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JP4493799B2 - Catalyst-integrated heat exchanger for exhaust gas heat recovery - Google Patents
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JP4493799B2 - Catalyst-integrated heat exchanger for exhaust gas heat recovery - Google Patents

Catalyst-integrated heat exchanger for exhaust gas heat recovery Download PDF

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JP4493799B2
JP4493799B2 JP2000142376A JP2000142376A JP4493799B2 JP 4493799 B2 JP4493799 B2 JP 4493799B2 JP 2000142376 A JP2000142376 A JP 2000142376A JP 2000142376 A JP2000142376 A JP 2000142376A JP 4493799 B2 JP4493799 B2 JP 4493799B2
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catalyst
exhaust gas
heat
inner case
flows
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JP2001323813A (en
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秀孝 新長
純 小野
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T Rad Co Ltd
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T Rad Co Ltd
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    • 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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Description

【0001】
【発明の属する技術分野】
本願発明は、内燃機関等の燃焼装置の排気ガスを浄化する触媒と、排気ガスの熱を回収するための熱交換器とが一体化された排気ガス熱回収用の触媒一体型熱交換器に関する。
【0002】
【従来の技術】
従来、この種の触媒一体型熱交換器として、例えば特開2000−45764号公報で開示されたエンジンの排ガス浄化およびその排ガス熱回収装置が知られている。この装置では、触媒を通過して浄化された排気ガスが熱交換室を流れる際に、該熱交換室に周方向に間隔をおいて配設された複数の熱交換パイプを流れる冷却水との間で熱交換が行われ、排気ガスの熱が冷却水に回収される。
【0003】
【発明が解決しようとする課題】
ところで、この従来技術において、複数(24本)の熱交換パイプは熱交換器本体の上端壁および下端壁により支持される。このとき、十分な熱回収を行うためには多数の熱交換パイプが必要となり、部品点数が増大すると共に、その組立工数が増大して、装置の組立に多大な時間を要することになり、その生産性が必ずしも良好でななかった。また、前記従来技術のように熱交換パイプを環状に配置した場合、各パイプの周囲、特にその径方向内方および外方に、排気ガスが流通するための空間を確保する必要があるため、結果として熱交換器の外径が大きくなっていた。さらに、各熱交換パイプは、ロウ付けや溶接により上端壁および下端壁に固定されるのが通常であるため、ロウ付けや溶接をする分、製造コストが増大する難点があるうえ、ロウ付けまたは溶接する箇所が増加して、この点でも生産性の低下をもたらしていた。
【0004】
本発明は、このような事情に鑑みてなされたものであり、排気ガス熱回収用の触媒一体型熱交換器において、生産性の向上を図ると共に熱交換器のコンパクト化を図ることを共通の目的とし、請求項2記載の発明は、さらに、製造コストの削減を図ることを目的とする。
【0005】
求項1に記載の発明は、排気ガスが流通する内ケースと、該内ケースを囲繞すると共に該内ケースとの間に排気ガス熱の熱回収流体が流通する流体室を形成する外ケースと、前記内ケース内に収容された触媒と、該触媒を通過した排気ガスと前記流体室の熱回収流体と間での熱交換を行う伝熱部とを備え、前記内ケースに流入した燃焼装置の排気ガスが、前記触媒を通過し、次いで前記伝熱部を通過した後、前記内ケースから流出する排気ガス熱回収用の触媒一体型熱交換器において、前記伝熱部は、前記内ケースの筒状の流体室形成部分を外側通路壁とし、前記触媒と前記内ケースとの間に配置された中間筒を内側通路壁として形成された筒状のガス通路と、多数の山部および谷部が屈曲形成されたフィンとを備え、該フィンは、前記流体室形成部分および前記中間筒に前記山部および前記谷部がそれぞれ接触するように前記ガス通路内に配置され、前記中間筒内には、底壁を有する触媒収容筒が設けられ、該収容筒内に、前記触媒がその一端面と前記底壁との間に第1反転室が形成されるように収容され、前記収容筒内の前記触媒の中心部を前記底壁へ向かい貫通して排気ガスの流入管が設けられ、これにより、流入管内をその上流側から下流側に流れて前記触媒の前記一端面に達する排気ガスが、前記第1反転室で反転して前記触媒の前記一端面から触媒中をその他端面へ通過するようにされ、前記収容筒、前記中間筒および前記内ケースを前記流入管の上流側から覆い、かつ前記触媒の前記他端面に接して第2反転室が形成されるように、前記内ケースに蓋体が固定され、前記蓋体は、前記触媒の前記他端面から前記第2反転室内に流入する排気ガスが、前記伝熱部へ反転状態で流入するように形成されていることを特徴とする排気ガス熱回収用の触媒一体型熱交換器である。
【0006】
この請求項1記載の発明によれば、筒状のガス通路に配置されたフィンにより伝熱面積が大きくされているため、触媒を通過して浄化された排気ガスの熱は、排気ガスがガス通路を流通する際、該フィンを介して、熱回収流体が流通する流体室を形成する流体室形成部分に効率よく伝達されて、効率よく熱回収流体に回収される。そして、フィンは流体室形成部分と中間筒との間に配置されて、その山部および谷部が、流体室形成部分および中間筒にそれぞれ接触するようにされているため、流体室形成部分と中間筒にそれぞれ相当する二つの部材の間に熱交換パイプが配置されて、それら部材の間において熱交換パイプの径方向内方および外方に間隙を確保する必要があるものと比較すると、流体室形成部分および中間筒の間の間隙は小さくて済む。
【0007】
その結果、ガス通路に配置されたフィンの大きな伝熱面積によって高い熱交換率が確保されたうえで、フィンが配置される流体室形成部分および中間筒との間の間隙を小さくとどめることが可能となって、熱交換器の外径が大きくなることが抑制され、熱交換器をコンパクトにすることができる。
【0008】
請求項2記載の発明は、請求項1記載の排気ガス熱回収用の触媒一体型熱交換器において、前記フィンは、前記流体室形成部分および前記中間筒の間に圧入されているものである。
【0009】
この請求項2記載の発明によれば、フィンは、外側通路壁と中間筒との間に圧入されることで固定されるため、ロウ付けや溶接が不要になると共に、組立も比較的短時間ですむ。
【0010】
その結果、次の効果が奏される。すなわち、フィンが圧入により固定されることで、ロウ付けや溶接箇所が減少するため、熱交換器の製造コストを削減することができ、さらに熱交換器の組立時間が短縮されるため、生産性が向上する。
【0011】
請求項3記載の発明は、請求項1記載の排気ガス熱回収用の触媒一体型熱交換器において、前記内ケースおよび前記外ケースの少なくとも一方は、両端部が開放した筒状のケース本体と、該両端部にそれぞれ固定された同一仕様の蓋体とを備え、該蓋体には、排気ガスまたは熱回収流体の流入管または流出管が接続される孔が設けられているものである。
【0012】
この請求項3記載の発明によれば、内ケースまたは外ケースの蓋体には、同一仕様のものを共用でき、しかもその共用される蓋体に、流入管または流出管が接続される孔も設けられるため、流入管用および流出管用の孔を個別に設ける必要がない。
その結果、請求項1または請求項2記載の発明の効果に加えて、蓋体が共用されるため、蓋体を形成するための装置の種類を少なくすることが可能となって、製造コストの削減に寄与でき、しかも流入管用および流出管用の孔も共用されるため、それら孔が設けられていない蓋体のみが共用され、それら孔が個別に設けられる場合に比べて、孔の加工工程が単純化されて、生産性の向上に寄与できるという効果が奏される。
【0013】
請求項4記載の発明は、請求項1乃至3のいずれかに記載の排気ガス熱回収用の触媒一体型熱交換器において、前記触媒収容筒と前記中間筒の間に、前記第2反転室からの排気ガスが流入するように、微小間隙をもつ保温層が形成されていることを特徴とする。
【0014】
【発明の実施の形態】
以下、本願発明の実施例を図1ないし図5を参照して説明する。
図1において、本願発明の実施例である排気ガス熱回収用の触媒一体型熱交換器1は、発電機、ポンプ等を駆動するために使用される燃焼装置としての内燃機関から排出された排気ガスが流通する排気系に配置されるものであり、内部に排気ガスが流通する排気ガス室4を形成すべく両端部に蓋体を有する内ケース2と、該内ケース2を略同心に囲繞して配置されて両端部に蓋体を有する外ケース3とを備える。内ケース2と外ケース3との間には間隙が形成され、この間隙により形成される空間は、排気ガスの熱を回収する熱回収流体、例えば前記内燃機関の冷却水が流通する流体室5を形成する。
【0015】
