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JPH033878B2 - - Google Patents
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JPH033878B2 - - Google Patents

Info

Publication number
JPH033878B2
JPH033878B2 JP57097887A JP9788782A JPH033878B2 JP H033878 B2 JPH033878 B2 JP H033878B2 JP 57097887 A JP57097887 A JP 57097887A JP 9788782 A JP9788782 A JP 9788782A JP H033878 B2 JPH033878 B2 JP H033878B2
Authority
JP
Japan
Prior art keywords
gas
heat exchanger
heat
heat storage
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.)
Expired - Lifetime
Application number
JP57097887A
Other languages
Japanese (ja)
Other versions
JPS58182099A (en
Inventor
Mihyaraku Sutanisuroo
Heruman Berunto
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.)
Apparatebau Rothemuehle Brandt and Kritzler GmbH
Original Assignee
Apparatebau Rothemuehle Brandt and Kritzler 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 Apparatebau Rothemuehle Brandt and Kritzler GmbH filed Critical Apparatebau Rothemuehle Brandt and Kritzler 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)
  • Cleaning In General (AREA)
  • Incineration Of Waste (AREA)
  • Pressure Welding/Diffusion-Bonding (AREA)

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ための熱
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種種の熱交換器系
が知られている。広く行き渉つているのは例えば
ユングストローム(Ljungstro¨m)原理に従う回
転熱交換器であつて、これは定置の形状板、管ま
たは薄板の形の蓄熱部材を備え、これが高温気体
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(例えば蒸気または
水)が流過し、その外面のまわりを気体が流れる
ような熱交換器もしばしば利用される。
Various heat exchanger systems are known for heating or cooling gases. Widespread are, for example, rotary heat exchangers according to the Ljungstro¨m principle, which comprise a heat storage element in the form of stationary shaped plates, tubes or sheets, which converts a hot gas stream into a cold gas stream. It moves cyclically into the flow, 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, around the outer surface of which a gas flows.

塵を多量に保持する気体の加熱または冷却に公
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り付
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 crust formation 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 gas. be.

このような熱交換器系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高め、さらに
気体と熱交換面の間の熱伝達を妨害する。
The crust formed on such heat exchanger systems increases the pressure drop in the heat exchanger and further impedes heat transfer between the gas and the heat exchange surfaces.

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。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
「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。
The known heat exchangers installed in such systems are therefore partially equipped with extremely complex purification devices. 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 2948201
Publication No.). 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(例えば米国特許第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
によつて圧力損失が著しく高くなり従つてこれが
周期的に交換されまたは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つて熱交換面を浄化する。
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。
It is also known (e.g. U.S. Pat. No. 793,648) to place a layer of deposits of discrete particles, such as spheres, in front of the actual heat exchange surface as dirt trapping means; Deposits in the bed cause a significant pressure drop and must therefore be replaced or cleaned periodically. In another system, described in US 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. to clean the heat exchange surface.
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、長い作動時間に渉つて熱伝
達および圧力損失が一定に保持できるようにして
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. be.

この目的はこの発明によれば、定常的にまたは
ときどき流動化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つて達成される。
This purpose, according to the invention, consists of 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 fluidized bed. This can be achieved by deploying them in dangerous parts of the country.

