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JP6957752B2 - Internal combustion engine and nitrogen enrichment device - Google Patents
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JP6957752B2 - Internal combustion engine and nitrogen enrichment device - Google Patents

Internal combustion engine and nitrogen enrichment device Download PDF

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JP6957752B2
JP6957752B2 JP2020525599A JP2020525599A JP6957752B2 JP 6957752 B2 JP6957752 B2 JP 6957752B2 JP 2020525599 A JP2020525599 A JP 2020525599A JP 2020525599 A JP2020525599 A JP 2020525599A JP 6957752 B2 JP6957752 B2 JP 6957752B2
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nitrogen
air
gas
oxygen
internal combustion
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JPWO2019244728A1 (en
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理晴 葛西
宜郎 川下
野田 徹
雄大 太田
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Nissan Motor Co Ltd
Sumitomo Chemical Co Ltd
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Sumitomo Chemical Co Ltd
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/22Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by diffusion
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02BINTERNAL-COMBUSTION PISTON ENGINES; COMBUSTION ENGINES IN GENERAL
    • F02B51/00Other methods of operating engines involving pretreating of, or adding substances to, combustion air, fuel, or fuel-air mixture of the engines
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02MSUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
    • F02M27/00Apparatus for treating combustion-air, fuel, or fuel-air mixture, by catalysts, electric means, magnetism, rays, sound waves, or the like
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02TCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T10/00Road transport of goods or passengers
    • Y02T10/10Internal combustion engine [ICE] based vehicles
    • Y02T10/12Improving ICE efficiencies

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)
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Description

この発明は、燃焼用空気として窒素富化空気を用い、酸素と燃料との混合比が理論混合比となるようにして燃焼を行う内燃機関、および、この種の内燃機関に好適な窒素富化装置に関する。 The present invention uses nitrogen-enriched air as combustion air and performs combustion so that the mixing ratio of oxygen and fuel becomes the theoretical mixing ratio, and nitrogen-enriched engine suitable for this type of internal combustion engine. Regarding the device.

特許文献1には、車両用の内燃機関として、空気中の酸素を一部除去して窒素富化空気を生成し、この窒素富化空気を内燃機関の燃焼室に供給して、理論空燃比よりも大きな空燃比でもって燃焼を行うようにした内燃機関が開示されている。この特許文献1では、多数のポリイミド樹脂製中空糸を束状にまとめた窒素富化エア発生ユニットを用い、加熱加圧した空気を中空糸の中心孔に導入して、中空糸の壁を酸素分子が通過することによって、窒素富化空気を得る構成となっている。 According to Patent Document 1, as an internal combustion engine for a vehicle, a part of oxygen in the air is removed to generate nitrogen-enriched air, and this nitrogen-enriched air is supplied to the combustion chamber of the internal combustion engine to provide a theoretical air-fuel ratio. An internal combustion engine is disclosed in which combustion is performed with a larger air-fuel ratio. In Patent Document 1, a nitrogen-enriched air generating unit in which a large number of polyimide resin hollow fibers are bundled is used, and heated and pressurized air is introduced into the center hole of the hollow fiber to oxygenate the wall of the hollow fiber. The structure is such that nitrogen-enriched air is obtained by the passage of molecules.

上記特許文献1においては、酸素が排出される側の空間の構成について特には開示がなく、酸素が透過する中空糸の外側は大気つまり通常の酸素濃度の空気が存在するものと考えられる。従って、中空糸の壁の内側と外側との間で本質的に酸素分圧差が得られない。そのため、酸素を除去して窒素富化するためには、必然的に空気を高圧に加圧して中空糸に導入する必要があるが、このように空気を加圧したとしても、所望の窒素富化レベルを実現できない可能性がある。 In the above-mentioned Patent Document 1, there is no particular disclosure about the composition of the space on the side where oxygen is discharged, and it is considered that the atmosphere, that is, the air having a normal oxygen concentration exists on the outside of the hollow fiber through which oxygen permeates. Therefore, essentially no oxygen partial pressure difference can be obtained between the inside and outside of the hollow fiber wall. Therefore, in order to remove oxygen and enrich the nitrogen, it is inevitably necessary to pressurize the air to a high pressure and introduce it into the hollow fiber. However, even if the air is pressurized in this way, the desired nitrogen richness is required. It may not be possible to achieve the conversion level.

特開2004−190570号公報Japanese Unexamined Patent Publication No. 2004-190570

この発明においては、燃焼に供される窒素富化空気を得るための窒素富化装置に、酸素の除去を助成するスイープガスとして内燃機関の排気ガスを導入する。 In the present invention, the exhaust gas of an internal combustion engine is introduced as a sweep gas that assists the removal of oxygen into a nitrogen-enriched device for obtaining nitrogen-enriched air to be used for combustion.

内燃機関から排出される排気ガスは、酸素濃度が低いガスであるため、この排気ガスをスイープガスとして窒素富化装置に導入することによって、空気からの酸素除去の効率が向上する。 Since the exhaust gas discharged from the internal combustion engine is a gas having a low oxygen concentration, the efficiency of oxygen removal from the air is improved by introducing this exhaust gas as a sweep gas into the nitrogen enrichment device.

この発明によれば、窒素富化装置に導入されるスイープガスとして内燃機関自体が排出する排気ガスを利用することで酸素除去の効率が向上する。従って、窒素富化レベルを高く得ることが容易となる。 According to the present invention, the efficiency of oxygen removal is improved by using the exhaust gas discharged by the internal combustion engine itself as the sweep gas introduced into the nitrogen enrichment device. Therefore, it becomes easy to obtain a high nitrogen enrichment level.

