの導入口に流量制御ダンパーを設けることを好ましい態様とし、更に又、前記接線式サイクロンと低濃度排ガス導出管との間に、接線式サイクロン通過後の浄化ガスを前記低濃度排ガスと合流させるための排出管を配設するとともに、該排出管にエアーノズル又はモータ駆動ファンを配置した構成となすことを好ましい態様とするものである。   The apparatus according to the present invention is preferably configured such that the cyclone collecting means includes a plurality of tangential cyclones having different processing capacities, and a flow rate control damper is provided at an inlet of each tangential cyclone. Between the tangential cyclone and the low-concentration exhaust gas outlet pipe, an exhaust pipe for merging the purified gas after passing the tangential cyclone with the low-concentration exhaust gas is provided, and an air nozzle or a motor-driven fan is provided in the exhaust pipe. It is a preferred embodiment to have a configuration in which is arranged.

更に、本発明装置においては、前記管状捕集部がほぼ水平に配置されること、又は前記管状捕集部がほぼ垂直かつ上向きに配置されること、或いは前記管状捕集部がほぼ垂直かつ下向きに配置されることを好ましい態様とするものである。   Furthermore, in the device according to the present invention, the tubular collecting part is arranged substantially horizontally, or the tubular collecting part is arranged substantially vertically and upward, or the tubular collecting part is substantially vertical and downward. It is a preferred embodiment that they are arranged in the above.

本発明に係る重油以下の低質燃料を使用する大排気量ディーゼルエンジン排ガス処理装置は、捕集管の長さをL、捕集管の内径をDとした場合の関係が5D≦L≦15Dの条件を満足する長尺な捕集管を有する管状捕集部の外部でPMを遠心分離させる方式を採用したことにより、長尺な管状捕集部において排ガス中のPMが管状の捕集壁面に捕集されて塊状となり、このPM塊が管状で長尺な捕集壁面に付着と剥離を繰返しながら該管状の捕集壁面付近をPMが徐々に濃縮化されていくことによりPMを高濃度に含んだ排ガス流となって下流へ流れ、該管状捕集部内においてPMの高濃度排ガスと管状捕集部の軸心付近をPMが徐々に希薄化されていくことによりPMを低濃度にしか含有しない低濃度排ガスに分離され、PMの高濃度排ガスは管状で長尺な捕集壁面付近を、PMの低濃度排ガスは管状捕集部の軸心部付近をそれぞれ流れる現象が発生するので、PMが濃縮された高濃度排ガスのみを管状の捕集壁面付近からサイクロン捕集手段へ導くことができる。即ち、本発明装置によれば、全排ガス量に対しては一部ではあるがPMの高濃度排ガスのみをサイクロンへ導くことができるので、サイクロンを小型化できる。一方、PMが希薄化された低濃度排ガス(浄化された排ガス)は長尺な管状捕集部の下流側で軸心付近に連設されている低濃度排ガス導出管より外部へ放出される。 In the exhaust gas treatment apparatus for a large displacement diesel engine using low quality fuel of heavy oil or less according to the present invention, the relationship when the length of the collecting pipe is L and the inner diameter of the collecting pipe is D is 5D ≦ L ≦ 15D By adopting a method of centrifuging PM outside the tubular collection part having a long collection tube that satisfies the above conditions, the PM in the exhaust gas is tubular in the long tubular collection part. The PM mass is concentrated in the vicinity of the tubular collection wall surface while repeatedly adhering to and peeling from the long collection wall surface. As the exhaust gas flow contained in the pipe, it flows downstream, and the PM is gradually diluted in the vicinity of the high concentration exhaust gas of PM and the axial center of the tubular collection part. Separated into low-concentration exhaust gas that does not contain, high-concentration exhaust of PM Scan is an elongate collecting near the wall of a tubular, since the low concentration exhaust gas in the PM phenomena flowing near the axial center of the tubular collecting part respectively occurs, capturing tubular only high concentration exhaust gas PM enriched It can be led from the vicinity of the collecting wall to the cyclone collecting means. That is, according to the apparatus of the present invention, only a high concentration exhaust gas of PM can be guided to the cyclone although it is a part of the total exhaust gas amount, the cyclone can be downsized. On the other hand, low-concentration exhaust gas (purified exhaust gas) in which PM has been diluted is discharged to the outside from a low-concentration exhaust gas outlet pipe connected in the vicinity of the shaft center on the downstream side of the long tubular collection part.

又、本発明装置によれば、サイクロン捕集手段を複数の接線式サイクロンで構成し、高濃度排ガス導出部より排出されるPMの高濃度排ガスを当該排ガスの流量に応じて選択的に該接線式サイクロンへ導入する方式となすことにより、ガイドベーンを配設した前記特許文献4に記載のディーゼルエンジン排ガス浄化装置の軸流式サイクロンと比較して捕集性能の優れた接線式サイクロンの「流入する流体の接線速度が速いと捕集効率が高くなる」という作用効果に加え、舶用エンジンにおける主機及び補機の並列運転や単独運転に伴う運転状況の変化やエンジンの負荷率の大きな変動による排気ガス流量の大幅な増減に応じて接線式サイクロンの処理能力と台数を適正に選択することが可能となり、排ガス流量の変化に対応してPMの高い捕集率を確保することができる。更に、前記低濃度排ガス導出管に配設したダンパーの開度を制御することにより前記接線式サイクロンへの排ガス流入速度(接線速度)を適正に制御することができるので、PMの高い捕集率を維持しかつ当該排ガス浄化装置での過大な圧損による燃費の悪化等の問題も解消することができる。   Further, according to the apparatus of the present invention, the cyclone collecting means is constituted by a plurality of tangential cyclones, and the high concentration exhaust gas of PM discharged from the high concentration exhaust gas deriving section is selectively selected according to the flow rate of the exhaust gas. By adopting a method of introducing into a cyclone type cyclone, the “flow-in” of a tangential type cyclone with superior collection performance compared to the axial flow type cyclone of the diesel engine exhaust gas purification device described in Patent Document 4 in which a guide vane is disposed. In addition to the effect that the trapping efficiency increases when the tangential speed of the fluid is high, the exhaust due to changes in the operating status of the marine engine due to the parallel operation or independent operation of the main engine and auxiliary machinery, or large fluctuations in the load factor of the engine The processing capacity and number of tangential cyclones can be selected appropriately according to the significant increase / decrease in the gas flow rate. It is possible to secure the rate. Furthermore, since the exhaust gas inflow rate (tangential velocity) to the tangential cyclone can be properly controlled by controlling the opening degree of the damper disposed in the low concentration exhaust gas outlet pipe, a high collection rate of PM In addition, problems such as deterioration in fuel consumption due to excessive pressure loss in the exhaust gas purification apparatus can be solved.

本発明に係る重油以下の低質燃料を使用する大排気量ディーゼルエンジン排ガス処理装置は又、管状捕集部の下流側にテーパ状に拡径するテーパ管状部又は該テーパ管状部に連なる大径管状部を設けることにより、高濃度排ガス流がテーパ管状部により徐々に減速され、大径管状部の内周面に連設した高濃度排ガス導出部にPMを確実に導入させることができる。更に、管状捕集部のテーパ管状部と該テーパ管状部に連なる大径管状部領域の内周面付近にまで放電電極を延長して設けた構成とすることにより、より効果的にPMを捕集することができ、排ガスのさらなる浄化をはかることができる。 The exhaust gas treatment apparatus for a large displacement diesel engine using low-quality fuel of heavy oil or less according to the present invention is also a tapered tubular portion that expands in a tapered shape downstream of the tubular collection portion or a large diameter continuous to the tapered tubular portion. By providing the tubular portion, the high-concentration exhaust gas flow is gradually decelerated by the tapered tubular portion, and PM can be reliably introduced into the high-concentration exhaust gas outlet portion continuously provided on the inner peripheral surface of the large-diameter tubular portion. Furthermore, the PM is more effectively captured by adopting a configuration in which the discharge electrode is extended to the vicinity of the inner peripheral surface of the tapered tubular portion of the tubular collecting portion and the large-diameter tubular portion region connected to the tapered tubular portion. The exhaust gas can be collected and the exhaust gas can be further purified.