内ケース2は、流入側端部6aおよび流出側端部6bが開放された金属製、例えばステンレス製の円筒状のケース本体6と、その両端部6a,6bにそれぞれ溶接等により気密に固定された流入側蓋体7および流出側蓋体8とを有する。なお、円筒状のケース本体6の中心軸線Lは、熱交換器1の中心軸線Lとなっている。流入側蓋体7は、内ケース2に内燃機関から排出された排気ガスを導入するための金属製、例えばステンレス製の流入管9が気密に接続されて固定される、ケース本体6と略同心の装着孔7aをその中心部に有し、流出側蓋体8は、浄化されかつ熱交換された後の排気ガスを排出するための流出管10が気密に接続されて固定される、ケース本体6と略同心の装着孔8aをその中心部に有する。ここで、流入側蓋体7と流出側蓋体8とは、金属製、例えばステンレス製の板材をプレス加工することにより、同一仕様、すなわち形状、構造、寸法等が同一に形成される。そして、各蓋体7,8は、装着孔7a,8aおよび後述する突起7c,8cを有すると共に、軸方向に延びる外周縁部7b,8bがケース本体6の両端部6a,6bの外周面に嵌合して溶接等により固定される嵌合部を構成する略円板状の部材である。
【0016】
また、図2および図3をも併せて参照すると、外ケース3は、内ケース2のケース本体6との間に径方向間隙を形成すべく内ケース2よりも大きな内径を有すると共に、ケース本体6よりも軸方向の長さが長い、流入側端部11aおよび流出側端部11bが開放された金属製、例えばステンレス製の円筒状のケース本体11と、その両端部11a,11bにそれぞれ溶接等により液密に固定された流入側蓋体12および流出側蓋体13とを有する。流入側蓋体12は、熱交換器1へ熱回収流体を導入するための流入管14が液密に接続されて固定される、中心軸線Lから偏心した位置にある装着孔12aを有し、流出側蓋体13は、熱交換後の熱回収流体を排出するための流出管15が液密に接続されて固定される、中心軸線Lから偏心した位置にある装着孔13aを有する。ここで、流入側蓋体12と流出側蓋体13とは、金属製、例えばステンレス製の板材をプレス加工することにより、同一仕様、すなわち形状、構造、寸法等が同一に形成される。そして、各蓋体12,13は、装着孔12a,13aを有すると共に、軸方向に延びる外周縁部12b,13bがケース本体11の両端部11a,11bの外周面に嵌合して溶接等により固定される嵌合部を構成し、内周縁部12c,13cが流入側蓋体7または流出側蓋体8の外面に装着孔7a,8aと略同心に接合されて液密に固定される接合部を構成する略円環状の部材である。なお、この実施例では、流入管14および流出管15も同一仕様の部材で構成される。
【0017】
流体室5は、主として流入側蓋体12および流出側蓋体8との間に形成される円環状の第1流体室5aと、主としてケース本体6とケース本体11との間に形成される円筒状の第2流体室5bと、主として流出側蓋体13および流入側蓋体7との間に形成される円環状の第3流体室5cとからなる。第2流体室5bは螺旋状の通路から構成され、この螺旋状の通路は、ケース本体6の外周面およびケース本体11の内周面に接触して固定される螺旋管16が、ケース本体6とケース本体11との間を螺旋状に延びて配置されることで形成される。
【0018】
また、第1,第3流体室5a,5cは、中心軸線Lと略同心の環状の通路からなり、第1流体室5aに流入管14が開口し、第3流体室5cに流出管15が開口している。そして、両蓋体12,13は、両装着孔12a,13aが軸方向から見て蓋体12,13の直径方向に対向した位置を占めるように、ケース本体11の両端部11a,11bにそれぞれ固定され、また流入管14は螺旋管16の上流側端部16aと略同一の周方向位置にあり、流出管15は螺旋管16の下流側端部16bと略同一の周方向位置にある。
【0019】
一方、排気ガス室4を形成する内ケース2の内部には、円筒状に形成された触媒17およびその収容筒18が、内ケース2と略同心に配置されて収容される。この触媒17は、排気ガス中に含まれているHC、CO等の有害成分を無害化して排気ガスを浄化するそれ自体は周知の触媒17であり、上流側端部18aおよび下流側端部18bが開放した金属製、例えばステンレス製の円筒状の収容筒18に気密に挿入されて収容される。触媒17の内側に収容筒18と略同心に設けられた貫通孔からなる中心孔17cには、流入管9が気密に挿入され、排気ガスの流れに対して上流に位置する上流側端部9aは、流入側蓋体7を貫通して内ケース2の外側に位置し、内燃機関の排気管と熱交換器1とを接続するための接続フランジ19に圧入される。なお、19aは、締結用ボルトのための4つのネジ孔である(図2参照)。また、流入管9の下流側端部9bは、触媒17において、排気ガスの流れに対して上流に位置する上流側端面17aと略面一になるようにされる。したがって、触媒17においては、その上流側端面17aおよび下流側端面17bが、それぞれ排気ガスの流入口および流出口になる。
【0020】
収容筒18の上流側端部18aは、触媒17の上流側端面17aよりも軸方向に所定長さ延び、上流側端部18aに気密に固定された円板からなる底壁20により閉塞される。そして、触媒17の上流側端面17aと底壁20との間に、流入管9から流入した排気ガスが径方向外方に向かい、その後反転して触媒17の上流側端面17aに向かう流れが生じる第1反転室21が形成される。それゆえ、流入管9は第1反転室21の中心部に開口している。なお、収容筒18の下流側端部18bは、流入側蓋体7に向かって開放しており、触媒17の下流側端面17bと略面一とされる。
【0021】
さらに、内ケース2内には、収容筒18とケース本体6との間において、収容筒18と略同心に径方向の微小間隙(後述する、ケース本体6と中間筒22との間の径方向の所定間隙の1/5程度)を介して金属製、例えばステンレス製の円筒状の中間筒22が収容される。収容筒18よりも長い軸方向長さを有する中間筒22の下流側端部22bは、収容筒18の上流側端部18aよりも軸方向に所定長さ延び、該下流側端部22bに、中間筒22と略同心の小孔23aが設けられた円板からなる有孔底壁23が気密に固定される。それゆえ、底壁20と有孔底壁23との間に、微小間隙により形成される筒状の空間から形成される保温層24から流入した排気ガスが集合する第1集合室25が形成される。そして、流出管10に対して略同心に配置された小孔23aは、排気ガスを第1集合室25から流出させると共に、中心軸線Lが上下方向を指向するように配置されて、流出管10が熱交換器1の下部に配置される場合は、凝縮して液体となった排気ガス中の水分を第1集合室25から排出するドレン孔としても機能する。また、中間筒22の上流側端部22aは、流入側蓋体7に向かって開放しており、触媒17の下流側端面17bと略面一とされる。
【0022】
また、ケース本体6は、触媒17の下流側端面17b、収容筒18の下流側端部18bおよび中間筒22の上流側端部22aよりも軸方向に所定長さ延びると共に、中間筒22の下流側端部22bよりも軸方向に延びている。そして、触媒17の下流側端面17b、収容筒18の下流側端部18bおよび中間筒22の上流側端部22aと、流入側蓋体7との間に、触媒17の下流側端面17bから流入した浄化後の排気ガスの流れの向きが反転して、保温層24の上流側開口24aおよび後述する伝熱部28のガス通路29の上流側開口29aに向かう流れが生じる第2反転室26が形成される。それゆえ、触媒17を通過した直後の高温の排気ガスのうち、触媒17の保温を行うのに十分な量である少量が保温層24に流入して、残りは全てガス通路29に流入する。さらに、有孔底壁23と流出側蓋体8との間に、ガス通路29の下流端開口29bから流入した熱交換後の排気ガスが集合する第2集合室27が形成され、該第2集合室27に流出管10が開口する。
【0023】
一方、触媒17と流体室5との間に配置されて、浄化された排気ガスと熱回収流体との熱交換を行うための伝熱部28は、内ケース2において流体室5形成部分でもあるケース本体6を外側通路壁とし、中間筒22を内側通路壁として形成された円筒状のガス通路29と、後述する蛇腹状のフィン30とからなる。
【0024】
図4および図5に図示されるように、フィン30は、1枚の金属製、例えばステンレス製の薄板を交互に多数回折り返すことで形成された多数の山部30cおよび谷部30dを有すると共に、中間筒22と略同一の軸方向長さを有し、それら山部30cがケース本体6の内周面に、それら谷部30dが中間筒22の外周面にそれぞれ接触する態様で、径方向に所定間隙をおいて配置されたケース本体6と中間筒22との間の全周に渡って、径方向に押圧された状態で圧入される。そして、ケース本体6と中間筒22との間に形成される全体として円筒状のガス通路29は、フィン30によって、軸方向に延びる多数の小ガス通路29cに周方向に分割される。なお、熱交換器1を組み立てるに当たっては、このガス通路29を形成するケース本体6と、中間筒22と、両者の間に圧入されて、上流側端部30aおよび下流側端部30bが中間筒22の上流側端部22aおよび下流側端部22bとそれぞれ略面一となったフィン30とが、一つのユニットとなるように、予め組み付けられる。
【0025】
さらに、図1ないし図3に図示されるように、流入側蓋体7および流出側蓋体8には、内ケース2の内部に向けて軸方向に突出する3個の突起7c,8cが、同一円周上で周方向に等間隔に設けられている。そして、流入側蓋体7においては、3個の突起7cが触媒17の下流側端面17bに当接することで、第2反転室26の軸方向の寸法を予め設計された値になるようにすると共に、内ケース2に対する触媒17の軸方向の位置決めを容易にし、さらに収容筒18と、内ケース2および微小間隙を介して配置される中間筒22との同心性が確実にしかも容易に得られるようにしている。また、流出側蓋体8においては、3個の突起8cが有孔底壁23に当接することで、第2集合室27の軸方向の寸法が、第2反転室26のそれと同一になるようにして、第2反転室26および第2集合室27での排気ガスの流動性を略同等とすると共に、内ケース2に対する中間筒22の軸方向の位置決めを容易にしている。
【0026】
次に、この実施例の作用について説明する。
図示されない内燃機関から排出された排気ガスは、流入管9を、触媒17への挿入部分で触媒17を加熱しつつ矢印A方向に流れて第1反転室21の中心部に流入し、底壁20に当たってその流れの向きが変更されて径方向外方に略均一に流れた後、反転されて触媒17に流入して、浄化される。浄化された排気ガスは触媒17から第2反転室26に流入し、流入側蓋体7に当たってその流れの向きが変更されて径方向外方に略均一に流れた後、反転されて、その少量が保温層24に流入する。
