JPS6026299Y2 - rotary heat exchanger - Google Patents

rotary heat exchanger

Info

Publication number
JPS6026299Y2
JPS6026299Y2 JP1976130090U JP13009076U JPS6026299Y2 JP S6026299 Y2 JPS6026299 Y2 JP S6026299Y2 JP 1976130090 U JP1976130090 U JP 1976130090U JP 13009076 U JP13009076 U JP 13009076U JP S6026299 Y2 JPS6026299 Y2 JP S6026299Y2
Authority
JP
Japan
Prior art keywords
casing
heat transfer
heat exchanger
pipe
dust
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.)
Expired
Application number
JP1976130090U
Other languages
Japanese (ja)
Other versions
JPS5347656U (en
Inventor
秋一 高田
博太郎 金子
Original Assignee
株式会社荏原製作所
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 株式会社荏原製作所 filed Critical 株式会社荏原製作所
Priority to JP1976130090U priority Critical patent/JPS6026299Y2/en
Publication of JPS5347656U publication Critical patent/JPS5347656U/ja
Application granted granted Critical
Publication of JPS6026299Y2 publication Critical patent/JPS6026299Y2/en
Expired legal-status Critical Current

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Description

【考案の詳細な説明】 本考案は、廃ガスの有する熱を回収して廃熱再生率を高
めるために用いられる伝熱型のガス−ガス熱交換器に関
するものである。
[Detailed Description of the Invention] The present invention relates to a heat transfer type gas-gas heat exchanger used to recover heat possessed by waste gas and increase the waste heat regeneration rate.

現在廃ガスの熱回収をはかるため各種の熱交換器が使用
されているが、その一つとして伝熱部を回転させる回転
式の畜熱型熱交換器が圧力損失が少なく効果的であるこ
とで多用されるに至っている。
Currently, various heat exchangers are used to recover heat from waste gas, and one of them is a rotary heat storage type heat exchanger that rotates the heat transfer part, which is effective with low pressure loss. It has come to be widely used.

そして熱交換器の型式に応じて各種の対策が考えられて
いるものの、いずれも含塵ガスに対しては廃ガス中のガ
ス]・が伝熱部の伝熱面に付着して性能が低下したり閉
塞などで運転に支障をきたすことも多い等問題点がまだ
あった。
Various countermeasures have been considered depending on the type of heat exchanger, but in all cases, the gas in the waste gas adheres to the heat transfer surface of the heat transfer section, reducing performance. There were still problems, such as traffic jams and blockages that often interfered with driving.

本考案では、これら従来の欠点を適確に排除しようとす
るもので、回転式熱交換器の特徴をいかして効果的なダ
スト除去排出を可能とし、廃熱再生率を著しく高くして
運転できる回転式熱交換器を提供することを目的とする
ものである。
The present invention attempts to eliminate these conventional drawbacks, and makes use of the characteristics of the rotary heat exchanger to enable effective dust removal and discharge, allowing operation with a significantly high waste heat regeneration rate. The purpose is to provide a rotary heat exchanger.

本考案の他の目的は、含塵ガスでの熱回収を良好にし連
続運転によっても安全に操業でき保守管理もらくで排風
での含塵率の低下をも容易にし集塵の事後処理も良好に
保証できる安価な熱交換器とすることにある。
Other purposes of the present invention are to improve heat recovery from dust-containing gas, enable safe operation even in continuous operation, require less maintenance, and facilitate the reduction of dust content in exhaust air, allowing for post-processing of dust collection. The objective is to provide an inexpensive heat exchanger that can be guaranteed well.

本考案は、加熱側ガスの人出口と被加熱側ガスの人出口
とを備えたケーシング内に回転される伝熱部が熱の移動
を可能にするフィン付きヒートパイプで回転仕切板に設
けらている回転式熱交換器において、加熱側又は被加熱
側の少なくとも一方のケーシング内の伝熱部の内側より
外周に向けて流体を噴射せしめるように伝熱部内側に噴
射管を配し、かつケーシング内のダスト排出用のべくダ
スト排出管を噴射管が設けられているケーシングに取り
付けたことを特徴とする回転式熱交換器である。
In the present invention, a rotating heat transfer part is installed in a rotating partition plate with a finned heat pipe that enables heat transfer in a casing that has an outlet for heating side gas and an outlet for heated side gas. In a rotary heat exchanger, an injection pipe is arranged inside the heat transfer section so as to inject fluid from the inside of the heat transfer section toward the outer periphery in at least one of the casings on the heating side or the heated side, and This rotary heat exchanger is characterized in that a dust discharge pipe is attached to a casing provided with an injection pipe for discharging dust inside the casing.