更に本発明装置は、前記サイクロン捕集手段を、処理能力の異なる複数の接線式サイクロン、例えば小処理能力接線式サイクロン、中処理能力接線式サイクロン、大処理能力接線式サイクロンの3種類のサイクロンで構成するとともに、各接線式サイクロンの導入口に流量制御ダンパーを設けることにより、重油以下の低質燃料を使用する舶用大排気量ディーゼルエンジンにおける主機及び補機の並列運転や単独運転に伴う運転状況の変化やエンジンの負荷率の大きな変動による排気ガス流量の大幅な増減に応じて接線式サイクロンをより適正に選択使用することが可能となるのみならず、低濃度排ガス導出管に配設したダンパーと合わせて各接線式サイクロン毎に設けた流量制御ダンパーを制御することにより各接線式サイクロンへの排ガス流入速度をより適正に制御することが可能となる。又更に、前記接線式サイクロンと低濃度排ガス導出管との間に、接線式サイクロン通過後の浄化ガスを前記低濃度排ガスと合流させるための排出管を配設するとともに、該排出管にエアーノズル又はモータ駆動ファンを配置した構成とすることにより、接線式サイクロン通過後の浄化ガス流が増速吸引され、当該排ガス浄化装置での圧損もより改善され燃費の向上に寄与する。 Furthermore, in the present invention apparatus, the cyclone collecting means is composed of a plurality of tangential cyclones having different processing capacities, for example, three types of cyclones: a small processing capacity tangential cyclone, a medium processing capacity tangential cyclone, and a large processing capacity tangential cyclone. In addition, by installing a flow control damper at the inlet of each tangential cyclone, the operating situation associated with the parallel operation and independent operation of the main engine and auxiliary machinery in a large displacement diesel engine for ships that uses low quality fuel below heavy oil Not only can the tangential cyclone be more appropriately selected and used in response to a significant increase or decrease in exhaust gas flow rate due to changes or large fluctuations in the engine load factor, but also a damper installed in the low concentration exhaust gas outlet pipe In addition, by controlling the flow control damper provided for each tangential cyclone, the exhaust to each tangential cyclone is reduced. It is possible to control the flow rate more properly. Furthermore, a discharge pipe is provided between the tangential cyclone and the low-concentration exhaust gas outlet pipe to join the purified gas after passing the tangential cyclone with the low-concentration exhaust gas, and an air nozzle is provided in the exhaust pipe. Alternatively, by adopting a configuration in which the motor drive fan is arranged, the purified gas flow after passing through the tangential cyclone is sucked at a higher speed, and the pressure loss in the exhaust gas purification device is further improved, contributing to the improvement of fuel consumption.

本発明装置は又、前記管状捕集部をほぼ水平に配置した場合には、管状捕集部がエンジンが設置されている機関室の床面に対しほぼ一定の高さとなるので捕集管や放電電極等に対するメンテナンス時の作業性が良好となること、前記管状捕集部を前記床面に対しほぼ垂直かつ上向きに配置した場合には、該管状捕集部が煙突への排気管の配管を兼ねることができるので省スペースがはかられること、前記管状捕集部を前記床面に対しほぼ垂直かつ下向きに配置した場合には、落下するPMが捕集し易くなるのみならず、捕集壁面に付着したSOFやサルフェート等が液状化した場合、その液状成分が捕集壁面を流下し捕集し易い上、サルフェート等により腐食した重い酸化スケールが壁面から剥離し落下しても捕集し易いこと、等の利点が得られる。   In the present invention device, when the tubular collection part is arranged substantially horizontally, the tubular collection part is substantially constant with respect to the floor of the engine room where the engine is installed. When the maintenance work for the discharge electrode or the like is good, and when the tubular collecting part is arranged substantially vertically and upward with respect to the floor surface, the tubular collecting part is connected to the exhaust pipe to the chimney. Space can be saved, and when the tubular collection part is arranged substantially vertically and downward with respect to the floor surface, the falling PM is not only easily collected, but also captured. When SOF or sulfate adhering to the collecting wall liquefies, the liquid component easily flows down the collecting wall and collects even if heavy oxide scale corroded by the sulfate peels off from the wall and falls. Benefits such as easy to do It is.

本発明の第1実施例装置の全体構成を示す概略縦断面図である。It is a schematic longitudinal cross-sectional view which shows the whole structure of the 1st Example apparatus of this invention. 本発明の第2実施例装置の全体構成を示す概略縦断面図である。It is a schematic longitudinal cross-sectional view which shows the whole structure of the 2nd Example apparatus of this invention. 本発明の第3の実施例装置の要部を拡大して示す概略縦断面図である。It is a schematic longitudinal cross-sectional view which expands and shows the principal part of the 3rd Example apparatus of this invention. 本発明の第3の実施例装置の変形例の要部を拡大して示す概略縦断面図である。It is a schematic longitudinal cross-sectional view which expands and shows the principal part of the modification of the 3rd Example apparatus of this invention. 本発明の第4実施例装置の要部を拡大して示す概略縦断面図である。It is a schematic longitudinal cross-sectional view which expands and shows the principal part of the 4th Example apparatus of this invention. 図5のa−a線上の拡大断面図である。It is an expanded sectional view on the aa line of FIG. 本発明の第5の実施例装置の全体構成を一部省略して示す概略縦断面図である。It is a schematic longitudinal cross-sectional view which abbreviate | omits and shows a part of whole structure of the 5th Example apparatus of this invention. 本発明装置におけるサイクロン捕集手段の他の実施例を模式的に示す説明図である。It is explanatory drawing which shows typically the other Example of the cyclone collection means in this invention apparatus. 本発明装置における接線式サイクロン通過後の浄化ガスの増速吸引部を拡大して模式的に示す説明図で、(a)はエアーノズル方式、(b)はモータ駆動ファン方式をそれぞれ示す。FIG. 4 is an explanatory diagram schematically showing an enlarged speed-up suction portion of the purified gas after passing through a tangential cyclone in the apparatus of the present invention, where (a) shows an air nozzle system and (b) shows a motor-driven fan system. 本発明装置における管状捕集部をほぼ垂直かつ下向きに配置した例を示す概略図である。It is the schematic which shows the example which has arrange | positioned the tubular collection part in this invention apparatus substantially perpendicularly and downward. 本発明装置における管状捕集部をほぼ垂直かつ上向きに配置した例を示す概略図である。It is the schematic which shows the example which has arrange | positioned the tubular collection part in this invention apparatus substantially perpendicularly and upwards. 従来のディーゼルエンジン排ガス処理装置の一例を示す概略縦断面図である。It is a schematic longitudinal cross-sectional view which shows an example of the conventional diesel engine exhaust gas processing apparatus. 従来のディーゼルエンジン排ガス処理装置の他の例を示す概略縦断面図である。It is a schematic longitudinal cross-sectional view which shows the other example of the conventional diesel engine exhaust gas processing apparatus. 従来のディーゼルエンジン排ガス処理装置の別の例を示す概略縦断面図である。It is a schematic longitudinal cross-sectional view which shows another example of the conventional diesel engine exhaust gas processing apparatus. 従来のディーゼルエンジン排ガス処理装置の更に別の例を示す概略縦断面図である。It is a schematic longitudinal cross-sectional view which shows another example of the conventional diesel engine exhaust gas processing apparatus. 従来のディーゼルエンジン排ガス処理装置の更に別の例を一部破断して示す概略縦断面図である。It is a general | schematic longitudinal cross-sectional view which shows another example of the conventional diesel engine exhaust gas processing apparatus partially fractured | ruptured. 図16に示すディーゼルエンジン排ガス処理装置の部分拡大断面図である。It is a partial expanded sectional view of the diesel engine exhaust gas processing apparatus shown in FIG.

