JPH0432290B2 - - Google Patents

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Publication number
JPH0432290B2
JPH0432290B2 JP56160404A JP16040481A JPH0432290B2 JP H0432290 B2 JPH0432290 B2 JP H0432290B2 JP 56160404 A JP56160404 A JP 56160404A JP 16040481 A JP16040481 A JP 16040481A JP H0432290 B2 JPH0432290 B2 JP H0432290B2
Authority
JP
Japan
Prior art keywords
heat exchange
wall
heat
resistant
perforated
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
JP56160404A
Other languages
Japanese (ja)
Other versions
JPS5792696A (en
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 filed Critical
Publication of JPS5792696A publication Critical patent/JPS5792696A/en
Publication of JPH0432290B2 publication Critical patent/JPH0432290B2/ja
Granted legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F21/00Constructions of heat-exchange apparatus characterised by the selection of particular materials
    • F28F21/04Constructions of heat-exchange apparatus characterised by the selection of particular materials of ceramic; of concrete; of natural stone
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G7/00Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
    • F23G7/06Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases
    • F23G7/061Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating
    • F23G7/065Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating using gaseous or liquid fuel
    • F23G7/066Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating using gaseous or liquid fuel preheating the waste gas by the heat of the combustion, e.g. recuperation type incinerator
    • F23G7/068Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating using gaseous or liquid fuel preheating the waste gas by the heat of the combustion, e.g. recuperation type incinerator using regenerative heat recovery means

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Ceramic Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Chimneys And Flues (AREA)
  • Incineration Of Waste (AREA)
  • Air Supply (AREA)

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、熱交換装置の耐熱構造に関し、特
に、蓄熱式熱交換装置に使用することができる耐
熱性ブロツク又はれんがで形成した内側保持壁
(熱交換素子を保持するための擁壁)に関する。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a heat-resistant structure for a heat exchange device, and in particular to an inner retaining wall (heat-resistant structure) formed of a heat-resistant block or brick that can be used in a regenerative heat exchange device. Retaining wall for holding replacement elements).

従来の技術及びその問題点 近年のエネルギーコストの高騰に伴い、熱を保
存して燃料コストを節減することができる装置を
求める要望が増大している。このような装置の1
例として米国特許第3895918号には、汚染防止の
ための蓄熱装置が開示されている。同特許の装置
では、多数の等角間隔に配置された熱交換部によ
つて囲繞された中央高温燃焼室又は焼却室が設け
られている。これらの熱交換部は、燃焼室と、工
業プロセスからの有毒な排出物(産業排出物)な
どのような汚染物の外部供給源に連通している。
産業排出物は、所定の作動中サイクル中上記熱交
換部のうちの所定の幾つかへ自動ダンパーによつ
て供給される。各熱交換部は、外側を有孔鋼壁
(外側保持壁)によつて保持され、内側(燃焼室
側)を別の有孔又はルーバー型金属壁(内側保持
壁)によつて保持された多数のセラミツク製(耐
熱)熱交換素子の堆積体から成る熱交換床を有し
ている。上記内外2つの保持壁の間の空間内へ多
数の熱交換素子が装入されるので、それらの熱交
換素子の総重量により大きな側方スラストが保持
壁に及ぼされる。
BACKGROUND OF THE INVENTION As energy costs have increased in recent years, there has been an increasing demand for devices that can conserve heat and reduce fuel costs. One of such devices
For example, US Pat. No. 3,895,918 discloses a heat storage device for pollution prevention. The device of that patent includes a central high temperature combustion chamber or incineration chamber surrounded by a number of equiangularly spaced heat exchange sections. These heat exchange sections communicate with the combustion chamber and an external source of pollutants, such as toxic emissions from industrial processes (industrial emissions).
Industrial effluent is fed by automatic dampers to a predetermined number of the heat exchange sections during a predetermined operating cycle. Each heat exchange section is held on the outside by a perforated steel wall (outer retaining wall) and on the inside (combustion chamber side) by another perforated or louvered metal wall (inner retaining wall). It has a heat exchange bed consisting of a stack of a large number of ceramic (high temperature) heat exchange elements. Since a large number of heat exchange elements are inserted into the space between the two inner and outer retaining walls, a large lateral thrust is exerted on the retaining wall due to the total weight of the heat exchange elements.

