JPS5813987A - Heat transmitting device - Google Patents
Heat transmitting deviceInfo
- Publication number
- JPS5813987A JPS5813987A JP11263481A JP11263481A JPS5813987A JP S5813987 A JPS5813987 A JP S5813987A JP 11263481 A JP11263481 A JP 11263481A JP 11263481 A JP11263481 A JP 11263481A JP S5813987 A JPS5813987 A JP S5813987A
- Authority
- JP
- Japan
- Prior art keywords
- heat transmitting
- paths
- flat plates
- flat plate
- heat
- 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
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F1/00—Tubular elements; Assemblies of tubular elements
- F28F1/10—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
- F28F1/12—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element
- F28F1/14—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending longitudinally
- F28F1/22—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending longitudinally the means having portions engaging further tubular elements
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/08—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being otherwise bent, e.g. in a serpentine or zig-zag
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/08—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being otherwise bent, e.g. in a serpentine or zig-zag
- F28D7/082—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being otherwise bent, e.g. in a serpentine or zig-zag with serpentine or zig-zag configuration
- F28D7/085—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being otherwise bent, e.g. in a serpentine or zig-zag with serpentine or zig-zag configuration in the form of parallel conduits coupled by bent portions
- F28D7/087—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being otherwise bent, e.g. in a serpentine or zig-zag with serpentine or zig-zag configuration in the form of parallel conduits coupled by bent portions assembled in arrays, each array being arranged in the same plane
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F19/00—Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers
Abstract
Description
【発明の詳細な説明】
本発明は廃熱回収などの熱交換に際して汚れの減少に効
果がらり、しかも高圧流体が導入でき、そのうえ腐食性
ガスに強い伝熱装置に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a heat transfer device that is effective in reducing contamination during heat exchange such as waste heat recovery, can introduce high-pressure fluid, and is resistant to corrosive gases.
一般にディーゼルエンジンは良質の燃料油を使用すると
きは廃ガスも比−較的清浄であるが、近年石油事情の逼
迫から重質分、硫黄分等が増加し、品質の低下に伴って
附設した排ガスエコノマイザ−9廃熱ボイラ等における
伝熱管束の排ガス側の汚れがますますひどく、伝熱効率
は低下し、そのうえ腐食が増大するなどの好ましくない
状態となっている。極端な場合は媒による粉塵燥発を惹
起る
す危険性もある。また耐食性を考慮してガラス。In general, when diesel engines use high-quality fuel oil, the exhaust gas is relatively clean, but in recent years, due to the tight oil situation, the heavy content and sulfur content have increased, and the quality has deteriorated. Exhaust Gas Economizer 9 The exhaust gas side of the heat transfer tube bundle in waste heat boilers and the like is becoming increasingly contaminated, resulting in unfavorable conditions such as reduced heat transfer efficiency and increased corrosion. In extreme cases, there is a risk that the medium may cause dust to dry out. Also glass for corrosion resistance.
カーベイトなどの伝熱管の使用も考えられるが、強度上
問題がある。It is possible to use a heat transfer tube such as a carbide, but this poses a problem in terms of strength.