図1に本発明の第1の実施例装置として示す重油以下の低質燃料を使用する大排気量ディーゼルエンジン排ガス処理装置は、大きく分けて電気集塵手段を構成する管状捕集部1と分別捕集手段を構成する分別捕集部2とからなり、PM粒子を捕集するために設ける管状捕集部1は、集塵電極を構成する所定長さの、捕集壁面1−1kを有する捕集管1−1と排ガス中に含まれるPMに帯電させる放電電極1−2とを備えている。集塵電極を構成する捕集管1−1には、上流側(ディーゼルエンジン側)の端部に排ガス導入口1−1aを有し、下流側の端部の軸心付近にPMの低濃度排ガス導出管3を、下流側の端部の内周面付近にPMの高濃度排ガス導出部1−1bをそれぞれ連設している。放電電極1−2は、集塵電極を構成する捕集管1−1の軸心付近をほぼ全長にわたって延びる主電極1−2aと、該主電極1−2aの長手方向に所望の間隔で配設された放射状に突出する電極針1−2bの群とによって構成されている。このように構成された放電電極1−2は、捕集管1−1の排ガス導入口1−1a側に設けたシールエアー導入管部1−1cと、低濃度排ガス導出管3の入口部位に設けたシールエアー導入管部3−1に垂設した支持体4を介して主電極1−2aの両端部が支持されている。なお、図示しないが、放電電極1−2は必要に応じ捕集管1−1の内部より絶縁されたステーにより所望間隔を有して支持されている。又、放電電極1−2は外部に設置された高圧電源装置(図示せず)に配線されて制御された高圧電源の供給を受けている。 FIG. 1 shows an exhaust gas treatment apparatus for a large displacement diesel engine using a low-quality fuel equal to or less than heavy oil shown as the first embodiment of the present invention. The tubular collecting part 1 which is composed of a separate collecting part 2 constituting a collecting means and provided for collecting PM particles has a collecting wall surface 1-1k having a predetermined length constituting a dust collecting electrode. A collection tube 1-1 and a discharge electrode 1-2 for charging PM contained in the exhaust gas are provided. The collection tube 1-1 constituting the dust collection electrode has an exhaust gas introduction port 1-1a at an end portion on the upstream side (diesel engine side), and a low concentration of PM in the vicinity of the axial center of the downstream end portion. The exhaust gas outlet pipe 3 is provided with a PM high-concentration exhaust gas outlet portion 1-1b in the vicinity of the inner peripheral surface of the downstream end. The discharge electrode 1-2 is arranged at a desired interval in the longitudinal direction of the main electrode 1-2a extending substantially over the entire length around the axial center of the collection tube 1-1 constituting the dust collection electrode. And a group of electrode needles 1-2b protruding radially. The discharge electrode 1-2 configured as described above is provided at the inlet portion of the seal air introduction pipe portion 1-1c provided on the exhaust gas introduction port 1-1a side of the collection pipe 1-1 and the low concentration exhaust gas outlet pipe 3. Both ends of the main electrode 1-2a are supported through a support body 4 suspended from the provided seal air introduction pipe section 3-1. Although not shown, the discharge electrode 1-2 is supported at a desired interval by a stay insulated from the inside of the collecting tube 1-1 as necessary. Further, the discharge electrode 1-2 is supplied with a controlled high voltage power source by being wired to a high voltage power source device (not shown) installed outside.

前記排ガスの流れ方向における管状捕集部1の下流側に設けられた分別捕集部2は、分別手段としてのサイクロン捕集手段2−1により構成されている。このサイクロン捕集手段2−1は、捕集管1−1の高濃度排ガス導出部1−1bに連通管5−1を介して接続された1台の接線式サイクロン2−1aで構成され、さらに該接線式サイクロン2−1aと前記低濃度排ガス導出管3との間に、接線式サイクロン2−1a通過後の浄化ガスを低濃度排ガス導出管3内を流れる低濃度排ガスに合流させるための排出管6−1を配設している。又、前記低濃度排ガス導出管3には、接線式サイクロン2−1aへの高濃度排ガス流入量及び流入速度と低濃度排ガス放出量の流量調整を行うための流量制御ダンパー7を設けている。
なお、図1の鎖線部は、重油以下の低質燃料を使用する舶用大排気量ディーゼルエンジンにおける主機12と補機13の組合せを例示したものである。この重油以下の低質燃料を使用する舶用大排気量ディーゼルエンジンの場合、エンジン運転は主機12と補機13の並列運転及び各々単独運転があると共に各エンジンの負荷も大きく変動するため排気ガス流総量が大幅に変動する。又、重油以下の低質燃料を使用する大排気量エンジンの場合、前記前記捕集管1−1を複数並設(図面省略)する場合もある。
The fraction collection part 2 provided in the downstream of the tubular collection part 1 in the flow direction of the exhaust gas is composed of a cyclone collection means 2-1 as a separation means. The cyclone collecting means 2-1 is composed of one tangential cyclone 2-1a connected to the high concentration exhaust gas deriving portion 1-1b of the collecting pipe 1-1 via a communication pipe 5-1. Further, between the tangential cyclone 2-1a and the low concentration exhaust gas outlet pipe 3, the purified gas after passing through the tangential cyclone 2-1a is joined to the low concentration exhaust gas flowing in the low concentration exhaust gas outlet pipe 3. A discharge pipe 6-1 is provided. The low-concentration exhaust gas outlet pipe 3 is provided with a flow control damper 7 for adjusting the flow rate of the high-concentration exhaust gas flow rate and flow rate into the tangential cyclone 2-1a and the low-concentration exhaust gas discharge rate.
In addition, the chain line part of FIG. 1 illustrates the combination of the main engine 12 and the auxiliary machine 13 in the marine large displacement diesel engine which uses the low quality fuel below heavy oil . In the case of a marine large displacement diesel engine using a low quality fuel less than this heavy oil , the engine operation includes the parallel operation of the main engine 12 and the auxiliary machine 13 and the independent operation of each, and the load on each engine also varies greatly, so the exhaust gas flow total amount Will fluctuate significantly. Further, in the case of a large displacement engine using a low quality fuel less than heavy oil , a plurality of the collecting pipes 1-1 may be arranged in parallel (not shown).

図2に本発明の第2の実施例装置として示す重油以下の低質燃料を使用する大排気量ディーゼルエンジン排ガス処理装置は、サイクロン捕集手段2−1を2台の接線式サイクロン2−1aで構成した以外は前記第1の実施例装置と同様の構成を有するものである。即ち、捕集管1−1の高濃度排ガス導出部1−1bに連通管5−1、5−2を介して2台の接線式サイクロン2−1aを並列的に接続してサイクロン捕集手段2−1を構成するとともに、この場合も各接線式サイクロン2−1a通過後の浄化ガスをそれぞれ低濃度排ガス導出管3内を流れる低濃度排ガスに合流させるための排出管6−1、6−2を配設している。 FIG. 2 shows an exhaust gas treatment apparatus for a large displacement diesel engine using low quality fuel less than heavy oil shown as the second embodiment of the present invention. The exhaust gas treatment apparatus for a large displacement diesel engine includes two tangential cyclones 2-1a. Except for the configuration described above, the configuration is the same as that of the first embodiment apparatus. That is, two tangential cyclones 2-1a are connected in parallel to the high-concentration exhaust gas deriving portion 1-1b of the collecting pipe 1-1 via the communication pipes 5-1, 5-2, and the cyclone collecting means. In this case, the exhaust pipes 6-1, 6- 6 for joining the purified gas after passing through each tangential cyclone 2-1a to the low-concentration exhaust gas flowing in the low-concentration exhaust gas outlet pipe 3 respectively. 2 is disposed.