【0027】
保温層24に流入した少量の排気ガスは、収容筒18と中間筒22の間を軸方向に流れて、小孔23aから流出するため、保温層24には常時排気ガスの流れが存在し、触媒17通過直後の高温の排気ガスが効率よく保温層24に流入する。したがって、熱回収流体と熱交換を行う伝熱部28を構成する中間筒22は比較的低温となるものの、保温層24には高温の排気ガスが常時供給されて、保温層24の排気ガスがスムーズに入れ替わるので、保温層24に存在する排気ガスがその低温の影響を受けることは殆どなく、保温層24が高温に維持され、触媒17も浄化率の高い高温状態に維持される。
【0028】
第2反転室26の残りの全て排気ガスは、伝熱部28のガス通路29に流入して、多数の小ガス通路29cを軸方向に流れる。そして、ガス通路29内は、全周に渡って配置されたフィン30により伝熱面積が大きくされているため、触媒17通過直後の高温の排気ガスの熱は、排気ガスがガス通路29を流通する際、フィン30を介して、熱回収流体が流通する流体室5を形成するケース本体6に効率よく伝達されて、高い熱交換率での熱交換が行われる。
【0029】
ケース本体6を介して熱回収流体と熱交換をした後の低温の排気ガスは、外周側から第2集合室27に流入し、その流れの向きが径方向内方に変更されて中心部に向かい、流出管10を矢印B方向に流れて、熱交換器1の外部に流出する。
【0030】
一方、熱回収流体は、流入管9を矢印C方向に流れて、第1流体室5aに流入して流出側蓋体8を介して第2集合室27の排気ガスと熱交換をして、排気ガスの熱を回収する。その後、熱回収流体は螺旋状の長くされた通路からなる第2流体室5bを流れて、伝熱部28を流れる排気ガスと熱交換をして、排気ガスの熱を回収する。さらに、第2流体室5bを経て第3流体室5cに流入した熱回収流体は、流入側蓋体7を介して第2反転室26の排気ガスと熱交換をして、排気ガスの熱を回収した後、流出管15を矢印D方向に流れて、熱交換器1での熱回収を終了して、外部に流出する。
【0031】
この実施例は、前述のように構成されているので、次のような効果を奏する。
ガス通路29の全周に配置されたフィン30によって大きな伝熱面積が確保されて高い熱交換率が得られる。また、触媒17通過直後の高温の排気ガスが伝熱部28に流入するため、伝熱部28で排気ガスの熱を高い熱交換率で熱回収できる。
【0032】
フィン30はケース本体6と中間筒22との間に配置されて、その山部30cおよび谷部30dが、ケース本体6と中間筒22にそれぞれ接触するようにされているため、ケース本体6および中間筒22にそれぞれ相当する二つの部材の間に熱交換パイプが配置されて、それら部材の間において熱交換パイプの径方向内方および外方に間隙を確保する必要があるものと比較すると、ケース本体6と中間筒22の間の径方向の間隙は小さくて済む。そのため、フィン30の大きな伝熱面積によって高い熱交換率が確保されたうえで、フィン30が配置されるケース本体6と中間筒22との間の径方向の間隙を小さくとどめることが可能となって、熱交換器1の外径が大きくなることが抑制され、熱交換器1をコンパクトにすることができる。
【0033】
フィン30は、ケース本体6と中間筒22との間に圧入されることで固定されるため、ロウ付けや溶接が不要となるとと共に、組立も比較的短時間ですむ。その結果、フィン30が圧入により固定されることで、ロウ付けや溶接箇所が減少するため、熱交換器1の製造コストを削減することができ、さらに熱交換器1の組立時間が短縮されるため、生産性が向上する。
【0034】
さらに、フィン30は、一枚の薄板から形成されるので、部品点数を削減できて組立工数を削減できること、さらに、ケース本体6と中間筒22とフィン30とが、予め一つのユニットとなるようにされることから組立性が向上して、熱交換器1の生産性の向上に寄与できる。
【0035】
内ケース2の両蓋体7,8には同一仕様のものを共用でき、また外ケース3の両蓋体12,13にも同一仕様のものを共用できるので、それら蓋体7,8,12,13を形成するためのプレス加工装置の種類を少なくすることが可能となって、製造コストの削減に寄与できる。しかも、共用される蓋体7,8,12,13に、流入管9,14または流出管10,15が接続される装着孔7a,8a,12a,13aも設けられるため、流入管用および流出管用の孔を個別に設ける必要がなく、それら装着孔が設けられていない蓋体のみが共用され、それら装着孔が個別に設けられる場合に比べて、装着孔の加工工程が単純化されて、生産性の向上に寄与できる。また、流入管14および流出管15も共用できるので、この点でも製造コスト削減に寄与できる。
【0036】
保温層24の排気ガスがスムーズに入れ替わるので、保温層24により触媒17が高い浄化率で機能する高温状態が維持され、触媒17の浄化性能を維持または向上できる。また、触媒17の中心孔17cに流入管9が挿入され、その保温層24が設けられていることで、内燃機関の始動時から触媒17が活性化するまでの時間が短縮されるため、浄化性能を向上させることができる。
【0037】
流入管9からの排気ガスは、第1反転室21で径方向外方に略均一に流れて触媒17に流入し、第2反転室26で径方向外方に略均一に流れて伝熱部28を通った後、第2集合室27で径方向内方に流れて中心部に向かい、流出管10から熱交換器1の外部に流出する。そのため、排気ガスは、内ケース2内で全体に渡って満遍なくしかもスムーズに流れる。このように、内ケース2内での排気ガスの流れおよび流出管10からの流出がスムーズであることから、この点でも伝熱部28、流入側,流出側蓋体7,8からの伝熱による熱交換率の向上に寄与できる。
【0038】
さらに、排気ガスは、触媒17の中心孔17cに挿入された流入管9の下流側端部9bから第1反転室21に流入し、第1反転室21で径方向の略均一に流れて触媒17に流入するため、排気ガスを反転させずに触媒に流入させる場合に必要となる、小径の流入管から大径の触媒に一様に排気ガスが流入するようにするために軸方向にある程度の長さ有するディフューザ部が不要となるので、流入管9の上流側端部9aから触媒17の、上流側端部9a側とは反対側の端面である上流側端面17aまでの軸方向の寸法を短くすることができて、熱交換器1の軸方向の長さを短くすることができ、コンパクトな熱交換器1とすることができる。
【0039】
また、熱交換器1の軸方向の長さが短いにも拘わらず、熱回収流体は、第1,第3流体室5a,5cにおける、それぞれ流出側蓋体8および流入側蓋体7を介しての熱回収に加えて、螺旋状に長くされた通路からなる第2流体室5bにおける伝熱部28のケース本体6を介しての熱回収により、排気ガスの熱を効果的に回収することができる。
【0040】
流入側蓋体7の3個の突起7cが触媒17の下流側端面に当接するようにされているため、第2反転室26の軸方向の寸法を設定値にすることが容易にできると共に、内ケース2に対する触媒17の軸方向の位置決めが容易にでき、さらに収容筒18と、内ケース2および中間筒22との同心性を確実にしかも容易に得ることができる。また、流出側蓋体8の3個の突起8cが有孔底壁23に当接するようにされているため、第2集合室27の軸方向の寸法が第2反転室26のそれと同一になるようにして、第2反転室26および第2集合室27での排気ガスの流動性を略同等とすることができると共に、内ケース2に対する中間筒22の軸方向の位置決めが容易にできる。
【0041】
以下、前述した実施例の一部の構成を変更した実施例について、変更した構成に関して説明する。
前記実施例では、内ケース2および外ケース3のそれぞれの流入側蓋体7,12および流出側蓋体8,13が共用されていたが、内ケース2および外ケース3のいずれか一方の流入側蓋体7,12および流出側蓋体8,13が共用されるようになっていてもよい。また、各ケース本体6,11、中間筒22、収容筒18は、円筒状以外の筒状の部材であってもよい。
【0042】
前記実施例では、フィン30は、ケース本体6と中間筒22との間に圧入されることで固定されたが、フィンの固定をロウ付けにより行うこともできる。そして、この場合でも、シート状のロウ材を、フィン30とケース本体6との間およびフィン30と中間筒22との間にぞれぞれ挟持させた状態で、炉中に入れて加熱することで、簡単にフィン30をケース本体6および中間筒22に固定できるので、熱交換パイプを使用した前記従来技術に比べ組立工数の削減ができ、生産性が向上する。
【0043】
さらに、前記実施例では、フィン30は1枚の薄板から形成されていたが、ガス通路29に配置されるフィン30を、1枚の薄板から形成されたフィンを、ガス通路29での排気ガスの流れに対して直列に、複数個、例えば2個または3個配置して構成することもできる。そして、この場合にも部品点数は、熱交換パイプを使用した前記従来技術に比べて少なくなり、組立工数が削減されて、生産性が向上する。
【0044】
また、燃焼装置としては、内燃機関以外に、ボイラー等、燃焼を行う装置であればどのような装置でもよく、その場合には、熱回収流体としては、給湯用等の単なる水であってよく、さらには空気等の気体であってもよい。また、両蓋体7,8に形成された突起7c,8cは3個であったが、4個以上であってもよい。
【図面の簡単な説明】
【図1】本願発明の実施例である排気ガス熱回収用の触媒一体型熱交換器の縦断面図であり、図2のI−I線断面図である。
【図2】図1のII矢視図である。
【図3】図1のIII矢視図である。
【図4】図1のIV−IV線断面図である。
【図5】図4の部分拡大図である。
【符号の説明】
1…熱交換器、2…内ケース、3…外ケース、4…排気ガス室、5…流体室、6…ケース本体、7…流入側蓋体、7a…装着孔、8…流出側蓋体、8a…装着孔、9…流入管、10…流出管、11…ケース本体、12…流入側蓋体、13…流出側蓋体、14…流入管、15…流出管、16…螺旋管、17…触媒、18…収容筒、19…接続フランジ、20…底壁、21…第1反転室、22…中間筒、23…有孔底壁、23a…小孔、24…保温層、25…第1集合室、26…第2反転室、27…第2集合室、28…伝熱部、29…ガス通路、30…フィン、30c…山部、30d…谷部、
L…中心軸線。
