JPS601046B2 - Flue gas desulfurization equipment - Google Patents

Flue gas desulfurization equipment

Info

Publication number
JPS601046B2
JPS601046B2 JP55061224A JP6122480A JPS601046B2 JP S601046 B2 JPS601046 B2 JP S601046B2 JP 55061224 A JP55061224 A JP 55061224A JP 6122480 A JP6122480 A JP 6122480A JP S601046 B2 JPS601046 B2 JP S601046B2
Authority
JP
Japan
Prior art keywords
lining
mounting bracket
gas desulfurization
flue gas
brick
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
Application number
JP55061224A
Other languages
Japanese (ja)
Other versions
JPS56157784A (en
Inventor
敏信 島
静哉 前原
賢 梨木
正志 時広
光志 越智
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.)
Mitsubishi Power Ltd
Original Assignee
Babcock Hitachi KK
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 Babcock Hitachi KK filed Critical Babcock Hitachi KK
Priority to JP55061224A priority Critical patent/JPS601046B2/en
Publication of JPS56157784A publication Critical patent/JPS56157784A/en
Publication of JPS601046B2 publication Critical patent/JPS601046B2/en
Expired legal-status Critical Current

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  • Treating Waste Gases (AREA)
  • Separation Of Particles Using Liquids (AREA)
  • Furnace Housings, Linings, Walls, And Ceilings (AREA)

Description

【発明の詳細な説明】 本発明は排煙脱硫装置に関し、特に排煙脱硫装置の粉じ
ん塔等に内張りするラィニング構造に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a flue gas desulfurization system, and more particularly to a lining structure for lining a dust tower or the like of a flue gas desulfurization system.

従来、ダスト混合方式(スート混合方式ともいう)によ
る重油焚ボィラ排ガス脱硫装置では、石灰石、亜硫酸石
コゥ、および石コウが循環スラリ液に含まれること、な
らびに塩素イオン、フッ素イオンがスラリ中にほとんど
含まれないことから、除じん塔(重油焚の場合は冷却塔
と称する)のスロー卜部内壁は、第1図および第2図に
示すように、断面L字型の不連続な取付金具7A(SU
S314)にシリカ(Si02)系の煉瓦6Aを取付け
、さらにSi02系の目地材9Aで煉瓦間の空隙を充填
していた。
Conventionally, in heavy oil-fired boiler exhaust gas desulfurization equipment using the dust mixing method (also called the soot mixing method), limestone, sulfite stone, and gypsum are contained in the circulating slurry liquid, and chlorine ions and fluoride ions are mostly contained in the slurry. As shown in Figs. 1 and 2, the inner wall of the throw section of the dust removal tower (referred to as a cooling tower in the case of heavy oil burning) is equipped with a discontinuous mounting bracket 7A (with an L-shaped cross section). SU
Silica (Si02)-based bricks 6A were attached to S314), and the gaps between the bricks were further filled with Si02-based joint material 9A.