上記図1、図2に示す重油以下の低質燃料を使用する大排気量ディーゼルエンジン排ガス処理装置において、排ガス導入口1−1aより捕集管1−1内に流入した排ガス中のPMは、集塵電極を構成する当該捕集管1−1の内壁である捕集壁面1−1kと放電電極1−2との間における放電によって帯電されるので、帯電されたPM粒子はクーロン力によって捕集壁面1−1kに捕集される。捕集管1−1の捕集壁面1−1kに捕集されたPM粒子には時間の経過と共に軸心付近の排気ガス流から捕集されたPM粒子が更に堆積されて次第に成長して塊状となり、このPM塊が排気流による剥離と放電(帯電)に伴うクーロン力による管状の捕集壁面1−1kへの再付着を繰返しながら捕集壁面の近傍を濃縮されながら流れていくことによりPMを高濃度に含んだ排ガス流となると同時に、捕集管1−1のほぼ軸心部付近を流れる排ガス中のPMは捕集壁面1−1kに捕集されて次第に希薄化されて低濃度にしかPMを含まない排ガス流となって下流へ流れていく。即ち、排ガス導入口1−1aより捕集管1−1内に流入した排ガスは、管状捕集部1を流下する過程においてPMの高濃度排ガス流と低濃度排ガス流に分離され、捕集管1−1内壁の捕集壁面1−1kの近傍を高濃度排ガス流が、捕集管1−1のほぼ軸心部付近を低濃度排ガス流となって捕集管1−1の下流へ流れていく。そして、図1に示す重油以下の低質燃料を使用する大排気量ディーゼルエンジン排ガス処理装置の場合は、捕集管1−1の下流において、捕集管1−1内壁の捕集壁面1−1k近傍を流れてきたPMの高濃度排ガス流は、該捕集管1−1の高濃度排ガス導出部1−1bより連通管5−1を介して接線式サイクロン2−1aに導入されてPMが遠心分離され、図2に示す重油以下の低質燃料を使用する大排気量ディーゼルエンジン排ガス処理装置の場合は、捕集管1−1内壁の捕集壁面1−1k近傍を流れてきた高濃度排ガス流は、該捕集管1−1の高濃度排ガス導出部1−1bより連通管5−1、5−2を介して2台の接線式サイクロン2−1aに導入されてPMが遠心分離される。一方、捕集管1−1のほぼ軸心部付近を流れるPMの低濃度排ガス流は、図1、図2に示す重油以下の低質燃料を使用する大排気量ディーゼルエンジン排ガス処理装置共に該捕集管1−1のほぼ軸心部付近に設置された低濃度排ガス導出管3を通して外部へ放出される。又、前記接線式サイクロン2−1aで浄化された排ガス流は、それぞれ排出管6−1、6−1及び6−2を介して低濃度排ガス導出管3内を流れる低濃度排ガス流に合流される。
なお、サイクロン捕集手段2−1を2台の接線式サイクロン2−1aで構成した図2に示す重油以下の低質燃料を使用する大排気量ディーゼルエンジン排ガス処理装置の場合は、高濃度排ガス導出部1−1bより排出される高濃度排ガス流の流量に応じて使用する台数を設定すればよく、又、2台の接線式サイクロン2−1aを交互に使用することもできる。
In the exhaust gas treatment apparatus for a large displacement diesel engine using low quality fuel less than heavy oil shown in FIGS. 1 and 2, PM in the exhaust gas flowing into the collection pipe 1-1 from the exhaust gas inlet 1-1a is Since it is charged by the discharge between the collection wall 1-1k, which is the inner wall of the collection tube 1-1 constituting the dust collection electrode, and the discharge electrode 1-2, the charged PM particles are captured by the Coulomb force. Collected on the collecting wall 1-1k. The PM particles collected on the collection wall surface 1-1k of the collection tube 1-1 are further accumulated with the PM particles collected from the exhaust gas flow near the axis with the passage of time, and gradually grow to form a lump. This PM mass flows while being concentrated in the vicinity of the collection wall surface while repeatedly adhering to the tubular collection wall surface 1-1k by the Coulomb force due to separation and discharge (charging) due to the exhaust flow. As a result, the PM in the exhaust gas flowing in the vicinity of the axial center of the collection pipe 1-1 is collected on the collection wall 1-1k and gradually diluted to a low concentration. However, it becomes an exhaust gas flow containing only PM and flows downstream. That is, the exhaust gas flowing into the collection pipe 1-1 from the exhaust gas introduction port 1-1a is separated into a PM high-concentration exhaust gas stream and a low-concentration exhaust gas stream in the process of flowing down the tubular collection section 1, and the collection pipe 1-1 The high-concentration exhaust gas flow near the collection wall surface 1-1k of the inner wall becomes a low-concentration exhaust gas flow near the axial center of the collection tube 1-1 and flows downstream of the collection tube 1-1. To go. And in the case of the exhaust gas treatment apparatus for a large displacement diesel engine using the low quality fuel below the heavy oil shown in FIG. 1, the collection wall surface 1- 1 of the inner wall of the collection tube 1-1 is downstream of the collection tube 1-1. The high-concentration exhaust gas flow of PM flowing in the vicinity of 1k is introduced into the tangential cyclone 2-1a from the high-concentration exhaust gas deriving unit 1-1b of the collection pipe 1-1 through the communication pipe 5-1, and PM. In the case of an exhaust gas treatment device for a large displacement diesel engine that uses a low-quality fuel equal to or less than heavy oil shown in FIG. 2, the high flow that has flowed in the vicinity of the collection wall 1-1k of the inner wall of the collection tube 1-1 Concentrated exhaust gas flow is introduced into the two tangential cyclones 2-1a from the high concentration exhaust gas deriving unit 1-1b of the collection pipe 1-1 through the communication pipes 5-1, 5-2, and the PM is centrifuged. To be separated. On the other hand, the PM low-concentration exhaust gas flow that flows almost in the vicinity of the axial center of the collection pipe 1-1 is the same as that of the exhaust gas treatment apparatus for large-displacement diesel engines using low-quality fuel below heavy oil shown in FIGS. It is discharged to the outside through the low-concentration exhaust gas outlet pipe 3 installed in the vicinity of the axial center of the collection pipe 1-1. The exhaust gas flow purified by the tangential cyclone 2-1a is joined to the low-concentration exhaust gas flow flowing through the low-concentration exhaust gas outlet pipe 3 through the exhaust pipes 6-1, 6-1 and 6-2, respectively. The
In the case of the exhaust gas treatment apparatus for a large displacement diesel engine using the low quality fuel below the heavy oil shown in FIG. 2 in which the cyclone collecting means 2-1 is constituted by two tangential cyclones 2-1a, a high concentration exhaust gas is used. What is necessary is just to set the number of units used according to the flow volume of the high concentration exhaust gas flow discharged | emitted from the derivation | leading-out part 1-1b, and can also use two tangential type cyclones 2-1a alternately.

上記のように、図1、図2に示す本願発明の重油以下の低質燃料を使用する大排気量ディーゼルエンジン排ガス処理装置の場合は、PMの高濃度排ガスのみ(全排ガス量の一部)をサイクロンへ導くことができるので、小型のサイクロンで効率よくPMを捕集・分別回収することができる。 As described above, in the case of the exhaust gas treatment device for a large displacement diesel engine using the low quality fuel of the present invention or less shown in FIG. 1 and FIG. 2, only high concentration exhaust gas of PM (a part of the total exhaust gas amount) Therefore, PM can be efficiently collected and separated and collected with a small cyclone.