この発明に係る内燃機関の吸排気系の構成を模式的に示した説明図。The explanatory view which shows typically the structure of the intake / exhaust system of the internal combustion engine which concerns on this invention. シート状の気体分離膜の例を示す説明図。Explanatory drawing which shows an example of a sheet-like gas separation membrane. 気体分離膜として中空状膜の例を示す説明図。Explanatory drawing which shows an example of a hollow membrane as a gas separation membrane. 気体分離膜エレメントの一例を一部を切り開いた形で示す斜視図。The perspective view which shows an example of a gas separation membrane element in a partially cut-out form.

以下、この発明の一実施例を図面に基づいて詳細に説明する。 Hereinafter, an embodiment of the present invention will be described in detail with reference to the drawings.

図1は、この発明が適用された一実施例の車両用内燃機関の吸排気系の構成を模式的に示した構成説明図である。内燃機関1は、主に理論混合比(ここで混合比とは酸素と燃料との混合比をいう)近傍での燃焼を行う内燃機関であり、例えば、ガソリンを燃料とする4ストロークサイクルの火花点火式内燃機関からなる。内燃機関1の各々の気筒には、筒内へ向けて燃料の供給を行う燃料噴射弁2と、筒内に形成された混合気への点火を行う点火プラグ3と、がそれぞれ設けられている。各気筒の燃焼室4には、吸気弁5によって開閉される吸気ポート6と、排気弁7によって開閉される排気ポート8と、がそれぞれ接続されている。なお、燃料噴射弁2を、吸気弁5上流の吸気ポート6へ向けて燃料を噴射するように配置した、いわゆる吸気ポート噴射形式の構成であってもよい。燃料噴射弁2による燃料の噴射量(換言すれば噴射期間)ならびに噴射時期、および点火プラグ3による点火時期は、エンジンコントローラ10によってそれぞれ制御される。 FIG. 1 is a configuration explanatory view schematically showing a configuration of an intake / exhaust system of an internal combustion engine for a vehicle according to an embodiment to which the present invention is applied. The internal combustion engine 1 is an internal combustion engine that mainly burns in the vicinity of a theoretical mixing ratio (here, the mixing ratio means a mixing ratio of oxygen and fuel). For example, a spark of a 4-stroke cycle using gasoline as fuel. It consists of an ignition type internal combustion engine. Each cylinder of the internal combustion engine 1 is provided with a fuel injection valve 2 for supplying fuel into the cylinder and a spark plug 3 for igniting the air-fuel mixture formed in the cylinder. .. An intake port 6 opened and closed by an intake valve 5 and an exhaust port 8 opened and closed by an exhaust valve 7 are connected to the combustion chamber 4 of each cylinder. The fuel injection valve 2 may be arranged so as to inject fuel toward the intake port 6 upstream of the intake valve 5, which may be a so-called intake port injection type configuration. The fuel injection amount (in other words, the injection period) and the injection timing by the fuel injection valve 2 and the ignition timing by the spark plug 3 are controlled by the engine controller 10, respectively.

内燃機関1は、吸気の過給を行う過給機として例えばターボ過給機11を備えている。このターボ過給機11は、タービン12とコンプレッサ13とを含んで構成されている。 The internal combustion engine 1 includes, for example, a turbocharger 11 as a supercharger for supercharging the intake air. The turbocharger 11 includes a turbine 12 and a compressor 13.

内燃機関1の吸気ポート6に至る吸気通路15の通路途中には、外部から取り込んだ空気から酸素を一部除去して窒素富化空気を生成する窒素富化装置16が配置されている。吸気通路15における窒素富化装置16の出口と吸気ポート6との間には、エンジンコントローラ10からの制御信号によって開度が制御される電子制御型スロットルバルブ17が配置されている。吸気通路15における窒素富化装置16の上流側には、ターボ過給機11のコンプレッサ13が位置し、さらに該コンプレッサ13の上流側に、外部から取り込まれる空気の流量(例えば質量流量)を計測するエアフロメータ18が設けられている。エアフロメータ18の上流側には、図示しないエアクリーナが配置されている。また、コンプレッサ13と窒素富化装置16との間には、コンプレッサ13により圧縮されて高温となった空気流を冷却する例えば水冷式あるいは空冷式のインタクーラ19が設けられている。 A nitrogen enrichment device 16 is arranged in the middle of the intake passage 15 leading to the intake port 6 of the internal combustion engine 1 to generate nitrogen-enriched air by partially removing oxygen from the air taken in from the outside. An electronically controlled throttle valve 17 whose opening degree is controlled by a control signal from the engine controller 10 is arranged between the outlet of the nitrogen enrichment device 16 and the intake port 6 in the intake passage 15. The compressor 13 of the turbocharger 11 is located on the upstream side of the nitrogen enrichment device 16 in the intake passage 15, and further, the flow rate of air taken in from the outside (for example, mass flow rate) is measured on the upstream side of the compressor 13. An air flow meter 18 is provided. An air cleaner (not shown) is arranged on the upstream side of the air flow meter 18. Further, between the compressor 13 and the nitrogen enrichment device 16, for example, a water-cooled or air-cooled intercooler 19 for cooling the air flow compressed by the compressor 13 and having a high temperature is provided.