産業排出物は、処理サイクル中熱交換部のうち
の所定の1つ又はそれ以上の熱交換部を通して通
流せしめられると、該排出物の温度は、前のサイ
クルにおいて燃焼室内で浄化されたガスがその熱
交換部を通して排出されたときに得られて該熱交
換部の熱交換素子内に蓄えられている残留熱によ
つて高められる。このように入来(熱交換装置内
へ入つてきた)産業排出物は、所定の予備加熱さ
れた後、燃焼室内に入り、その有害成分は、燃焼
室内で酸化せしめられる。浄化された排出物は、
次いで燃焼室から他の熱交換部を通して排気回路
へ排出され周囲大気へ放出される。
When the industrial effluent is forced to flow through a given one or more of the heat exchange sections during a treatment cycle, the temperature of the effluent is equal to that of the gas purified in the combustion chamber in the previous cycle. is enhanced by the residual heat obtained when the heat is discharged through the heat exchange section and stored in the heat exchange elements of the heat exchange section. The incoming industrial waste (into the heat exchanger) enters the combustion chamber after a certain preheating, and its harmful components are oxidized in the combustion chamber. The purified waste is
It is then discharged from the combustion chamber through another heat exchanger into the exhaust circuit and into the surrounding atmosphere.

このような蓄熱構造体においては、セラミツク
製熱交換素子によつて及ぼされる側方スラストを
受止めるために、従来は多くの場合鋼製タイロツ
ドを前面保持壁(高温面)と後面保持壁(低温
面)との間に水平に張設することが必要であつ
た。これらのタイロツドは、又、熱による高温面
の曲りや撓みを防止する働きをもする。タイロツ
ドの緊張度を調節するためにタイロツドの端部に
は特別のベルビル(皿型)ワツシヤとナツトが用
いられる。又、補強の目的で前面保持壁の側縁に
は特別の水平ピンが打込まれる。焼却温度が約
649〜871℃(1200〜1600〓)に達する装置の場
合、高温面は、クリープ性の低い、例えば高ニツ
ケル−クロム含有鋼のような非常に高価な材料で
形成されるのが普通であつた。燃焼室を更に高
い、約871〜982℃(1600〜1800〓)領域の温度で
作動させる場合は、そのような高価な鋼を一層多
く使用しなければならない。
In such heat storage structures, in order to absorb the lateral thrust exerted by the ceramic heat exchange elements, steel tie rods were conventionally used in many cases between the front retaining wall (hot side) and the rear retaining wall (low temperature side). It was necessary to install it horizontally between the These tie rods also serve to prevent the hot surfaces from bending or deflecting due to heat. Special Belleville washers and nuts are used at the end of the tie rod to adjust the tension of the tie rod. Special horizontal pins are also driven into the side edges of the front retaining wall for reinforcement purposes. The incineration temperature is approx.
For equipment reaching temperatures of 649-871°C (1200-1600°), the hot surfaces were typically made of very expensive materials with low creep properties, such as high nickel-chromium steels. . If the combustion chamber is to be operated at higher temperatures, in the range of about 871-982°C (1600-1800°), even more of such expensive steel must be used.

更に、在来の熱交換装置の内側(前面)保持壁
は、産業排出物のある種の成分の腐敗作用又はそ
の他の化学的破壊作用を受けることが多く、金属
製の内側(前面)保持壁の寿命が短縮される。金
属製の前面保持壁は、又、実質的に熱交換性を有
していない。
Furthermore, the inner (front) retaining wall of conventional heat exchange equipment is often subject to the decomposition or other chemical destructive effects of certain components of industrial effluents, and the inner (front) retaining wall made of metal life span is shortened. The metal front retaining wall also has substantially no heat exchange properties.

熱交換特性を得るために従来からチエツカー盤
状の耐熱壁が使用されているが、それらは相当な
負荷に耐えることができるようには構成されてい
ない。米国特許第2125193号は、各耐熱ブロツク
の側縁に溝を形成して、隣接するブロツクの溝と
溝とが協同して軸線方向の開口を形成し、それら
の開口を通して酸素を流すようにする構成を開示
しているが、円形の燃焼室の囲壁に組込まれた、
軸線方向の貫通通路を有する多数の耐熱ブロツク
から成る水平のアーチ状(湾曲した)壁を教示し
ていない。
Although checkerboard-like refractory walls have traditionally been used to provide heat exchange properties, they are not constructed to withstand significant loads. U.S. Pat. No. 2,125,193 discloses forming grooves on the side edges of each refractory block such that the grooves of adjacent blocks cooperate to form axial openings through which oxygen flows. Although the configuration is disclosed, it is incorporated into the surrounding wall of the circular combustion chamber.
It does not teach horizontal arched (curved) walls consisting of multiple refractory blocks with axial passages through them.

