JPS606013A - Catalyst converter associated with heat-exchanger - Google Patents

Catalyst converter associated with heat-exchanger

Info

Publication number
JPS606013A
JPS606013A JP58112840A JP11284083A JPS606013A JP S606013 A JPS606013 A JP S606013A JP 58112840 A JP58112840 A JP 58112840A JP 11284083 A JP11284083 A JP 11284083A JP S606013 A JPS606013 A JP S606013A
Authority
JP
Japan
Prior art keywords
exhaust gas
oil
catalyst
heat
case
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP58112840A
Other languages
Japanese (ja)
Other versions
JPS647207B2 (en
Inventor
Kazuya Nomura
野村 和雄
Motomitsu Erikawa
江利川 基光
Masakazu Sekiguchi
関口 正和
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
KOGATA GAS REIBOU GIJUTSU KENKYU KUMIAI
Original Assignee
KOGATA GAS REIBOU GIJUTSU KENKYU KUMIAI
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by KOGATA GAS REIBOU GIJUTSU KENKYU KUMIAI filed Critical KOGATA GAS REIBOU GIJUTSU KENKYU KUMIAI
Priority to JP58112840A priority Critical patent/JPS606013A/en
Publication of JPS606013A publication Critical patent/JPS606013A/en
Publication of JPS647207B2 publication Critical patent/JPS647207B2/ja
Granted legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N3/00Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
    • F01N3/08Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
    • F01N3/10Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust
    • F01N3/24Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by constructional aspects of converting apparatus
    • F01N3/28Construction of catalytic reactors
    • F01N3/2882Catalytic reactors combined or associated with other devices, e.g. exhaust silencers or other exhaust purification devices
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N3/00Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
    • F01N3/08Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
    • F01N3/10Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust
    • F01N3/24Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by constructional aspects of converting apparatus
    • F01N3/28Construction of catalytic reactors
    • F01N3/2882Catalytic reactors combined or associated with other devices, e.g. exhaust silencers or other exhaust purification devices
    • F01N3/2889Catalytic reactors combined or associated with other devices, e.g. exhaust silencers or other exhaust purification devices with heat exchangers in a single housing
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N2240/00Combination or association of two or more different exhaust treating devices, or of at least one such device with an auxiliary device, not covered by indexing codes F01N2230/00 or F01N2250/00, one of the devices being
    • F01N2240/02Combination or association of two or more different exhaust treating devices, or of at least one such device with an auxiliary device, not covered by indexing codes F01N2230/00 or F01N2250/00, one of the devices being a heat exchanger
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N2250/00Combinations of different methods of purification
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N2330/00Structure of catalyst support or particle filter
    • F01N2330/08Granular material
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N2570/00Exhaust treating apparatus eliminating, absorbing or adsorbing specific elements or compounds

Abstract

PURPOSE:To prevent discharge of lamp soot at the initial stage of engine starting, by leading exhaust gas through an oil catcher provided in the center of pellet catalyst layer. CONSTITUTION:A baffled oil catcher 11 is provided in the center of a pellet catalyst layer 12. Oil in the exhaust gas at the initial stage of engine starting is stored in the oil catcher 11 to discharge oil-less exhaust gas through catalyst 12, reheating section 13, heat-exchanger 15 contained in the case 2 and exhaust gas outlet 16. Upon sufficient heating of catalyst through continuous running of engine, the oil catcher 11 is heated from the outside to gasify the oil which is purified together with the exhaust gas through catalyst 12 and reheating section 13 and discharged.

Description

【発明の詳細な説明】 イ)産業上の利用分野 本発明はエンジンの排気ガス全浄化すると共に排気ガス
の熱を回収する熱交換器付き触媒コンバータに関する。
DETAILED DESCRIPTION OF THE INVENTION A) Field of Industrial Application The present invention relates to a catalytic converter with a heat exchanger that completely purifies exhaust gas from an engine and recovers heat from the exhaust gas.

口)従来技術 エンジンの排気ガスを浄化する触媒コンバータには例え
ば第1図〜第4図に示すような種々の型式のものが考え
られる。
BACKGROUND ART Various types of catalytic converters for purifying exhaust gas from engines can be considered, such as those shown in FIGS. 1 to 4, for example.

