JPS58123072A - Heat accumulation type waste-heat recovery device - Google Patents

Heat accumulation type waste-heat recovery device

Info

Publication number
JPS58123072A
JPS58123072A JP57004300A JP430082A JPS58123072A JP S58123072 A JPS58123072 A JP S58123072A JP 57004300 A JP57004300 A JP 57004300A JP 430082 A JP430082 A JP 430082A JP S58123072 A JPS58123072 A JP S58123072A
Authority
JP
Japan
Prior art keywords
heat
low
energy
pump
condenser
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.)
Pending
Application number
JP57004300A
Other languages
Japanese (ja)
Inventor
水津 勝一
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.)
Mitsui Engineering and Shipbuilding Co Ltd
Mitsui Zosen KK
Original Assignee
Mitsui Engineering and Shipbuilding Co Ltd
Mitsui Zosen KK
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 Mitsui Engineering and Shipbuilding Co Ltd, Mitsui Zosen KK filed Critical Mitsui Engineering and Shipbuilding Co Ltd
Priority to JP57004300A priority Critical patent/JPS58123072A/en
Publication of JPS58123072A publication Critical patent/JPS58123072A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A30/00Adapting or protecting infrastructure or their operation
    • Y02A30/27Relating to heating, ventilation or air conditioning [HVAC] technologies
    • Y02A30/274Relating to heating, ventilation or air conditioning [HVAC] technologies using waste energy, e.g. from internal combustion engine

Landscapes

  • Processing Of Solid Wastes (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Central Heating Systems (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 本’A@は、圧縮式ヒートポンプを利用した蓄熱臘廃熱
回収装置Kllする。
DETAILED DESCRIPTION OF THE INVENTION This 'A@' is a heat storage waste heat recovery device using a compression heat pump.

近年、省エネルギ化のg&情から、従来無駄に捨てられ
ていた廃熱エネルギを効率よく回収し、その有効利用を
図ることが望まれている。しかし、このような廃熱エネ
ルギを回収して利用する装置を構成するうえで、問題と
されることは、上述した廃熱源としては、各種機器、装
置の冷却水などのような低レベルのものから、たとえば
ボイラ。
In recent years, due to the desire to save energy, it has been desired to efficiently recover waste heat energy, which was previously wasted, and to utilize it effectively. However, when constructing a device that recovers and utilizes waste heat energy, the problem is that the waste heat sources mentioned above are low-level sources such as cooling water for various devices and devices. From, for example, a boiler.

加熱炉などの各種燃焼設備の排ガスなどのような高レベ
ルo4oiで各種存在し、しかもその廃熱量が経時的に
変動する一方、利用側においてもその利用方法が輿なる
ばかりか、熱消費量−経時的に適宜変動するもので、こ
れらの点を考慮し多様なニーズに対志し得る効率のよい
ものとしなければならないことである。
Various kinds of high-level O4OI exist, such as exhaust gas from various combustion equipment such as heating furnaces, and the amount of waste heat fluctuates over time. It changes as appropriate over time, and it is necessary to take these points into consideration and create an efficient system that can meet diverse needs.

そして、従来この種の廃熱回収装置として知られるもの
は、主に、単一廃熱源、単一用途に対し設計され、しか
も廃熱源、利用側が共に量的に大幅に変化する場合に対
しては何ら考慮されていないため、効率的にみてまだま
だ問題の多いものでめり九。
Conventionally, this type of waste heat recovery equipment is mainly designed for a single waste heat source and a single purpose, and moreover, it is designed for cases where both the waste heat source and the user side change significantly in quantity. Since no consideration has been given to this, there are still many problems in terms of efficiency.