排気ポート8に接続された排気通路21の通路途中には、排気の浄化を行う三元触媒を用いた触媒コンバータ22が配置されている。この触媒コンバータ22は、タービン12の下流側に位置している。触媒コンバータ22の上流側つまりタービン12と触媒コンバータ22との間には、いわゆる排気空燃比を検出する空燃比センサ23が配置されている。空燃比センサ23としては、排気空燃比に応じた出力が得られるいわゆるリニア空燃比センサであってもよく、あるいは、理論空燃比相当よりもリーンであるかリッチであるかを示す出力が得られるいわゆるO2センサであってもよい。触媒コンバータ22の下流側には図示しない消音器が設けられており、排気通路21の先端は、この消音器を介して大気に開放されている。 A catalyst converter 22 using a three-way catalyst for purifying exhaust gas is arranged in the middle of the passage 21 of the exhaust passage 21 connected to the exhaust port 8. The catalytic converter 22 is located on the downstream side of the turbine 12. An air-fuel ratio sensor 23 for detecting the so-called exhaust air-fuel ratio is arranged on the upstream side of the catalyst converter 22, that is, between the turbine 12 and the catalyst converter 22. The air-fuel ratio sensor 23 may be a so-called linear air-fuel ratio sensor that can obtain an output according to the exhaust air-fuel ratio, or an output indicating whether it is leaner or richer than the theoretical air-fuel ratio equivalent can be obtained. It may be a so-called O2 sensor. A silencer (not shown) is provided on the downstream side of the catalytic converter 22, and the tip of the exhaust passage 21 is open to the atmosphere via the silencer.

また、触媒コンバータ22の下流側において、排気通路21から排気分岐通路25が分岐している。この排気分岐通路25の先端は、窒素富化装置16に接続されており、窒素富化装置16での酸素の除去を助成するスイープガスとして排気ガスを窒素富化装置16に導いている。排気分岐通路25の通路途中には、窒素富化装置16に導入される前に排気流を冷却する例えば水冷式あるいは空冷式の排気ガスクーラ26が設けられている。窒素富化装置16からさらに延びる排気分岐通路25の先端側は、そのまま大気に開放されていてもよく、あるいは図示しない消音器の上流側もしくは下流側かつ触媒コンバータ22の下流側で排気通路21と合流するように構成してもよい。 Further, on the downstream side of the catalytic converter 22, the exhaust branch passage 25 branches from the exhaust passage 21. The tip of the exhaust branch passage 25 is connected to the nitrogen enrichment device 16, and guides the exhaust gas to the nitrogen enrichment device 16 as a sweep gas that assists the removal of oxygen in the nitrogen enrichment device 16. In the middle of the exhaust branch passage 25, for example, a water-cooled or air-cooled exhaust gas cooler 26 for cooling the exhaust flow before being introduced into the nitrogen enrichment device 16 is provided. The tip side of the exhaust branch passage 25 further extending from the nitrogen enrichment device 16 may be open to the atmosphere as it is, or the exhaust passage 21 and the exhaust passage 21 are located upstream or downstream of the silencer (not shown) and downstream of the catalytic converter 22. It may be configured to merge.

なお、エンジンコントローラ10には、上記のエアフロメータ18および空燃比センサ23のほかに、機関回転速度を示す図示せぬクランク角センサや、運転者によるアクセルペダルの踏み込み量を検出する図示せぬアクセル開度センサ、等の種々のセンサ類が接続されている。 In addition to the above-mentioned air flow meter 18 and air-fuel ratio sensor 23, the engine controller 10 includes a crank angle sensor (not shown) that indicates the engine rotation speed, and an accelerator (not shown) that detects the amount of depression of the accelerator pedal by the driver. Various sensors such as an opening sensor are connected.

窒素富化装置16は、図示しないエアクリーナを通して外部から取り込まれた空気が吸気通路15を介して導入される吸気室31と、排気分岐通路25を介して排気ガスが導入される排気室32と、これらの吸気室31と排気室32とを互いに隔てるとともに酸素が選択的に透過可能な気体分離膜33と、を備えている。従って、吸気室31を流れる空気の一部の酸素は、気体分離膜33を通して排気室32側へ移動する。吸気室31の入口側となる吸気通路15を吸気入口通路15Aとし吸気室31の出口側となる吸気通路15を吸気出口通路15Bと呼ぶこととすると、吸気入口通路15Aには大気と同様の組成(窒素約79%、酸素約21%)を有する空気が流れ、吸気出口通路15Bからは酸素の一部が除去されて相対的に窒素をより多く含む窒素富化空気が流れ出ることとなる。また、排気室32の入口側となる排気分岐通路25を排気入口通路25Aとし排気室32の出口側となる排気分岐通路25を排気出口通路25Bと呼ぶこととすると、排気入口通路25Aには本質的に酸素を殆ど含まない排気ガスが流れ、排気出口通路25Bからは気体分離膜33を透過した酸素が同伴した排気ガスが流れ出る。 The nitrogen enrichment device 16 includes an intake chamber 31 in which air taken in from the outside through an air cleaner (not shown) is introduced through an intake passage 15, and an exhaust chamber 32 in which exhaust gas is introduced through an exhaust branch passage 25. A gas separation film 33 that separates the intake chamber 31 and the exhaust chamber 32 from each other and allows oxygen to selectively permeate is provided. Therefore, a part of oxygen in the air flowing through the intake chamber 31 moves to the exhaust chamber 32 side through the gas separation membrane 33. Assuming that the intake passage 15 on the inlet side of the intake chamber 31 is referred to as the intake inlet passage 15A and the intake passage 15 on the outlet side of the intake chamber 31 is referred to as the intake outlet passage 15B, the intake inlet passage 15A has the same composition as the air. Air having (about 79% nitrogen, about 21% oxygen) flows, and a part of oxygen is removed from the intake outlet passage 15B, and nitrogen-enriched air containing a relatively large amount of nitrogen flows out. Further, assuming that the exhaust branch passage 25 on the inlet side of the exhaust chamber 32 is referred to as the exhaust inlet passage 25A and the exhaust branch passage 25 on the outlet side of the exhaust chamber 32 is referred to as the exhaust outlet passage 25B, the exhaust inlet passage 25A is essentially. Exhaust gas containing almost no oxygen flows out, and exhaust gas accompanied by oxygen that has passed through the gas separation film 33 flows out from the exhaust outlet passage 25B.