従来、エコノマイザ−2廃熱ボイラなどに使用される伝
熱装置は裸管をそのまま使用したり、あるいは熱伝達を
考慮して狭い間隔で多数のフィンを植設したもの、また
はフィンを螺旋状に巻付け、または長手方向竪形にフィ
ンを溶接したフィンチューブ、あるいは平板型熱交−器
か採用されている。このうち特に、管′を用いた熱交換
器では汚れた場合の清掃は厄介であるが、反面耐圧力が
あるので高圧装置に使用できる利点があり、また平板型
熱交換器は耐圧力は小さいか清掃に優れているなど、そ
れぞれの特長を有する。本発明は管を世いた熱交換器及
び平板型熱交換器の長所を兼ね鍋え、即ち耐圧力があり
しかも清掃が容易であって、長時間連続運転ができると
いう運転管理の信頼性に着目してなされたものである。Conventionally, heat transfer devices used in economizer 2 waste heat boilers, etc. have either used bare tubes as they are, or have had many fins installed at narrow intervals to improve heat transfer, or have fins arranged in a spiral shape. A finned tube with fins wrapped or welded vertically in the longitudinal direction, or a flat plate heat exchanger are used. Among these, heat exchangers using tubes are particularly troublesome to clean when they become dirty, but on the other hand, they have the advantage of being able to withstand high pressure, so they can be used in high-pressure equipment, and flat plate heat exchangers have a low pressure resistance. Each type has its own characteristics, such as superior cleaning ability. The present invention combines the advantages of the tube-based heat exchanger and the flat plate heat exchanger, and focuses on the reliability of operation management, which is pressure resistant, easy to clean, and can be operated continuously for a long time. It was done by
第1図に示す伝熱管モジュール1は材質が炭素鋼、ステ
ンレス鋼の場合で、例えば直径10111111の複数
の裸管2 、2’、 2″が単列平行に並び、2枚の平
板6,3′が裸管を挟持し、第2図のように相対する切
線位ffi、4.4’をシーム溶接して固着し平板状に
形成されている。各裸管は平板間で折流し、出入口には
ヘラグー5,5′が設けられている。平行な平板の上下
端部は滑らかな先端封止部7.が形成され、必要に応じ
て平板前後部を裸管が貫通する封止板で塞ぎ、平板間を
密封構造とすることもできる。また、この密封構造内に
熱媒体を充填して伝熱を一層向上させることもできる。The heat exchanger tube module 1 shown in FIG. 1 is made of carbon steel or stainless steel. For example, a plurality of bare tubes 2, 2', 2" with a diameter of 10111111 are arranged in a single row in parallel, and two flat plates 6, 3 are arranged in parallel. ' holds the bare tube, and as shown in Figure 2, the opposing cutting lines ffi, 4.4' are seam-welded and fixed to form a flat plate.Each bare tube is bent between the flat plates, and an inlet/outlet Helagoos 5 and 5' are provided at the upper and lower ends of the parallel flat plates. Smooth tip sealing parts 7. It is also possible to form a sealed structure between the flat plates.Furthermore, it is also possible to fill this sealed structure with a heat medium to further improve heat transfer.
材質か銅。material or copper.
アルミニウムの場合はろう付等を用いてもよい。In the case of aluminum, brazing or the like may be used.
なお裸管と平板の固着は溶接、ろう付に限るものではな
い。Note that fixing the bare tube and the flat plate is not limited to welding or brazing.
このよう女形状の伝熱管モジュールは、第3図のように
各モジュールl 、 +’、 1”・・・は相互に例え
ば20Wrmの距離のある通路6.6′・・を隔て、復
数箇連結して伝熱装置か形成され、通路6,6′・・・
は廃ガスの流れに平行になる位置で煙道(図示せず)内
に設置される。従って矢印向方の煙道ガスは平滑な通路
6,6′・・を通過することとなり、たとえ煙道ガスが
汚れていても媒、灰は平板には固着し難く、多少付着し
ても清掃は容易で、裸管2 、2’。In such a female-shaped heat exchanger tube module, as shown in FIG. A heat transfer device is formed by connecting the passages 6, 6'...
is installed in the flue (not shown) in a position parallel to the flow of waste gas. Therefore, the flue gas in the direction of the arrow passes through the smooth passages 6, 6', etc. Even if the flue gas is dirty, the medium and ash are difficult to stick to the flat plate, and even if some adhere to it, it can be cleaned. It is easy to use bare tubes 2 and 2'.
2″は平板3,6′で覆われているため伝熱効率は幾分
犠牲となるが、長期間の連続運転が可能となり、信頼性
が伝熱効率の低下を補って余りかある。2'' is covered with flat plates 3 and 6', so heat transfer efficiency is sacrificed to some extent, but long-term continuous operation is possible, and reliability more than compensates for the decrease in heat transfer efficiency.