まず第1図の型式のものは、排気ガスが排気ガス人口1
からコンバータケース2の触媒室6内に導入され、触媒
ケース40内側にある触媒固定層5に固定された・・ニ
カム型触媒6の中を通り、破卵熱流体層7と熱交換可能
に設けられた排気ガス熱交換部8を通つてコンバータケ
ース2から排出されるようになっている。従って (a) 触媒6および触媒固定層5の熱がケース2を通
って外部に放熱されるので排熱回収率が低下し、コンバ
ータケース2の温度が高いことから断熱の必要が生ずる
、 (b) 工/ジン始動初期には排気ガス温度が低く触媒
6も@度が低いので、エンジンオイルの溜りが排気ガス
熱交換部8にできたり、また油煙として排出され排出抵
抗の上昇や外観上の問題を生ずる、 (C) 触媒6にハニカム型のものを用いると、担体お
よび触媒固定層5の耐熱性により反応温度を上げること
ができないため、排気ガス中の可燃物の量が減ると浄化
効率か著しく低下する、 以上(a)〜(C)の問題がある。
First of all, in the model shown in Figure 1, the exhaust gas is 1 exhaust gas population.
The catalyst is introduced into the catalyst chamber 6 of the converter case 2 and fixed to the catalyst fixed layer 5 inside the catalyst case 40. The exhaust gas is discharged from the converter case 2 through the exhaust gas heat exchange section 8. Therefore, (a) the heat of the catalyst 6 and the fixed catalyst bed 5 is radiated to the outside through the case 2, reducing the exhaust heat recovery rate, and the high temperature of the converter case 2 requires insulation; (b) ) At the beginning of engine/engine startup, the exhaust gas temperature is low and the catalyst 6 temperature is also low, so a pool of engine oil may form in the exhaust gas heat exchange section 8, or it may be emitted as oil smoke, resulting in an increase in exhaust resistance or an appearance problem. (C) If a honeycomb type catalyst is used as the catalyst 6, the reaction temperature cannot be raised due to the heat resistance of the carrier and the fixed catalyst layer 5, so if the amount of combustibles in the exhaust gas is reduced, the purification efficiency will be reduced. There are problems (a) to (C) above, in which the amount of water is significantly reduced.

次に第2図の型式のものは、第1図のものに比してコン
バータケース2の内側に熱交換層としてケース冷却層9
が設けられたものであり、従って第1図qもののケース
の温度が高いという問題点は解消されるが、他の問題点
は第1図のものと同じである。
Next, the model shown in Fig. 2 has a case cooling layer 9 as a heat exchange layer inside the converter case 2, compared to the model shown in Fig. 1.
Although the problem of the high temperature of the case shown in FIG. 1q is solved, the other problems are the same as those in FIG. 1.

次に第6図の型式のものは、第2図のものに比して触媒
固定層5をケース冷却層9に直接接触するように配置し
たものであり、従って触媒担体および固定層5は冷却層
9によって冷却されて触媒温度が低下して触媒担体およ
び固定層5vf、mけないが担体温度が低下してしまう
ため、排気ガスの浄化効率が低下することになる。また
他の問題点は第2図のものと同じである。
Next, in the model shown in FIG. 6, compared to the model shown in FIG. 2, the fixed catalyst bed 5 is arranged so as to be in direct contact with the case cooling layer 9, so that the catalyst carrier and the fixed bed 5 are cooled. The catalyst temperature decreases due to cooling by the layer 9, and the catalyst carrier temperature and the fixed layer 5vf also decrease, although the carrier temperature also decreases, resulting in a decrease in exhaust gas purification efficiency. Further, other problems are the same as those in FIG.

次に第4図の型式のものは、触媒層10をベレッビ型に
したものであり、この場合反応温度は上げられるが、排
気ガス中の可燃物の量が比較的少ない場合浄化効率が低
Fしてしまい、捷だオイル溜りや油煙の発生は改良され
ない。
Next, the type shown in Fig. 4 has a Berebbi type catalyst layer 10. In this case, the reaction temperature can be raised, but if the amount of combustibles in the exhaust gas is relatively small, the purification efficiency is low. As a result, the problem of oil puddles and oil smoke cannot be improved.

ハ)発明の目的 本発明の目的は排熱回収率および浄化効率が高く、且つ
オイル溜りや白煙を防止した熱交換封器付き触媒コンバ
ータを提供することにある。
C) Object of the Invention An object of the present invention is to provide a catalytic converter with a heat exchange seal that has a high exhaust heat recovery rate and purification efficiency, and prevents oil accumulation and white smoke.