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a catalyst-integrated heat exchanger for exhaust gas heat recovery in which a catalyst for purifying exhaust gas of a combustion apparatus such as an internal combustion engine and a heat exchanger for recovering heat of the exhaust gas are integrated. .
[0002]
[Prior art]
Conventionally, as this type of catalyst-integrated heat exchanger, for example, an exhaust gas purification of an engine and an exhaust gas heat recovery device disclosed in JP 2000-45764 A are known. In this apparatus, when the exhaust gas that has been purified by passing through the catalyst flows through the heat exchange chamber, the exhaust gas is mixed with cooling water that flows through a plurality of heat exchange pipes arranged in the heat exchange chamber at intervals in the circumferential direction. Heat exchange is performed between the two, and the heat of the exhaust gas is recovered in the cooling water.
[0003]
[Problems to be solved by the invention]
By the way, in this prior art, a plurality (24) of heat exchange pipes are supported by the upper end wall and the lower end wall of the heat exchanger body. At this time, in order to perform sufficient heat recovery, a large number of heat exchange pipes are required, the number of parts increases, the assembly man-hours increase, and it takes a lot of time to assemble the device. Productivity was not always good. In addition, when the heat exchange pipes are arranged in an annular shape as in the prior art, it is necessary to secure a space for the exhaust gas to circulate around each pipe, particularly in the radially inward and outward directions, As a result, the outer diameter of the heat exchanger was increased. Furthermore, since each heat exchange pipe is usually fixed to the upper end wall and the lower end wall by brazing or welding, there is a problem that the manufacturing cost increases due to brazing or welding, and brazing or The number of locations to be welded has increased, and this has led to a decrease in productivity.
[0004]
  Main departureAkira was made in view of these circumstances.And exhaustA common object of the catalyst-integrated heat exchanger for recovering heat of gas gas is to improve productivity and to make the heat exchanger compact, and the invention according to claim 2 further reduces the manufacturing cost. It aims to plan.
[0005]
  ContractThe invention described in claim 1 includes an inner case in which exhaust gas flows, and an outer case that surrounds the inner case and forms a fluid chamber in which a heat recovery fluid of exhaust gas heat flows between the inner case and the inner case. A combustion apparatus having a catalyst housed in the inner case, and a heat transfer section for exchanging heat between the exhaust gas that has passed through the catalyst and the heat recovery fluid in the fluid chamber, The exhaust gas passes through the catalyst and then passes through the heat transfer section, and then flows out of the inner case. Then, the heat transfer section is connected to the inner case. A cylindrical gas chamber formed using the cylindrical fluid chamber forming portion as an outer passage wall, and an intermediate tube disposed between the catalyst and the inner case as an inner passage wall, and a number of peaks and valleys A fin having a bent portion, and the fin includes the fluid The peaks and the valleys are disposed in the gas passage so as to respectively contact forming portions and said intermediate cylinderThe intermediate cylinder is provided with a catalyst accommodating cylinder having a bottom wall, and the catalyst is accommodated in the accommodating cylinder so that a first inversion chamber is formed between one end surface of the intermediate cylinder and the bottom wall. And an exhaust gas inflow pipe is provided through the central portion of the catalyst in the housing cylinder toward the bottom wall, whereby the exhaust gas flows from the upstream side to the downstream side in the inflow pipe. Exhaust gas reaching the end surface is reversed in the first reversing chamber so as to pass through the catalyst from the one end surface of the catalyst to the other end surface, and the inflow pipe passes through the storage tube, the intermediate tube, and the inner case. A lid body is fixed to the inner case so as to form a second reversing chamber in contact with the other end surface of the catalyst and from the other end surface of the catalyst. Exhaust gas flowing into the second reversing chamber flows into the heat transfer section in a reversing state. It is formed so as toA catalyst-integrated heat exchanger for recovering exhaust gas heat.
