JPS58182099A - Method of purifying heat exchanger - Google Patents

Method of purifying heat exchanger

Info

Publication number
JPS58182099A
JPS58182099A JP57097887A JP9788782A JPS58182099A JP S58182099 A JPS58182099 A JP S58182099A JP 57097887 A JP57097887 A JP 57097887A JP 9788782 A JP9788782 A JP 9788782A JP S58182099 A JPS58182099 A JP S58182099A
Authority
JP
Japan
Prior art keywords
gas
heat exchanger
heat
layer
elements
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
JP57097887A
Other languages
Japanese (ja)
Other versions
JPH033878B2 (en
Inventor
スタニスロ−・ミヒヤラク
ベルント・ヘルマン
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.)
Hitachi Zosen Inova Steinmueller GmbH
Original Assignee
L&C Steinmueller GmbH
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 L&C Steinmueller GmbH filed Critical L&C Steinmueller GmbH
Publication of JPS58182099A publication Critical patent/JPS58182099A/en
Publication of JPH033878B2 publication Critical patent/JPH033878B2/ja
Granted legal-status Critical Current

Links

Classifications

    • 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
    • F28D13/00Heat-exchange apparatus using a fluidised bed
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F19/00Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers
    • 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
    • F28G9/00Cleaning by flushing or washing, e.g. with chemical solvents
    • F28G9/005Cleaning by flushing or washing, e.g. with chemical solvents of regenerative heat exchanger

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Incineration Of Waste (AREA)
  • Pressure Welding/Diffusion-Bonding (AREA)
  • Cleaning In General (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】 この発明は気体を加熱または冷却するだめの熱交換器系
の浄化方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for purifying a heat exchanger system for heating or cooling gas.

気体の加熱または冷却のため桶種の熱交換器系が知られ
ている。広く行き渉っているのは例えばユングストロー
ム(Ljungstr′6m )原理に従う回転熱交換
器であって、これは定置の形状板、管または薄板の形の
熱貯蔵物を備え、これが測温気体流から低温気体流へ循
環的に動いてその際に熱を吸収しまた放出する。管また
はその他の中空体の中を高温媒体または低温媒体(例え
ば蒸気まだは水)が流過し、その外面のまわシを気体が
流れるような熱交換器もしばしば利用される。
Pub-type heat exchanger systems for heating or cooling gases are known. Widespread are, for example, rotary heat exchangers according to the Ljungström principle, which have a heat store in the form of stationary shaped plates, tubes or sheets, which is connected to a temperature-measuring gas stream. It moves cyclically from the air to the cold gas stream, absorbing and releasing heat as it does so. Heat exchangers are also often used in which a hot or cold medium (for example steam or water) flows through a tube or other hollow body, and a gas flows around its outer surface.

塵を多量に保持する気体の加熱まだは冷却に公知の熱交
換器を使用した際には沈積物が熱交換面上に容易に形成
される。露点以下になる場合または湿式で浄化された煙
−道ガスのように水滴またはエアゾルが気体に伴なわれ
る場合には、熱交換器系においてかさぶた状外皮の形成
およびねば)付きを除くことが極めて困難である。
When known heat exchangers are used to heat or cool dust-laden gases, deposits easily form on the heat exchange surfaces. It is extremely difficult to eliminate crusting and stickiness in heat exchanger systems when temperatures are below the dew point or when water droplets or aerosols are entrained in the gas, such as in wet-purified flue gases. Have difficulty.

このような熱交換器糸に形成されたかさぶた状外皮は熱
交換器における圧力損失を尚め、さらに気体と熱交換面
の間の熱伝達を妨害する。
The scab-like skin formed on such heat exchanger threads reduces pressure losses in the heat exchanger and further impedes heat transfer between the gas and the heat exchange surface.

そのためこのような系に配備される周知の熱交換器は部
分的に極めて複雑な浄化装置を装着する。
The known heat exchangers installed in such systems are therefore partially equipped with extremely complex purification devices.