本発明はこのような事情Kilみてなされた−ので、低
熱源から高熱源へと熱エネルギを移送せしめる装置とし
て知られ為圧縮式ヒートポンプに、低、A濫用としてO
二/)の蓄熱器を巧みKJI會わぜることによって、廃
IIIk?ll、利用側O量的な変動にかかわらず、各
種0I111Ikエネルギを効率よく回収するとと−に
、多様なニーズに対応してその有効利Mを図ることが可
′mな蓄熱臘廃鴎晴収装置を提供するものでhh。
The present invention was made in view of the above circumstances.Therefore, the present invention has been made in consideration of the above-mentioned circumstances.As a result, the compression heat pump, which is known as a device that transfers thermal energy from a low heat source to a high heat source, is used.
By skillfully combining the heat storage device of 2/) with KJI, it is possible to eliminate IIIk? Ill, regardless of the fluctuations in the amount of energy on the user side, it is possible to efficiently recover various types of energy, and to make effective use of it in response to various needs. It provides equipment hh.

以下、本発明を図面に示し九実施例を用い工詳mKa明
する。
Hereinafter, the present invention will be explained in detail with reference to the drawings and nine embodiments.

81図は本発1jliK係ゐ蓄熱層廃熱lIl駅装置0
−実施4P4を示すtのでhや、内園におい工、全体を
符号10で示すものは、僑熱渾から高熱源へと熱エネル
ギを移送せしめる圧縮式と一トポンプを用いたtm回収
サイクル、艦−トポンプO圧纏過−を担当する往復動圧
縮機等の圧縮機11およびその飄−用エンジン等O駆―
機12と、同じくヒートポツプの膨張過程を1!IA蟻
すみ受1m1113および膨張弁14等を備えている。
Figure 81 shows the main station 1jliK related thermal storage layer waste heat lIl station equipment 0
- Implementation 4P4 is indicated by t and h, and the Uchizono odorworks, which are indicated by the numeral 10, are the tm recovery cycle using a compression type and one pump, which transfer heat energy from a hot water tank to a high heat source. The compressor 11, such as a reciprocating compressor, which is in charge of the O pump O pressure collection, and the O drive engine, etc.
Machine 12 and the same heat pop expansion process as 1! It is equipped with an IA dovetail receiver 1m1113, an expansion valve 14, etc.

そして、本発明によれば、上述した回収サイクル10内
に、低、高温用とし工の二つの蓄熱!15゜1@と、放
熱用熱交換器として第1および第2の放熱器17.18
とを組み込んでおり、これらを前述した圧縮機11.受
液1113および膨張弁14に選択的に接続することに
よpヒートポンプの蒸発過程を担轟する蒸発器、tたは
凝縮器として作用させるように構成している。
According to the present invention, there are two heat storage systems in the recovery cycle 10, one for low temperature and one for high temperature. 15°1@, and the first and second heat radiators 17.18 as heat exchangers for heat radiation.
The above-mentioned compressor 11. By selectively connecting to the receiving liquid 1113 and the expansion valve 14, it is configured to function as an evaporator or condenser that supports the evaporation process of the p-heat pump.

すなわち、前記低温側蓄熱器15には低温廃熱源が導び
かれてその熱エネルギが蓄えられるとともに、この低温
側蓄熱器15は上述した回収サイクル10に選択的に接
続されてヒートポンプの蒸発器とし’[)役割を果たす
ように構成されている。
That is, a low-temperature waste heat source is led to the low-temperature side heat storage device 15 and its thermal energy is stored therein, and the low-temperature side heat storage device 15 is selectively connected to the recovery cycle 10 described above to function as an evaporator of the heat pump. '[) is configured to play a role.

まえ、前記高温側蓄熱器16には高温廃熱源が導びかれ
てその熱エネルギが蓄えられるとともに、この高温側蓄
熱器16は上述した回収サイクル10に選択的に接続さ
れ℃ヒートポンプの蒸発器または凝縮器としての役割を
呆たすように構成されている。
First, a high-temperature waste heat source is led to the high-temperature side heat storage 16 and its thermal energy is stored, and the high-temperature side heat storage 16 is selectively connected to the above-mentioned recovery cycle 10 and is connected to the evaporator of a °C heat pump or It is constructed so that it does not function as a condenser.

