JPS6199100A - Exhaust gas heat exchanger - Google Patents

Exhaust gas heat exchanger

Info

Publication number
JPS6199100A
JPS6199100A JP22096384A JP22096384A JPS6199100A JP S6199100 A JPS6199100 A JP S6199100A JP 22096384 A JP22096384 A JP 22096384A JP 22096384 A JP22096384 A JP 22096384A JP S6199100 A JPS6199100 A JP S6199100A
Authority
JP
Japan
Prior art keywords
exhaust gas
pipe
heat exchanger
flows
brine
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
JP22096384A
Other languages
Japanese (ja)
Inventor
Kunio Aigami
相上 国雄
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.)
Subaru Corp
Original Assignee
Fuji Heavy Industries Ltd
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 Fuji Heavy Industries Ltd filed Critical Fuji Heavy Industries Ltd
Priority to JP22096384A priority Critical patent/JPS6199100A/en
Publication of JPS6199100A publication Critical patent/JPS6199100A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28GCLEANING OF INTERNAL OR EXTERNAL SURFACES OF HEAT-EXCHANGE OR HEAT-TRANSFER CONDUITS, e.g. WATER TUBES OR BOILERS
    • F28G1/00Non-rotary, e.g. reciprocated, appliances
    • F28G1/12Fluid-propelled scrapers, bullets, or like solid bodies
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B08CLEANING
    • B08BCLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
    • B08B9/00Cleaning hollow articles by methods or apparatus specially adapted thereto
    • B08B9/02Cleaning pipes or tubes or systems of pipes or tubes
    • B08B9/027Cleaning the internal surfaces; Removal of blockages
    • B08B9/04Cleaning the internal surfaces; Removal of blockages using cleaning devices introduced into and moved along the pipes
    • B08B9/053Cleaning the internal surfaces; Removal of blockages using cleaning devices introduced into and moved along the pipes moved along the pipes by a fluid, e.g. by fluid pressure or by suction
    • B08B9/055Cleaning the internal surfaces; Removal of blockages using cleaning devices introduced into and moved along the pipes moved along the pipes by a fluid, e.g. by fluid pressure or by suction the cleaning devices conforming to, or being conformable to, substantially the same cross-section of the pipes, e.g. pigs or moles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B08CLEANING
    • B08BCLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
    • B08B9/00Cleaning hollow articles by methods or apparatus specially adapted thereto
    • B08B9/02Cleaning pipes or tubes or systems of pipes or tubes
    • B08B9/027Cleaning the internal surfaces; Removal of blockages
    • B08B9/04Cleaning the internal surfaces; Removal of blockages using cleaning devices introduced into and moved along the pipes
    • B08B9/053Cleaning the internal surfaces; Removal of blockages using cleaning devices introduced into and moved along the pipes moved along the pipes by a fluid, e.g. by fluid pressure or by suction
    • B08B9/057Cleaning the internal surfaces; Removal of blockages using cleaning devices introduced into and moved along the pipes moved along the pipes by a fluid, e.g. by fluid pressure or by suction the cleaning devices being entrained discrete elements, e.g. balls, grinding elements, brushes
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/06Heat-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 having a single U-bend

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Physics & Mathematics (AREA)
  • General Engineering & Computer Science (AREA)
  • Fluid Mechanics (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Thermal Sciences (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

PURPOSE:To discharge soot adhered to and accumulated on the inside of the heat exchanger by removing it automatically and prevent the deterioration of heat exchanging efficiency by a method wherein a multitude of floating bodies, formed with protuberances on the outer surface thereof, is accommodated in an exhaust gas pipe. CONSTITUTION:The flotation body 14 is constituted by combining three sheets of circular sheet members 16, made of heat resistant thin metal or the like and formed with a multitude of sawteeth-like protuberances 16 on the circumference thereof, and the weight thereof is a degree that it is floated by the exhaust gas while the size thereof is made larger than small holes formed on venting plates 7, 9. The exhaust gas enters from an exhaust gas inlet pipe 6, flows through the exhaust gas pipe 2 and is discharged out of an exhaust gas outlet pipe 8 while brine enters from a brine inlet pipe 11, flows through a duct section 10 and a fluid pipe 12, then, flows through a section enclosed by the exhaust gas pipe 2 and an outer tubular pipe 3 and, thereafter, is discharged out of a brine outlet pipe 13. The floatation bodies 14, accommodated in the exhaust gas pipe 2, are floated by the exhaust gas and collide against the outer surface of the fluid pipe 12, the outer surface of the duct section 10 or the inner surface of the exhaust gas pipe 2 while soot, adhered to and accumulated on the surfaces, is dropped by scraping by the protuberances 15 and is discharged to the outside of the heat exchanger together with the exhaust gas.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、エンジンの排気ガスと流体との間で熱交換で
きるようにした排気ガス熱交換器に係り、特に排気ガス
による煤を自動的に除去できるよう改良した排気ガス熱
交換器に関するものである。
[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to an exhaust gas heat exchanger capable of exchanging heat between engine exhaust gas and fluid, and in particular, relates to an exhaust gas heat exchanger that can automatically remove soot from exhaust gas. This article relates to an improved exhaust gas heat exchanger that can remove