発明が解決しようとする課題及び発明の目的 本発明は、蓄熱式熱交換装置の従来の熱交換素
子保持壁に随伴する上述した問題点を解決するこ
とを企図したものであり、その目的は、熱交換装
置に使用される在来の熱交換素子保持壁より耐熱
性が高く、従来の保持壁に比べて組立及び維持が
容易であり、化学的攻撃に対する耐性が高く、従
来の金属製の壁より熱交換作用が優れておりそれ
が組込まれる燃焼室囲壁(炉壁)全体に従来の金
属/コンクリート構造の壁より高い強度を付与す
ることができる耐熱壁を提供することである。
Problems to be Solved by the Invention and Objectives of the Invention The present invention is intended to solve the above-mentioned problems associated with the conventional heat exchange element retaining wall of a regenerative heat exchange device, and its purpose is to: More heat resistant than conventional heat exchange element retaining walls used in heat exchange equipment, easier to assemble and maintain than traditional retaining walls, and more resistant to chemical attack, compared to traditional metal walls It is an object of the present invention to provide a heat-resistant wall that has a more excellent heat exchange effect and can impart higher strength to the entire combustion chamber surrounding wall (furnace wall) in which it is incorporated than walls of conventional metal/concrete structures.

課題を解決するための手段 本発明は、蓄熱式熱交換装置の熱交換素子の堆
積体を保持するための内側保持壁として、円弧状
に湾曲した列の形に直接突き合わせて水平方向に
連結した複数の耐腐蝕性耐熱有孔ブロツクの複数
列を上下に積重することによつて構成された一体
構造の湾曲した熱交換素子保持壁を蓄熱式熱交換
装置の中央燃焼室の囲壁に組込むことによつて上
記課題を解決する。上記各有孔ブロツクの孔は、
内側保持壁の両側に位置する前記燃焼室と、対応
する1つの前記熱交換部とを連絡するガス導管を
構成し、有孔ブロツクの孔の断面寸法は、前記熱
交換素子が該熱交換部内を通る高圧ガスの圧力を
受けて該孔を通り抜けるのを防止するように定め
る。
Means for Solving the Problems The present invention provides an inner retaining wall for retaining a stack of heat exchange elements of a regenerative heat exchange device, in which a series of rows curved in an arc are directly abutted and connected in the horizontal direction. A curved heat exchange element retaining wall having a monolithic structure constructed by stacking a plurality of rows of a plurality of corrosion-resistant heat-resistant perforated blocks vertically is incorporated into the surrounding wall of a central combustion chamber of a regenerative heat exchange device. This solves the above problem. The holes in each of the above perforated blocks are as follows:
A gas conduit is configured to connect the combustion chambers located on both sides of the inner retaining wall and the corresponding one of the heat exchange sections, and the cross-sectional dimensions of the holes of the perforated block are such that the heat exchange elements are in the heat exchange section. The hole is designed to prevent high-pressure gas from passing through the hole.

本発明による上記湾曲した内側保持壁は、より
経済的に製造することができ、より高い燃焼温度
及び化学的攻撃に耐えることができ、熱交換素子
によつて及ぼされる側方スラスト圧に対抗するこ
とができる。
The curved inner retaining wall according to the invention can be manufactured more economically, can withstand higher combustion temperatures and chemical attacks, and counteracts the lateral thrust pressures exerted by the heat exchange elements. be able to.