そして熱交換面を蒸気、空気または水の吹付けで掃除す
ることが知られている。この際には大抵は著しく高い圧
力と極めて高い装置費用とが必要である(ドイツ連邦共
和国特許公開第2948201号公報)。蒸気罐の領域
では例えば熱交換面を1鋼球の雨」で周期的に清掃する
ような機械的浄化方法も知られている。
It is then known to clean heat exchange surfaces with steam, air or water spray. This usually requires very high pressures and very high equipment costs (DE 29 48 201). In the area of steam cans, mechanical cleaning methods are also known, for example, in which the heat exchange surfaces are periodically cleaned with a rain of steel balls.

例れば球のような分離した粒子の堆積層を汚れ捕捉手段
として本来の熱交換面の前方に配備すること(例えば米
国%許第793648号明細書)も知られているが、こ
の解決では堆積層における沈積物によって圧力損失が著
しく高くなり従ってこれが周期的に交換されまたけ浄化
されなければならない。米国特許第3872918号明
細書に記載されている別の方式では回転熱交換器が堆積
層の形の多くの可動の要素で充たされ、これら要素が熱
を管壁に伝達しその運動によって熱交換面を浄化する。
It is also known (e.g. U.S. Pat. No. 793,648) to place a layer of separated particles, such as spheres, in front of the actual heat exchange surface as dirt trapping means, but this solution does not Deposits in the deposited layer cause significant pressure losses and must therefore be replaced and cleaned periodically. In another system, described in U.S. Pat. No. 3,872,918, a rotary heat exchanger is filled with a number of moving elements in the form of stacked layers, which transfer heat to the tube walls and, by their movement, Clean the exchange surface.

この解決では装置費用が比較的高くなると考えられ、堆
積層において圧力損失が大きく、さらにこのような層で
の比較的小さい運動は浄化効果を著しく限定する。
This solution would result in relatively high equipment costs, high pressure losses in the deposited layer, and moreover, the relatively small movements in such a layer significantly limit the cleaning effect.

この発明の目的は、長い作動時間に渉って熱伝達および
圧力損失が一定に保持できる↓うにして気体の加熱また
冷却に使用される熱交換器を簡単かつ有効に浄化する方
法を提供することにある。
The object of the invention is to provide a simple and effective method for purifying heat exchangers used for heating or cooling gases in such a way that heat transfer and pressure losses can be kept constant over long operating times. There is a particular thing.

この目的はこの発明によれば、定常的にまたはときどき
渦動層を形成するような気体の中で自由に動くことがで
きる多くの球、中空の球またはサドル形状体などの要素
を熱交換器の危険な部分に配備することによって達成さ
れる。
This purpose, according to the invention, is to provide a heat exchanger with elements such as a number of spheres, hollow spheres or saddle-shaped bodies that can move freely in the gas, either constantly or occasionally forming a vortex layer. This is achieved by deploying it in dangerous areas.

詳しく言えばこの発明によって、回転熱貯蔵物または回
転気体通路を有し若しくはその代シに高温または低温の
気体が流入する室を有し、気体を通す隔壁が気体流に横
向きに配置される気体−気体−熱交換器を浄化する方法
において、熱貯蔵物それ自身によっても形成できる少く
とも2つの前記隔壁の間に、上方から下方への気体の流
入によって堆積層を形成し下方から上方への気体の流入
によって渦動層を形成するような多くの態別に動くこと
ができる要素を収容し、かかる渦動層を駆動の際に熱交
換器の少くとも1つの区域で保持し、渦動層を形成する
前記要素の相互衝突および相互摩擦によって沈積物を定
常的に除去することを特徴とする方法が提供される。ま
た気体が管、ひれ付き管またはその他の中空体を流過す
る第2の媒体によって加熱または冷却されるような熱交
換器を浄化する方法において、気体空間の中に多くの分
離した要素を収容し、これによって熱交換器の駆動の際
に渦動層を形成しその衝突および摩擦によって熱交換面
を定常的に沈積物なしに保持することを特徴とする方法
も提供される。これらの実施例として、要素が球、中空
の球またはサド形状体として形成され、まだ要素が潜熱
貯蔵物または熱容量の高い材料を備えまたはこれらで形
成される。この浄化方法は半径向きに気体が流入するよ
うな回転熱交換器に利用できる。
More specifically, the invention provides a gas storage system having a rotating heat store or a rotating gas passageway, or having a chamber into which a hot or cold gas flows, and in which a gas-permeable partition is arranged transversely to the gas flow. - a method for purifying a gas-heat exchanger, in which a deposit layer is formed between at least two said partitions, which may also be formed by the heat store itself, by an inflow of gas from above downwards; Contains elements that can be moved in a number of ways, such as forming a fluidized bed by the inflow of gas, and such fluidized bed is retained in at least one area of the heat exchanger during actuation to form a fluidized bed. A method is provided, characterized in that deposits are constantly removed by mutual collision and mutual friction of the elements. Also a method of purifying heat exchangers in which the gas is heated or cooled by a second medium flowing through a tube, fin tube or other hollow body, containing a number of separate elements within the gas space. However, this also provides a method which is characterized in that during the operation of the heat exchanger a fluidized layer is formed and by its collisions and friction the heat exchange surfaces are kept constantly and free of deposits. Examples of these include the elements being formed as spheres, hollow spheres or sadoids, yet the elements comprising or being made of latent heat storage or high heat capacity materials. This purification method can be used in rotary heat exchangers with radial gas flow.