二)発明の構成 本発明の熱交換器付き触媒コンノく一夕は、コンバータ
ケースと、(非気ガス人口と接続して10己ケース内に
設けら)tたオイルキャッチャと、前目己オイルキャッ
チャに隣接し前記オイルキャッチャを通った排気ガスが
通過可能に且つ前記オイルキャッチャを通る排気ガスを
予熱可能に配設されたベレット型触媒層と、前記ケース
θ)内側に前す己触媒層ケ通った排気ガスを被加熱流体
と熱交換させて冷却するように設けられたケース熱交換
部と金有したものである。
2) Structure of the Invention The catalytic converter with heat exchanger of the present invention includes a converter case, an oil catcher (connected to a non-gas gas supply and provided in the case), and a front oil catcher. a pellet-type catalyst layer adjacent to the catcher and disposed to allow exhaust gas passing through the oil catcher to pass therethrough and to preheat the exhaust gas passing through the oil catcher; It is equipped with a case heat exchange section that is provided to cool the passing exhaust gas by exchanging heat with the fluid to be heated.

ホ)実施例 以下本発明による熱交換器付き触媒コンバータの実施例
について、第5図を参照して説明する。
e) Examples Hereinafter, examples of the catalytic converter with heat exchanger according to the present invention will be described with reference to FIG.

エンジン(は、7’i’i ’暖房給湯運転7行なうヒ
ートボップ式空気調和装置の圧縮機駆動用として用いら
れ、エンジンの1,1[熱を・給湯熱源、暖房補助熱源
等に有効に利用するとともにヒートボング式冷凍機全給
湯熱源として利用rることもできる。
The engine (7'i'i') is used to drive the compressor of a heat bop type air conditioner that performs heating and hot water supply operation. At the same time, the heat bong type refrigerator can also be used as a heat source for all hot water supply.

第5図において、エンジンの排気ガスは排気ガス人口1
から導入され、その排気ガス人口−1はコンバータケー
ス2の内部に設けられたオイルキャッチャ11に接続ざ
11ている。ケース2μ一般にステンレス鋼製であり、
オイルキャッチャ11は一般に金網、発泡金属等ρ・ら
作ら1する。
In Figure 5, the engine exhaust gas has an exhaust gas population of 1
The exhaust gas population -1 is connected to an oil catcher 11 provided inside the converter case 2. Case 2μ is generally made of stainless steel,
The oil catcher 11 is generally made of wire mesh, foamed metal, or the like.

オイルキャッチャ11の外側に隣接してベレット型触媒
層12が設けら1しており、排気ガス人口1から導入さ
rtオイルキャッチャ11全通った排気ガスはオイルキ
ャッチャ110下viL端から反転して触姪l錆12を
通過する際、この触媒層にて酸化発熱してオイルキャッ
チャ11を通る排気ガスを予熱することができるように
なっている。コンバータケース2の内側にケース熱交換
部14が設けられ、そのケース熱交換部14の内周向と
触媒ノー120外筒の外周面との間に筒状空間の再加熱
部16が形成されており、触媒層12を通った排気ガス
は触媒7f412の下流端から反転して再7Jl]熱1
5316を通り、ケース熱交換部14を通る被加熱流体
、例えば市水と熱交換されて冷却されるようになってい
る。
A pellet-type catalyst layer 12 is provided adjacent to the outside of the oil catcher 11, and the exhaust gas that is introduced from the exhaust gas population 1 and has passed through the entire rt oil catcher 11 is reversed and touched from the bottom viL end of the oil catcher 110. When the exhaust gas passes through the oil catcher 12, heat is generated by oxidation in this catalyst layer, so that the exhaust gas passing through the oil catcher 11 can be preheated. A case heat exchange section 14 is provided inside the converter case 2, and a cylindrical space reheating section 16 is formed between the inner circumference of the case heat exchange section 14 and the outer circumference of the outer cylinder of the catalyst no. Then, the exhaust gas that has passed through the catalyst layer 12 is reversed from the downstream end of the catalyst 7f412 and regenerated 7Jl] heat 1
5316, and is cooled by exchanging heat with a fluid to be heated, such as city water, passing through the case heat exchange section 14.