気体分離膜33は、例えば公知の高分子膜からなり、図2に示すようなシート状膜であってもよく、図3に示すような中空状膜であってもよい。 The gas separation membrane 33 is made of, for example, a known polymer membrane, and may be a sheet-like membrane as shown in FIG. 2 or a hollow membrane as shown in FIG.

すなわち、図2の例では、気体分離膜33が吸気室31と排気室32とを隔てるシート状膜33として構成される。シート状膜33は、それ自体で取り扱いが可能な自立膜であってもよく、あるいは、酸素を選択的に透過させる分離機能層とこれを支持する支持層とが積層された複合膜であってもよい。シート状膜33を挟んで吸気室31となる一方の側を矢印Aで示すように空気が流れ、排気室32となる他方の側を矢印Gで示すようにスイープガスとなる排気ガスが流れる。そして、空気流A中の酸素が矢印O2で示すようにシート状膜33を透過し、スイープガスとなる排気ガス流G中に排出される。なお、図では、空気流Aと排気ガス流Gとが同じ方向に流れるが、空気流Aと排気ガス流Gとが互いに反対方向に流れる構成であってもよい。 That is, in the example of FIG. 2, the gas separation membrane 33 is configured as a sheet-like membrane 33 that separates the intake chamber 31 and the exhaust chamber 32. The sheet-like membrane 33 may be a self-supporting membrane that can be handled by itself, or is a composite membrane in which a separation function layer that selectively permeates oxygen and a support layer that supports the separation functional layer are laminated. May be good. Air flows on one side of the intake chamber 31 that sandwiches the sheet-like membrane 33 as shown by an arrow A, and exhaust gas that becomes a sweep gas flows on the other side of the exhaust chamber 32 as shown by an arrow G. Then, oxygen in the air flow A permeates through the sheet-like membrane 33 as shown by the arrow O2, and is discharged into the exhaust gas flow G which becomes the sweep gas. In the figure, the air flow A and the exhaust gas flow G flow in the same direction, but the air flow A and the exhaust gas flow G may flow in opposite directions.

図3の例では、気体分離膜33が中空状膜33として構成される。すなわち、比較的に径が大きな管状あるいは比較的に径が細いいわゆる中空糸状に構成される。中空状膜33は、それ自体で取り扱いが可能な自立膜であってもよく、あるいは、酸素を選択的に透過させる分離機能層とこれを支持する支持層とが積層された複合膜であってもよい。複合膜の例では、例えば、中空状の支持層の外周表面に分離機能層が設けられる。一つの例では、中空状膜33の外側を矢印Aで示すように空気が流れ、中空状膜33の内側を矢印Gで示すようにスイープガスとなる排気ガスが流れる。なお、図では、空気流Aと排気ガス流Gとが同じ方向に流れるが、空気流Aと排気ガス流Gとが互いに反対方向に流れる構成であってもよい。 In the example of FIG. 3, the gas separation membrane 33 is configured as a hollow membrane 33. That is, it is formed in a tubular shape having a relatively large diameter or a so-called hollow thread shape having a relatively small diameter. The hollow membrane 33 may be a self-supporting membrane that can be handled by itself, or is a composite membrane in which a separation function layer that selectively permeates oxygen and a support layer that supports the separation functional layer are laminated. May be good. In the example of the composite membrane, for example, a separation function layer is provided on the outer peripheral surface of the hollow support layer. In one example, air flows on the outside of the hollow membrane 33 as shown by an arrow A, and exhaust gas as a sweep gas flows on the inside of the hollow membrane 33 as shown by an arrow G. In the figure, the air flow A and the exhaust gas flow G flow in the same direction, but the air flow A and the exhaust gas flow G may flow in opposite directions.

好ましい一つの実施例では、窒素富化装置16において、気体分離膜33として、上記シート状膜33が集積・一体化されたスパイラル型またはプリーツ型の気体分離膜エレメントが用いられる。そして、この気体分離膜エレメントが、排気室32の側に排気ガスの流れを導く流路を備えている。 In one preferred embodiment, in the nitrogen enrichment apparatus 16, as the gas separation membrane 33, a spiral type or pleated type gas separation membrane element in which the sheet-like membrane 33 is integrated and integrated is used. The gas separation membrane element is provided with a flow path that guides the flow of exhaust gas on the side of the exhaust chamber 32.

図4は、スパイラル型の気体分離膜エレメント41の一構成例を示している。この気体分離膜エレメント41は、複数のガス通過孔(図示せず)が開口した集ガス管46を中心として、シート状をなす複数のリーフ42を空気側流路部材43とともにスパイラル状に巻回したものであり、この気体分離膜エレメント41を円筒状をなすケーシング(図示せず)の中に収容することで窒素富化装置16が構成される。 FIG. 4 shows a configuration example of the spiral type gas separation membrane element 41. The gas separation membrane element 41 spirally winds a plurality of sheet-shaped leaves 42 together with an air-side flow path member 43 around a gas collecting pipe 46 in which a plurality of gas passage holes (not shown) are opened. The nitrogen enrichment device 16 is configured by accommodating the gas separation membrane element 41 in a cylindrical casing (not shown).