回転熱交換器において、渦動層の中の要素は衝突まだは
摩擦によって熱交換面の定常的な浄化を達成する。回転
熱交換器では、湿気と含有塵の共同作用によって形成さ
れるかさぶた状外皮および沈積物が特に低温気体の流入
区域に生成されることが見出されている。この流入区域
側はこの発明によれば自流で作動し垂直の軸線を有する
回転熱交換器の際に要素が堆積層の形で汚れ捕捉手段の
役をするからこの要素によってねばυ付きのないように
保護され、回転体の回転(甘だけ別の公知の熱交換器系
の際の気体通路の回転または移動)の際には要素は渦動
層に変化しこれにおいて衝突および摩擦によって沈積物
を自動的に除去する。
In rotary heat exchangers, the elements in the fluidized bed achieve constant cleaning of the heat exchange surfaces by collision or friction. It has been found that in rotary heat exchangers, crusts and deposits formed by the joint action of moisture and contained dust are produced, especially in the cold gas inlet areas. According to the invention, on the side of this inlet area, in the case of a rotary heat exchanger that operates with self-flow and has a vertical axis, this element serves as a dirt trapping means in the form of a deposit layer, so that no sticky residue is caused by this element. During the rotation of the rotating body (rotation or movement of the gas passages as in other known heat exchanger systems) the elements transform into a vortex layer in which deposits are automatically removed by collisions and friction. to remove.

特定の利用面ではこのような装置を熱交換器の両側すな
わち低温気体流入側および高温気体流入側に配備するこ
とが有利である。直流で駆動される熱交換器の場合には
要素が流入側に配置され、この流入は要素が熱交換器の
両側で渦動層になるように行なわれる。
In certain applications it is advantageous to arrange such devices on both sides of the heat exchanger, ie on the cold gas inlet side and on the hot gas inlet side. In the case of heat exchangers driven by direct current, the elements are arranged on the inlet side, the inflow being such that the elements form a fluidized bed on both sides of the heat exchanger.

この方法は半径向き流入の公知の回転熱交換器にも難な
く適用できる。
This method can also be easily applied to known rotary heat exchangers with radial flow.

この発明の浄化方法に適した要素および公知の熱交換器
系へのこれの配備の実施例を第1図から第4図に示す。
Examples of elements suitable for the purification method of the invention and their arrangement in known heat exchanger systems are shown in FIGS. 1 to 4.

第1図は浄化のだめの球形状(中空のまたは中空でない
球)の要素1を示す。
FIG. 1 shows a spherical (hollow or solid sphere) element 1 of the purification reservoir.

第2図はサドル形状物体として形成された浄化のための
要素1aを示す。
FIG. 2 shows a cleaning element 1a formed as a saddle-shaped object.

第6図はユングストローム(Ljungstr葛m)原
理に従って回転体2、ハウジング6および垂直軸4を有
しこの発明の方法に適した熱交換器をボす。
FIG. 6 shows a heat exchanger suitable for the method of the invention, having a rotating body 2, a housing 6 and a vertical shaft 4 according to the Ljungström principle.