さらに、前記ll5lおよび縞2の放熱器17.18は
それぞれ上述したー収サイクル10に選択的に接続され
、と−トポンプの凝縮器としての役割を釆丸し、利用側
に熱エネルギを与えその有効利用を図れるように構成さ
れ工いる。
Furthermore, the heat sinks 17 and 18 of the stripes 1 and 2 are selectively connected to the above-mentioned collection cycle 10, respectively, to complete the role of the top pump condenser, and provide heat energy to the user side. It is structured and designed so that it can be used effectively.

この場合、本実3119+1では、嬉lの放熱4i11
17は直接熱利用部として常温水等を供給する管路11
1が配管され、前述した回状サイクル10にで得られ良
熱エネルギを用いて利用側の要求に応じ九温度レベルの
温水を九は蒸気を供給できるように構成されている。
In this case, in Honjitsu 3119+1, the heat dissipation 4i11 of
17 is a pipe 11 that supplies room temperature water etc. as a direct heat utilization part.
1 is piped to the above-mentioned circular cycle 10, and is configured to be able to supply hot water and steam at nine temperature levels according to the user's request using the high thermal energy obtained in the above-mentioned circular cycle 10.

また、jI2の放熱!!18は間接熱利用部としてラン
キンサイクルによる発電装置2Gに組込まれ、このサイ
クル中でS発器として作用するように構成されている。
Also, the heat dissipation of jI2! ! Reference numeral 18 is incorporated into the power generation device 2G based on the Rankine cycle as an indirect heat utilization section, and is configured to act as an S generator during this cycle.

そして、ζ011i2o放熱!118内で熱エネルギを
与えられた感体がタービン21を駆動し、発m1122
を回し、電力を発生し、これを利用側に供給することが
可−となる。なお、図中23は復水器、24は給水ポン
プである・さて、上述し九構成による蓄熱産廃熱回収装
置の#縄を、第2図以下に示す使用例を用いて説明する
And ζ011i2o heat dissipation! The sensitive body given thermal energy in 118 drives the turbine 21, and the emitted light m1122
It is now possible to generate electricity by rotating it and supplying it to the user. In the figure, 23 is a condenser, and 24 is a water supply pump. Now, the heat storage industrial waste heat recovery apparatus having the above-mentioned nine configurations will be explained using an example of use shown in FIG. 2 and below.

まず、第2図に示す状態は、最も一般的なta状虐であ
り、低温側蓄熱器15を低熱源とし王用い蒸発器として
作用させるとともに、altの放熱器11を凝縮器とし
て作用させており、これにより管路1sにて供給される
常温水等を利用側の要求に応じた温度レベルの温水また
は蒸気を供給する場合を示している。この場合、温度レ
ベルの制御は圧縮機11による吐出圧と容量を可変とし
、その出口側に設は九圧カコントローラ30により吐出
圧を制御することによって容易に行なえるものである◎
また、必要に応じ工は、負荷変動に対処で亀るように、
高温側蓄熱器16と管路1Bの出口側とを管路31にて
接続し、高温側蓄熱器16からの温水供給を行なえるよ
うに構成するとよい。
First, the state shown in Fig. 2 is the most common TA situation, in which the low-temperature side heat storage device 15 is used as a low heat source and acts as a main evaporator, and the alt heat radiator 11 acts as a condenser. This shows a case in which hot water or steam at a temperature level corresponding to the user's request is supplied instead of room temperature water or the like supplied through the pipe line 1s. In this case, the temperature level can be easily controlled by making the discharge pressure and capacity of the compressor 11 variable, and by controlling the discharge pressure with a nine-pressure controller 30 installed on the outlet side.
In addition, as necessary, construction work will be carried out to help cope with load fluctuations.
It is preferable to connect the high temperature side heat storage device 16 and the outlet side of the pipe line 1B through a pipe line 31 so that hot water can be supplied from the high temperature side heat storage device 16.

この場合、蓄熱器16内の蓄熱材が水であれば直接、そ
れ以外は熱交換器等を介して供給するようにすればよい
In this case, if the heat storage material in the heat storage device 16 is water, it may be supplied directly; otherwise, it may be supplied via a heat exchanger or the like.