各々のリーフ42は、一部を展開かつ切り開いて示すように、シート状膜33aとシート状膜33bとを重ね合わせ、周縁部42aにおいて接着剤により互いに接着したものである。シート状膜33aとシート状膜33bとの間には、両者の対向面間でガスが通流し得るように連通する空隙を有するガス側流路部材45が挟み込まれている。連通する空隙を有するガス側流路部材45の構造としては、例えばネット、メッシュ、編み物が挙げられる。また、周縁部42aに加えて、仕切り部42bにおいてもシート状膜33aとシート状膜33bとが互いに接着されている。なお、周縁部42aおよび仕切り部42bは、ガス側流路部材45を介して、シート状膜33aとシート状膜33bとが互いに接着されていてもよい。これにより、リーフ42の内部(つまりシート状膜33とシート状膜33bとの間)に、矢印Gで示すように排気ガスがUターンする形に流れる流路47が形成されている。なお、仕切り部42bは、図4に図示される形状に限らず、リーフ42の内部に排気ガス流れの滞留を抑制し、シート状膜の全面に排気ガスが行き渡るように設けられることが好ましい。このリーフ42内の排気ガスの流路47は、一端が集ガス管46の入口部46aに連通し、他端が出口部に連通している。つまり、集ガス管46の入口部46aから矢印G1で示すように導入された排気ガスは、各リーフ42の内部のUターン形状の流路47を流れ、かつ集ガス管46の他端の出口部から矢印G2で示すように排出される。 Each leaf 42 is formed by superimposing a sheet-like film 33a and a sheet-like film 33b and adhering them to each other with an adhesive at a peripheral edge portion 42a, as shown by developing and cutting a part thereof. A gas-side flow path member 45 having a gap that allows the gas to flow between the facing surfaces of the sheet-like film 33a and the sheet-like film 33b is sandwiched between the sheet-like film 33a and the sheet-like film 33b. Examples of the structure of the gas-side flow path member 45 having a communication gap include a net, a mesh, and knitting. Further, in addition to the peripheral edge portion 42a, the sheet-like film 33a and the sheet-like film 33b are also adhered to each other in the partition portion 42b. The peripheral portion 42a and the partition portion 42b may have the sheet-like film 33a and the sheet-like film 33b adhered to each other via the gas-side flow path member 45. As a result, a flow path 47 through which the exhaust gas flows in a U-turn is formed inside the leaf 42 (that is, between the sheet-like film 33 and the sheet-like film 33b) as shown by an arrow G. The partition portion 42b is not limited to the shape shown in FIG. 4, and it is preferable that the partition portion 42b is provided so as to suppress the retention of the exhaust gas flow inside the leaf 42 and to spread the exhaust gas over the entire surface of the sheet-like film. One end of the exhaust gas flow path 47 in the leaf 42 communicates with the inlet portion 46a of the gas collecting pipe 46, and the other end communicates with the outlet portion. That is, the exhaust gas introduced from the inlet portion 46a of the gas collecting pipe 46 as shown by an arrow G1 flows through the U-turn-shaped flow path 47 inside each leaf 42, and exits at the other end of the gas collecting pipe 46. It is discharged from the portion as shown by the arrow G2.

また、各リーフ42の間に介在する空気側流路部材43は、隣接する2つのリーフ42の間に空気用の流路を確保するように、連通する空隙を有する構造が好ましく、例えばネット、メッシュ、編み物が挙げられる。空気は、円筒状をなすケーシングにおいて該ケーシングの一端部から他端部へと軸方向に沿って流れるように案内される。つまり、各リーフ42のシート状膜33の表面に沿って矢印Aで示すように空気が流れる。このように空気が流れる際に、シート状膜33を通して一部の酸素が排気ガス側へ通過する。そのため、矢印Aのように流れる空気は、窒素富化空気となって気体分離膜エレメント41から流れ出る。 Further, the air-side flow path member 43 interposed between the leaves 42 preferably has a structure having a communication gap so as to secure a flow path for air between two adjacent leaves 42, for example, a net. Examples include mesh and knitting. Air is guided to flow along the axial direction from one end to the other end of the cylindrical casing. That is, air flows along the surface of the sheet-like film 33 of each leaf 42 as shown by an arrow A. When the air flows in this way, a part of oxygen passes to the exhaust gas side through the sheet-like membrane 33. Therefore, the air flowing as shown by the arrow A becomes nitrogen-enriched air and flows out from the gas separation membrane element 41.

なお、上述のスパイラル型の気体分離膜エレメント41に類似した構成は、国際公開WO2016/024523に記載されている。また、プリーツ型の気体分離膜エレメントの一構成例は、特開2007−222841号公報に記載されている。本発明においては、これらの公知の気体分離膜エレメントを用いることができる。 A configuration similar to the spiral type gas separation membrane element 41 described above is described in International Publication WO 2016/024523. A configuration example of a pleated gas separation membrane element is described in Japanese Patent Application Laid-Open No. 2007-222841. In the present invention, these known gas separation membrane elements can be used.