[従来の技術] 一般に、エンジンの排気ガスににる排熱を利用するため
に排気ガス熱交換器が用いられている。
[Prior Art] Generally, an exhaust gas heat exchanger is used to utilize exhaust heat in engine exhaust gas.

例えば、エンジン駆動ヒートポンプ装η等においては、
このエンジンめ排気ガスによる排熱のほかにエンジンの
水冷Wによる熱を冷IJII水熱交換器で回収すること
ができるために、電動ヒートポンプ装置よりもエネルギ
ー利用効率が優れており、各種給湯装置等として利用さ
れている。この種のエンジン駆動ヒートポンプ8i置に
用いられる排気ガス熱交換器は、排気ガス管内を流通す
る排気ガスと流体管内を流通するブライン等の流体との
間で相Uに熱交換できる貫流式の栴造となっている。
For example, in engine-driven heat pump equipment, etc.
In addition to the exhaust heat from the engine exhaust gas, the heat from the water cooling W of the engine can be recovered by the cold IJII water heat exchanger, making it more efficient in energy use than electric heat pump devices, and is used in various water heaters, etc. It is used as. The exhaust gas heat exchanger used in this type of engine-driven heat pump 8i is a once-through type heat exchanger that can exchange heat between the exhaust gas flowing in the exhaust gas pipe and the fluid such as brine flowing in the fluid pipe. It is constructed.

[゛発明が解決しようとする問題点] しかしながら、このような従来の排気ガス熱交換器では
、排気ガスが流通する熱交換器内部に煤が付着堆積して
熱交換効率を著しく低下させていた。又、煤が付着した
場合には、定期的に熱交換器を分解して清掃しなければ
ならず煩しい作業を必要としていた。
[Problems to be solved by the invention] However, in such conventional exhaust gas heat exchangers, soot adheres and accumulates inside the heat exchanger through which exhaust gas flows, significantly reducing heat exchange efficiency. . Furthermore, if soot adheres to the heat exchanger, the heat exchanger must be periodically disassembled and cleaned, which requires troublesome work.

尚、実開昭47−4312号公報には、排気ガス清浄装
置における循環式冷却装置に関する従来の技術が開示さ
れているが、この従来の技術は内部に付着した排気ガス
の煤を除去できるものではない。
Incidentally, Japanese Utility Model Application Publication No. 47-4312 discloses a conventional technique regarding a circulation type cooling device in an exhaust gas purifying device, but this conventional technique is capable of removing soot from exhaust gas adhering to the inside. isn't it.

本発明は、このような従来の問題点等に着目してなされ
たもので、排気ガス熱交換器内部に付着堆積する煤を、
何ら煩しい作業を必要とせず自動的に除去して、熱交換
効率の低下を防止できる排気ガス熱交換器を提供するこ
とを目的としている。
The present invention has been made by focusing on such conventional problems, and is aimed at reducing soot that adheres and accumulates inside an exhaust gas heat exchanger.
It is an object of the present invention to provide an exhaust gas heat exchanger that can be automatically removed without any troublesome work and can prevent a decrease in heat exchange efficiency.

[問題点を解決するための手段1 上記問題点を解決するために、本発明の排気ガス熱交換
器は、排気ガスが流れる排気ガス管内に、該排気ガスで
浮遊するとともに、外面に突起を形成した浮遊体を多数
収納するように構成している。
[Means for Solving the Problems 1] In order to solve the above problems, the exhaust gas heat exchanger of the present invention has a structure in which the exhaust gas floats in the exhaust gas pipe through which the exhaust gas flows, and has protrusions on the outer surface. It is configured to store a large number of formed floating bodies.