この場合、器壁11はメンブレンラィニング8で被覆さ
れているが、取付金具7AはSUS31&程度の金属で
も充分な耐食性があることから、ライニング8は施され
ていない。これに対し石炭焚ボィラや嫌結炉等に付設さ
れる排ガス脱硫装置は、重油焚ボィラ等と比較して取扱
うガス中のダストが多いことから、ダスト分離方式(別
称スート分離方式)が採用されることが多い。このため
、脱硫装置の除じん塔の循環液には多量のダスト、塩素
イオン、フッ素イオンが含まれ、前述の安価なSO2系
煉瓦および目地材は耐食性がないため使用することがで
きず、高価なSIC系またはA夕203系煉瓦、目地材
を採用する必要がある。また構造的にも取付金具をメソ
フレンラィニングで被覆する必要があるが、第1図に示
すような煉瓦毎に設けられた不連続の取付金具では、メ
ンプレンライニングの施工が困難で、充分な防食性を期
待することができなかった。第2図は、器壁11のラィ
ニング構造を示す断面図で、器偏11へのラィニングの
施工は、器壁11へ不連続な取付金具7Aを溶接によっ
て接合し、その後にメンブレンラィニング8で内張りす
るが、不連続な取付金具7Aが多数点在しているので、
メンブレンライニング8の施工を容易に行なうためには
、不連続な取付金具7Aの位置でくりぬいて第2図のよ
うにメンブレンライニング8の表面から不連続な取付金
具7Aを突出させ、しかる後に、目地材9A、煉瓦6A
を内張りしてし、た。ところが、メンブレンラィニング
8は不連続な取付金具7Aを突出させるために、メンブ
レンラィニング8を切り抜く(または切れ目を入れる)
ので、メンブレンラィニング8自体は取付金具7Aの位
置で不連続なものとなり、この不連続なメンブレンラィ
ニング8は循環液等の浸透によって取付金具7A、器壁
11への腐食へと発展する。一方、煉瓦6Aに耐食性に
富んだSIC系またはAそ203系煉瓦、目地材9Aを
用いても、煉瓦6A、目地材9Aは耐摩耗性はあるが、
これらの煉瓦6A自体はポーラスであるために塩素イオ
ン、フッ素イオンを含有した循環液が煉瓦6Aに浸透し
、この浸透した循環液によって取付金具7A、不連続な
メンブレンラィニング8の切れ目から器壁11を腐食す
る欠点があった。
In this case, the vessel wall 11 is covered with a membrane lining 8, but the lining 8 is not applied to the mounting fitting 7A since even a metal of SUS31& grade has sufficient corrosion resistance. On the other hand, exhaust gas desulfurization equipment attached to coal-fired boilers and desulphurizing furnaces handles more dust than heavy oil-fired boilers, so a dust separation method (also known as a soot separation method) is adopted. Often. For this reason, the circulating fluid in the dust removal tower of the desulfurization equipment contains a large amount of dust, chlorine ions, and fluorine ions, and the inexpensive SO2 bricks and joint materials mentioned above cannot be used because they do not have corrosion resistance, and are expensive. It is necessary to use SIC type or A-203 type bricks and joint material. In addition, from a structural standpoint, it is necessary to cover the mounting brackets with mesofrene lining, but with discontinuous mounting brackets provided for each brick as shown in Figure 1, it is difficult to install membrane lining, and there is insufficient It was not possible to expect good corrosion protection. FIG. 2 is a cross-sectional view showing the lining structure of the vessel wall 11. The construction of the lining on the vessel wall 11 involves joining the discontinuous mounting bracket 7A to the vessel wall 11 by welding, and then attaching the membrane lining 8. Although it is lined, there are many discontinuous mounting brackets 7A scattered around, so
In order to easily install the membrane lining 8, the discontinuous fittings 7A are hollowed out at the positions of the discontinuous fittings 7A, and the discontinuous fittings 7A are made to protrude from the surface of the membrane lining 8 as shown in FIG. Material 9A, brick 6A
I lined it with lining. However, in order to protrude the discontinuous mounting bracket 7A, the membrane lining 8 is cut out (or a cut is made).
Therefore, the membrane lining 8 itself becomes discontinuous at the position of the fitting 7A, and this discontinuous membrane lining 8 develops into corrosion of the fitting 7A and the vessel wall 11 due to penetration of circulating fluid, etc. On the other hand, even if the brick 6A is a highly corrosion-resistant SIC or A-203 brick, and the joint material 9A is used, the brick 6A and the joint material 9A are wear resistant, but
Since these bricks 6A themselves are porous, circulating fluid containing chlorine ions and fluoride ions penetrates into the bricks 6A, and this penetrating circulating fluid flows through the mounting bracket 7A and the discontinuous membrane lining 8 to the vessel wall. 11 had the disadvantage of corroding.

本発明の目的は、前述の問題点に鑑み、メンブレンライ
ニングの施工を容易にし、かつ連続したメンブレンラィ
ニングで内張りして脱硫装置の循環液等の浸透を防止す
ることにある。
SUMMARY OF THE INVENTION In view of the above-mentioned problems, an object of the present invention is to facilitate the construction of a membrane lining and to prevent the permeation of circulating fluid of a desulfurization device by lining with a continuous membrane lining.

本発明は、石炭焚排ガス脱硫装置の除じん塔スロー卜部
のように耐食性、耐摩耗性を必要とする個所に、長片状
の取付金具を設け、連続的なメンブレンライニングによ
って、該取付金具の周囲を内張りしたものである。
The present invention provides a long strip-shaped mounting bracket in a place that requires corrosion resistance and wear resistance, such as the throat section of a dust removal tower of a coal-fired flue gas desulfurization equipment, and uses a continuous membrane lining to secure the mounting bracket. The surrounding area is lined with lining.

以下、本発明を実施例によりさらに詳しく説明する。Hereinafter, the present invention will be explained in more detail with reference to Examples.

第3図は、本発明の煉瓦構造物が適用される排煙脱硫装
置の除じん塔と吸収塔を示す部分切欠図である。
FIG. 3 is a partially cutaway view showing a dust removal tower and an absorption tower of a flue gas desulfurization apparatus to which the brick structure of the present invention is applied.

排ガスは矢印に示すように、先ず除じん塔1に入り、ス
プレーノズル5から贋霧される循環液により冷却、除じ
んされ、スロー卜部4を通ってェリミネータ3でミスト
が除去された後、吸収塔2に入る。除じん塔のスロー卜
部4には、耐フッ酸性、耐摩耗性を考慮して防食メンブ
レンライニングとブリツクライニング(煉瓦ブロックと
目地材の組合せ)が施工される。第4図は、上記スロー
卜部4内壁の断面図であり、第5図は、第4図の取付金
具7の取付状態を示す斜視図である。
As shown by the arrow, the exhaust gas first enters the dust removal tower 1, where it is cooled and dust removed by the circulating liquid that is atomized from the spray nozzle 5, passes through the throw section 4, the mist is removed by the eliminator 3, and then is absorbed. Enter tower 2. The throw section 4 of the dust removal tower is provided with anticorrosion membrane lining and brick lining (a combination of brick blocks and joint material) in consideration of hydrofluoric acid resistance and abrasion resistance. FIG. 4 is a sectional view of the inner wall of the throw section 4, and FIG. 5 is a perspective view showing how the mounting bracket 7 of FIG. 4 is attached.