上記のように構成された内燃機関1においては、窒素富化装置16において空気から酸素を一部除去することによって窒素富化空気が生成され、この窒素富化空気が内燃機関1の燃焼室4に供給されて燃焼に供される。燃料噴射弁2から供給される燃料の噴射量およびスロットルバルブ17を介して燃焼室4に導入される窒素富化空気の流量は、空燃比センサ23を用いた公知のフィードバック制御によって、排気空燃比が理論空燃比相当のものとなるように、換言すれば燃焼室4における酸素と燃料との混合比が理論混合比となるように、それぞれ制御される。例えば、内燃機関1の発生トルクを何らかの形で検出ないし推定し、運転者の要求に応じたトルクが得られるようにスロットルバルブ17の開度を制御した上で、理論混合比となるように燃料噴射量をフィードバック制御することが可能である。これにより、排気ガス中のHC、CO、NOxが触媒コンバータ22の三元触媒によって同時に浄化される。 In the internal combustion engine 1 configured as described above, nitrogen-enriched air is generated by partially removing oxygen from the air in the nitrogen-enriching device 16, and the nitrogen-enriched air is used as the combustion chamber 4 of the internal combustion engine 1. It is supplied to and used for combustion. The injection amount of fuel supplied from the fuel injection valve 2 and the flow rate of the nitrogen-enriched air introduced into the combustion chamber 4 via the throttle valve 17 are determined by the known feedback control using the air-fuel ratio sensor 23 to determine the exhaust air-fuel ratio. Is controlled to be equivalent to the stoichiometric air-fuel ratio, in other words, the mixing ratio of oxygen and fuel in the combustion chamber 4 is controlled to be the stoichiometric mixing ratio. For example, the torque generated by the internal combustion engine 1 is detected or estimated in some way, the opening degree of the throttle valve 17 is controlled so that the torque according to the driver's request can be obtained, and then the fuel is adjusted to the theoretical mixing ratio. It is possible to control the injection amount by feedback. As a result, HC, CO, and NOx in the exhaust gas are simultaneously purified by the three-way catalyst of the catalyst converter 22.

また、図示しない筒内圧センサによって筒内圧を検出することによって燃焼室4内の酸素濃度を推定することも可能であり、エアフロメータ18が検出する空気量と併せて燃焼室4内の酸素量を求めるようにしてもよい。 It is also possible to estimate the oxygen concentration in the combustion chamber 4 by detecting the in-cylinder pressure with an in-cylinder pressure sensor (not shown), and the amount of oxygen in the combustion chamber 4 is calculated together with the amount of air detected by the air flow meter 18. You may ask for it.

燃焼用の空気として酸素濃度が大気よりも低い窒素富化空気を用いることにより、理論混合比とするのに必要な空気量が増大する。つまり、見かけ上の空燃比が大となる。この結果、一般的なリーンバーンエンジンと同様に、燃焼温度が低くなり、燃焼効率が向上する。またポンピングロスも低減するため、燃焼効率の向上と併せて、燃料消費率が改善される。他方、一般的なリーンバーンエンジンとは異なり、燃料量に対し過剰となる酸素が存在しないので、燃焼温度が低いことによってNOxの発生が本質的に少なくなる上に、触媒下での還元処理が可能となる。従って、一般的な三元触媒でもって排気ガス中のHC、CO、NOxを同時に浄化することが可能である。 By using nitrogen-enriched air having an oxygen concentration lower than that of the atmosphere as the combustion air, the amount of air required for the theoretical mixing ratio is increased. That is, the apparent air-fuel ratio becomes large. As a result, the combustion temperature is lowered and the combustion efficiency is improved as in the case of a general lean burn engine. Moreover, since the pumping loss is also reduced, the fuel consumption rate is improved along with the improvement of the combustion efficiency. On the other hand, unlike a general lean burn engine, there is no oxygen that is excessive with respect to the amount of fuel, so the generation of NOx is essentially reduced due to the low combustion temperature, and the reduction treatment under the catalyst is performed. It will be possible. Therefore, it is possible to simultaneously purify HC, CO, and NOx in the exhaust gas with a general three-way catalyst.

ここで、上記実施例のように窒素富化装置16にスイープガスとして内燃機関1の排気ガスを導入する構成にあっては、排気ガス中の酸素濃度が低いことから、気体分離膜33を介した酸素除去の効率が高くなる。つまり、気体分離膜33における酸素の透過量は、気体分離膜33を挟んで一方の側と他方の側とでの酸素分圧の差に依存する。燃焼により酸素が消費された排気ガスは、本質的に酸素濃度が非常に低いので、これをスイープガスとして利用することで、気体分離膜33を通した酸素の除去を効果的に助成することができる。従って、比較的小型の窒素富化装置16でもって窒素富化レベルを高く得ることが可能となる。換言すれば、吸気室31側と排気室32側とでの絶対圧の差が小さくても、酸素の除去を効率よく行うことができる。なお、窒素富化レベルは、スイープガスの流量で調整できる。スイープガスの流量の調整方法としては、例えば図1の排気分岐通路25に分配される排気ガスの分配比で行うことができ、分配比の調整手段としては、排気分岐通路25よりも下流の排気通路21に備わる流量調整バルブ(図示せず)が挙げられる。この流量調整バルブは、エンジンコントローラ10によって制御されてもよい。 Here, in the configuration in which the exhaust gas of the internal combustion engine 1 is introduced as the sweep gas into the nitrogen enrichment device 16 as in the above embodiment, since the oxygen concentration in the exhaust gas is low, the gas separation membrane 33 is used. The efficiency of oxygen removal is increased. That is, the amount of oxygen permeated by the gas separation membrane 33 depends on the difference in oxygen partial pressure between one side and the other side of the gas separation membrane 33. Exhaust gas whose oxygen is consumed by combustion has a very low oxygen concentration in nature, and by using this as a sweep gas, it is possible to effectively support the removal of oxygen through the gas separation membrane 33. can. Therefore, it is possible to obtain a high nitrogen enrichment level with a relatively small nitrogen enrichment device 16. In other words, oxygen can be efficiently removed even if the difference in absolute pressure between the intake chamber 31 side and the exhaust chamber 32 side is small. The nitrogen enrichment level can be adjusted by the flow rate of the sweep gas. As a method of adjusting the flow rate of the sweep gas, for example, the distribution ratio of the exhaust gas distributed to the exhaust branch passage 25 of FIG. 1 can be used, and as a means of adjusting the distribution ratio, the exhaust gas downstream of the exhaust branch passage 25 A flow rate adjusting valve (not shown) provided in the passage 21 can be mentioned. This flow rate adjusting valve may be controlled by the engine controller 10.