実施例 第1図を参照すると、本発明に従つて構成した
蓄熱式熱交換装置(以下、単に「熱交換装置」又
は「装置」とも称する)10が示されている。装
置10は、複数の半径方向内方へ突入したバーナ
21を備えた円屋根型中央燃焼室(以下、単に
「燃焼室」又は「室」とも称する)11を有して
いる。燃焼室11は、断面円形であり、円形の燃
焼室囲壁(以下、単に「囲壁」とも称する)27
によつて囲われている。室11の周りに、即ち室
11の囲壁27の外側に複数の熱交換部12が円
周方向に間隔をおいて配設されている。各熱交換
部12は、金属板から成る有孔(透気性即ちガス
透過性)外側熱交換素子保持壁(以下、「有孔又
は透気性外側保持壁」又は「外側保持壁」又は
「保持壁」とも称する)23と、該保持壁23の
内側に配設された多数の耐熱性熱交換素子24を
有する熱交換床を備えている。産業排出物(以
下、単に「排出物」とも称する)は、導入ダクト
17を通して円環状の導入リング16へ送られ、
それに連結した供給ダクト9(第2図参照)を通
して熱交換部12内の外側保持壁23の外側の空
間20へ供給される。各熱交換部に接続されてい
る各供給ダクト9内にはサイクルの変更を行うた
めに入口弁14が配設されている。空間20へは
熱交換部12の頂部を覆う頂壁25を貫通して別
のダクト26が接続されている。ダクト26は、
弁26aを備えており、必要に応じて前掲米国特
許第3895918号に記載されているようにパージガ
スを導入するためのものである。各熱交換部12
の空間20には更に、出口弁19を有する排出ダ
クト8が接続されている。ダクト8は、円環状の
排出リング15に接続され、排出リング15は排
気ダクト18に連結されている。排気ダクト18
は、排気ブロツク及び煙突(図示せず)に接続す
ることができる。
Embodiment Referring to FIG. 1, there is shown a regenerative heat exchange device (hereinafter also simply referred to as a "heat exchange device" or "device") 10 constructed in accordance with the present invention. The device 10 has a dome-shaped central combustion chamber 11 (hereinafter also simply referred to as "combustion chamber" or "chamber") with a plurality of radially inwardly projecting burners 21 . The combustion chamber 11 has a circular cross section, and a circular combustion chamber surrounding wall (hereinafter also simply referred to as "surrounding wall") 27
surrounded by. A plurality of heat exchange sections 12 are arranged around the chamber 11, that is, on the outside of the surrounding wall 27 of the chamber 11, at intervals in the circumferential direction. Each heat exchange section 12 includes a perforated (air permeable, gas permeable) outer heat exchange element retaining wall (hereinafter referred to as "perforated or gas permeable outer retaining wall" or "outer retaining wall" or "retaining wall") made of a metal plate. ) 23 and a heat exchange bed having a large number of high-temperature heat exchange elements 24 arranged inside the retaining wall 23. Industrial waste (hereinafter also simply referred to as "exhaust material") is sent to an annular introduction ring 16 through an introduction duct 17,
It is supplied to the space 20 outside the outer retaining wall 23 in the heat exchange section 12 through a supply duct 9 (see FIG. 2) connected thereto. An inlet valve 14 is arranged in each supply duct 9 connected to each heat exchanger for changing the cycle. Another duct 26 is connected to the space 20 through a top wall 25 covering the top of the heat exchange section 12 . The duct 26 is
A valve 26a is provided for introducing purge gas as described in U.S. Pat. No. 3,895,918, supra, if necessary. Each heat exchange section 12
Furthermore, a discharge duct 8 having an outlet valve 19 is connected to the space 20 . The duct 8 is connected to an annular exhaust ring 15, and the exhaust ring 15 is connected to an exhaust duct 18. Exhaust duct 18
can be connected to an exhaust block and chimney (not shown).

第2及び3図に示されているように、耐熱性熱
交換素子24の堆積体は、その外側は上述した有
孔外側保持壁(金属板)23によつて保持されて
おり、燃焼室11に隣接した内側は、燃焼室囲壁
27の一部分を構成する後述する湾曲した有孔
(透気性)壁部分27aによつて保持される。従
つて、有孔(透気性)壁部分27aは、「有孔
(透気性)内側熱交換素子保持壁」又は「有孔
(透気性)内側保持壁」と称することもできる。
円形の囲壁27は、円弧状に湾曲した有孔(透気
性)壁部分27aと、同様に円弧状に湾曲した無
孔(不透気性)壁部分27bとを円周方向に交互
に配置し連結することによつて構成し、燃焼室1
1のための連続した円筒形ライニングとして形成
する。
As shown in FIGS. 2 and 3, the stack of refractory heat exchange elements 24 is held on the outside by the above-mentioned perforated outer retaining wall (metal plate) 23, and the combustion chamber 11 The inner side adjacent to the combustion chamber is held by a curved perforated (air permeable) wall portion 27a, which will be described later, and which constitutes a portion of the combustion chamber surrounding wall 27. Therefore, the perforated (air permeable) wall portion 27a may also be referred to as a "perforated (air permeable) inner heat exchange element retaining wall" or "a perforated (air permeable) inner retaining wall".
The circular surrounding wall 27 includes arcuately curved perforated (air permeable) wall portions 27a and arcuately curved nonporous (air impermeable) wall portions 27b which are alternately arranged and connected in the circumferential direction. The combustion chamber 1 is configured by
Formed as a continuous cylindrical lining for 1.