本発明は平板を挟んで固着形成した伝熱管モジュールを
具えてなる伝熱装置であるから、管を用いだ熱交換器と
平板型熱交換器の長所を兼ね備え、管内に高圧流体を導
入できるのでその利用軸1j4Jは従来の平板型熱交換
器に較べて大幅に拡大でき、例えば高圧の排ガスボイラ
を経済的に作ることができる。そのうえボイラを廃ガス
中に設置しても表向に凹凸のない平板は媒、灰等の晴着
、沈槓がしにくく、また裸管は直接外部流体に接触しな
いため耐食性を考慮する必要がなく、例えば垣酸分を含
むごみ焼却炉布ガス中に設置して廃熱回収するとさもで
きる。また熱回収用途のみならず逆に裸管内に高温流体
を導入して冷却廃ガスを加熱し、ガス中の硫酸、塩酸の
結露を防止する排・梓加熱器等に使用することもできる
。もしコーテングの必要が生じても平板への塗布となり
、テフロンコーテングなど従来の間隔の狭いフィンチュ
ーブはもとより凹凸のある平板型熱交換器のコーテング
に・ 較べて容易となる。Since the present invention is a heat transfer device comprising a heat transfer tube module fixedly formed with a flat plate in between, it has the advantages of a heat exchanger using tubes and a flat plate heat exchanger, and high pressure fluid can be introduced into the tubes. The usable axis 1j4J can be greatly expanded compared to the conventional flat plate heat exchanger, and for example, a high-pressure exhaust gas boiler can be economically produced. Furthermore, even if the boiler is installed in waste gas, a flat plate with no irregularities on its surface will not allow medium, ash, etc. to settle or settle, and since bare pipes do not come into direct contact with external fluid, there is no need to consider corrosion resistance. For example, waste heat can be recovered by installing the waste incinerator in a waste incinerator gas containing acid. Moreover, it can be used not only for heat recovery purposes, but also for exhaust/azusa heaters that introduce high-temperature fluid into bare pipes to heat cooled waste gas and prevent condensation of sulfuric acid and hydrochloric acid in the gas. If coating is required, it can be applied to a flat plate, which is easier than coating conventional narrowly spaced fin tubes such as Teflon coating, as well as coating uneven flat plate heat exchangers.
一方、伝熱について伝熱管モジュールは、裸管と平板と
は線接触であるため伝熱効率の低下は避ケラレナいが、
密封構造としてこの内部に熱媒体を充填することによっ
て伝熱効率を改善でき、上記のように汚れが少ないので
、汚れによる清掃までの間隔は、長期にわたり大幅に延
長できるから長期間の運転継続が伝熱効率の低下を補っ
て余りがあり、運転管理が容易で信頼性に富み、たとえ
汚れても凹凸のない平板は清掃が容易である等の効果が
ある。On the other hand, regarding heat transfer, in the heat transfer tube module, there is a line contact between the bare tube and the flat plate, so a decrease in heat transfer efficiency can be avoided.
Heat transfer efficiency can be improved by filling the interior with a heat medium as a sealed structure, and as there is less dirt as mentioned above, the interval between cleaning due to dirt can be significantly extended over a long period of time, allowing continued operation for a long time. This more than compensates for the decrease in thermal efficiency, operation management is easy and reliable, and even if it gets dirty, the flat plate is smooth and easy to clean.
以上のように本発明においては伝熱装置の汚れに対して
効果があり、しかも高圧流体を取扱うこ、!:ができ、
さらに腐食性ガスに対しても使用できるので応用範囲は
広く、例えばディーゼルエンジン廃熱ボイラ、産業廃棄
物燃焼炉のエコノマイザ−1既設陸上ボイラのエコノマ
イザ−およヒ附属する温水器、こみ焼却炉の排煙加熱器
、高温腐食性布ガスの熱回収などに利用できその効果は
太きい。As described above, the present invention is effective against contamination of heat transfer devices, and is also effective in handling high-pressure fluids! : can be done,
Furthermore, it can be used for corrosive gases, so it has a wide range of applications, such as diesel engine waste heat boilers, economizers for industrial waste combustion furnaces, economizers for existing land boilers, attached water heaters, and waste incinerators. It can be used in flue gas heaters, heat recovery from high-temperature corrosive cloth gas, and has great effects.