例えば、理論空燃比が14.7であるとすると、見かけ上の空燃比を30前後まで高めるためには、大気中の約21%である酸素濃度を半減し、酸素10%、窒素90%程度の高い窒素富化レベルの窒素富化空気を生成する必要がある。仮に従来のように酸素の移動先が大気であると、本質的に酸素分圧差がないことから、過給機により絶対圧を高くしても酸素除去の効率は低く、従って、このような窒素富化レベルの高い窒素富化空気を得るのは一般に困難である。あるいは、車両への搭載が困難となるような非常に大型の窒素富化装置が必要となる。 For example, assuming that the theoretical air-fuel ratio is 14.7, in order to raise the apparent air-fuel ratio to around 30, the oxygen concentration, which is about 21% in the atmosphere, is halved, and the oxygen concentration is as high as 10% and nitrogen is about 90%. It is necessary to produce nitrogen-enriched air at the nitrogen-enriched level. If the destination of oxygen is the atmosphere as in the past, there is essentially no difference in oxygen partial pressure, so even if the absolute pressure is increased by a supercharger, the efficiency of oxygen removal is low. Therefore, such nitrogen It is generally difficult to obtain nitrogen-enriched air with high enrichment levels. Alternatively, a very large nitrogen enrichment device that is difficult to mount in a vehicle is required.

これに対し、上記実施例によれば、車両に搭載可能な比較的小型の窒素富化装置16でもって高いレベルの窒素富化空気を容易に生成できる。特に、上記実施例では、三元触媒通過後の排気ガスが窒素富化装置16にスイープガスとして導入される。このように三元触媒を通過することで排気ガス中に残存していた酸素も消費されるため、窒素富化装置16に導入される排気ガスは酸素を殆ど含まないものとなる。従って、三元触媒を通過する前の排気ガスを導入した場合に比較して、酸素除去の効率がさらに高く得られるとともに、排気ガスによる酸素除去の助成作用がより安定したものとなる。 On the other hand, according to the above embodiment, a high level of nitrogen-enriched air can be easily generated by a relatively small nitrogen-enriching device 16 that can be mounted on a vehicle. In particular, in the above embodiment, the exhaust gas after passing through the three-way catalyst is introduced into the nitrogen enrichment device 16 as a sweep gas. Since the oxygen remaining in the exhaust gas is also consumed by passing through the three-way catalyst in this way, the exhaust gas introduced into the nitrogen enrichment device 16 contains almost no oxygen. Therefore, as compared with the case where the exhaust gas before passing through the three-way catalyst is introduced, the efficiency of oxygen removal can be further increased, and the subsidizing action of oxygen removal by the exhaust gas becomes more stable.

さらに上記実施例では、吸気室31へ導入される空気は、ターボ過給機11によって加圧されていることから、排気室32内の排気ガスよりも高い絶対圧とすることができる。このように空気を加圧することで、酸素除去がより効率的となる。 Further, in the above embodiment, since the air introduced into the intake chamber 31 is pressurized by the turbocharger 11, the absolute pressure can be higher than that of the exhaust gas in the exhaust chamber 32. By pressurizing the air in this way, oxygen removal becomes more efficient.

一実施例においては、上述した例のように、酸素10%、窒素90%程度の高い窒素富化レベルの窒素富化空気を生成することが可能であり、これにより、理論混合比での燃焼を見かけ上の空燃比が30程度のものとして実現することができる。 In one embodiment, as in the example described above, it is possible to generate nitrogen-enriched air with a high nitrogen-enriched level of about 10% oxygen and 90% nitrogen, whereby combustion at a theoretical mixing ratio is possible. It can be realized as having an apparent air-fuel ratio of about 30.

また、酸素除去を助成するスイープガスとなる排気ガスは、内燃機関1の運転ないし燃焼によって単純に生成されるガスであるので、スイープガスを生成するための付加的な装置が不要である。しかも、スイープガスの生成に伴って生じる追加的なエネルギ消費もない。従って、見かけ上の空燃比が高くなることで得られる燃料消費性能の向上がスイープガスの生成のために相殺されてしまうようなことがない。 Further, since the exhaust gas serving as the sweep gas that assists oxygen removal is a gas that is simply generated by the operation or combustion of the internal combustion engine 1, no additional device for generating the sweep gas is required. Moreover, there is no additional energy consumption associated with the generation of sweep gas. Therefore, the improvement in fuel consumption performance obtained by increasing the apparent air-fuel ratio is not offset by the generation of sweep gas.

以上、この発明の一実施例を詳細に説明したが、この発明は上記実施例に限定されるものではなく、種々の変更が可能である。 Although one embodiment of the present invention has been described in detail above, the present invention is not limited to the above embodiment, and various modifications can be made.

例えば、窒素富化装置としては上記実施例の高分子膜を利用したものに限らず、除去した酸素がスイープガスへと移動するものであれば、いかなる形式の窒素富化装置であってもよい。 For example, the nitrogen enrichment device is not limited to the one using the polymer membrane of the above embodiment, and any type of nitrogen enrichment device may be used as long as the removed oxygen moves to the sweep gas. ..