有孔(透気性)壁部分27aは、円弧状に湾曲
した列の形に突合わせ関係に連結した複数の耐腐
蝕性、耐熱性有孔ブロツク又はれんが28を複数
列上下に積重することによつて一体構造として構
成する。この湾曲した内側保持壁27aの凹面側
を燃焼室11に向けて配置し、内側保持壁の凸面
側を熱交換素子24の方に向け熱交換素子に接触
するように配置する。各列の有孔ブロツク28
は、他の列の有孔ブロツク28と互い違い関係に
なるように配置する。
The perforated (air-permeable) wall portion 27a is formed by stacking a plurality of corrosion-resistant and heat-resistant perforated blocks or bricks 28 in a plurality of vertically stacked rows connected in butt relation in a curved row. Therefore, it is constructed as an integral structure. The concave side of the curved inner retaining wall 27a is disposed toward the combustion chamber 11, and the convex side of the inner retaining wall is disposed toward the heat exchange element 24 so as to be in contact with the heat exchange element. Perforated blocks 28 in each row
are arranged in a staggered relationship with the perforated blocks 28 in other rows.

無孔(不透過性)壁部分27bは、複数の耐熱
性無孔れんが30を円周方向に連結し、かつ、上
下に積重することによつて構成する。有孔壁部分
27aは、それぞれの熱交換部12に対応させて
延設させ、無孔壁部分27bは、有孔壁部分27
aの間に介設する。各有孔壁部分27aの有孔ブ
ロツク28と、それに隣接する無孔壁部分27b
の無孔れんが30との間に遷移部即ち継手の役割
を果たす無孔れんが31,32を介設する。
The non-porous (impermeable) wall portion 27b is constructed by connecting a plurality of heat-resistant non-porous bricks 30 in the circumferential direction and stacking them one above the other. The perforated wall portions 27a extend corresponding to the respective heat exchange parts 12, and the non-perforated wall portions 27b extend from the perforated wall portions 27.
interposed between a. Perforated block 28 of each perforated wall portion 27a and adjacent non-perforated wall portion 27b
Non-porous bricks 31 and 32 are interposed between the non-porous bricks 30 and the non-porous bricks 31 and 32, which serve as transition parts or joints.

無孔れんが30,31,32の後側即ち外側に
は、例えば「モノブロツク」又はその他の市販さ
れている低密度又は高密度の高温断熱材(れんが
の形であつてもよい)から成る外壁34を設け
る。更に、無孔れんが30,31,32並びに各
熱交換部12を囲繞し、それらを支持するための
金属殻体35を設ける。
On the rear or outer side of the solid bricks 30, 31, 32 there is an outer wall 34 made of e.g. "monobloc" or other commercially available low density or high density high temperature insulation material (which may be in the form of bricks). will be established. Further, a metal shell 35 is provided to surround the non-porous bricks 30, 31, 32 and each heat exchange section 12 and support them.

第2〜4図に示されるように、各耐熱性有孔ブ
ロツク28は、産業排出物を処理するために燃焼
室11内へ通し、該排出物を放出するために燃焼
室から流出させるための多数の貫通した孔又は通
路28bを有する。図示の特定の実施例では、各
ブロツク28の多数の孔28bの断面積合計がそ
のブロツクの垂直断面積の1/3となるようになさ れている。この比率は、不必要に高い圧力降下を
生じさせることなく、燃焼室内で排出物を完全に
浄化させるのに十分な流量を保持することにより
この特定の設備の全体の熱効率を良好に維持する
ものであることが確認された。もちろん、ブロツ
ク28の孔又は通路28bの個数又は寸法は、そ
れぞれの用途に応じて定めることができる。一般
には、通路28bの合計容積は、そのブロツクの
容積の約30〜40%とする。孔又は通路28bは、
内側保持壁27aの両側に位置する燃焼室11
と、対応する1つの熱交換部12とを連絡するガ
ス導管を構成する。孔又は通路28bの断面寸法
は、熱交換素子24が熱交換部12内を通る高圧
ガスの圧力を受けて孔又は通路28bを通り抜け
るのを防止するように定める。
As shown in Figures 2-4, each refractory perforated block 28 is provided for passage of industrial emissions into the combustion chamber 11 for treatment and for exiting the combustion chamber for release of the emissions. It has a number of through holes or passages 28b. In the particular embodiment shown, the total cross-sectional area of the holes 28b in each block 28 is one third of the vertical cross-sectional area of that block. This ratio maintains good overall thermal efficiency for this particular installation by maintaining sufficient flow to fully purify emissions within the combustion chamber without creating unnecessarily high pressure drops. It was confirmed that Of course, the number and size of holes or passages 28b in block 28 can be determined depending on the particular application. Generally, the total volume of passageways 28b will be approximately 30-40% of the volume of the block. The hole or passage 28b is
Combustion chambers 11 located on both sides of the inner retaining wall 27a
A gas conduit is configured to connect the heat exchange section 12 and one corresponding heat exchange section 12. The cross-sectional dimensions of the holes or passages 28b are determined to prevent the heat exchange element 24 from passing through the holes or passages 28b under the pressure of the high pressure gas passing through the heat exchange section 12.