[作用] 次に作用を説明する。排気ガス管内に収納された多数の
浮遊体は排気ガスにより浮遊し、排気ガス管の内面、あ
るいは液体の流れる流体管の外面に衝突して付着堆積し
た煤を該浮遊体外面の突起で掻き落す。そして、この掻
き落された煤は排気ガスとともに外部に排出される。従
って、内部に付着堆積する煤を、何ら煩しい作業を必要
とせずに自動的に除去して、熱交換効率の低下を防止す
ることができる。
[Operation] Next, the operation will be explained. A large number of floating bodies housed in the exhaust gas pipe are suspended by the exhaust gas, and the protrusions on the outer surface of the floating bodies scrape off the soot deposited by colliding with the inner surface of the exhaust gas pipe or the outer surface of the fluid pipe through which liquid flows. . This scraped soot is then discharged to the outside together with the exhaust gas. Therefore, the soot deposited inside can be automatically removed without any troublesome work, and a decrease in heat exchange efficiency can be prevented.

[実施例] 以下図面を参照して本発明による実施例を具体的に説明
する。
[Examples] Examples according to the present invention will be specifically described below with reference to the drawings.

第1図乃至第4図は本発明の第一実施例に係り、第1図
は排気ガス熱交換器の断面図、第2図は浮遊体の斜視図
、第3図は第2図の浮遊体を構成する1枚の板材の正面
図、第4図は第3図の側面図である。
1 to 4 relate to the first embodiment of the present invention, FIG. 1 is a sectional view of the exhaust gas heat exchanger, FIG. 2 is a perspective view of the floating body, and FIG. 3 is the floating body of FIG. 2. FIG. 4 is a front view of one plate forming the body, and FIG. 4 is a side view of FIG. 3.

これらの図において符号1は排気ガス熱交換器であり、
この排気ガス熱交換器1は排気ガスが流通する排気ガス
管2に外筒管3を外装した二垂管に形成され、その上端
側を上部仕切板4で、又その下端側を中央が次第に低く
なるよう傾斜を形成した底部仕切板5で閉塞されている
。前記底部仕切板5の中央部の最も低くなった部分には
、排気ガス管2内に連通する排気ガス入口管6が接続さ
れ、又その接続口部分には小孔が多数形成された下側通
気板7が設けられている。前記上部仕切板4のほぼ中央
部には、排気ガス管2内に連通ずる排気ガス出口管8が
接続され、又その接続口部分には小孔が多数形成された
上側通気板9が設けられている。又、前記排気ガス管2
内の上部には、ブラインが流入するダ久°ト部10が設
けられている。そして、このダクト部10の一側部には
、該ダクト部10内部に連通ずるブライン入口管11の
一端が接続され、他端側は排気ガス管2と外筒管3の側
壁をともに貫通して外部に延出されている。又、前記ダ
クト部10の下側には、該ダクト部10内部に連通ずる
ブラインが流れる流体管12、・・・の一端が接続され
、他端側は排気ガス管2内を通って下側の底部仕切板5
を貫通して外に突出され、さらにその端部側をほぼU字
状に曲折して、再び底部仕切板5に外筒管3内に連通す
るよう接続されている。前記外筒管3の上側の一側部に
は、該外筒管3内に連通ずるブライン出口管13が接続
されている。
In these figures, numeral 1 is an exhaust gas heat exchanger,
This exhaust gas heat exchanger 1 is formed into two vertical pipes in which an exhaust gas pipe 2 through which exhaust gas flows is sheathed with an outer cylindrical pipe 3, and the upper end thereof is surrounded by an upper partition plate 4, and the lower end thereof is gradually It is closed by a bottom partition plate 5 which is sloped to be lower. An exhaust gas inlet pipe 6 that communicates with the inside of the exhaust gas pipe 2 is connected to the lowest central part of the bottom partition plate 5, and the lower part of the bottom partition plate 5 has a number of small holes formed at its connection port. A ventilation plate 7 is provided. An exhaust gas outlet pipe 8 communicating with the inside of the exhaust gas pipe 2 is connected to approximately the center of the upper partition plate 4, and an upper ventilation plate 9 in which a large number of small holes are formed is provided at the connection port. ing. Moreover, the exhaust gas pipe 2
A duct section 10 into which brine flows is provided at the upper part of the chamber. One end of a brine inlet pipe 11 communicating with the inside of the duct part 10 is connected to one side of the duct part 10, and the other end passes through the side walls of both the exhaust gas pipe 2 and the outer cylinder pipe 3. It is extended outside. Further, one end of a fluid pipe 12, through which brine flows, which communicates with the inside of the duct part 10, is connected to the lower side of the duct part 10, and the other end passes through the exhaust gas pipe 2 to the lower side. bottom partition plate 5
The end portion thereof is bent into a substantially U-shape, and is again connected to the bottom partition plate 5 so as to communicate with the inside of the outer cylindrical tube 3. A brine outlet pipe 13 communicating with the inside of the outer tube 3 is connected to one upper side of the outer tube 3.