図は本発明の実施例を示し、第1図は伝熱管モジュール
の斜視図、第2図は裸管と平板との溶接箇所を示した説
明図、第3図は伝熱管モジュールの配置dを示す説り1
図である。
1・・・伝熱管モジュール 2 、2’、 2″
・・裸管6.5′・・・平板 4,4′
・・・切線位1a5.5′・・・出入口
6,6′・・・通路7・・先端封止部
特許出願人 株式会社笹倉機械製作所The figures show an embodiment of the present invention, in which Fig. 1 is a perspective view of a heat exchanger tube module, Fig. 2 is an explanatory diagram showing the welding points between a bare tube and a flat plate, and Fig. 3 is an illustration of the arrangement d of the heat exchanger tube module. Explanation 1
It is a diagram. 1... Heat exchanger tube module 2, 2', 2''
...Bare tube 6.5'...Flat plate 4,4'
... Cut line position 1a5.5' ... Entrance/exit
6, 6'...Passage 7...Tip sealing part Patent applicant Sasakura Machinery Co., Ltd.
Claims (1)
てなる伝熱装置。A heat transfer device comprising a heat transfer tube module in which a bare tube is sandwiched and fixed between flat plates.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11263481A JPS5813987A (en) | 1981-07-17 | 1981-07-17 | Heat transmitting device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11263481A JPS5813987A (en) | 1981-07-17 | 1981-07-17 | Heat transmitting device |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5813987A true JPS5813987A (en) | 1983-01-26 |
JPS6217155B2 JPS6217155B2 (en) | 1987-04-16 |
Family
ID=14591630
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP11263481A Granted JPS5813987A (en) | 1981-07-17 | 1981-07-17 | Heat transmitting device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5813987A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2586290A1 (en) * | 1985-08-14 | 1987-02-20 | Stein Industrie | DEVICE FOR PROTECTING EXCHANGERS PLACED IN A CONDUIT OF FUMES CHARGED WITH ASH FILLED PARTICLES |
JPS6372768U (en) * | 1986-10-31 | 1988-05-16 | ||
WO2013089315A1 (en) * | 2011-12-13 | 2013-06-20 | 주식회사 코렌스 | Apparatus for generating superheated vapor using wave fin |
WO2013089314A1 (en) * | 2011-12-13 | 2013-06-20 | 주식회사 코렌스 | Apparatus for generating superheated vapor using waste heat recovery |
-
1981
- 1981-07-17 JP JP11263481A patent/JPS5813987A/en active Granted
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2586290A1 (en) * | 1985-08-14 | 1987-02-20 | Stein Industrie | DEVICE FOR PROTECTING EXCHANGERS PLACED IN A CONDUIT OF FUMES CHARGED WITH ASH FILLED PARTICLES |
US4667733A (en) * | 1985-08-14 | 1987-05-26 | Stein Industrie | Protective device for heat exchangers placed in a duct for smoke filled with fine particles of ash |
JPS6372768U (en) * | 1986-10-31 | 1988-05-16 | ||
WO2013089315A1 (en) * | 2011-12-13 | 2013-06-20 | 주식회사 코렌스 | Apparatus for generating superheated vapor using wave fin |
WO2013089314A1 (en) * | 2011-12-13 | 2013-06-20 | 주식회사 코렌스 | Apparatus for generating superheated vapor using waste heat recovery |
US9631539B2 (en) | 2011-12-13 | 2017-04-25 | Korens Co., Ltd. | Apparatus for generating superheated vapor using wave fin |
Also Published As
Publication number | Publication date |
---|---|
JPS6217155B2 (en) | 1987-04-16 |
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