図示の実施例では、各ブロツク28の一側縁に
垂直突条28aを、そして他側縁に垂直溝28c
を形成し、各ブロツクの突条28aを隣接するブ
ロツクの溝28cに嵌合させることができるよう
にする。各ブロツク28は、図示の実施例では、
第3図に示されるような水平断面形状を有してお
り、各熱交換床13の内側にアーチ形の(円弧状
に湾曲した)有孔(透気性)内側保持壁27dを
組立てるのを容易にし、従つて、燃焼室囲壁27
全体のたが強度(円筒形に結合する強度)を強く
する。このように、各ブロツク28は、それらの
組立を容易にするとともに、熱交換素子24の堆
積体によつて及ぼされる側方スラストに対抗する
ように互いに嵌合する垂直部分(垂直突条28a
と垂直溝28c)を有する。ブロツク28は、各
熱交換部12の非平行な(U字形の)壁によつて
画定される開口の前面に延設させる。
In the illustrated embodiment, each block 28 has a vertical ridge 28a on one side edge and a vertical groove 28c on the other side edge.
, so that the protrusion 28a of each block can be fitted into the groove 28c of the adjacent block. Each block 28, in the illustrated embodiment, includes:
It has a horizontal cross-sectional shape as shown in FIG. 3, making it easy to assemble an arch-shaped (circularly curved) perforated (air permeable) inner retaining wall 27d inside each heat exchange bed 13. Therefore, the combustion chamber surrounding wall 27
Increase the overall hoop strength (strength of joining into the cylindrical shape). In this way, each block 28 has vertical portions (vertical ridges 28a
and a vertical groove 28c). The block 28 extends in front of the opening defined by the non-parallel (U-shaped) walls of each heat exchange section 12.

発明の効果 円弧状に湾曲した耐腐蝕性耐熱有孔ブロツク2
8から成る内側保持壁27aは、従来の平坦な金
属製の内側保持壁に比べて大きな機械的強度を発
揮するばかりでなく、相当な製造コストの節約を
も達成することが認められた。その組立は、単純
な石工作業と同様であり、従来の金属製内側保持
壁とは異り、特別な鋼も、特別なワツシヤも、特
別なタイロツドも、特別な側縁打込みピンも必要
とせず、その他の装置及び組立費用も必要としな
い。しかも、この壁構造は、非常に高価な特殊な
鋼に頼ることなく、より高い燃焼温度及びその有
害作用に耐えるので、蓄熱式熱交換装置の運転コ
ストをも節減することができる。従来の鋼壁は、
耐熱材料より化学的攻撃(腐蝕、酸化など)に弱
く、耐熱材料ほど装置の熱交換性を高めることが
できなかつた。
Effects of the invention Corrosion-resistant and heat-resistant perforated block 2 curved in an arc shape
It has been found that the inner retaining wall 27a consisting of 8 not only exhibits greater mechanical strength than conventional flat metal inner retaining walls, but also achieves considerable manufacturing cost savings. Its assembly is similar to simple masonry work and, unlike traditional metal inner retaining walls, does not require special steel, special washers, special tie rods, or special side drive pins. , no other equipment or assembly costs are required. Moreover, the operating costs of the regenerative heat exchanger can also be reduced, since this wall structure withstands higher combustion temperatures and their harmful effects without resorting to very expensive special steels. Traditional steel walls are
It is more susceptible to chemical attacks (corrosion, oxidation, etc.) than heat-resistant materials, and cannot improve the heat exchange performance of devices as much as heat-resistant materials.