[0006]
According to the first aspect of the present invention, since the heat transfer area is increased by the fins arranged in the cylindrical gas passage, the heat of the exhaust gas purified by passing through the catalyst is obtained from the exhaust gas. When flowing through the passage, the heat recovery fluid is efficiently transmitted to the fluid chamber forming portion that forms the fluid chamber through which the heat recovery fluid flows, and is efficiently recovered into the heat recovery fluid. And since the fin is disposed between the fluid chamber forming portion and the intermediate cylinder, and the crest and trough thereof are in contact with the fluid chamber forming portion and the intermediate cylinder, respectively, the fluid chamber forming portion and Compared with the case where a heat exchange pipe is arranged between two members corresponding to the intermediate cylinders and a gap needs to be secured between the members in the radially inward and outward directions of the heat exchange pipe. The gap between the chamber forming portion and the intermediate cylinder may be small.
[0007]
As a result, a large heat transfer area of the fins arranged in the gas passage ensures a high heat exchange rate, and the gap between the fluid chamber forming portion where the fins are arranged and the intermediate cylinder can be kept small. Thus, an increase in the outer diameter of the heat exchanger is suppressed, and the heat exchanger can be made compact.
[0008]
According to a second aspect of the present invention, in the catalyst-integrated heat exchanger for exhaust gas heat recovery according to the first aspect, the fin is press-fitted between the fluid chamber forming portion and the intermediate cylinder. .
[0009]
According to the second aspect of the present invention, since the fin is fixed by being press-fitted between the outer passage wall and the intermediate cylinder, brazing and welding are not required, and assembly is also relatively short. That's okay.
[0010]
As a result, the following effects are exhibited. In other words, since the fins are fixed by press fitting, brazing and welding locations are reduced, so that the manufacturing cost of the heat exchanger can be reduced, and the assembly time of the heat exchanger is further reduced, so that productivity Will improve.
[0011]
According to a third aspect of the present invention, in the catalyst-integrated heat exchanger for exhaust gas heat recovery according to the first aspect, at least one of the inner case and the outer case includes a cylindrical case body having both ends open. And a lid of the same specification fixed to each of the both ends, and the lid is provided with a hole to which an inflow pipe or an outflow pipe for exhaust gas or heat recovery fluid is connected.
[0012]
  According to the third aspect of the present invention, the lid of the inner case or the outer case can share the same specification, and the inflow pipe or the outflow pipe is connected to the shared lid. Since it is provided, it is not necessary to provide holes for the inflow pipe and the outflow pipe separately.
  As a result, in addition to the effects of the invention described in claim 1 or claim 2, since the lid is shared, it is possible to reduce the number of types of devices for forming the lid, thereby reducing the manufacturing cost. Since the holes for the inflow pipe and the outflow pipe can also be shared, only the lid that is not provided with these holes is shared, and the hole machining process is reduced compared to the case where these holes are provided individually. Simplified and effective in improving productivity.
[0013]
  The invention according to claim 44. The catalyst-integrated heat exchanger for exhaust gas heat recovery according to claim 1, wherein the exhaust gas from the second inversion chamber flows between the catalyst housing cylinder and the intermediate cylinder. In addition, a heat insulating layer having a minute gap is formed.
[0014]
DETAILED DESCRIPTION OF THE INVENTION
Embodiments of the present invention will be described below with reference to FIGS.
In FIG. 1, a catalyst-integrated heat exchanger 1 for exhaust gas heat recovery, which is an embodiment of the present invention, is exhausted from an internal combustion engine as a combustion device used to drive a generator, a pump, and the like. An inner case 2 having lids at both ends so as to form an exhaust gas chamber 4 through which exhaust gas flows, and an inner case 2 that is disposed substantially concentrically are disposed in an exhaust system through which gas flows. And an outer case 3 having lids at both ends. A gap is formed between the inner case 2 and the outer case 3, and a space formed by the gap is a fluid chamber 5 in which a heat recovery fluid that recovers the heat of the exhaust gas, for example, cooling water of the internal combustion engine flows. Form.
[0015]
The inner case 2 is hermetically fixed by welding or the like to a metal case, for example, a stainless steel cylindrical case body 6 with an inflow side end portion 6a and an outflow side end portion 6b open, and both ends 6a and 6b. Inflow side lid body 7 and outflow side lid body 8. The central axis L of the cylindrical case body 6 is the central axis L of the heat exchanger 1. The inflow side cover body 7 is substantially concentric with the case body 6 to which an inflow pipe 9 made of metal, for example, stainless steel, for introducing the exhaust gas discharged from the internal combustion engine is hermetically connected and fixed to the inner case 2. A mounting body 7a at the center thereof, and the outflow side cover 8 has a case main body in which an outflow pipe 10 for exhausting exhaust gas after being purified and heat exchanged is hermetically connected and fixed. 6 has a mounting hole 8a substantially concentric with the central portion thereof. Here, the inflow side lid body 7 and the outflow side lid body 8 are formed to have the same specifications, that is, the same shape, structure, dimensions, and the like by pressing a metal plate, for example, a stainless steel plate. The lid bodies 7 and 8 have mounting holes 7a and 8a and projections 7c and 8c, which will be described later, and outer peripheral edge portions 7b and 8b extending in the axial direction on the outer peripheral surfaces of both end portions 6a and 6b of the case body 6. It is a substantially disk-shaped member that constitutes a fitting portion that is fitted and fixed by welding or the like.
[0016]
2 and 3 together, the outer case 3 has a larger inner diameter than the inner case 2 so as to form a radial gap between the inner case 2 and the case main body 6, and the case main body. A cylindrical case body 11 made of a metal, for example, stainless steel, having an inflow end 11a and an outflow end 11b that are longer in the axial direction than 6, and welded to both ends 11a and 11b, respectively. An inflow side lid body 12 and an outflow side lid body 13 that are liquid-tightly fixed by, for example. The inflow side cover body 12 has a mounting hole 12a at a position eccentric from the central axis L, to which an inflow pipe 14 for introducing a heat recovery fluid into the heat exchanger 1 is connected and fixed in a liquid-tight manner. The outflow side cover body 13 has a mounting hole 13a at a position eccentric from the central axis L, to which an outflow pipe 15 for discharging the heat recovery fluid after heat exchange is connected and fixed in a liquid-tight manner. Here, the inflow side lid body 12 and the outflow side lid body 13 are formed to have the same specifications, that is, the same shape, structure, dimensions, and the like by pressing a metal plate, for example, a stainless steel plate. The lid bodies 12 and 13 have mounting holes 12a and 13a, and outer peripheral edge portions 12b and 13b extending in the axial direction are fitted to the outer peripheral surfaces of both end portions 11a and 11b of the case main body 11 by welding or the like. A fixed fitting portion is formed, and the inner peripheral edge portions 12c and 13c are joined to the outer surface of the inflow side lid body 7 or the outflow side lid body 8 substantially concentrically with the mounting holes 7a and 8a and fixed in a liquid-tight manner. It is the substantially annular member which comprises a part. In this embodiment, the inflow pipe 14 and the outflow pipe 15 are also composed of members having the same specifications.
[0017]
The fluid chamber 5 includes an annular first fluid chamber 5a formed mainly between the inflow side lid body 12 and the outflow side lid body 8, and a cylinder formed mainly between the case body 6 and the case body 11. And the annular third fluid chamber 5c formed mainly between the outflow side lid body 13 and the inflow side lid body 7. The second fluid chamber 5b is formed of a spiral passage, and the spiral passage 16 includes a spiral tube 16 fixed in contact with the outer peripheral surface of the case body 6 and the inner peripheral surface of the case body 11. And the case main body 11 are formed by extending in a spiral manner.
[0018]
The first and third fluid chambers 5a and 5c are formed of an annular passage substantially concentric with the central axis L, the inflow pipe 14 is opened in the first fluid chamber 5a, and the outflow pipe 15 is formed in the third fluid chamber 5c. It is open. The lid bodies 12 and 13 are respectively provided at both end portions 11a and 11b of the case body 11 so that the mounting holes 12a and 13a occupy positions in the diameter direction of the lid bodies 12 and 13 when viewed from the axial direction. The inflow pipe 14 is fixed at the substantially same circumferential position as the upstream end 16a of the spiral pipe 16, and the outflow pipe 15 is located at the same circumferential position as the downstream end 16b of the spiral pipe 16.