要素1.1aはかさぶた状外皮の形成の危険がある低温
気体8の流入側で汚れ捕捉手段の作用をする堆積層7を
形成し、この要素は高温気体9の流出側で渦動層乙の中
で浄化される。
Element 1.1a forms a deposit layer 7 which acts as a dirt trapping means on the inlet side of the cold gas 8, where there is a risk of the formation of a crust, and this element forms in the vortex layer A on the outlet side of the hot gas 9. It is purified by

第4図は加熱媒体または冷却媒体11が流過する管7を
有し渦動層の中に存する要素1.1aを持つ気体10を
加熱−まだは冷却するだめの管熱交換器を示す。
FIG. 4 shows a tube heat exchanger with tubes 7 through which a heating or cooling medium 11 flows and for heating--but not yet cooling--a gas 10 with an element 1.1a located in a fluidized bed.

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

第1図は球状の要素の斜視図、第2図はサドル形状の要
素の斜視図、第6図はユングストローム原理による熱交
換器を略示する斜視図、第4図は別の熱交換を略示する
斜視図である。 図面において、1と1aは要素、2は回転体、3はハウ
ジング、6は渦動層、7は堆積層、7′は管、8は低温
区域、9は高温区域、11は高温または低温の媒体を示
す。 図面の浄書(内容に変更なし) 第1図 第2図 手続補正書(方式) 昭和  年  月  日 特許庁長官殿 1、事件の表示 昭和57年 特許願 第 9788’/ロ1 、発明の名称 熱交換器を浄化する方法 3、補正をする者 事件との関係   特許出願人 住所 r手漕齋シ乙τでパ54yp7 )。 4、代理人 〒105  住所 東京都港区西新橋1丁目1番15号
物産ビル別館 電話(591) 0261459−
1 is a perspective view of a spherical element, FIG. 2 is a perspective view of a saddle-shaped element, FIG. 6 is a perspective view schematically showing a heat exchanger according to the Ljungström principle, and FIG. 4 is a perspective view of an alternative heat exchanger. FIG. 2 is a schematic perspective view; In the drawings, 1 and 1a are elements, 2 is a rotating body, 3 is a housing, 6 is a fluidized layer, 7 is a deposited layer, 7' is a tube, 8 is a low temperature zone, 9 is a high temperature zone, and 11 is a hot or cold medium. shows. Engraving of the drawings (no change in content) Figure 1 Figure 2 Procedural amendment (method) Date of 1939 To the Commissioner of the Japan Patent Office 1, Indication of the case 1988 Patent application No. 9788'/B1, Name of the invention Method for purifying the exchanger 3, relationship with the case of the person making the amendment Patent applicant address r rowsaishi ot τ de pa 54yp7). 4. Agent Address: Bussan Building Annex, 1-1-15 Nishi-Shinbashi, Minato-ku, Tokyo Phone: (591) 0261459-

Claims (1)