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

第1図は、本発明の熱交換装置の平面図、第2
図は第1図の熱交換装置の燃焼室の内側からみた
壁構造の部分透視図、第3図は第2図の壁構造の
部分断面図、第4図は第3図の線4−4に沿つて
みた側面図である。 8……排出ダクト、9……供給ダクト、11…
…中央燃焼室、12……熱交換部、23……有孔
(透気性)外側保持壁、24……耐熱性熱交換素
子、27……囲壁、27a……有孔(透気性)壁
部分(有孔内側保持壁)、27b……無孔(不透
気性)壁部分、28……耐腐蝕性、耐熱性有孔
(透気性)ブロツク又はれんが、28a……垂直
突条、28b……孔又は通路、38c……垂直
溝、30……無孔(不透気性)れんが、31,3
2……無孔(不透気性)れんが(遷移部、継手)。
FIG. 1 is a plan view of the heat exchange device of the present invention, and FIG.
The figure is a partial perspective view of the wall structure seen from the inside of the combustion chamber of the heat exchanger in Figure 1, Figure 3 is a partial sectional view of the wall structure in Figure 2, and Figure 4 is line 4-4 in Figure 3. FIG. 8...Discharge duct, 9...Supply duct, 11...
... Central combustion chamber, 12 ... Heat exchange section, 23 ... Perforated (air permeable) outer retaining wall, 24 ... Heat resistant heat exchange element, 27 ... Surrounding wall, 27a ... Perforated (air permeable) wall portion (perforated inner retaining wall), 27b...non-porous (air impermeable) wall portion, 28...corrosion resistant, heat resistant perforated (air permeable) block or brick, 28a...vertical ridge, 28b... Hole or passage, 38c... Vertical groove, 30... Non-porous (impermeable) brick, 31,3
2...Non-porous (air-impermeable) brick (transition area, joint).

Claims (1)

【特許請求の範囲】 1 中央高温燃焼室11と、複数の隔置された耐
熱材30製の不透気性壁部分27bを備えた、該
燃焼室を囲繞する囲壁27とを有する熱交換装置
において、 (a) 前記囲壁27の外側に該囲壁と連接するよう
にして前記各不透気性壁部分27bの間の空間
のところに配設された熱交換部12と、該各熱
交換部内に複数個の熱交換素子24の堆積体を
保持するために設けられた内側保持壁27a及
び透気性外側保持壁23と、 (b) 前記各熱交換部12へ未浄化排出物を流入さ
せ、該熱交換部から浄化排出物を流出させるた
めに該各熱交換部に接続された手段とから成
り、 前記各熱交換部12の内側保持壁27aは、前
記囲壁27の前記隔置された不透気性壁部分27
bの間に透気性壁部分27aとして該囲壁に一体
的に組込まれており、該各内側保持壁27aは、
内面と前記熱交換部12に接しかつ該内面よりも
水平方向寸法の大きい外面とを有する耐腐蝕性耐
熱有孔ブロツク28を円弧状に湾曲した列の形に
並べて端面でつき合わせ互いに水平方向に連結し
た複数の該耐腐蝕性耐熱有孔ブロツク28の複数
列を上下に積重することによつて構成された一体
構造の湾曲した熱交換素子保持壁であり、該湾曲
した内側保持壁27aの凹面側を前記燃焼室11
に向けて配置し、該内側保持壁の凸面側を前記熱
交換素子24の方に向け熱交換素子に接触するよ
うに配置し、該各有孔ブロツク28の孔28b
は、該内側保持壁の両側に位置する前記燃焼室
と、対応する1つの前記熱交換部とを連絡するガ
ス導管を構成し、有孔ブロツク28の孔28bの
断面寸法は、前記熱交換素子が該熱交換部内を通
る高圧ガスの圧力を受けて該孔を通り抜けるのを
防止するように定められていることを特徴とする
熱交換装置。
[Scope of Claims] 1. A heat exchange device having a central high-temperature combustion chamber 11 and a surrounding wall 27 surrounding the combustion chamber, which includes a plurality of spaced apart air-impermeable wall portions 27b made of heat-resistant material 30. (a) a heat exchange part 12 disposed outside the surrounding wall 27 in a space between each of the air-impermeable wall parts 27b so as to be connected to the surrounding wall, and a plurality of heat exchange parts within each heat exchange part 12; an inner holding wall 27a and an air-permeable outer holding wall 23 provided to hold a stack of heat exchange elements 24; means connected to each heat exchange section for draining the purified effluent from the exchange section; the inner retaining wall 27a of each heat exchange section 12 comprises means connected to the spaced apart air impermeable wall 27 of the surrounding wall 27; wall part 27
b, each inner retaining wall 27a is integrally incorporated into the enclosure as an air-permeable wall portion 27a between
Corrosion-resistant and heat-resistant perforated blocks 28 having an inner surface and an outer surface that is in contact with the heat exchange section 12 and that is larger in horizontal dimension than the inner surface are arranged in a row curved in an arcuate shape and abutted at the end surfaces and are horizontally aligned with each other. It is a curved heat exchange element holding wall of an integral structure constructed by stacking a plurality of connected plural rows of the corrosion-resistant and heat-resistant perforated blocks 28 vertically, and the curved inner holding wall 27a is The concave side is the combustion chamber 11
The convex side of the inner retaining wall faces toward the heat exchange element 24 and is in contact with the heat exchange element, and the holes 28b of each perforated block 28
constitute a gas conduit that communicates the combustion chambers located on both sides of the inner retaining wall and the corresponding one of the heat exchange parts, and the cross-sectional dimension of the hole 28b of the perforated block 28 is equal to that of the heat exchange element. 1. A heat exchange device, characterized in that the heat exchanger is configured to prevent the high-pressure gas passing through the heat exchanger from passing through the hole under the pressure of the high-pressure gas passing through the heat exchange section.
JP16040481A 1980-10-14 1981-10-09 Heat exchanger Granted JPS5792696A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US19659080A 1980-10-14 1980-10-14