本考案を実施例につき図面を参照して説明すると、加熱
ガス入口1′と加熱ガス出口1″とを有する加熱側ケー
シング1が被加熱ガス入口2′と被加熱ガス出口2″と
を有する被加熱側ケーシング2に連続されて設けられ、
このケーシング1,2内に回転軸5を介して伝熱部4か
らなる羽根車が回転可能に設けられ、該羽根車の中央に
設けられた仕切板6て前記ケーシング1,2が加熱側ガ
ス流路3と被加熱側ガス流路3′とに区画されていると
共に、前記加熱側ガス流路3中にある伝熱部4の内側よ
り外周に向けて圧縮流体を噴射せしめる噴射管7を給気
管8に連らねて伝熱部4の内側で回転軸5に平行して配
備し、且つケーシング1の周壁例えばケーシング外径周
面に開口連通したタスト排出管9を設けてあり、前記伝
熱部内側に配した噴射管7から圧縮流体を噴射して伝熱
部4に付着したダストを除去してケーシング周壁に集め
、ケーシングに設置したダスト排出管9からダストを気
流を利用して排出するように構威しである。
The present invention will be described with reference to the drawings with reference to the drawings, in which a heating side casing 1 having a heating gas inlet 1' and a heating gas outlet 1'' has a heating side casing 1 having a heated gas inlet 2' and a heated gas outlet 2''. provided continuously to the heating side casing 2,
An impeller consisting of a heat transfer part 4 is rotatably provided in the casings 1 and 2 via a rotating shaft 5, and a partition plate 6 provided at the center of the impeller allows the casings 1 and 2 to be connected to the heating side gas. The injection pipe 7 is divided into a flow path 3 and a gas flow path 3' on the heated side, and injects compressed fluid from the inside of the heat transfer section 4 in the heating side gas flow path 3 toward the outer periphery. A dust discharge pipe 9 is provided which is connected to the air supply pipe 8, is arranged parallel to the rotating shaft 5 inside the heat transfer section 4, and is opened and communicated with the peripheral wall of the casing 1, for example, the outer circumferential surface of the casing. Compressed fluid is injected from the injection pipe 7 arranged inside the heat transfer part to remove dust attached to the heat transfer part 4 and collected on the casing peripheral wall, and the dust is removed from the dust discharge pipe 9 installed in the casing using airflow. It is arranged to be ejected.

前記伝熱部4を形成するヒートパイプは羽根兼用フィン
を設けて伝熱面を大きくしであるが複数配列されるヒー
トパイプを回転仕切板6の外周に羽根様に備えて羽根車
とし加熱側ガス流路3と被加熱側ガス流路3′とに跨っ
て存在するように腰加熱側ガス流路3のガスの運転エネ
ルギを利用して伝熱部4を回転させ、被加熱側のガスを
吸引せしめ同時にフィンとヒートパイプとにより熱の移
動を有効に遠戚でき熱交換できるようにしであるが、被
加熱側ガス流路3′のガスの運動エネルギを利用又は附
加して伝熱部4を回転させたり、或いはガスの運動エネ
ルギが小さい場合にはモータなどの駆動源で回転軸5を
介して伝熱部4を回転させ同様に合理的な熱交換を可能
とすることもできる。
The heat pipes forming the heat transfer section 4 are provided with fins that also serve as blades to increase the heat transfer surface, but a plurality of heat pipes arranged in a blade-like manner are provided on the outer periphery of the rotating partition plate 6 to form an impeller on the heating side. The heat transfer part 4 is rotated using the operating energy of the gas in the heating side gas passage 3 so that it exists across the gas passage 3 and the heated side gas passage 3', and the heated side gas At the same time, the fins and heat pipes can effectively transfer heat and enable heat exchange. 4, or if the kinetic energy of the gas is small, the heat transfer section 4 can be rotated via the rotating shaft 5 by a drive source such as a motor to similarly enable rational heat exchange.