詳しく言えばこの発明によつて、回転する蓄熱
部材を有し、または回転する気体通路を有し、ま
たは交代的に高温気体もしくは低温気体を流入さ
せる室を有し、気体を透過させる隔壁が気体の流
れに横向きに取付けられた、気体と気体の間の熱
交換をする熱交換器において、蓄熱部材それ自身
としても形成できる少くとも2つの前記隔壁の間
に、気体を上方から下向きに流したときに堆積層
を形成しかつ気体を下方から上向きに流したとき
に流動化層を形成するような、多くの別別に動く
ことのできる要素を収容し、かかる流動化層を、
作動の際に熱交換器の少くとも一つの区域で定常
的に維持し、流動化層を形成する前記要素の相互
衝突および相互摩擦によつて、沈積物を定常的に
除去すること、を特徴とする熱交換器を浄化する
方法が提供される。これらの実施例として、要素
が球、中空の球またはサドル形状体として形成さ
れ、また要素が潜熱貯蔵材料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。
Specifically, according to the present invention, a partition wall that has a rotating heat storage member, a rotating gas passage, or a chamber into which high-temperature gas or low-temperature gas is introduced alternately, and that allows gas to pass therethrough is a gas-permeable partition wall. In a heat exchanger for heat exchange between gases, which is installed transversely to the flow of gas, the gas flows downward from above between at least two said partitions, which may also be formed as heat storage members themselves. It contains a number of separately movable elements, sometimes forming a deposited layer and forming a fluidized layer when gas is flowed upward from below, and such a fluidized layer is
characterized by constant removal of deposits in at least one zone of the heat exchanger during operation by means of mutual collision and mutual friction of said elements forming a fluidized bed; A method for cleaning a heat exchanger is provided. Examples of these include the elements being formed as spheres, hollow spheres or saddle shapes, and the elements comprising or being formed of latent heat storage materials 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、流動化層の中の要素は
衝突または摩擦によつ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
共同作用によつ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
明によければ向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つてねばり付きの
ないように保護され、回転体の回転(または別の
公知の熱交換器系の際の気体通路の回転または移
動)の際には要素は流動化層に変化しこれにおい
て衝突および摩擦によつて沈積物を自動的に除去
する。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流動化層にな
るように行なわれる。
In rotary heat exchangers, the elements in the fluidized bed achieve constant cleaning of the heat exchange surfaces by impingement 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, this inlet section side is free of sticky substances, since in rotary heat exchangers which operate in countercurrent and have a vertical axis, this element serves as dirt trapping means in the form of a deposit layer. During rotation of the rotor (or rotation or movement of the gas passages in other known heat exchanger systems) the element transforms into a fluidized bed in which it is protected by collisions and friction. Automatically removes deposits. In certain applications it is advantageous to provide such devices on both sides of the heat exchanger, ie on the cold inlet side and on the hot gas inlet side. In the case of a heat exchanger driven by direct current, the element is placed on the inlet side,
This flow is carried out in such a way that the elements become fluidized beds 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図は浄化のための球形状(中空のまたは中
空でない球)の要素1を示す。
FIG. 1 shows an element 1 of spherical shape (hollow or solid sphere) for purification.

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3図はユングストローム(Ljungstro¨m)原
理に従つて回転体2、ハウジング3および垂直軸
4を有してこの発明の方法に適した熱交換器を示
す。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
の流出側で流動化層6の中で浄化される。
FIG. 3 shows a heat exchanger according to the Ljungström principle having a rotating body 2, a housing 3 and a vertical shaft 4 and suitable for the method of the invention. The elements 1, 1a form a deposited 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
is purified in a fluidized bed 6 on the outlet side.

【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3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は流動化層、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。
1 is a perspective view of a spherical element, FIG. 2 is a perspective view of a saddle-shaped element, and FIG. 3 is a perspective view schematically showing a heat exchanger according to the Ljungström principle. 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 cold zone, 9 is a hot zone, and 11 is a hot or cold medium.

Claims (1)

【特許請求の範囲】 1 回転する蓄熱部材を有し、または回転する気
体通路を有し、または交代的に高温気体もしくは
低温気体を流入させる室を有し、気体を透過させ
る隔壁が気体の流れに横向きに取付けられた、気
体と気体の間の熱交換をする熱交換器において、
蓄熱部材それ自身としても形成できる少くとも2
つの前記隔壁の間に、気体を上方から下向きに流
したときに堆積層を形成しかつ気体を下方から上
向きに流したときに流動化層を形成するような、
多くの別別に動くことのできる要素を収容し、か
かる流動化層を、作動の際に熱交換器の少くとも
一つの区域で定常的に維持し、流動化層を形成す
る前記要素の相互衝突および相互摩擦によつて、
沈積物を定常的に除去すること、を特徴とする熱
交換器を浄化する方法。 2 半径向きに気体を流入させるような回転熱交
換器に使用される、特許請求の範囲第1項に記載
の方法。 3 前記要素が、球、中空の球、またはサドル形
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 前記要素に、潜熱を貯蔵する材料または熱容
量の高い材料が加えられ、または前記要素が、か
かる材料で作られる、特許請求の範囲第1項から
第3項のいずれか1項に記載の方法。
[Claims] 1. A device having a rotating heat storage member, or having a rotating gas passage, or having a chamber into which high-temperature gas or low-temperature gas is alternately introduced, and a partition wall that allows gas to pass through the gas flow. In a heat exchanger that exchanges heat between gases, it is installed horizontally on the
At least two heat storage elements which can also be formed as heat storage elements themselves.
Between the two partition walls, a deposited layer is formed when gas flows downward from above, and a fluidized layer is formed when gas flows upward from below.
accommodating a number of separately movable elements, maintaining such a fluidized bed constantly in at least one area of the heat exchanger during operation, and mutual collision of said elements forming a fluidized bed; and by mutual friction,
A method of purifying a heat exchanger, characterized by steadily removing deposits. 2. The method according to claim 1, which is used in a rotary heat exchanger that allows gas to flow in a radial direction. 3. A method according to claim 1 or 2, wherein the element is formed as a sphere, a hollow sphere or a saddle shape. 4. A method according to any one of claims 1 to 3, wherein a latent heat storage material or a high heat capacity material is added to the element or the element is made of such a 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 JPS58182099A (en) 1983-10-24
JPH033878B2 true 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) FI822107A7 (en)
FR (1) FR2525338B1 (en)
GB (1) GB2103329B (en)
NL (1) NL8202464A (en)
SE (1) SE8203533L (en)
ZA (1) ZA824548B (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100354593C (en) * 2003-06-13 2007-12-12 株洲工学院帅科机械清洗研究所 Horizontal tubular heat exchanger for fluidized on-line shell pass cleaning
CN1657860B (en) * 2004-02-16 2010-05-12 湖南工业大学 Vertical tube heat transfer equipment with fluidized on-line cleaning function outside the tube
US8129482B2 (en) 2008-02-27 2012-03-06 Westlake Longview Corporation Method of preventing or reducing polymer agglomeration on grid in fluidized-bed reactors
US8124697B2 (en) * 2008-02-27 2012-02-28 Westlake Longview Corporation Method of preventing or reducing agglomeration on grid in fluidized-bed vessel