[0019]
  On the other hand, inside the inner case 2 that forms the exhaust gas chamber 4, a catalyst 17 that is formed in a cylindrical shape and its accommodating cylinder 18 are arranged and accommodated substantially concentrically with the inner case 2. The catalyst 17 is a catalyst 17 that is known per se to purify exhaust gas by detoxifying harmful components such as HC and CO contained in the exhaust gas, and includes an upstream end 18a and a downstream end 18b. Is inserted in an airtight manner into a metal-made, for example, stainless-steel, cylindrical housing cylinder 18 and accommodated. An inflow pipe 9 is hermetically inserted into a center hole 17c formed of a through hole provided substantially concentrically with the accommodating cylinder 18 inside the catalyst 17, and an upstream end 9a located upstream with respect to the flow of exhaust gas. Is positioned on the outside of the inner case 2 through the inflow side lid 7 and is press-fitted into a connection flange 19 for connecting the exhaust pipe of the internal combustion engine and the heat exchanger 1. Reference numeral 19a denotes four screw holes for fastening bolts (see FIG. 2). Further, the downstream end 9b of the inflow pipe 9 is an upstream end surface located upstream of the exhaust gas flow in the catalyst 17.17aAnd be made to be almost flush with each other. Therefore, in the catalyst 17, the upstream end surface 17a and the downstream end surface 17b serve as an exhaust gas inlet and an outlet, respectively.
[0020]
The upstream end portion 18a of the housing cylinder 18 extends a predetermined length in the axial direction from the upstream end surface 17a of the catalyst 17, and is closed by a bottom wall 20 made of a disk that is airtightly fixed to the upstream end portion 18a. . Then, between the upstream end face 17a of the catalyst 17 and the bottom wall 20, the exhaust gas flowing in from the inflow pipe 9 goes radially outward, and then reverses to flow toward the upstream end face 17a of the catalyst 17. A first inversion chamber 21 is formed. Therefore, the inflow pipe 9 is open at the center of the first inversion chamber 21. The downstream end portion 18b of the storage cylinder 18 is open toward the inflow side lid body 7, and is substantially flush with the downstream end surface 17b of the catalyst 17.
[0021]
Further, in the inner case 2, a radial gap between the housing cylinder 18 and the case body 6 is substantially concentric with the housing cylinder 18 (a radial direction between the case body 6 and the intermediate cylinder 22 described later). The cylindrical intermediate tube 22 made of metal, for example, stainless steel, is accommodated through a predetermined gap (about 1/5 of the predetermined gap). The downstream end 22b of the intermediate cylinder 22 having an axial length longer than the housing cylinder 18 extends a predetermined length in the axial direction from the upstream end 18a of the housing cylinder 18, and the downstream end 22b A perforated bottom wall 23 made of a disk provided with a small hole 23a substantially concentric with the intermediate cylinder 22 is fixed in an airtight manner. Therefore, a first collecting chamber 25 is formed between the bottom wall 20 and the perforated bottom wall 23 in which the exhaust gas flowing in from the heat insulating layer 24 formed from the cylindrical space formed by the minute gaps gathers. The The small holes 23a disposed substantially concentrically with respect to the outflow pipe 10 allow exhaust gas to flow out from the first collecting chamber 25 and are arranged so that the central axis L is directed in the vertical direction. Is disposed in the lower part of the heat exchanger 1, it also functions as a drain hole for discharging moisture in the exhaust gas condensed into a liquid from the first collecting chamber 25. Further, the upstream end 22 a of the intermediate cylinder 22 is open toward the inflow side lid 7 and is substantially flush with the downstream end surface 17 b of the catalyst 17.
[0022]
Further, the case body 6 extends a predetermined length in the axial direction from the downstream end face 17b of the catalyst 17, the downstream end 18b of the housing cylinder 18 and the upstream end 22a of the intermediate cylinder 22, and is downstream of the intermediate cylinder 22. It extends in the axial direction from the side end 22b. Then, the downstream end surface 17 b of the catalyst 17, the downstream end portion 18 b of the housing cylinder 18, the upstream end portion 22 a of the intermediate cylinder 22, and the inflow side lid body 7 flow from the downstream end surface 17 b of the catalyst 17. The direction of the flow of the exhaust gas after purification is reversed, and the second reversing chamber 26 in which the flow toward the upstream opening 24a of the heat retaining layer 24 and the upstream opening 29a of the gas passage 29 of the heat transfer section 28 described later is generated. It is formed. Therefore, of the high-temperature exhaust gas immediately after passing through the catalyst 17, a small amount that is sufficient to keep the catalyst 17 warm flows into the heat retaining layer 24, and all the rest flows into the gas passage 29. Further, a second collecting chamber 27 is formed between the perforated bottom wall 23 and the outflow side lid 8, in which exhaust gas after heat exchange that has flowed in from the downstream end opening 29 b of the gas passage 29 gathers. The outflow pipe 10 opens into the collecting chamber 27.
[0023]
On the other hand, the heat transfer portion 28 that is disposed between the catalyst 17 and the fluid chamber 5 and performs heat exchange between the purified exhaust gas and the heat recovery fluid is also a fluid chamber 5 forming portion in the inner case 2. The case body 6 includes a cylindrical gas passage 29 formed with the outer passage wall as an outer passage wall and the intermediate tube 22 as an inner passage wall, and a bellows-like fin 30 described later.
[0024]
As shown in FIGS. 4 and 5, the fin 30 has a large number of crests 30c and troughs 30d formed by bending a single metal thin plate made of, for example, stainless steel alternately. The intermediate cylinder 22 has substantially the same axial length, the crests 30c are in contact with the inner peripheral surface of the case body 6 and the troughs 30d are in contact with the outer peripheral surface of the intermediate cylinder 22 in the radial direction. The case body 6 and the intermediate cylinder 22 which are arranged with a predetermined gap are press-fitted in a radially pressed state over the entire circumference. The generally cylindrical gas passage 29 formed between the case body 6 and the intermediate cylinder 22 is divided by the fins 30 into a large number of small gas passages 29c extending in the axial direction in the circumferential direction. In assembling the heat exchanger 1, the case main body 6 forming the gas passage 29 and the intermediate cylinder 22 are press-fitted between them, and the upstream end 30a and the downstream end 30b are connected to the intermediate cylinder. The fins 30 that are substantially flush with the upstream end 22a and the downstream end 22b of 22 are assembled in advance so as to form one unit.
[0025]
Further, as shown in FIGS. 1 to 3, the inflow side lid body 7 and the outflow side lid body 8 have three projections 7 c and 8 c that project in the axial direction toward the inside of the inner case 2. It is provided at equal intervals in the circumferential direction on the same circumference. In the inflow side lid body 7, the three protrusions 7 c abut on the downstream end surface 17 b of the catalyst 17, so that the axial dimension of the second reversing chamber 26 becomes a predesigned value. In addition, the positioning of the catalyst 17 in the axial direction with respect to the inner case 2 is facilitated, and the concentricity between the housing cylinder 18 and the inner casing 2 and the intermediate cylinder 22 disposed through the minute gap can be obtained reliably and easily. I am doing so. Further, in the outflow side lid 8, the three projections 8c abut against the perforated bottom wall 23 so that the axial dimension of the second collecting chamber 27 is the same as that of the second inversion chamber 26. Thus, the fluidity of the exhaust gas in the second reversing chamber 26 and the second collecting chamber 27 is made substantially equal, and the axial positioning of the intermediate cylinder 22 with respect to the inner case 2 is facilitated.
[0026]
Next, the operation of this embodiment will be described.
Exhaust gas discharged from an internal combustion engine (not shown) flows through the inflow pipe 9 in the direction of arrow A while heating the catalyst 17 at the portion inserted into the catalyst 17 and flows into the center of the first reversing chamber 21, The direction of the flow is changed when it hits 20 and flows almost uniformly outward in the radial direction, and then is reversed and flows into the catalyst 17 to be purified. The purified exhaust gas flows into the second reversing chamber 26 from the catalyst 17, hits the inflow side cover body 7, changes its flow direction, flows substantially uniformly outward in the radial direction, and then is reversed and a small amount thereof. Flows into the heat insulating layer 24.
[0027]
A small amount of exhaust gas that has flowed into the heat insulating layer 24 flows between the accommodating cylinder 18 and the intermediate cylinder 22 in the axial direction and flows out from the small holes 23a.Therefore, a flow of exhaust gas always exists in the heat insulating layer 24, Hot exhaust gas immediately after passing through the catalyst 17 efficiently flows into the heat retaining layer 24. Therefore, although the intermediate cylinder 22 constituting the heat transfer section 28 that exchanges heat with the heat recovery fluid is relatively low in temperature, the high temperature exhaust gas is always supplied to the heat retaining layer 24, and the exhaust gas in the heat retaining layer 24 is Since the gas is smoothly switched, the exhaust gas existing in the heat insulating layer 24 is hardly affected by the low temperature, the heat insulating layer 24 is maintained at a high temperature, and the catalyst 17 is also maintained in a high temperature state with a high purification rate.