また第1図例では前記噴射管7をケーシング1に設けた
例を示したが噴射管7は、加熱側ケーシング1又は被加
熱側ケーシング2の少なくとも一方にダスト排出管9と
共に備えられればよく、加熱側ガス流路3と被加熱側ガ
ス流路3′の連接形態も加熱側ガス流路3の両側に被加
熱側ガス流路3’、3’があるように、またこれと反対
に被加熱側ガス流路3′の両側に加熱側ガス流路3,3
があるようにダブルタイプのケーシング1,2及び羽根
車を構成することもできる。
Although the example in FIG. 1 shows an example in which the injection pipe 7 is provided in the casing 1, the injection pipe 7 may be provided in at least one of the heating side casing 1 and the heated side casing 2 together with the dust discharge pipe 9. The connection form of the heating side gas flow path 3 and the heated side gas flow path 3' is also such that there are heated side gas flow paths 3', 3' on both sides of the heating side gas flow path 3, and vice versa. Heating side gas flow paths 3, 3 are provided on both sides of the heating side gas flow path 3'.
It is also possible to configure the casings 1, 2 and impeller of double type so that

前記流体噴射管7は伝熱部4内側に近接し回転軸5に添
って設けられ伝熱部4の略全幅に流体の噴射するノズル
又はノズル孔を複数配列したものが用いられ、しかも前
記ダスト排出管9がケーシング外径周面内に生ずる回転
気流の一部を誘導するようにケーシング1の周壁の略接
線方向に接続される曲管が用いられるが、曲管に限らず
直線的配管にしてもよく、いずれにしても前記ダスト排
出管9を前記流体噴射管7が配備された位置と略反対側
のケーシング周壁に設けて、伝熱部4から除去したダス
トがケーシング内を飛散することなく周壁に集められる
機会を多くしてダスト排出管9に誘導しやすくし加熱ガ
ス出口1″から排出しないようにするのが効果的である
The fluid injection pipe 7 is provided close to the inside of the heat transfer section 4 and along the rotating shaft 5, and has a plurality of nozzles or nozzle holes arranged to eject fluid over substantially the entire width of the heat transfer section 4. A curved pipe is used in which the discharge pipe 9 is connected approximately tangentially to the peripheral wall of the casing 1 so that a part of the rotating air flow generated within the outer circumferential surface of the casing is guided, but it is not limited to a curved pipe. However, in any case, the dust discharge pipe 9 is provided on the casing peripheral wall substantially opposite to the position where the fluid injection pipe 7 is provided, so that the dust removed from the heat transfer section 4 is scattered within the casing. It is effective to increase the chances of the dust being collected on the peripheral wall instead of being collected, so that it can be easily guided to the dust discharge pipe 9, and to prevent it from being discharged from the heated gas outlet 1''.

さらに流体噴射管7に連絡される給気管8がポンプを必
要に応じ含む給気機構に連絡され高圧空気や蒸気等の圧
縮流体を伝熱部4に吹きつけて付着したダストの除去を
効果的に行なうようにしである。
Further, an air supply pipe 8 connected to the fluid injection pipe 7 is connected to an air supply mechanism including a pump as necessary, and blows compressed fluid such as high-pressure air or steam onto the heat transfer section 4 to effectively remove attached dust. It is recommended that you do so.

第3図の具体例ではダスト排出管9を集塵装置10に連
絡しダストDと浄化ガスgとに分離処理し浄化ガスgは
大気に放出又は熱交換器の廃ガス吐出側へ連絡したもの
である。
In the specific example shown in Fig. 3, the dust discharge pipe 9 is connected to the dust collector 10 and separated into dust D and purified gas g, and the purified gas g is released into the atmosphere or connected to the waste gas discharge side of the heat exchanger. It is.