再加熱部15の下流端は被80熱流体熱交換都15を経
て排気ガス出口16に接続されており、再加熱部13を
通った排気ガスは被加熱流体熱交換部15を辿って排気
ガス出口16から排出さtしるようになっている。一方
破卵熱流体熱交換部15は上流端か被加熱流体入口17
に接続され、下流がケース熱交換部14を経て被加熱流
体出口18に接続されており、被加熱流体熱交換部15
において排気ガスと被加熱流体、例えば市水とが熱交換
されるようになっている。
The downstream end of the reheating section 15 is connected to the exhaust gas outlet 16 via the heated fluid heat exchange section 15, and the exhaust gas that has passed through the reheating section 13 follows the heated fluid heat exchange section 15 and becomes the exhaust gas. It is designed to be discharged from an outlet 16. On the other hand, the broken egg thermofluid heat exchange section 15 is located at the upstream end or heated fluid inlet 17.
The downstream side is connected to the heated fluid outlet 18 via the case heat exchanger 14, and the heated fluid heat exchanger 15
In the exhaust gas and the fluid to be heated, for example, city water, heat is exchanged.

次に本発明による熱交@器付き触媒コンノ(−タの作用
について説明する。エンジン排気ガス人口1より流入し
た排気ガスはエンジン始動初期特上の温度が低いため、
オイルキャッチャ11によりオイル分を除かれるが、エ
ンジン始動后、排気ガス温度が高くなってくると、触媒
層12にて可燃分の燃焼が始壕9、その熱によりオイル
がガス化し、オイル分は素通りする。1だ、エンジン始
動初期時にオイルキャッチャ11にてとらえられたオイ
ル分は触媒層12にて熱せられてガス化され触媒層12
に排気カスとともに込られる。。
Next, the action of the catalytic converter with heat exchanger according to the present invention will be explained. Since the exhaust gas that has flowed in from the engine exhaust gas population 1 has a particularly low temperature at the initial stage of engine startup,
The oil content is removed by the oil catcher 11, but when the exhaust gas temperature rises after the engine is started, the combustion of combustible content begins in the catalyst layer 12, and the oil is gasified by the heat, and the oil content is Pass by. 1. The oil caught by the oil catcher 11 at the initial stage of engine startup is heated and gasified by the catalyst layer 12.
is carried along with the exhaust residue. .

オイルキャッチャ11こよジ予熱された排気ガスはベレ
ット型触媒層12に導かれ排気ガス中のメタン、−酸化
炭′$等の可燃成分は酸化燃焼される。その給米触媒層
の温度と排気ガスの温度か上昇する。高温の排気ガスは
再vIJ熱部16に導入され、ケース熱交換部14の壁
面に沿って流れることにより熱交換され排気ガス温肋C
ユ低下する。捷だこの時触媒ノー12は壁面に沿って流
れる排気ガスにより断熱されている。次(IC排気ガス
は被加熱流体熱交換部15に入り熱交換され更に温度が
低ト″し1こ状態で排気ガス出口16より排出される。
The exhaust gas slightly preheated by the oil catcher 11 is guided to the pellet type catalyst layer 12, where combustible components such as methane and carbon oxide in the exhaust gas are oxidized and burned. The temperature of the rice feeding catalyst layer and the temperature of the exhaust gas rise. The high-temperature exhaust gas is introduced into the vIJ heating section 16, where it flows along the wall surface of the case heat exchange section 14, exchanging heat, and converting it into the exhaust gas heating section C.
Yu decreases. At the time of decomposition, the catalyst no. 12 is insulated by the exhaust gas flowing along the wall surface. Next, the IC exhaust gas enters the heated fluid heat exchange section 15, undergoes heat exchange, and is further lowered in temperature before being discharged from the exhaust gas outlet 16.

被7Jl]熱流体、例えば市水は被υ口熱流体人口17
より流入し、その流体は被加熱流体熱交換部15でIJ
11熱され、更にケース熱交換部14金ηすれる間に再
加熱部16において再加熱さhて破卵熱流休出L118
から導出され、給湯、暖房等に1史用される。
7 Jl] Thermal fluid, for example, city water is υ mouth thermal fluid population 17
The fluid flows into the IJ in the heated fluid heat exchange section 15.
11, and further heated in the reheating section 16 while passing through the case heat exchange section 14, and the broken egg heat flow stops L118.
It was derived from , and has been used for hot water supply, heating, etc. for a long time.