Claims (7)

酸素と燃料との混合比が理論混合比近傍で運転する火花点火式内燃機関であって、
外部の空気から酸素を一部除去して燃焼に供される窒素富化空気を得る窒素富化装置と、
排気通路に設けられた三元触媒と、
内燃機関の排気ガス中のHC、CO、NOxが上記三元触媒において同時に浄化されるように空燃比センサを用いて上記混合比を理論混合比近傍にフィードバック制御する手段と、
を備え、
上記窒素富化装置は、上記のフィードバック制御中に、酸素の除去を助成するスイープガスとして上記三元触媒を通過した排気ガスが導入され、
このスイープガスにより酸素が一部除去されて得られた窒素富化空気が当該内燃機関の燃焼室に供給される、内燃機関。
A spark-ignition internal combustion engine that operates with a mixture ratio of oxygen and fuel near the theoretical mixture ratio.
A nitrogen-enriching device that removes some oxygen from the outside air to obtain nitrogen-enriched air for combustion.
The three-way catalyst provided in the exhaust passage and
A means for feedback-controlling the mixing ratio to the vicinity of the theoretical mixing ratio by using an air-fuel ratio sensor so that HC, CO, and NOx in the exhaust gas of the internal combustion engine are simultaneously purified in the three-way catalyst.
With
During the feedback control , the nitrogen enricher introduces exhaust gas that has passed through the three-way catalyst as a sweep gas that assists in the removal of oxygen.
An internal combustion engine in which nitrogen-enriched air obtained by partially removing oxygen by this sweep gas is supplied to the combustion chamber of the internal combustion engine.
上記スイープガスは、上記排気ガスが上記三元触媒を通過することで酸素を殆ど含まないガスとなっており、
上記窒素富化装置に導入された外部の空気中の酸素の一部が上記スイープガスへ移動することで窒素富化空気が得られる、請求項1に記載の内燃機関。
The sweep gas is a gas that contains almost no oxygen as the exhaust gas passes through the three-way catalyst.
The internal combustion engine according to claim 1, wherein nitrogen-enriched air is obtained by moving a part of oxygen in the external air introduced into the nitrogen-enriching device to the sweep gas.
上記窒素富化装置は、
外部の空気が導入される吸気室と、
上記排気ガスが導入される排気室と、
酸素が選択的に通過する気体分離膜と、
を備え、
上記気体分離膜が上記吸気室と上記排気室とを隔成するように配置されている、請求項1または2に記載の内燃機関。
The above nitrogen enrichment device
The intake chamber where outside air is introduced and
The exhaust chamber where the above exhaust gas is introduced and
A gas separation membrane through which oxygen selectively passes, and
With
The internal combustion engine according to claim 1 or 2, wherein the gas separation membrane is arranged so as to separate the intake chamber and the exhaust chamber.
外部から取り込んだ空気を加圧する過給機をさらに備え、
上記窒素富化装置に、上記過給機で加圧された空気が導入される、請求項1〜3のいずれかに記載の内燃機関。
Further equipped with a supercharger that pressurizes the air taken in from the outside,
The internal combustion engine according to any one of claims 1 to 3, wherein air pressurized by the supercharger is introduced into the nitrogen enrichment device.
酸素と燃料との混合比が空燃比センサを用いたフィードバック制御により理論混合比近傍で運転する火花点火式内燃機関に備わる窒素富化装置であって、
この窒素富化装置は、
外部の空気が導入され、窒素富化空気が排出される吸気室と、
上記空気から酸素を一部除去する気体分離膜と、
酸素の除去を助成するスイープガスとして、上記のフィードバック制御中の三元触媒によって浄化された内燃機関の排気ガスが導入される排気室と、
を備え、
上記吸気室から排出された窒素富化空気が上記内燃機関の燃焼室に供給されるように構成されるとともに、
上記気体分離膜が上記吸気室と上記排気室とを隔成するように配置されている、窒素富化装置。
It is a nitrogen enrichment device provided in a spark-ignition internal combustion engine that operates near the theoretical mixture ratio by feedback control using an air-fuel ratio sensor for the mixture ratio of oxygen and fuel.
This nitrogen enricher is
The intake chamber where outside air is introduced and nitrogen-enriched air is discharged,
A gas separation membrane that partially removes oxygen from the air,
As a sweep gas that assists in the removal of oxygen, an exhaust chamber into which the exhaust gas of the internal combustion engine purified by the three-way catalyst under the above feedback control is introduced, and
With
The nitrogen-enriched air discharged from the intake chamber is configured to be supplied to the combustion chamber of the internal combustion engine, and is also configured.
A nitrogen enrichment device in which the gas separation membrane is arranged so as to separate the intake chamber and the exhaust chamber.
上記気体分離膜が、シート状膜または中空状膜である、請求項に記載の窒素富化装置。 The nitrogen enrichment apparatus according to claim 5 , wherein the gas separation membrane is a sheet-like membrane or a hollow membrane. 上記気体分離膜が、上記シート状膜が集積・一体化されたスパイラル型またはプリーツ型の気体分離膜エレメントであり、
上記気体分離膜エレメントは、上記排気室の側にガスの流れを導く流路を備えている、請求項に記載の窒素富化装置。
The gas separation membrane is a spiral type or pleated type gas separation membrane element in which the sheet-like membrane is integrated and integrated.
The nitrogen enrichment device according to claim 6 , wherein the gas separation membrane element includes a flow path for guiding a gas flow on the side of the exhaust chamber.
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