次に、図3に第3の実施例装置として示す重油以下の低質燃料を使用する大排気量ディーゼルエンジン排ガス処理装置は、管状捕集部1の集塵電極を構成する捕集管1−1の下流側端部にテーパ状に拡径するテーパ管状部1−1dと該テーパ管状部に連なる大径管状部1−1eを形成し、前記大径管状部1−1eの軸心部付近に低濃度排ガス導出管3と内周面付近に高濃度排ガス導出部1−1bを連設した構成とした以外は、前記図1又は図2に示す重油以下の低質燃料を使用する大排気量ディーゼルエンジン排ガス処理装置と同様の構成を有するものである。かかる構成の重油以下の低質燃料を使用する大排気量ディーゼルエンジン排ガス処理装置の場合は、捕集管1−1の下流側端部において、高濃度排ガス流がテーパ管状部1−1dにより徐々に減速され、大径管状部1−1e内周面付近に連設した高濃度排ガス導出部1−1bにPMを確実に導入させることができる。なお、放電電極1−2の電極針1−2dは、捕集管1−1の下流側端部のテーパ管状部1−1bにまで連続して設けると更に好ましい。 Next, an exhaust gas treatment apparatus for a large displacement diesel engine using low quality fuel equal to or lower than heavy oil shown as the third embodiment apparatus in FIG. 3 is a collection pipe 1-constituting a dust collection electrode of the tubular collection section 1. 1 is formed with a tapered tubular portion 1-1d having a tapered diameter and a large-diameter tubular portion 1-1e connected to the tapered tubular portion, and in the vicinity of the axial center portion of the large-diameter tubular portion 1-1e. low concentrations except that the exhaust gas outlet pipe 3 and configuration provided continuously high concentration exhaust gas outlet portion 1-1b near the inner circumferential surface, a large amount of the exhaust gas using the following low quality heavy fuel oil as shown in FIG. 1 or FIG. 2 It has the same configuration as the exhaust gas treatment device for diesel engines. In the case of an exhaust gas treatment device for a large displacement diesel engine that uses a low-quality fuel of heavy oil or less having such a configuration, a high-concentration exhaust gas flow is gradually caused by a tapered tubular portion 1-1d at the downstream end of the collection tube 1-1. Therefore, PM can be surely introduced into the high concentration exhaust gas deriving portion 1-1b provided in the vicinity of the inner peripheral surface of the large diameter tubular portion 1-1e. It is more preferable that the electrode needle 1-2d of the discharge electrode 1-2 is continuously provided up to the tapered tubular portion 1-1b at the downstream end of the collection tube 1-1.

又、上記図3に示す重油以下の低質燃料を使用する大排気量ディーゼルエンジン排ガス処理装置において、図4に示すように捕集管1−1を下向きに垂直配置とした場合には、大径管状部1−1eの底壁面1−1e´を図示のように連通管5−1側へ下降傾斜させる。かかる手段をこうじるのは、落下したSOF、サルフェート等の液状成分をサイクロン側へ流下させて捕集し易くするためと、捕集管1−1内面の捕集壁面1−1kがPMやサルフェート等により腐食して酸化スケール(金属酸化スケール等)が発生した場合に、該捕集壁面1−1kから剥離した前記酸化スケールも捕集し易くするためである。 Further, in the exhaust gas treatment apparatus for a large displacement diesel engine using the low quality fuel below the heavy oil shown in FIG. 3, when the collection pipe 1-1 is vertically arranged as shown in FIG. The bottom wall surface 1-1e 'of the radial tubular portion 1-1e is inclined downward toward the communication tube 5-1 as shown in the drawing. This means is used to make it easier for liquid components such as SOF and sulfate to flow down to the cyclone and to collect them, and the collection wall surface 1-1k on the inner surface of the collection tube 1-1 is made of PM, sulfate, etc. This is to make it easier to collect the oxide scale peeled off from the collection wall surface 1-1k when an oxide scale (metal oxide scale or the like) is generated due to corrosion due to the above.

又、図5、図6に第4の実施例装置として示す重油以下の低質燃料を使用する大排気量ディーゼルエンジン排ガス処理装置は、管状捕集部1の集塵電極を構成する捕集管1−1の下流側端部にテーパ状に拡径するテーパ管状部1−1dと該テーパ管状部に連なる大径管状部1−1eを形成し、前記大径管状部1−1eの軸心部付近に低濃度排ガス導出管3と内周面付近に高濃度排ガス導出部1−1bを連設した構成とし、更に前記テーパ管状部1−1dと該テーパ管状部に連なる大径管状部1−1eの領域にまで放電電極1−2の主電極1−2a及び電極針1−2bを延長して設けた構成とした以外は、前記図1又は図2に示す重油以下の低質燃料を使用する大排気量ディーゼルエンジン排ガス処理装置と同様の構成を有するものである。なお、図中の1−2cは、複数に分岐された放電電極1−2の各々を支持する支持リングである。
かかる構成の重油以下の低質燃料を使用する大排気量ディーゼルエンジン排ガス処理装置の場合は、捕集管1−1の下流側端部において、高濃度排ガス流がテーパ管状部1−1dにより徐々に減速されるのでより効果的にPMを捕集することができるのみならず、大径管状部1−1eに流入してからもPM塊が成長してサイクロン捕集手段2−1での捕集効率をより高めて排ガスの更なる浄化をはかることができる。
Moreover, the exhaust gas treatment apparatus for a large displacement diesel engine using a low quality fuel equal to or less than heavy oil shown as the fourth embodiment apparatus in FIGS. 5 and 6 is a collection pipe constituting the dust collection electrode of the tubular collection section 1. 1-1, a tapered tubular portion 1-1d whose diameter is increased in a tapered shape and a large-diameter tubular portion 1-1e connected to the tapered tubular portion are formed at the downstream end of 1-1, and the axial center of the large-diameter tubular portion 1-1e A low-concentration exhaust gas outlet pipe 3 and a high-concentration exhaust gas outlet part 1-1b are connected in the vicinity of the inner peripheral surface, and the tapered tubular part 1-1d and the large-diameter tubular part 1 connected to the tapered tubular part. 1e, except that the main electrode 1-2a and the electrode needle 1-2b of the discharge electrode 1-2 are extended to the region 1e, and the low quality fuel below the heavy oil shown in FIG. 1 or 2 is used. those having the same configuration as the large engine diesel engine exhaust gas treatment apparatus for In addition, 1-2c in a figure is a support ring which supports each of the discharge electrode 1-2 branched into plurality.
In the case of an exhaust gas treatment device for a large displacement diesel engine that uses a low-quality fuel of heavy oil or less having such a configuration, a high-concentration exhaust gas flow is gradually caused by a tapered tubular portion 1-1d at the downstream end of the collection tube 1-1. In addition to being able to collect PM more effectively, the PM mass grows even after flowing into the large-diameter tubular portion 1-1e and is captured by the cyclone collecting means 2-1. The exhaust gas can be further purified by increasing the collection efficiency.