・\)発明の効果 本発明による熱交換器側き触媒コンバータは、ケース熱
交換部全り“−ス内に設けたのでケースからの放熱を妨
げ4)ことができ、またオイルキャッチャを設けたので
エンジン始吻初期のオイル溜りや油煙発生金抑えること
ができ、始動初Jυ」にはオイルを溜めておき、触媒1
を輔の温度が上ってきたらオイルを蒸発燃焼させること
により、オイル)留りや白煙を防止することかで@る。
・\) Effects of the Invention The heat exchanger side-mounted catalytic converter according to the present invention has the entire case heat exchange section inside the case, which prevents heat radiation from the case4), and also provides an oil catcher. Therefore, it is possible to reduce oil accumulation and oil smoke generation at the beginning of the engine startup, and by storing oil at the beginning of the engine startup, the catalyst 1
When the temperature of the tank rises, the oil is evaporated and burned to prevent oil buildup and white smoke.

またベレット型触媒を1史つとともに排気ガスを予熱可
能((シたので、可燃成分が少ない場合にも浄化効率の
低ドを少なくすることができ、またり”−ス熱交換部に
て熱交換しやすいような排気ガスの流れを作ったので、
被加熱流体熱交換部が簡略化でき排出抵抗金増710さ
せないようにすることができる。
In addition, it is possible to preheat the exhaust gas with a pellet-type catalyst, so even when there are few combustible components, it is possible to reduce the low purification efficiency. We created a flow of exhaust gas that makes it easy to replace.
The heated fluid heat exchange section can be simplified and an increase in discharge resistance 710 can be avoided.

特に本発明は潤滑油が燃える2サイクルエンジンに最適
である。
In particular, the present invention is most suitable for two-stroke engines that burn lubricating oil.

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

第1図〜紀4図は従来の触媒コンノく一夕の線図的説明
図、 第5図(r:J、不発明にLる熱交換器付き触媒コンノ
く−タの線ス的説明図である。 1 ・・・ 排気ガス入口 2 ・・・ コンバータケース 11 ・・・ オイルキャッチャ 12 ・・・ ベレット型触媒層 16 ・・・ 再υ口熱部 代理人 弁理士 藤 本 礒
Figures 1 to 4 are diagrammatic explanatory diagrams of a conventional catalytic converter; 1... Exhaust gas inlet 2... Converter case 11... Oil catcher 12... Bullet type catalyst layer 16... Patent attorney Isao Fujimoto

Claims (1)

【特許請求の範囲】[Claims] コンバータケースと、排気ガス人口と接続して前記ケー
ス内に設けられたオイルキャッチャと、前記オイルキャ
ッチャに隣接し前記オイルキャッチャを通った排気ガス
が通過可能に且つ前記オイルキャッチャを通る排気ガス
を予熱可能に配役されたベレット型触媒層と、前記ケー
スの内側に前記触媒層′fc通った排気ガスを被加熱流
体と熱交換させて冷却するように設けられたケース熱交
換部とを有していることを特徴とする熱交換器付き触媒
コンバータ。
a converter case, an oil catcher connected to the exhaust gas intake and provided in the case, adjacent to the oil catcher so that the exhaust gas passing through the oil catcher can pass therethrough, and preheating the exhaust gas passing through the oil catcher. A case heat exchange part is provided inside the case so that the exhaust gas passing through the catalyst layer 'fc is cooled by exchanging heat with the fluid to be heated. A catalytic converter with a heat exchanger.
JP58112840A 1983-06-24 1983-06-24 Catalyst converter associated with heat-exchanger Granted JPS606013A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58112840A JPS606013A (en) 1983-06-24 1983-06-24 Catalyst converter associated with heat-exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58112840A JPS606013A (en) 1983-06-24 1983-06-24 Catalyst converter associated with heat-exchanger

Publications (2)

Publication Number Publication Date
JPS606013A true JPS606013A (en) 1985-01-12
JPS647207B2 JPS647207B2 (en) 1989-02-08

Family

ID=14596844

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58112840A Granted JPS606013A (en) 1983-06-24 1983-06-24 Catalyst converter associated with heat-exchanger

Country Status (1)

Country Link
JP (1) JPS606013A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003193831A (en) * 2001-12-26 2003-07-09 Sanyo Electric Co Ltd Air conditioner

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003193831A (en) * 2001-12-26 2003-07-09 Sanyo Electric Co Ltd Air conditioner

Also Published As

Publication number Publication date
JPS647207B2 (en) 1989-02-08

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