一方、前記排気ガス管2内には、多数の浮遊体14、・
・・が収納されている。この浮遊体14は耐熱性の薄い
金属等の材質からなる円板状で、その円板の周囲にのこ
ぎり状の多数の突起15.・・・を形成した同形の3枚
の板材16.16.16からなり、その板材16.16
.16の中心部を共通にするとともに、該板材16.1
6.16のそれぞれの平面が互に直角となるように組合
わされて構成されている。尚、前記浮遊体14の垂さは
排気ガスにより浮遊する程度であり、又その大きさは前
記上側および下側通気板7.9に形成された小孔よりも
大きく形成されている。
On the other hand, inside the exhaust gas pipe 2, a large number of floating bodies 14,
... is stored. The floating body 14 has a disc shape made of a heat-resistant thin metal or the like, and has many saw-shaped protrusions 15 around the disc. Consisting of three plates 16.16.16 of the same shape forming ..., the plate 16.16
.. 16, and the center part of the plate material 16.1 is made common.
6.16 planes are combined so that they are perpendicular to each other. The height of the floating body 14 is such that it is suspended by the exhaust gas, and its size is larger than the small holes formed in the upper and lower ventilation plates 7.9.

このような構成では、排気ガスは排気ガス入口管6より
流入し排気ガス管2を流れて排気ガス出口管8より排出
され、一方ブラインはブライン入口管11より流入しダ
クト部10.流体管12゜・・・を流れ、さらに排気ガ
ス管2と外筒管3とで囲われた部分を流れブライン出口
管13より排出され、排気ガスとブラインとの間で熱交
換が行われる。このとき、排気ガス管2内に収納された
浮遊体14.・・・は排気ガスにより浮遊し、流体管1
2゜・・・の外面、ダクト部10外面あるいは排気ガス
管2の内面に衝突して、それらの表面に付着堆積した煤
が突起15.・・・により掻き落される。そして、前記
掻き落された煤は排気ガスとともに外に排出される。従
って、排気ガス熱交換器1を分解して清掃する等の煩し
い作業をすることなく自動的に煤を除去して熱交換効率
の低下を防止することができる。
In such a configuration, exhaust gas flows from the exhaust gas inlet pipe 6, flows through the exhaust gas pipe 2, and is discharged from the exhaust gas outlet pipe 8, while brine flows from the brine inlet pipe 11 and flows through the duct section 10. It flows through the fluid pipes 12.degree., further flows through a portion surrounded by the exhaust gas pipe 2 and the outer cylinder pipe 3, and is discharged from the brine outlet pipe 13, where heat exchange is performed between the exhaust gas and brine. At this time, the floating body 14 accommodated in the exhaust gas pipe 2. ... is suspended by the exhaust gas, and the fluid pipe 1
2°..., the outer surface of the duct part 10, or the inner surface of the exhaust gas pipe 2, and the soot that adheres and accumulates on those surfaces is deposited on the protrusion 15. It is scraped off by... The scraped off soot is then discharged to the outside together with the exhaust gas. Therefore, it is possible to automatically remove soot and prevent a decrease in heat exchange efficiency without performing troublesome work such as disassembling and cleaning the exhaust gas heat exchanger 1.