なお、第2図に示す稼動状態のとき図示される開閉弁は
すべて開弁され、それ以外は閉じ、られ、上述した回収
サイクル10が構成されるようになっている。
Incidentally, in the operating state shown in FIG. 2, all the illustrated on-off valves are opened, and the others are closed, so that the above-described recovery cycle 10 is configured.

また、鴫3図は高温側蓄熱器16を低熱源として用vh
九場合を示し、嬉2図に示す稼動状態より4′:1らに
高温レベルの温水壜九は蒸気が必要なとIiK嫁#hさ
れる。
In addition, Figure 3 shows the use of the high temperature side heat storage device 16 as a low heat source.
From the operating state shown in Figure 2, it is determined that hot water bottle 9, which is at a high temperature level of 4':1, requires steam.

さらに、鴫4図は高温廃熱源の温度レベルが低下したり
、利用側が無魚荷または少ない負荷の場合に、熱エネル
ギを高温側蓄熱!It 6に蓄えるようにし九稼動状態
を示し、低温側蓄熱器15を蒸発器として、高温側蓄熱
器16を凝縮器として作用させている。
In addition, Figure 4 allows thermal energy to be stored on the high temperature side when the temperature level of the high temperature waste heat source decreases, or when the user side has no fish cargo or a small load! The low temperature side heat storage device 15 is used as an evaporator, and the high temperature side heat storage device 16 is used as a condenser.

なお、高温側蓄熱1116KIl熱する場合、#Is図
に示すように、廃熱ボイラ32を付設し、これに外部の
廃ガス、さらには圧縮機11を駆動するエンジン12か
らの廃ガスを導び−て燃焼させ、その熱エネルギを回収
するようにすることもできる。また、低温備蓄熱器l5
O11度レベルが低いと龜には、l1l−に符号34を
もって示す経路にて^温儒蓄熱mil@から熱エネルギ
利用送るように構成すればよい。
In addition, when heating the high temperature side heat storage 1116KIl, as shown in the #Is figure, a waste heat boiler 32 is attached, and external waste gas and further waste gas from the engine 12 that drives the compressor 11 is guided to this. - It is also possible to burn it and recover its thermal energy. In addition, low temperature storage heat storage l5
If the O11 degree level is low, the configuration may be such that thermal energy is used and sent from the thermal storage mil@ via the route indicated by the reference numeral 34 to l1l-.

嬉6図は利用側に電力を供給する場合でろって、低温蓄
熱1i1st蒸発器として、第2の放熱器18を凝縮器
として回収サイクル10を構成し、発電装置20を作動
させてなる稼動状態を示している。
Figure 6 shows an operating state in which the power generator 20 is operated, with the recovery cycle 10 configured as a low-temperature heat storage 1i1st evaporator and the second radiator 18 as a condenser, when power is supplied to the user side. It shows.

この場合、発電装置20の経路の一部を管路33a。In this case, part of the route of the power generation device 20 is connected to the pipe 33a.

33bKて高温側蓄熱器16に接続し、その熱エネルギ
を併せて利用するようにしてもよい。そして、このよう
な構成において、タービン21にょ9直接、または発電
機22により得られた電力の一部を利用して前述した圧
縮機11駆動用のエンジン等の駆動機12を駆動するよ
うに構成すれば、ヒートポンプ効率の面で有利でおる。
33bK may be connected to the high temperature side heat storage device 16, and its thermal energy may also be utilized. In such a configuration, the drive machine 12 such as the engine for driving the compressor 11 described above is driven using part of the electric power obtained directly from the turbine 21 or the generator 22. This will be advantageous in terms of heat pump efficiency.

なお、上述した発電装置20に用いる媒体としては低沸
点のもOIi好ましい−のである。
Note that as the medium used in the above-mentioned power generation device 20, it is preferable to use OIi which has a low boiling point.

また、111g6図に示す稼動状態の変形例として、高
温側蓄熱器16をaI3図に示すように蒸発器として作
用させ、かつ凝縮器として!2の放熱器18を用いて発
電装置20を作動させるようにしてもよiことは明らか
であろう。
In addition, as a modification of the operating state shown in Fig. 111g6, the high temperature side heat storage device 16 is made to act as an evaporator as shown in Fig. aI3, and also as a condenser! It will be obvious that the power generation device 20 may be operated using two radiators 18.