第4図の具体例では加熱ガス例えば廃ガスのガス人出口
を前記実施例の逆の形態としたもので、前記圧縮流体噴
射管7とダスト排出管9との配備される相対位置が有効
な位置に選定されている。
In the specific example shown in FIG. 4, the gas outlet for heating gas, e.g., waste gas, is configured in the opposite manner to that of the previous embodiment, and the relative positions of the compressed fluid injection pipe 7 and the dust discharge pipe 9 are set to be effective. The location has been selected.

図中11はガスシール用のパツキン、12は軸受、13
は軸受サポートである。
In the figure, 11 is a gas seal gas seal, 12 is a bearing, and 13
is a bearing support.

G、G’は廃ガス、Dはダストを示す。G and G' indicate waste gas, and D indicates dust.

しかして加熱廃ガス(又は蒸気)は加熱ガス入口1′か
ら入って羽根兼用フィンのある伝熱部4をせん断力によ
って回転させ加熱ガス出口1″より排出される。
The heated waste gas (or steam) enters from the heated gas inlet 1', rotates the heat transfer section 4 having blades and fins by shearing force, and is discharged from the heated gas outlet 1''.

即ち、回転式熱交換器の廃ガスの加熱ガス入口1′から
接続方向に流入した廃ガスは加熱側ケーシング1に沿っ
て回転気流を形成し伝熱部4の外周より中心部に向って
流れ込む。
That is, the waste gas flowing in the connection direction from the heated gas inlet 1' of the rotary heat exchanger forms a rotating airflow along the heating side casing 1, and flows from the outer periphery of the heat transfer section 4 toward the center. .

この時の回転気流によって廃ガス中のダストの一部は伝
熱部4に到達する前に気流から分離してケーシング1周
壁に集まってダスト排出管9から一部の廃ガスと共に流
出する。
Due to the rotating airflow at this time, part of the dust in the waste gas is separated from the airflow before reaching the heat transfer section 4, collects on the peripheral wall of the casing 1, and flows out from the dust exhaust pipe 9 together with part of the waste gas.

一方伝熱部4に到達する残りのダストによって伝熱部4
へのダスト付着は避けられないため、伝熱部4の内側に
流体噴射管7を配して伝熱部4に付着したダスト除去を
行なう。
On the other hand, the remaining dust reaching the heat transfer part 4 causes the heat transfer part 4 to
Since dust adhesion to the heat transfer part 4 is unavoidable, a fluid injection pipe 7 is disposed inside the heat transfer part 4 to remove the dust adhering to the heat transfer part 4.

例えば噴射管7から高圧の空気や蒸気等の圧縮流体を伝
熱部4の内側から外周に向けて吹きつけるため、タスト
はケーシング1周壁にまで吹き飛ばされ前述の回転気流
に乗ってタスト排出管9から排出されることになる。
For example, since compressed fluid such as high-pressure air or steam is blown from the injection pipe 7 from the inside of the heat transfer section 4 toward the outer periphery, the tast is blown off to the circumferential wall of the casing 1 and carried by the aforementioned rotating airflow to the tast discharge pipe 9. It will be discharged from

さらに熱の移動は加熱ガスから伝熱部4のフィンに伝え
られヒートパイプによって被加熱側のケーシング2内の
伝熱部4に瞬時に移動しフィンを通して被加熱ガスに伝
わる。
Furthermore, the heat is transferred from the heated gas to the fins of the heat transfer section 4, and is instantaneously transferred to the heat transfer section 4 in the casing 2 on the heated side by the heat pipe, and is transferred to the heated gas through the fins.

このように加熱ガスの熱エネルギーと運動(圧力)エネ
ルギーが有効に被加熱ガスの吸引と加熱とに利用され、
送風機と熱交換器を兼ねることになって大量に一度に処
理できサイクル効率を大きく向上させて使用できるもの
である。
In this way, the thermal energy and kinetic (pressure) energy of the heated gas are effectively used to suck and heat the heated gas,
Since it functions as both a blower and a heat exchanger, it can process large quantities at once, greatly improving cycle efficiency.