Publications (2)

Publication Number Publication Date
JPS5792696A JPS5792696A (en) 1982-06-09
JPH0432290B2 true JPH0432290B2 (en) 1992-05-28

Family

ID=22726007

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16040481A Granted JPS5792696A (en) 1980-10-14 1981-10-09 Heat exchanger

Country Status (7)

Country Link
JP (1) JPS5792696A (en)
CA (1) CA1148930A (en)
CH (1) CH655171A5 (en)
DE (1) DE3139749C2 (en)
FR (1) FR2492056B1 (en)
GB (1) GB2087526A (en)
MX (1) MX154067A (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3331340A1 (en) * 1983-08-31 1985-04-11 Buderus Ag, 6330 Wetzlar Central heating boiler
US4779548A (en) * 1987-08-11 1988-10-25 Regenerative Environmental Equipment Company, Inc. Incineration apparatus with improved wall configuration
FR2622685B1 (en) * 1987-10-29 1990-01-19 Vicarb Sa GAS / LIQUID HEAT EXCHANGER WITH CONDENSATION
US4802423A (en) * 1987-12-01 1989-02-07 Regenerative Environmental Equipment Co. Inc. Combustion apparatus with auxiliary burning unit for liquid fluids

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3895918A (en) * 1973-01-16 1975-07-22 James H Mueller High efficiency, thermal regeneration anti-pollution system

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1639138A (en) * 1925-10-30 1927-08-16 Liptak Michael Furnace wall
GB278070A (en) * 1926-06-28 1927-09-28 Levi Snyder Longenecker Improvements in or relating to refractory blocks particularly for use in metallurgical furnaces
US3549136A (en) * 1968-06-17 1970-12-22 Bethlehem Steel Corp Checkers suitable for forming a checker work in a hot blast stove and method of forming same
JPS4882767U (en) * 1971-12-30 1973-10-08
JPS4887345U (en) * 1972-01-28 1973-10-22
US4108733A (en) * 1977-04-25 1978-08-22 Koppers Company, Inc. High efficiency coke oven regenerator checker brick

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3895918A (en) * 1973-01-16 1975-07-22 James H Mueller High efficiency, thermal regeneration anti-pollution system

Also Published As

Publication number Publication date
DE3139749C2 (en) 1985-08-01
MX154067A (en) 1987-04-23
DE3139749A1 (en) 1982-08-12
FR2492056A1 (en) 1982-04-16
GB2087526A (en) 1982-05-26
JPS5792696A (en) 1982-06-09
CA1148930A (en) 1983-06-28
FR2492056B1 (en) 1985-12-20
CH655171A5 (en) 1986-03-27

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