尚、この実施例では底部仕切板5中火の排気ガス入口管
6の接続部分において最も低く形成されているために、
浮遊体14がこの部分に集まり再び浮遊するようになっ
ている。又、浮遊体14は下側および上側通気板7.9
に形成された小孔よりも大きいため外に排出されること
がない。
In this embodiment, since the bottom partition plate 5 is formed at the lowest point at the connection part of the medium-heat exhaust gas inlet pipe 6,
The floating bodies 14 gather in this part and become floating again. The floating body 14 also has lower and upper ventilation plates 7.9.
Because it is larger than the small hole formed in the hole, it cannot be discharged outside.

第5図は本発明の第二実施例に係り浮遊体の斜視図であ
る。
FIG. 5 is a perspective view of a floating body according to a second embodiment of the present invention.

この実施例では、第一実施例と同様の構造からなる排気
ガス熱交換器の排気ガス管2内部に第5図に示す浮遊体
21が多数収納された構成となっている。この浮遊体2
1は球状体の表面に多数の突起22が形成されており、
第一実施例と同様の大きさおよび重さになっているとと
もに、耐熱性材料で形成され適度の硬さを有している。
In this embodiment, a large number of floating bodies 21 shown in FIG. 5 are housed inside the exhaust gas pipe 2 of the exhaust gas heat exchanger having the same structure as the first embodiment. This floating body 2
1 has a large number of protrusions 22 formed on the surface of a spherical body,
It has the same size and weight as the first embodiment, and is made of a heat-resistant material and has appropriate hardness.

このような構成では、浮遊体21.・・・が第一実施例
と同様に作用する。
In such a configuration, the floating body 21. ... works in the same way as in the first embodiment.

尚、前記実施例において浮遊体14.21は排気ガスに
より浮遊するとともに、表面に煤を掻き落すことができ
る突起15.22が形成されていればよく、その全体の
形状も球状等に限定されることなく任意の形状にするこ
とができる。又、排気ガス熱交換器の構造は、排気ガス
と流体とが熱交換できる貫流式等のものであればよ〈実
施例に限定されない。
Incidentally, in the above embodiment, the floating body 14.21 only needs to be floated by the exhaust gas and have protrusions 15.22 formed on the surface that can scrape off soot, and the overall shape is also limited to a spherical shape or the like. It can be made into any shape without needing to be shaped. Further, the structure of the exhaust gas heat exchanger is not limited to the embodiments, as long as it is of a once-through type or the like in which exhaust gas and fluid can exchange heat.

[発明の効果] 以上説明したように本発明によれば、排気ガス熱交換器
内部の排気ガス管内に外面に突起を形成した浮遊体を多
数収納するようにしているために、その内部に付着堆積
した煤を、何ら煩しい作業を必要とせずに自動的に除去
し、外に排出でき、熱交換効率の低下を防止できる効果
がある。
[Effects of the Invention] As explained above, according to the present invention, a large number of floating bodies having protrusions formed on the outer surface are housed in the exhaust gas pipe inside the exhaust gas heat exchanger, so that there is no adhesion to the inside of the floating bodies. Accumulated soot can be automatically removed and discharged to the outside without the need for any troublesome work, which has the effect of preventing a decrease in heat exchange efficiency.

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

第1図乃至第4図は本発明の第一実施例に係り、第1図
は排気ガス熱交換器の断面図、第2図は浮遊体の斜視図
、第3図は第2図の浮遊体を構成する1枚の板材の正面
図、第4図は第3図の側面図、第5図は本発明の第二実
施例に係り浮遊体の斜視図である。 1・・・排気ガス熱交換器 2・・・排気ガス管    3・・・外筒管4・・・°
上部仕切板    5・・・底部仕切板6・・・排気ガ
ス入口管  8・・・排気ガス出口管11・・・ブライ
ン入口管 12・・・流体管13・・・ブ)イン出口管
 14.21・・・浮遊体15.22・・・突起 代理人  弁理士  伊 藤  進1゛I+1.′、−
・ノ ーさtl−〆 第1図 第3図   第4図
1 to 4 relate to the first embodiment of the present invention, FIG. 1 is a sectional view of the exhaust gas heat exchanger, FIG. 2 is a perspective view of the floating body, and FIG. 3 is the floating body of FIG. 2. FIG. 4 is a side view of FIG. 3, and FIG. 5 is a perspective view of a floating body according to a second embodiment of the present invention. 1...Exhaust gas heat exchanger 2...Exhaust gas pipe 3...Outer cylinder pipe 4...°
Upper partition plate 5...Bottom partition plate 6...Exhaust gas inlet pipe 8...Exhaust gas outlet pipe 11...Brine inlet pipe 12...Fluid pipe 13...B) Inlet outlet pipe 14. 21...Floating body 15.22...Protrusion agent Patent attorney Susumu Ito 1゛I+1. ′,−
・Nosa tl-〆Figure 1 Figure 3 Figure 4