更に、図7に第5の実施例装置として示す重油以下の低質燃料を使用する大排気量ディーゼルエンジン排ガス処理装置は、捕集管1−1の手前に排ガス導入室1−1f、及び前記排ガス導入室1−1fと捕集管1−1との間に絞り部1−1gとテーパ拡径部1−1hを設けると共に、前記絞り部1−1gとテーパ拡径部1−1hにも電極針1−2bを設け、前記排ガス導入室1−1fへの排ガス導入口1−1aと、シールエアー導入室1−1iへのシールエアー導入口1−1jを、それぞれ対向させて設けた構成となしたものである。
かかる構成の重油以下の低質燃料を使用する大排気量ディーゼルエンジン排ガス処理装置において、捕集管1−1の長さをL、捕集管1−1の内径をDとした場合、3D≦L≦15D、好ましくは5D≦L≦10Dの条件を満足させるのが好ましい。その理由は、3D未満では排ガスの流れが整流しきれずに乱れがおさまりきれないので、捕集壁面1−1k部でのPMの濃化が促進されず、他方、15Dを超えると濃化の程度に差がなく、装置の大型化を招きスペース効率が悪化するためである。又、好ましい条件として5D≦L≦10Dとしたのは、5D以上であれば流れは特によく整流されて捕集壁面1−1k部付近へのPMの濃化が安定し、10D以内で濃化の程度に差が少なくなり実用上の効果が得られるので装置の大型化を抑制できるためである。なお、各部の寸法の一例を具体的に示すと、捕集管1−1の長さLは3m、捕集管1−1の内径はφ400mmでLとDの関係は5D≦L≦10Dの条件を満足するL=7.5Dであり、絞り部1−1gの長さは375mm、絞り部1−1gの内径はφ220mm、テーパ拡径部1−1hのテーパ角θは30度である。
更に、排ガス導入口1−1aより排ガス導入室1−1fへ流入された排ガスは、絞り部1−1gを経由することによりテーパ拡径部1−1hを経た排ガス流の乱れが抑制されてガス流れが速やかに安定化して捕集管内壁の捕集壁面1−1kでの濃化と捕集管軸心付近での希薄化が促進される。しかも絞り部1−1gにおいては、電極と粒子間距離が短いので全粒子を確実に帯電させることができて粒子を捕集管内壁の捕集壁面1−1kに付着させて捕集性能の向上がはかれる。なお、排ガスを対向させて排ガス導入室1−1fへ流入させることとしたのは、対称的に捕集管1−1へ流入させることにより排ガス流の流れのバランスが取れて排ガス流の乱れが少なくなって速やかに整流され、短い軸方向長さの流れでありながら良く整流されて好ましいからである。又、電極に対するシールエアーも対向させてシールエアー導入室1−1iに流入させると同様に好ましい。
Furthermore, an exhaust gas treatment apparatus for a large displacement diesel engine using low quality fuel less than heavy oil shown as a fifth embodiment apparatus in FIG. 7 includes an exhaust gas introduction chamber 1-1f in front of the collection pipe 1-1, A throttle part 1-1g and a taper enlarged part 1-1h are provided between the exhaust gas introduction chamber 1-1f and the collecting pipe 1-1, and the throttle part 1-1g and the taper enlarged part 1-1h are also provided. An electrode needle 1-2b is provided, and an exhaust gas introduction port 1-1a to the exhaust gas introduction chamber 1-1f and a seal air introduction port 1-1j to the seal air introduction chamber 1-1i are provided to face each other. It is what became.
In an exhaust gas treatment apparatus for a large displacement diesel engine using a low quality fuel of heavy oil or less having such a configuration, when the length of the collection pipe 1-1 is L and the inner diameter of the collection pipe 1-1 is D, 3D ≦ It is preferable to satisfy the condition of L ≦ 15D, preferably 5D ≦ L ≦ 10D. The reason is that if the flow is less than 3D, the flow of exhaust gas cannot be rectified and the turbulence cannot be suppressed, so the concentration of PM at the collecting wall 1-1k portion is not promoted. This is because the size of the apparatus is increased and the space efficiency is deteriorated. In addition, 5D ≦ L ≦ 10D as a preferable condition is that if 5D or more, the flow is particularly well rectified and the concentration of PM near the collecting wall 1-1k is stable, and the concentration is within 10D. This is because the size of the apparatus can be suppressed and the increase in size of the apparatus can be suppressed. In addition, when an example of the dimension of each part is shown concretely, the length L of the collection tube 1-1 is 3 m, the inner diameter D of the collection tube 1-1 is φ400 mm , and the relationship between L and D is 5D ≦ L ≦ 10D L = 7.5D satisfying the above condition, the length of the throttle part 1-1g is 375 mm, the inner diameter of the throttle part 1-1g is φ220 mm, and the taper angle θ of the taper enlarged part 1-1h is 30 degrees. .
Further, the exhaust gas flowing into the exhaust gas introduction chamber 1-1f from the exhaust gas introduction port 1-1a is prevented from being disturbed by the exhaust gas flow through the tapered enlarged portion 1-1h through the throttle portion 1-1g. The flow is quickly stabilized and the concentration of the inner wall of the collecting tube at the collecting wall surface 1-1k and the dilution near the collecting tube axis are promoted. In addition, since the distance between the electrode and the particle is short in the narrowed portion 1-1g, all the particles can be reliably charged, and the particles are attached to the collecting wall surface 1-1k of the inner wall of the collecting tube to improve the collecting performance. Is peeled off. The reason why the exhaust gas is opposed to flow into the exhaust gas introduction chamber 1-1f is that the flow of the exhaust gas flow is balanced by causing the exhaust gas to flow into the collection pipe 1-1 symmetrically, and the disturbance of the exhaust gas flow is caused. This is because the flow is reduced and quickly rectified, and is well rectified while having a short axial length. Further, it is also preferable that the seal air with respect to the electrode is made to face and flow into the seal air introduction chamber 1-1i.

次に、図8に示すサイクロン捕集手段は、処理能力の異なる複数の接線式サイクロン、例えば小処理能力接線式サイクロン2−1b、中処理能力接線式サイクロン2−1c、大処理能力接線式サイクロン2−1dの3種類のサイクロンで構成したもので、捕集管1−1の高濃度排ガス導出部1−1bに放射状位置に接続した連通管8−1、8−2、8−3を介して各接線式サイクロン2−1b、2−1c、2−1dを接続し、前記各連通管8−1、8−2、8−3の高濃度排ガス導入口に流量制御ダンパー9−1、9−2、9−3を設けた構成となしたものである。
このように処理能力の異なる複数の接線式サイクロンでサイクロン捕集手段を構成した場合には、舶用大排気量ディーゼルエンジンにおける主機及び補機の並列運転や単独運転に伴う運転状況の変化やエンジンの負荷率に応じて変化する排気ガス流量に対応して各接線式サイクロンをより適正に選択使用することが可能となるのみならず、低濃度排ガス導出管3に配設したダンパーと合わせて各接線式サイクロン毎に設けた流量制御ダンパー9−1、9−2、9−3を制御することにより各接線式サイクロンへの排ガスの流入接線速度をより適正に制御することが可能となり、高い捕集効率を広いエンジン負荷率の範囲等において確保、維持することができる。
Next, the cyclone collecting means shown in FIG. 8 includes a plurality of tangential cyclones having different throughputs, for example, a small throughput tangential cyclone 2-1b, a medium throughput tangential cyclone 2-1c, and a large throughput tangential cyclone. It is composed of three types of cyclones 2-1d, and is connected to communication pipes 8-1, 8-2, and 8-3 connected to the high concentration exhaust gas deriving portion 1-1b of the collecting pipe 1-1 in a radial position. The tangential cyclones 2-1b, 2-1c, and 2-1d are connected to the high-concentration exhaust gas inlets of the communication pipes 8-1, 8-2, and 8-3. -2 and 9-3.
In this way, when the cyclone collecting means is composed of a plurality of tangential cyclones with different processing capacities, changes in the operating conditions accompanying the parallel operation and independent operation of the main engine and auxiliary machinery in a large displacement diesel engine for ships, Each tangential cyclone can be selected and used more appropriately in response to the exhaust gas flow rate that changes in accordance with the load factor, and each tangent is combined with a damper disposed in the low concentration exhaust gas outlet pipe 3. By controlling the flow control dampers 9-1, 9-2, 9-3 provided for each type cyclone, it becomes possible to more appropriately control the inflow tangential speed of the exhaust gas to each tangential type cyclone, and high collection Efficiency can be secured and maintained over a wide range of engine load factors.

又、図9(a)(b)に示すように接線式サイクロン通過後の浄化ガスを前記低濃度排ガスと合流させるために配設した排出管6−1に、接線式サイクロン通過後の浄化ガスを増速吸引するためのエアーノズル10又はモータ11−1にて駆動されるファン11を設置することにより、接線式サイクロン通過後の浄化ガス流に運動エネルギーが付与されて増速吸引され、当該排ガス浄化装置での圧損もより小さくなるよう改善されて燃費を向上させることができる。   Further, as shown in FIGS. 9 (a) and 9 (b), the purified gas after passing through the tangential cyclone is connected to a discharge pipe 6-1 arranged to join the purified gas after passing through the tangential cyclone with the low-concentration exhaust gas. By installing the air nozzle 10 for speeding up suction or the fan 11 driven by the motor 11-1, the purified gas flow after passing through the tangential cyclone is given kinetic energy and suctioned at a speed, It is improved so that the pressure loss in the exhaust gas purifying apparatus is also reduced, and the fuel consumption can be improved.