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US1762320A (en) * 1927-09-17 1930-06-10 Int Comb Eng Corp Rotary air heater
DE621722C (en) * 1932-02-07 1935-11-12 Gustav Bojner Regenerator with housing rotatable about a horizontal axis
US2680008A (en) * 1950-12-28 1954-06-01 Air Preheater Pellet cells in rotary regenerative heat exchanger
GB708369A (en) * 1950-12-28 1954-05-05 Svenska Rotor Maskiner Ab Improvements in rotary regenerative air preheaters or like rotary drum apparatus
GB793648A (en) * 1954-11-12 1958-04-23 Svenska Rotor Maskiner Ab Improvements in heat exchangers of the rotary regenerative type
GB868368A (en) * 1958-10-10 1961-05-17 British Iron Steel Research Improvements in or relating to heat exchangers
DE1083058B (en) * 1959-07-10 1960-06-09 Schmidt Sche Heissdampf Process for keeping the heating surfaces of waste heat boilers clean and equipment for carrying out the process
US3627036A (en) * 1970-01-29 1971-12-14 William W Gilbert Heat exchange system
FR2083799A5 (en) * 1970-03-27 1971-12-17 Tokyo Shibaura Electric Co
US3814176A (en) * 1973-01-22 1974-06-04 R Seth Fixed-fluidized bed dry cooling tower
US3872918A (en) * 1974-02-21 1975-03-25 Stalker Corp Heat exchanger
US4300625A (en) * 1975-01-21 1981-11-17 Mikhailov Gerold M Preventing deposition on the inner surfaces of heat exchange apparatus
US3999602A (en) * 1975-10-21 1976-12-28 The United States Of America As Represented By The United States Energy Research And Development Administration Matrix heat exchanger including a liquid, thermal couplant
JPS5448349A (en) * 1977-09-26 1979-04-16 Japan Gasoline Method of treating dust attached to inner surface of rotary convection heattexchanger
DE2951279A1 (en) * 1979-12-20 1981-07-16 L. & C. Steinmüller GmbH, 5270 Gummersbach REGENERATIVE HEAT EXCHANGER
DE3035386C2 (en) * 1980-09-19 1985-08-29 Apparatebau Rothemühle Brandt + Kritzler GmbH, 5963 Wenden Use of heat-transferring elements designed as hollow spheres or as hollow polyhedra in a regenerative heat exchanger

Also Published As

Publication number Publication date
FR2525338B1 (en) 1988-01-15
GB2103329B (en) 1985-01-16
DE3213988A1 (en) 1983-10-20
FI822107L (en) 1983-10-17
SE8203533L (en) 1983-10-17
DE3213988C2 (en) 1988-03-03
ZA824548B (en) 1983-04-27
FI822107A0 (en) 1982-06-11
ATA220182A (en) 1984-04-15
GB2103329A (en) 1983-02-16
FI822107A7 (en) 1983-10-17
FR2525338A1 (en) 1983-10-21
NL8202464A (en) 1983-11-16
AT376496B (en) 1984-11-26
JPS58182099A (en) 1983-10-24

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