【特許請求の範囲】 1、 回転熱貯蔵物または回転気体通路を有し若しくは
その代りに高温または低温の気体が流入する室を有し、
気体を通す隔壁が気体流に横向きに配置される気体−気
体−熱交換器を浄化する方法において、熱貯蔵物それ自
身によっても形成できる少くとも2つの前記隔壁の間に
、上方から下方への気体の流入によって堆積層を形成し
下方から上方への気体の流入によって渦動層を形成する
ような多くの態別に動くことができる要素を収容し、か
かる渦動層を駆動の際に熱交換器の少くとも1つの区域
で保持し、渦動層を形成する前記要素の相互衝突および
相互摩擦によって沈積物を定常的に除去することを特徴
とする方法。 ゛2.半径向きに気体が流入するよう斤回転熱交換器に
利用される特許請求の範囲第1項に記載の方法。 6、要素が球、中空の球またはサド形状体として形成さ
れる特許請求の範囲第1項または第2項に記載の方法。 4、要素が潜熱貯蔵物または熱實量の高い材料を備えま
たはこれらで形成される特許請求の範囲第1項、第2m
、第3項のいずれか1項に記載の方法。 5、 気体が管、ひれ付き管またはその他の中空体を流
過する第2の媒体によって加熱または冷却されるような
熱交換器を浄化する方法において、気体空間の中に多く
の分離した要素を収容し、これによって熱交換器の駆動
の際に渦動層を形成しその衝突およびJI!擦によって
熱交換面を定常的に沈積物なしに保持することを特徴と
する方法。 6 要素が球、中空の球またはサド形状体として形成さ
れる特許請求の範囲第5項に記載の方法。 Z 要素が潜熱貯蔵物まだは熱答量の筒い材料を備えま
たはこれらで形成される特許請求の範囲第5項または第
6項に記載の方法。
[Claims] 1. Having a rotating heat storage device or a rotating gas passage, or having a chamber into which high-temperature or low-temperature gas flows instead,
In a method for purifying gas-gas heat exchangers in which the gas-permeable partitions are arranged transversely to the gas flow, between at least two said partitions, which may also be formed by the heat store itself, there is a It houses elements that can move in many ways, such as forming a deposited layer by the inflow of gas and forming a fluidized layer by the inflow of gas from below upwards, and when driving such a fluidized layer, the heat exchanger A method characterized in that deposits are constantly removed by mutual impact and mutual friction of said elements, which are retained in at least one zone and form a vortex layer.゛2. 2. The method of claim 1, wherein the method is applied to a rotary loaf heat exchanger with radial gas flow. 6. A method according to claim 1 or 2, wherein the element is formed as a sphere, a hollow sphere or a sadoid. 4. Claims 1 and 2m in which the element comprises or is formed of a latent heat storage material or a material with high thermal density.
, the method according to any one of paragraph 3. 5. In a method of purifying a heat exchanger in which the gas is heated or cooled by a second medium flowing through a tube, fin tube or other hollow body, a number of separate elements are placed in the gas space. This forms a vortex layer when the heat exchanger is driven, and its collision and JI! A method characterized in that the heat exchange surface is kept constantly free of deposits by rubbing. 6. A method according to claim 5, wherein the element is formed as a sphere, a hollow sphere or a sadoid. 7. A method as claimed in claim 5 or 6, in which the Z element comprises or is formed of a latent heat storage or heat response tubular material.
JP57097887A 1982-04-16 1982-06-09 Method of purifying heat exchanger Granted JPS58182099A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE19823213988 DE3213988A1 (en) 1982-04-16 1982-04-16 METHOD FOR CLEANING GAS FLOWED HEAT EXCHANGERS
DE3213988.8 1982-04-16

Publications (2)

Publication Number Publication Date
JPS58182099A true JPS58182099A (en) 1983-10-24
JPH033878B2 JPH033878B2 (en) 1991-01-21

Family

ID=6161034

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57097887A Granted JPS58182099A (en) 1982-04-16 1982-06-09 Method of purifying heat exchanger

Country Status (9)

Country Link
JP (1) JPS58182099A (en)
AT (1) AT376496B (en)
DE (1) DE3213988A1 (en)
FI (1) FI822107L (en)
FR (1) FR2525338B1 (en)
GB (1) GB2103329B (en)
NL (1) NL8202464A (en)
SE (1) SE8203533L (en)
ZA (1) ZA824548B (en)

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* Cited by examiner, † Cited by third party
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JP2011515205A (en) * 2008-02-27 2011-05-19 ウエストレイク ロングビュー コーポレイション Method for preventing or reducing agglomeration on a grid in a fluidized bed container

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* Cited by examiner, † Cited by third party
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CN100354593C (en) * 2003-06-13 2007-12-12 株洲工学院帅科机械清洗研究所 Horizontal column type heat exchanger exterior dirt three-phase fluidization in-situ cleaning process
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GB2103329A (en) 1983-02-16
FI822107A0 (en) 1982-06-11
GB2103329B (en) 1985-01-16
FR2525338A1 (en) 1983-10-21
FI822107L (en) 1983-10-17
JPH033878B2 (en) 1991-01-21
SE8203533L (en) 1983-10-17
ZA824548B (en) 1983-04-27
DE3213988A1 (en) 1983-10-20
NL8202464A (en) 1983-11-16
DE3213988C2 (en) 1988-03-03
AT376496B (en) 1984-11-26
ATA220182A (en) 1984-04-15
FR2525338B1 (en) 1988-01-15

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