更に又、図10、図11はそれぞれ本発明装置における管状捕集部1、例えば図3〜図5に示す捕集管1−1の下流側端部にテーパ状に拡径する1−1eを有する管状捕集部1を機関室床面に対しほぼ垂直に配置した場合を例示したもので、図10は前記管状捕集部1をほぼ垂直かつ下向きに配置した例、図11は前記管状捕集部1をほぼ垂直かつ上向きに配置した例をそれぞれ示す。ここで、図10に示すように管状捕集部1をほぼ垂直かつ下向きに配置した場合には、該管状捕集部1が煙突(図示せず)への排気管の配管を兼ねることができるので省スペースがはかられる利点がある。一方、図11に示すように管状捕集部1を垂直かつ上向きに配置した場合には、落下するPMが捕集し易くなるのみならず、捕集壁面に付着したSOFやサルフェート等が液状化した場合、その液状成分が捕集壁面を流下し捕集し易い上、サルフェート等により腐食した重い酸化スケールが壁面から剥離し落下しても捕集し易い利点がある。なお、管状捕集部1をほぼ水平に配置した場合には、管状捕集部1がエンジンが設置されている機関室の床面に対しほぼ一定の高さとなるので捕集管や放電電極等に対するメンテナンス時の作業性が良好となる利点がある。   Further, FIGS. 10 and 11 respectively show a tubular collecting portion 1 in the apparatus of the present invention, for example, 1-1e that expands in a taper shape at the downstream end of the collecting tube 1-1 shown in FIGS. FIG. 10 shows an example in which the tubular collecting part 1 is arranged substantially perpendicular to the engine room floor, FIG. 10 shows an example in which the tubular collecting part 1 is arranged substantially vertically and downward, and FIG. 11 shows the tubular collecting part. An example in which the collecting unit 1 is arranged substantially vertically and upward is shown. Here, as shown in FIG. 10, when the tubular collection part 1 is arranged substantially vertically and downward, the tubular collection part 1 can also serve as an exhaust pipe piping to a chimney (not shown). Therefore, there is an advantage that space saving can be taken. On the other hand, when the tubular collecting portion 1 is arranged vertically and upward as shown in FIG. 11, not only the falling PM is easily collected, but also SOF, sulfate, etc. adhering to the collecting wall surface are liquefied. In this case, there is an advantage that the liquid component easily flows down the collecting wall surface and is easily collected even if a heavy oxide scale corroded by sulfate or the like peels off from the wall surface and falls. In addition, when the tubular collection part 1 is arrange | positioned substantially horizontal, since the tubular collection part 1 becomes substantially constant height with respect to the floor surface of the engine room in which the engine is installed, a collection tube, a discharge electrode, etc. There is an advantage that workability during maintenance is good.

本発明に係る大排気量ディーゼルエンジン排ガス処理装置は、予めPMが濃縮されて高濃度化された全排ガス量の一部の流れをサイクロンへ導入して排ガスを浄化する方式であるから、サイクロンを小型化できる上、サイクロン捕集手段を複数の接線式サイクロンで構成し、高濃度排ガス導出部より排出されるPMの高濃度排ガス流を当該排ガスの流量に応じて選択的に該接線式サイクロンへ導入する方式となすことにより、軸流式サイクロンより捕集性能の優れた接線式サイクロンの作用効果に加え、重油以下の低質燃料を使用する舶用大排気量ディーゼルエンジンにおける主機及び補機の並列運転や単独運転に伴う運転状況の変化やエンジンの負荷率の変動に伴う排気ガス流量(流速)の大幅な増減に応じて接線式サイクロンの処理能力と台数とのバランスを取りながら適正に選択することが可能となり、排ガス流量の各変化に対応してPMの高い捕集率を確保、維持することができ、又、低濃度排ガス導出管に配設したダンパーの開度を制御することにより前記接線式サイクロンへの排ガスの流入接線速度を適正に制御することができるので、PMの高い捕集率を確保、維持しかつ当該排ガス浄化装置での過大な圧損による燃費の悪化等の問題も解消することができる等、多くの優れた効果を奏することから、舶用、車両用、産業用等の各種用途の重油以下の低質燃料を使用する重油以下の低質燃料を使用する大排気量ディーゼルエンジン排ガスの浄化処理に大きく寄与する。 Since the exhaust gas treatment apparatus for a large displacement diesel engine according to the present invention is a system for purifying exhaust gas by introducing a partial flow of the total exhaust gas amount, which has been concentrated in advance and enriched, into the cyclone. The cyclone collecting means is composed of a plurality of tangential cyclones, and the high concentration exhaust gas flow of PM discharged from the high concentration exhaust gas deriving section is selectively selected according to the flow rate of the exhaust gas. In addition to the effects of a tangential cyclone with better collection performance than an axial flow type cyclone, the main engine and auxiliary machine in a large displacement diesel engine for marine engines that use low quality fuel below heavy oil can be used in parallel. Processing capacity of tangential cyclone in response to a drastic increase or decrease in exhaust gas flow rate (velocity) due to changes in operating conditions due to operation or single operation or fluctuations in engine load factor It is possible to make a proper selection while balancing the number of units and the number of units to ensure and maintain a high PM collection rate corresponding to each change in the exhaust gas flow rate. By controlling the opening of the installed damper, the inflow tangential speed of the exhaust gas to the tangential cyclone can be controlled appropriately, so that a high PM collection rate is secured and maintained and the exhaust gas purification device Since it has many excellent effects, such as the problem of deterioration of fuel consumption due to excessive pressure loss can be solved, it is less than heavy oil using low quality fuel less than heavy oil for various uses such as marine, vehicle, industrial etc. This greatly contributes to the purification of exhaust gas for large displacement diesel engines that use low quality fuel .

1 管状捕集部
1−1 捕集管
1−1a 排ガス導入口
1−1b 高濃度排ガス導出部
1−1c シールエアー導入管部
1−1d テーパ管状部
1−1e 大径管状部
1−1f 排ガス導入室
1−1g 絞り部
1−1h テーパ拡径部
1−1i シールエアー導入室
1−1j シールエアー導入口
1−1k 捕集壁面
1−2 放電電極
1−2a 主電極
1−2b 電極針
1−2c 支持リング
2 分別捕集部
2−1 サイクロン捕集手段
2−1a 接線式サイクロン
2−1b 小処理能力接線式サイクロン
2−1c 中処理能力接線式サイクロン
2−1d 大処理能力接線式サイクロン
3 低濃度排ガス導出管
3−1 シールエアー導入管部
4 支持体
5−1、5−2、8−1、8−2、8−3 連通管
6−1、6−2 排出管
7、9−1、9−2、9−3 流量制御ダンパー
10 エアーノズル
11 ファン
11−1 モータ
12 主機
13 補機
DESCRIPTION OF SYMBOLS 1 Tubular collection part 1-1 Collection pipe 1-1a Exhaust gas inlet 1-1b High concentration exhaust gas extraction part 1-1c Seal air introduction pipe part 1-1d Tapered tubular part 1-1e Large diameter tubular part 1-1f Exhaust gas Introduction chamber 1-1g Restriction portion 1-1h Tapered diameter expansion portion 1-1i Seal air introduction chamber 1-1j Seal air introduction port 1-1k Collection wall surface 1-2 Discharge electrode 1-2a Main electrode 1-2b Electrode needle 1 -2c Support ring 2 Separation collection part 2-1 Cyclone collection means 2-1a Tangential cyclone 2-1b Small throughput tangential cyclone 2-1c Medium throughput tangential cyclone 2-1d Large throughput tangential cyclone 3 Low concentration exhaust gas outlet pipe 3-1 Seal air introduction pipe section 4 Support body 5-1, 5-2, 8-1, 8-2, 8-3 Communication pipe 6-1, 6-2 Discharge pipe 7, 9- 1, 9-2, 9-3 Flow rate Please damper 10 air nozzle 11 fan 11-1 motor 12 main engine 13 auxiliary