[0028]
  All remaining in second reversal chamber 26ofThe exhaust gas flows into the gas passages 29 of the heat transfer section 28 and flows in the axial direction through many small gas passages 29c. Since the heat transfer area is enlarged by the fins 30 arranged all around the inside of the gas passage 29, the exhaust gas flows through the gas passage 29 as the heat of the hot exhaust gas immediately after passing through the catalyst 17 In doing so, the heat is efficiently transferred to the case body 6 that forms the fluid chamber 5 through which the heat recovery fluid flows, through the fins 30, and heat exchange is performed at a high heat exchange rate.
[0029]
The low-temperature exhaust gas after heat exchange with the heat recovery fluid via the case body 6 flows into the second collecting chamber 27 from the outer peripheral side, and the flow direction is changed radially inward to the central portion. On the other hand, it flows through the outflow pipe 10 in the direction of arrow B and flows out of the heat exchanger 1.
[0030]
On the other hand, the heat recovery fluid flows in the inflow pipe 9 in the direction of arrow C, flows into the first fluid chamber 5a, exchanges heat with the exhaust gas in the second collecting chamber 27 via the outflow side lid 8, Recover exhaust gas heat. Thereafter, the heat recovery fluid flows through the second fluid chamber 5b formed of a spirally elongated passage, exchanges heat with the exhaust gas flowing through the heat transfer section 28, and recovers the heat of the exhaust gas. Furthermore, the heat recovery fluid that has flowed into the third fluid chamber 5c through the second fluid chamber 5b exchanges heat with the exhaust gas in the second reversing chamber 26 via the inflow side lid body 7, and then heats the exhaust gas. After the recovery, it flows through the outflow pipe 15 in the direction of arrow D, finishes the heat recovery in the heat exchanger 1, and flows out to the outside.
[0031]
Since this embodiment is configured as described above, the following effects can be obtained.
A large heat transfer area is secured by the fins 30 arranged on the entire circumference of the gas passage 29, and a high heat exchange rate is obtained. Further, since the high-temperature exhaust gas immediately after passing through the catalyst 17 flows into the heat transfer section 28, the heat transfer section 28 can recover the heat of the exhaust gas with a high heat exchange rate.
[0032]
Since the fin 30 is disposed between the case main body 6 and the intermediate cylinder 22, and the crest 30c and the trough 30d are in contact with the case main body 6 and the intermediate cylinder 22, respectively. Compared with the one in which the heat exchange pipe is arranged between two members corresponding to the intermediate cylinder 22 and it is necessary to secure a gap between the members in the radial direction inside and outside of the heat exchange pipe, The radial gap between the case body 6 and the intermediate cylinder 22 can be small. Therefore, a high heat exchange rate is ensured by the large heat transfer area of the fins 30, and the radial gap between the case body 6 and the intermediate cylinder 22 where the fins 30 are disposed can be kept small. Thus, an increase in the outer diameter of the heat exchanger 1 is suppressed, and the heat exchanger 1 can be made compact.
[0033]
Since the fin 30 is fixed by being press-fitted between the case body 6 and the intermediate cylinder 22, brazing and welding are not required, and assembly is also relatively short. As a result, since the fins 30 are fixed by press fitting, brazing and welding locations are reduced, so that the manufacturing cost of the heat exchanger 1 can be reduced, and the assembly time of the heat exchanger 1 is further shortened. Therefore, productivity is improved.
[0034]
Further, since the fin 30 is formed from a single thin plate, the number of parts can be reduced and the number of assembling steps can be reduced. Further, the case body 6, the intermediate tube 22, and the fin 30 are made into one unit in advance. Therefore, the assemblability is improved and the productivity of the heat exchanger 1 can be improved.
[0035]
The lids 7 and 8 of the inner case 2 can share the same specifications, and the lids 12 and 13 of the outer case 3 can also share the same specifications, so the lids 7, 8, 12 , 13 can be reduced in the number of types of press working apparatuses, which can contribute to the reduction of manufacturing costs. Moreover, since the shared lids 7, 8, 12, 13 are also provided with mounting holes 7a, 8a, 12a, 13a to which the inflow pipes 9, 14 or the outflow pipes 10, 15 are connected, for inflow pipes and outflow pipes. There is no need to provide individual holes, and only the lid that is not provided with these mounting holes is shared. Compared to the case where these mounting holes are provided individually, the mounting hole processing process is simplified and production is performed. It can contribute to the improvement of sex. In addition, since the inflow pipe 14 and the outflow pipe 15 can be shared, this point can also contribute to the reduction of the manufacturing cost.
[0036]
Since the exhaust gas in the heat retaining layer 24 is smoothly replaced, the heat retaining layer 24 maintains a high temperature state in which the catalyst 17 functions at a high purification rate, and the purification performance of the catalyst 17 can be maintained or improved. Further, since the inflow pipe 9 is inserted into the center hole 17c of the catalyst 17 and the heat insulating layer 24 is provided, the time from the start of the internal combustion engine to the activation of the catalyst 17 is shortened. Performance can be improved.
[0037]
The exhaust gas from the inflow pipe 9 flows almost uniformly radially outward in the first reversing chamber 21 and flows into the catalyst 17, and flows substantially uniformly radially outward in the second reversing chamber 26. After passing through 28, it flows radially inward in the second collecting chamber 27, travels toward the center, and flows out of the heat exchanger 1 from the outflow pipe 10. Therefore, the exhaust gas flows evenly and smoothly throughout the inner case 2. As described above, since the exhaust gas flow in the inner case 2 and the outflow from the outflow pipe 10 are smooth, the heat transfer from the heat transfer section 28, the inflow side, and the outflow side lids 7 and 8 also in this respect. It can contribute to the improvement of the heat exchange rate.
[0038]
Further, the exhaust gas flows into the first reversing chamber 21 from the downstream end 9b of the inflow pipe 9 inserted into the center hole 17c of the catalyst 17, and flows in the first reversing chamber 21 substantially uniformly in the radial direction. In order to allow the exhaust gas to flow uniformly into the large-diameter catalyst from the small-diameter inflow pipe, which is necessary when the exhaust gas flows into the catalyst without being reversed, Therefore, the axial dimension from the upstream end 9a of the inflow pipe 9 to the upstream end surface 17a, which is the end surface opposite to the upstream end 9a, of the catalyst 17 is eliminated. Can be shortened, the axial length of the heat exchanger 1 can be shortened, and a compact heat exchanger 1 can be obtained.
[0039]
In addition, although the axial length of the heat exchanger 1 is short, the heat recovery fluid passes through the outflow side cover 8 and the inflow side cover 7 in the first and third fluid chambers 5a and 5c, respectively. In addition to all the heat recovery, the heat of the exhaust gas can be effectively recovered through heat recovery through the case body 6 of the heat transfer section 28 in the second fluid chamber 5b formed of a spirally elongated passage. Can do.
[0040]
Since the three protrusions 7c of the inflow side lid body 7 are in contact with the downstream end face of the catalyst 17, the axial dimension of the second reversing chamber 26 can be easily set to a set value, Positioning of the catalyst 17 in the axial direction with respect to the inner case 2 can be easily performed, and concentricity between the housing cylinder 18 and the inner case 2 and the intermediate cylinder 22 can be reliably and easily obtained. Further, since the three protrusions 8c of the outflow side cover 8 are in contact with the perforated bottom wall 23, the axial dimension of the second collecting chamber 27 is the same as that of the second reversing chamber 26. Thus, the fluidity of the exhaust gas in the second reversing chamber 26 and the second collecting chamber 27 can be made substantially equal, and the intermediate cylinder 22 can be easily positioned in the axial direction with respect to the inner case 2.
[0041]
Hereinafter, an example in which a part of the configuration of the above-described embodiment is changed will be described with respect to the changed configuration.
In the above-described embodiment, the inflow side lids 7 and 12 and the outflow side lids 8 and 13 of the inner case 2 and the outer case 3 are shared, but the inflow of either the inner case 2 or the outer case 3 is used. The side lid bodies 7 and 12 and the outflow side lid bodies 8 and 13 may be shared. Moreover, each case main body 6,11, the intermediate | middle cylinder 22, and the accommodating cylinder 18 may be cylindrical members other than a cylindrical shape.