したがって、上述した構成による装置では、ヒートポン
プによる回収サイクル10と二つの蓄熱器15,1@と
を巧みに組合わせることにょう工、廃熱源、利用側の量
的、温度レベルの変動を吸収することができ、これによ
り廃熱エネルギを効率よく回収するとと−に、温水9@
気さらには電力というように利用側の多様なニーズに対
応してその回収エネルギを有効に、v%l用することが
可能となるO また、このような構成による装置を小型化し、パッケー
ジタイプとして移動可能に構成すれば、場所的制約がな
くなり、あらゆる熱源、利用側に対処できるもので、そ
の利点は大きい。
Therefore, in the device having the above-mentioned configuration, fluctuations in quantity and temperature level of the heat pump, waste heat source, and user side can be absorbed by skillfully combining the recovery cycle 10 by the heat pump and the two heat storage units 15,1@. As a result, waste heat energy can be efficiently recovered, and hot water9@
This makes it possible to effectively use the recovered energy to meet the diverse needs of users, such as air and electricity. If it is configured to be movable, there will be no space restrictions and it will be able to handle all types of heat sources and users, which is a great advantage.

なお、前述し九実施例では、放熱用熱交換器として第1
および第2の放熱l117.IIを用い九て同時に温水
等と電力を得るように構成すr5は自由で、その他各部
の構成も適宜変頁できる−のである。
In addition, in the ninth embodiment described above, the first heat exchanger is used as the heat radiating heat exchanger.
and second heat dissipation l117. The R5 can be configured to obtain hot water, etc. and electric power at the same time using II, and the configuration of other parts can be changed as appropriate.

さらに、本発明による装置では、前述し九稼―方法のう
ち、第2図、第4図、および第6図に示す状態は同時に
稼動することができるものでらり、このようにすればエ
ネルギ利用の多様化を図れ、その有用性は大でるる。
Furthermore, in the apparatus according to the present invention, among the nine operating methods described above, the states shown in FIGS. 2, 4, and 6 can be operated simultaneously, and in this way, the energy Diversify its use and its usefulness will be great.

を九、本発明による装置において、回収サイクル10に
用いるヒートポンプとして、圧縮機11の上流側で媒体
を自己発熱または外部の廃熱源等により加熱し、圧縮機
駆動に必要な駆動エネルギを減じてなる加熱昇圧タイプ
のものを利用することは自由でろり、さらにこの回収装
置により回収する熱エネルギを、廃熱源のほかに、たと
えば太陽熱などの他のエネルギ源をも利用するようにし
てもよいものである。
(9) In the apparatus according to the present invention, as a heat pump used in the recovery cycle 10, the medium is heated upstream of the compressor 11 by self-heating or an external waste heat source, etc., to reduce the driving energy necessary for driving the compressor. It is possible to use a heating and pressurizing type, and the heat energy recovered by this recovery device may also be used not only from waste heat sources but also from other energy sources such as solar heat. be.

以上説明し九ように、本発明に係る蓄熱型廃熱回収装置
にキれば、圧縮式ヒートポンプに、低。
As explained above, the heat storage type waste heat recovery device according to the present invention has a low cost compared to a compression type heat pump.

高温用としての二つの蓄熱器と放熱用熱交換器を組合わ
せ、かつこれら二つの蓄熱器と熱交換器とをヒートポン
プの蒸発器または凝縮器とし工遇択的に作用させるよう
にしたので、簡単な構成にもかかわらず、廃熱源、利用
側の量的、温度レベル的な変動に対処し、各種廃熱エネ
ルギを効率よく回収するとともに、その回収エネルギを
多様なニーズに対処して有効に利用することができると
いう優れた効果を奏する。
Two heat storage devices for high temperature use and a heat exchanger for heat radiation are combined, and these two heat storage devices and the heat exchanger are selectively operated as the evaporator or condenser of the heat pump. Despite its simple configuration, it can deal with fluctuations in quantity and temperature levels of waste heat sources and users, efficiently recover various types of waste heat energy, and effectively utilize the recovered energy to meet a variety of needs. It can be used with great effect.