本案は加熱側ガスの人出口と被加熱側ガスの人出口とを
備えたケーシング内に回転される伝熱部が熱の移動を可
能にするフィン付きヒートパイプで回転仕切板に設けら
れている回転式熱交換器において、加熱側又は被加熱側
の少なくとも一方のケーシング内の伝熱部の内側より外
周に向けて流体を噴射せしめるように伝熱部内側に噴射
管を配し、かつケーシング内のダスト排出用のダスト排
出管を噴射管が設けられているケーシングに取り付けた
ことにより、廃ガス中のダストは伝熱部に付着すること
なく適確に除去され伝熱性能を低下させたり閉塞によっ
て運転に支障をきたすことなく安全高性能に運転するこ
とが可能であって、しかも伝熱部の内側に配したダスト
除去噴射管とケーシングに取り付けたダスト排出管とか
らの組合せで排熱再生率(温度効率)を著しく高くする
ことが容易であるほか、集めたダストの系外排出も容易
で熱交換器としての大容量化が可能であるし、且つ容積
、重量も小さく熱通過率を高めたコンパクトな伝熱面が
常用されて温度差をも大きくとれて熱交換機能を増大腰
さらに遠心力によってヒートパイプの能力をあげること
ができるので熱を効率よく回収し、含塵ガスの取扱いも
簡単で保守管理面もらくで、長期にわたって正常な運転
がてき構成も簡単で大量生産に適し著しく経済的な熱交
換器とすることができる。
In this case, a rotating heat transfer part is installed in a rotating partition plate with a finned heat pipe that enables heat transfer, in a casing equipped with an outlet for the heating side gas and an outlet for the heated side gas. In a rotary heat exchanger, an injection pipe is disposed inside the heat transfer part so as to inject fluid from the inside of the heat transfer part in the casing on the heating side or the heated side toward the outer periphery, and the injection pipe is arranged inside the casing. By attaching the dust discharge pipe for dust discharge to the casing where the injection pipe is installed, dust in the waste gas can be properly removed without adhering to the heat transfer part, reducing heat transfer performance or clogging. It is possible to operate safely and with high performance without causing any trouble to the operation, and in addition, the exhaust heat is regenerated by the combination of the dust removal injection pipe placed inside the heat transfer part and the dust exhaust pipe attached to the casing. It is easy to significantly increase the thermal efficiency (temperature efficiency), it is easy to discharge the collected dust out of the system, and it is possible to increase the capacity of the heat exchanger.It is also small in volume and weight, and has a low heat transfer rate. The high compact heat transfer surface is commonly used to increase the temperature difference and increase the heat exchange function.Furthermore, the centrifugal force can increase the heat pipe capacity, allowing efficient heat recovery and handling of dust-containing gas. The heat exchanger is easy to maintain, easy to maintain, can operate normally for a long period of time, and is simple in construction, suitable for mass production, and extremely economical.

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

図面は本考案の実施例を示し、第1図は縦断面図、第2
図は側面図、第3図及び第4図はそれぞれ他の実施例の
切断側面図である。 1・・・・・・加熱側ケーシング、1′・・・・・・加
熱ガス入口、1z・・・・・加熱ガス出口、2・・・・
・・被加熱側ケーシング、2′・・・・・・被加熱ガス
入口、2″・・・・・・被加熱ガス出口、3・・・・・
・加熱側ガス流路、3′・・・・・・被加熱側ガス流路
、4・・・・・・伝熱部、5・・・・・・回転軸、6・
・・・・・仕切板、7・・・・・・噴射管、8・・・・
・・給気管、9・・・・・・排出管、10・・・・・・
集塵装置、11・・・・・・パツキン、12・・・・・
・軸受、13・・・・・・軸受サポート。
The drawings show an embodiment of the present invention, with FIG. 1 being a longitudinal sectional view and FIG.
The figure is a side view, and FIGS. 3 and 4 are cutaway side views of other embodiments. 1... Heating side casing, 1'... Heating gas inlet, 1z... Heating gas outlet, 2...
...Heated side casing, 2'...Heated gas inlet, 2''...Heated gas outlet, 3...
・Heating side gas flow path, 3'...Heated side gas flow path, 4...Heat transfer part, 5...Rotating shaft, 6.
...Partition plate, 7...Injection pipe, 8...
...Air supply pipe, 9...Discharge pipe, 10...
Dust collector, 11... Packing, 12...
・Bearing, 13...Bearing support.