[0042]
In the embodiment, the fin 30 is fixed by being press-fitted between the case main body 6 and the intermediate cylinder 22, but the fin can be fixed by brazing. Even in this case, the sheet-like brazing material is put in the furnace and heated while being sandwiched between the fin 30 and the case body 6 and between the fin 30 and the intermediate cylinder 22. Thus, since the fin 30 can be easily fixed to the case body 6 and the intermediate cylinder 22, the number of assembling steps can be reduced as compared with the conventional technique using the heat exchange pipe, and the productivity is improved.
[0043]
Further, in the above embodiment, the fin 30 is formed from one thin plate, but the fin 30 disposed in the gas passage 29 is replaced with the fin formed from one thin plate as the exhaust gas in the gas passage 29. A plurality of, for example, two or three, for example, may be arranged in series with respect to the flow. Also in this case, the number of parts is reduced as compared with the prior art using the heat exchange pipe, the number of assembling steps is reduced, and the productivity is improved.
[0044]
In addition to the internal combustion engine, the combustion apparatus may be any apparatus that performs combustion, such as a boiler. In that case, the heat recovery fluid may be simple water for hot water supply or the like. Further, a gas such as air may be used. Further, the number of projections 7c and 8c formed on both lids 7 and 8 is three, but may be four or more.
[Brief description of the drawings]
FIG. 1 is a longitudinal sectional view of a catalyst-integrated heat exchanger for exhaust gas heat recovery according to an embodiment of the present invention, and is a sectional view taken along line II in FIG.
FIG. 2 is a view taken in the direction of arrow II in FIG.
FIG. 3 is a view taken in the direction of arrow III in FIG.
4 is a cross-sectional view taken along line IV-IV in FIG.
FIG. 5 is a partially enlarged view of FIG. 4;
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 ... Heat exchanger, 2 ... Inner case, 3 ... Outer case, 4 ... Exhaust gas chamber, 5 ... Fluid chamber, 6 ... Case main body, 7 ... Inflow side cover body, 7a ... Mounting hole, 8 ... Outflow side cover body 8a ... mounting hole, 9 ... inflow pipe, 10 ... outflow pipe, 11 ... case body, 12 ... inflow side lid, 13 ... outflow side lid, 14 ... inflow pipe, 15 ... outflow pipe, 16 ... spiral pipe, 17 ... Catalyst, 18 ... Housing cylinder, 19 ... Connection flange, 20 ... Bottom wall, 21 ... First reversing chamber, 22 ... Intermediate cylinder, 23 ... Perforated bottom wall, 23a ... Small hole, 24 ... Thermal insulation layer, 25 ... 1st collective chamber, 26 ... 2nd reversing chamber, 27 ... 2nd collective chamber, 28 ... heat transfer part, 29 ... gas passage, 30 ... fin, 30c ... mountain part, 30d ... valley part,
L: Center axis.

Claims (4)

排気ガスが流通する内ケースと、該内ケースを囲繞すると共に該内ケースとの間に排気ガス熱の熱回収流体が流通する流体室を形成する外ケースと、前記内ケース内に収容された触媒と、該触媒を通過した排気ガスと前記流体室の熱回収流体と間での熱交換を行う伝熱部とを備え、前記内ケースに流入した燃焼装置の排気ガスが、前記触媒を通過し、次いで前記伝熱部を通過した後、前記内ケースから流出する排気ガス熱回収用の触媒一体型熱交換器において、
前記伝熱部は、前記内ケースの筒状の流体室形成部分を外側通路壁とし、前記触媒と前記内ケースとの間に配置された中間筒を内側通路壁として形成された筒状のガス通路と、多数の山部および谷部が屈曲形成されたフィンとを備え、該フィンは、前記流体室形成部分および前記中間筒に前記山部および前記谷部がそれぞれ接触するように前記ガス通路内に配置され
前記中間筒内には、底壁を有する触媒収容筒が設けられ、該収容筒内に、前記触媒がその一端面と前記底壁との間に第1反転室が形成されるように収容され、前記収容筒内の前記触媒の中心部を前記底壁へ向かい貫通して排気ガスの流入管が設けられ、これにより、流入管内をその上流側から下流側に流れて前記触媒の前記一端面に達する排気ガスが、前記第1反転室で反転して前記触媒の前記一端面から触媒中をその他端面へ通過するようにされ、
前記収容筒、前記中間筒および前記内ケースを前記流入管の上流側から覆い、かつ前記触媒の前記他端面に接して第2反転室が形成されるように、前記内ケースに蓋体が固定され、前記蓋体は、前記触媒の前記他端面から前記第2反転室内に流入する排気ガスが、前記伝熱部へ反転状態で流入するように形成されていることを特徴とする排気ガス熱回収用の触媒一体型熱交換器。
An inner case through which exhaust gas flows, an outer case that surrounds the inner case and forms a fluid chamber through which heat recovery fluid of exhaust gas heat flows between the inner case, and the inner case are housed in the inner case A catalyst, and a heat transfer section that exchanges heat between the exhaust gas that has passed through the catalyst and the heat recovery fluid in the fluid chamber, and the exhaust gas of the combustion device that has flowed into the inner case passes through the catalyst Then, after passing through the heat transfer section, in the catalyst-integrated heat exchanger for recovering heat of exhaust gas flowing out from the inner case,
The heat transfer section is a cylindrical gas formed with a cylindrical fluid chamber forming portion of the inner case as an outer passage wall and an intermediate tube disposed between the catalyst and the inner case as an inner passage wall. A plurality of crests and troughs bent to form the gas passages so that the crests and troughs are in contact with the fluid chamber forming portion and the intermediate cylinder, respectively. It is located within,
A catalyst housing cylinder having a bottom wall is provided in the intermediate cylinder, and the catalyst is accommodated in the housing cylinder so that a first inversion chamber is formed between one end surface of the intermediate cylinder and the bottom wall. An exhaust gas inflow pipe is provided through the central portion of the catalyst in the housing cylinder toward the bottom wall, whereby the end face of the catalyst flows through the inflow pipe from the upstream side to the downstream side. The exhaust gas reaching to is reversed in the first reversing chamber so as to pass from the one end surface of the catalyst to the other end surface through the catalyst,
The lid is fixed to the inner case so as to cover the housing cylinder, the intermediate cylinder and the inner case from the upstream side of the inflow pipe and to form a second reversing chamber in contact with the other end surface of the catalyst. The lid body is formed such that exhaust gas flowing into the second reversal chamber from the other end surface of the catalyst flows into the heat transfer section in a reversed state. Catalyst-integrated heat exchanger for recovery.
前記フィンは、前記流体室形成部分および前記中間筒の間に圧入されていることを特徴とする請求項1記載の排気ガス熱回収用の触媒一体型熱交換器。  The catalyst-integrated heat exchanger for exhaust gas heat recovery according to claim 1, wherein the fin is press-fitted between the fluid chamber forming portion and the intermediate cylinder. 前記内ケースおよび前記外ケースの少なくとも一方は、両端部が開放した筒状のケース本体と、該両端部にそれぞれ固定された同一仕様の蓋体とを備え、該蓋体には、排気ガスまたは熱回収流体の流入管または流出管が接続される孔が設けられていることを特徴とする請求項1または請求項2記載の排気ガス熱回収用の触媒一体型熱交換器。  At least one of the inner case and the outer case includes a cylindrical case body having both ends opened, and lids of the same specification that are respectively fixed to the both ends. 3. A catalyst-integrated heat exchanger for exhaust gas heat recovery according to claim 1, wherein a hole to which an inflow pipe or an outflow pipe for heat recovery fluid is connected is provided. 前記触媒収容筒と前記中間筒の間に、前記第2反転室からの排気ガスが流入するように、微小間隙をもつ保温層が形成されていることを特徴とする請求項1乃至3のいずれかに記載の排気ガス熱回収用の触媒一体型熱交換器。4. A heat insulating layer having a minute gap is formed between the catalyst housing cylinder and the intermediate cylinder so that exhaust gas from the second inversion chamber flows. A catalyst-integrated heat exchanger for exhaust gas heat recovery according to claim 1.
JP2000142376A 2000-05-15 2000-05-15 Catalyst-integrated heat exchanger for exhaust gas heat recovery Expired - Fee Related JP4493799B2 (en)

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