Claims (1)

【特許請求の範囲】[Claims] 排気ガス管内を流通する排気ガスと流体管内を流通する
流体との間で熱交換するようにした排気ガス熱交換器に
おいて、前記排気ガス管内に、排気ガスで浮遊するとと
もに外面に突起を形成した浮遊体を多数収納するように
したことを特徴とする排気ガス熱交換器。
In an exhaust gas heat exchanger that exchanges heat between exhaust gas flowing in an exhaust gas pipe and fluid flowing in a fluid pipe, a protrusion is formed on the outer surface of the exhaust gas pipe while floating in the exhaust gas. An exhaust gas heat exchanger characterized by storing a large number of floating bodies.
JP22096384A 1984-10-19 1984-10-19 Exhaust gas heat exchanger Pending JPS6199100A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22096384A JPS6199100A (en) 1984-10-19 1984-10-19 Exhaust gas heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22096384A JPS6199100A (en) 1984-10-19 1984-10-19 Exhaust gas heat exchanger

Publications (1)

Publication Number Publication Date
JPS6199100A true JPS6199100A (en) 1986-05-17

Family

ID=16759296

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22096384A Pending JPS6199100A (en) 1984-10-19 1984-10-19 Exhaust gas heat exchanger

Country Status (1)

Country Link
JP (1) JPS6199100A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006010771A1 (en) * 2004-07-29 2006-02-02 Twister B.V. Heat exchanger vessel with means for recirculating cleaning particles

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006010771A1 (en) * 2004-07-29 2006-02-02 Twister B.V. Heat exchanger vessel with means for recirculating cleaning particles
EA009751B1 (en) * 2004-07-29 2008-04-28 Твистер Б.В. Heat exchanger vessel with means for recirculating cleaning particles
US7900691B2 (en) 2004-07-29 2011-03-08 Twister B.V. Heat exchanger vessel with means for recirculating cleaning particles
CN101010557B (en) 2004-07-29 2011-06-08 缠绕机公司 Heat exchanger vessel with means for recirculating cleaning particles

Similar Documents

Publication Publication Date Title
CN210689299U (en) Efficient energy-saving tubular heat exchanger
CN218545386U (en) Self-cleaning heat exchange device
CN201229131Y (en) Shell and tube type acoustic cavitation sewerage heat exchanger
CN212931095U (en) Novel tube-plate heat exchanger
CN110645814A (en) Fluoroplastic shell-and-tube heat exchanger based on novel structure
CN201000286Y (en) Sewage water and surface water cold/heat source tube cluster on-line anti-soil heat exchanger
CN219058593U (en) High-thermal-conductivity waste water evaporator
CN217503972U (en) Positive displacement water heater
CN215064016U (en) Dry-type evaporimeter self-cleaning device
JP3591970B2 (en) Multi-tube heat exchanger
CN219415862U (en) Gas heat exchanger with flue gas treatment mechanism
JPS6233299A (en) Heat exchanger
JPH0655076U (en) Heat exchanger
CN111530116B (en) Medium-high temperature waste gas treatment system with multistage oil-gas separation function
JPS6314221Y2 (en)
CN222210466U (en) Wet fume purifier
CN211178059U (en) Fluoroplastic shell-and-tube heat exchanger based on novel structure
CN210197401U (en) Special oil smoke purification integrated machine for steam cabinet
CN221325194U (en) Novel heat exchanger with convex wave node tube
CN221505745U (en) Heat exchanger
CN217661558U (en) Evaporator plate countercurrent series washing device
CN210801703U (en) Evaporator capable of filtering
CN214537585U (en) Descaling device for high-temperature closed cooling tower
RU2205333C1 (en) Contact surface waste-heat water heater
CN211570717U (en) Water cooling equipment for quenching of heavy truck automobile parts