Claims (1)

【実用新案登録請求の範囲】 1 加熱側ガスの人出口と被加熱側ガスの入出口とを備
えたケーシング内に回転される伝熱部が熱の移動を可能
にするフィン付きヒートパイプで回転仕切板に設けられ
ている回転式熱交換器において、加熱側又は被加熱側の
少なくとも一方のケーシング内の伝熱部の内側より外周
に向けて流体を噴射せしめるように伝熱部内側に噴射管
を配し、かつケーシング内のダスト排出用のダスト排出
管を噴射管が設けられているケーシングに取り付けたこ
とを特徴とする回転式熱交換器。 2 前記噴射管が、伝熱部の回転軸に添って設けられ伝
熱部の略全幅に流体を噴射するノズル又はノズル孔を複
数間ダ1ルたものである実用新案登録請求の範囲第1項
記載の回転式熱交換器。 3 前記ダスト排出管が、ケーシング外径局面に開口連
通されているものである実用新案登録請求の範囲第1項
又は第2項記載の回転式熱交換器。 4 前記タスト排出管が、ケーシング外径周面内に生す
る回転気流の一部を誘導する略接線方向に接続される曲
管である実用新案登録請求の範囲第3項記載の回転式熱
交換器。 5 前記ダスト排出管が、前記噴射管が配備された位置
と略反対側のケーシング周壁に設けられている実用新案
登録請求の範囲第3項又は第4項記載の回転式熱交換器
[Scope of Claim for Utility Model Registration] 1. A rotating heat transfer part in a casing with an outlet for heating gas and an inlet and outlet for heated gas rotates with a finned heat pipe that enables heat transfer. In a rotary heat exchanger provided on a partition plate, an injection pipe is installed inside the heat transfer section so as to inject fluid from the inside of the heat transfer section toward the outer periphery in the casing on at least one of the heating side and the heated side. A rotary heat exchanger characterized in that a dust discharge pipe for discharging dust inside the casing is attached to a casing in which an injection pipe is provided. 2. Utility model registration claim 1, wherein the injection pipe is a plurality of nozzles or nozzle holes arranged along the rotation axis of the heat transfer section and injecting fluid over substantially the entire width of the heat transfer section. Rotary heat exchanger as described in section. 3. The rotary heat exchanger according to claim 1 or 2, wherein the dust discharge pipe is open and communicated with an outer diameter surface of the casing. 4. The rotary heat exchanger according to claim 3, wherein the tost discharge pipe is a curved pipe connected in a substantially tangential direction that guides a part of the rotating airflow generated within the outer circumferential surface of the casing. vessel. 5. The rotary heat exchanger according to claim 3 or 4, wherein the dust discharge pipe is provided on a peripheral wall of the casing substantially opposite to the position where the injection pipe is provided.
JP1976130090U 1976-09-28 1976-09-28 rotary heat exchanger Expired JPS6026299Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1976130090U JPS6026299Y2 (en) 1976-09-28 1976-09-28 rotary heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1976130090U JPS6026299Y2 (en) 1976-09-28 1976-09-28 rotary heat exchanger

Publications (2)

Publication Number Publication Date
JPS5347656U JPS5347656U (en) 1978-04-22
JPS6026299Y2 true JPS6026299Y2 (en) 1985-08-07

Family

ID=28739244

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1976130090U Expired JPS6026299Y2 (en) 1976-09-28 1976-09-28 rotary heat exchanger

Country Status (1)

Country Link
JP (1) JPS6026299Y2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104764338A (en) * 2015-03-19 2015-07-08 南京华电节能环保设备有限公司 Heat pipe type smoke pulverized coal heating device

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS55140405U (en) * 1979-03-30 1980-10-07
JPH0430007Y2 (en) * 1987-06-04 1992-07-21

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS49128354A (en) * 1973-04-11 1974-12-09
JPS5021350A (en) * 1973-06-27 1975-03-06

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS49128354A (en) * 1973-04-11 1974-12-09
JPS5021350A (en) * 1973-06-27 1975-03-06

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104764338A (en) * 2015-03-19 2015-07-08 南京华电节能环保设备有限公司 Heat pipe type smoke pulverized coal heating device

Also Published As

Publication number Publication date
JPS5347656U (en) 1978-04-22

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