Claims (6)

重油以下の低質燃料を使用する大排気量ディーゼルエンジンの排ガス中に含まれる粒状物質に帯電させる放電電極、及び帯電された前記粒状物質を捕集する集塵電極を構成する所定長さの管状捕集部を有し、かつ前記放電電極は前記管状捕集部を構成する捕集管内に管軸方向に配設された主電極と該主電極に間隔配設された放射状に突出する複数本の電極針とによって構成された電気集塵手段と、前記管状捕集部から剥離した粒状物質を分別して捕集するサイクロン方式の分別捕集手段を備えたディーゼルエンジン排ガス処理装置において、前記管状捕集部の下流側の軸心付近に粒状物質の低濃度排ガス導出管を、同管状捕集部の下流側の内周面付近に高濃度排ガス導出部をそれぞれ設け、粒状物質の高濃度排ガス導出部に前記粒状物質を捕集するサイクロン捕集手段を連設するとともに、該サイクロン捕集手段を接線式サイクロンで構成し、前記低濃度排ガス導出管に配設したダンパーの開度を制御することにより前記接線式サイクロンへの排ガス流入速度を制御する仕組みとなし、さらに前記捕集管の長さをL、該捕集管の内径をDとした場合、その関係が5D≦L≦15Dの条件を満たすことを特徴とする重油以下の低質燃料を使用する大排気量ディーゼルエンジン排ガス処理装置。 A tubular electrode of a predetermined length that constitutes a discharge electrode for charging particulate matter contained in the exhaust gas of a large displacement diesel engine using heavy oil or lower quality fuel, and a dust collecting electrode for collecting the charged particulate matter. It has a collecting unit, and the discharge electrode is a plurality of radially protruding, which is the interval provided to the main electrode and the main electrode disposed in the pipe axis direction in the collecting tube constituting the tubular collecting part In the exhaust gas treatment apparatus for a diesel engine, comprising: the electrostatic dust collecting means constituted by the electrode needles; and the cyclone type separation collecting means for separating and collecting the particulate matter separated from the tubular collecting portion. A particulate matter low-concentration exhaust gas outlet pipe is provided in the vicinity of the shaft downstream of the collection part, and a high-concentration exhaust gas outlet part is provided in the vicinity of the inner peripheral surface downstream of the tubular collection part. The granular material in the outlet The cyclone collecting means to be collected is connected continuously, the cyclone collecting means is constituted by a tangential cyclone, and the opening degree of the damper disposed in the low-concentration exhaust gas outlet pipe is controlled to thereby connect the cyclone collecting means to the tangential cyclone. it such a mechanism for controlling the exhaust gas inflow rate, further the length of the collecting tube L, if the inner diameter of the collecting tube was D, a feature that the relationship of 5D ≦ L ≦ 15D satisfy Exhaust gas treatment equipment for large-displacement diesel engines that uses low-quality fuel that is less than heavy oil . 前記サイクロン捕集手段を複数の接線式サイクロンで構成し、前記高濃度排ガス導出部より排出される高濃度排ガスを当該排ガスの流量に応じて選択的に前記接線式サイクロンへ導入する方式となすことを特徴とする請求項1に記載の重油以下の低質燃料を使用する大排気量ディーゼルエンジン排ガス処理装置。 The cyclone collecting means is composed of a plurality of tangential cyclones, and the high concentration exhaust gas discharged from the high concentration exhaust gas deriving section is selectively introduced into the tangential cyclone according to the flow rate of the exhaust gas. The exhaust gas treatment apparatus for a large displacement diesel engine using low quality fuel equal to or less than heavy oil according to claim 1. 前記管状捕集部は、その下流側端部にテーパ状に拡径するテーパ管状部と該テーパ管状部に連なる大径管状部を有し、前記大径管状部の軸心付近に低濃度排ガス導出管と同大径管状部の内周面付近に高濃度排ガス導出部がそれぞれ連設された構成となすことを特徴とする請求項1又は2に記載の重油以下の低質燃料を使用する大排気量ディーゼルエンジン排ガス処理装置。 The tubular collecting portion has a tapered tubular portion that expands in a tapered shape at a downstream end thereof and a large-diameter tubular portion that continues to the tapered tubular portion, and a low-concentration exhaust gas near the axial center of the large-diameter tubular portion large that uses heavy oil following low quality fuels according to the vicinity of the inner peripheral surface of the outlet pipe and university diameter pipe-shaped part to claim 1 or 2 high concentration exhaust gas outlet portion and wherein the configuration and Nasukoto which is continuously provided respectively Exhaust gas treatment equipment for diesel engines. 前記管状捕集部のテーパ管状部又は該テーパ管状部に連なる大径管状部の領域にまで放電電極を延長して設けた構成となすことを特徴とする請求項3に記載の重油以下の低質燃料を使用する大排気量ディーゼルエンジン排ガス処理装置。 The low quality of heavy oil or less according to claim 3, wherein the discharge electrode is extended to a region of a tapered tubular portion of the tubular collecting portion or a large-diameter tubular portion connected to the tapered tubular portion. Exhaust gas treatment equipment for large displacement diesel engines using fuel . 前記サイクロン捕集手段は、処理能力の異なる複数の接線式サイクロンで構成するとともに、各接線式サイクロンの導入口に流量制御ダンパーを設けることを特徴とする請求項1〜4のいずれか1項に記載の重油以下の低質燃料を使用する大排気量ディーゼルエンジン排ガス処理装置。 The cyclone collecting means is constituted by a plurality of tangential cyclones having different processing capacities, and a flow rate control damper is provided at the inlet of each tangential cyclone. Exhaust gas treatment equipment for large displacement diesel engines using low quality fuel below the stated heavy oil . 前記接線式サイクロンと低濃度排ガス導出管との間に、接線式サイクロン通過後の浄化ガスを前記低濃度排ガスと合流させるための排出管を配設するとともに、該排出管にエアーノズル又はモータ駆動ファンを配置した構成となすことを特徴とする請求項1〜5のいずれか1項に記載の重油以下の低質燃料を使用する大排気量ディーゼルエンジン排ガス処理装置。 Between the tangential cyclone and the low-concentration exhaust gas outlet pipe, a discharge pipe for merging the purified gas after passing the tangential cyclone with the low-concentration exhaust gas is disposed, and an air nozzle or a motor drive is provided in the exhaust pipe. The exhaust gas treatment apparatus for a large displacement diesel engine using low quality fuel equal to or less than heavy oil according to any one of claims 1 to 5, wherein a fan is arranged.
JP2010256160A 2010-11-16 2010-11-16 Exhaust gas treatment equipment for large displacement diesel engines using low quality fuels below heavy oil Expired - Fee Related JP5863087B2 (en)

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JP2010256160A JP5863087B2 (en) 2010-11-16 2010-11-16 Exhaust gas treatment equipment for large displacement diesel engines using low quality fuels below heavy oil
PCT/JP2011/067318 WO2012066825A1 (en) 2010-11-16 2011-07-28 Exhaust gas processing device for diesel engine
CN201180055097.0A CN103261596B (en) 2010-11-16 2011-07-28 The exhaust gas treatment device of diesel engine
EP11842356.5A EP2642095B1 (en) 2010-11-16 2011-07-28 Exhaust gas processing device for diesel engine
KR1020137015397A KR101423016B1 (en) 2010-11-16 2011-07-28 Exhaust gas treatment equipment for diesel engine

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CN103261596A (en) 2013-08-21
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