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

第1図は本発@に係為蓄熱臘廃熱回収装置の一実施ガを
示す全体の概略構成図、嬉2図ないし第6図はその使用
ガを説明する曳めの要部構成図である。 10・・・・回収サイクル(ヒートポンプ)、11・・
・・圧縮機、14・・・・膨張弁、15・・・・低温側
蓄熱器、1B・・・・高温側蓄熱器、17.lit・・
譬・放熱器(放熱用熱交換器)、19・・・・管路、2
0・・・・発電装置。 41軒出願人 三井造船株式会社 代 理 人  山  川  政  樹(ほか1名)第3
図         1゜ / − / 第5図 タト曲違Hトガχ
Figure 1 is an overall schematic configuration diagram showing one implementation of the heat storage/waste heat recovery device used in this plant, and Figures 2 to 6 are configuration diagrams of the main parts of the system to explain its use. be. 10...Recovery cycle (heat pump), 11...
...Compressor, 14...Expansion valve, 15...Low temperature side heat storage device, 1B...High temperature side heat storage device, 17. lit...
Parable: Heat radiator (heat exchanger for heat radiation), 19... Pipe line, 2
0...Power generation device. 41 applicants Mitsui Engineering & Shipbuilding Co., Ltd. Agent Masaki Yamakawa (and 1 other person) 3rd
Fig. 1゜/-/ Fig. 5 Tato music difference H Toga χ

Claims (1)

【特許請求の範囲】[Claims] S尭量にで低熱源かb熱エネルギを回収するとともに、
凝縮器に’CI4熱源に対し熱エネルギを与える圧縮式
ヒートポンプと、低温廃熱源からO熱エネルギを蓄えゐ
とともに、前記ヒートポンプの経絡途中に選択的に纏4
11堪れ酋紀蒸働器として作用する低温側蓄熱器と、高
温廃熱源からO熱エネルギを蓄えるとともに、前記ヒー
トポンプO経略途中に選択的に秦続され前記lIA弛量
★九は凝縮器として作用する高温備蓄熱量と、酋ff1
k−)ポンプOm路通中Kjl択的K11l總され前記
凝縮器として作用し利用側に熱エネルギを都える放熱用
熱交換器を備え九ことを脣倣とする蓄熱部廃熱回収装置
In addition to recovering heat energy from a low heat source or b by reducing the amount of S,
The condenser is equipped with a compression heat pump that provides heat energy to the 'CI4 heat source, stores O heat energy from a low-temperature waste heat source, and selectively collects it in the middle of the meridian of the heat pump.
11 A low-temperature side heat storage device that acts as a steamer, and a low-temperature side heat storage device that stores O heat energy from a high-temperature waste heat source, and is selectively connected in the middle of the heat pump O passage, and the IIA slack amount★9 acts as a condenser. The amount of high temperature storage heat that acts and the amount of heat ff1
k-) A waste heat recovery device for a heat storage section, which is equipped with a heat exchanger for dissipating heat that acts as the condenser and stores heat energy to the user side, with the pump Om running through the passageway Kjl optional K11l.
JP57004300A 1982-01-14 1982-01-14 Heat accumulation type waste-heat recovery device Pending JPS58123072A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57004300A JPS58123072A (en) 1982-01-14 1982-01-14 Heat accumulation type waste-heat recovery device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57004300A JPS58123072A (en) 1982-01-14 1982-01-14 Heat accumulation type waste-heat recovery device

Publications (1)

Publication Number Publication Date
JPS58123072A true JPS58123072A (en) 1983-07-22

Family

ID=11580658

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57004300A Pending JPS58123072A (en) 1982-01-14 1982-01-14 Heat accumulation type waste-heat recovery device

Country Status (1)

Country Link
JP (1) JPS58123072A (en)

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