図において、容器壁11には断面L字状の連続的な最片
からなる敬付金具7が水平に、かつ上下多段に取付けら
れている。このように取付金具7は、第5図に示す如く
、連続した取付金具7であるために、取付金具7の外周
の長さは同一長さになり、このために、メンブレンラィ
ニング8は第4図に示す如く取付金具7の外周でひだ状
となる連続的なメンブレンライニング8となるが、その
長さはいずれの場所においても同一寸法になるために「
広幅のメンブレンライニング8を一様に、容易に施すこ
とができるのである。これによって紋付金具7の全面に
器壁11から連続してメンブレンラィニング8が施され
る。取付金具7に係合される煉瓦ブロック6は、高耐食
性のS℃またはA夕203系煉瓦であり、また目地材9
も同じくSICまたはA〆203系のものである。また
目地材9または煉瓦6の使用量を少なくするために、そ
れらの一部(この場合には取付金具7下部の自地材の一
部)に耐食性の固体10が挿入されている。固体10と
しては、その周囲の目地材、煉瓦よりも安価で、かつ耐
食性のある無機材料(煉瓦その他の耐火物を含む)が用
いられる。上記実施例によれば、連続した敬付金具7お
よび連続した広幅のメンフレンラィニング8を用いたこ
とにより、ラィニングに切れ目がなくなり、従って切れ
目からの腐食性の液、ガスの浸透による取付金具の腐食
がなくなり、かつラィニング施工を容易にし、その信頼
性を高めることができる。
In the figure, mounting brackets 7 made of continuous pieces having an L-shaped cross section are attached to a container wall 11 horizontally and in multiple stages above and below. As shown in FIG. 5, since the mounting brackets 7 are continuous, the lengths of the outer circumferences of the mounting brackets 7 are the same, and for this reason, the membrane lining 8 is As shown in Figure 4, a continuous membrane lining 8 becomes pleated around the outer periphery of the mounting bracket 7, but its length is the same at any location, so
A wide membrane lining 8 can be uniformly and easily applied. As a result, the membrane lining 8 is applied continuously from the vessel wall 11 to the entire surface of the crest fitting 7. The brick block 6 that is engaged with the mounting bracket 7 is made of highly corrosion-resistant S°C or A203 series brick, and the joint material 9
It is also of the SIC or A〆203 series. Furthermore, in order to reduce the amount of joint material 9 or brick 6 used, a corrosion-resistant solid material 10 is inserted into a part of them (in this case, a part of the original material under mounting bracket 7). As the solid 10, an inorganic material (including bricks and other refractories) that is cheaper than the surrounding joint material and bricks and has corrosion resistance is used. According to the above embodiment, by using the continuous mounting bracket 7 and the continuous wide membrane lining 8, there is no cut in the lining, and therefore corrosive liquid or gas can penetrate through the cut in the mounting bracket. This eliminates corrosion and makes lining construction easier and increases its reliability.

以上、本発明によれば、石炭焚ボィラの排ガス脱硫装置
の除じん塔のように耐フッ素酸性が問題となるブリック
ラィニング施工において、取付金具およびメンブレンラ
ィニングを従来の不連続型から連続型にしたことにより
、取付金具のラィニングに切れ目がなくなり、施工が容
易になり、かつラィニングの信頼性を著しく高めること
ができる。
As described above, according to the present invention, in brick lining construction where fluorine acid resistance is a problem, such as in dust removal towers of exhaust gas desulfurization equipment of coal-fired boilers, the mounting bracket and membrane lining can be changed from the conventional discontinuous type to the continuous type. By doing so, there is no cut in the lining of the mounting bracket, making construction easier and significantly increasing the reliability of the lining.

また、取付金具はメンプレンラィニングで周囲が被覆さ
れるために必ずしも耐食性材料でなくてもよく、安価に
製作でき、また異種材同志の溶接を行わないので、熔接
作業の手間も省ける。これらは、近年の石油不足からく
る石炭焚ボィラの増加に対し、その環境対策としての脱
硫装置の経済性に大きく寄与するものである。
In addition, since the mounting bracket is surrounded by a membrane lining, it does not necessarily have to be made of a corrosion-resistant material, and can be manufactured at low cost, and since dissimilar materials are not welded together, welding work can be saved. These greatly contribute to the economic efficiency of desulfurization equipment as an environmental measure against the increase in the number of coal-fired boilers due to oil shortages in recent years.

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

第1図は、排煙脱硫装置のスロー卜部における従来の煉
瓦取付金具の取付状態を示す切欠斜視図、第2図は、第
1図の排煙脱硫装置のスロー卜部内壁の断面図、第3図
は、ダスト分離方式による排煙脱硫装置のスロー卜部付
近の切欠図、第4図は、本発明の実施例を示すスロー卜
部のラィニング構造を示す断面図、第5図は、第4図の
実施例における取付金具の取付状態を示す切欠斜視図で
ある。 1…除じん塔、4・・・スロー卜部、6,6A…煉瓦ブ
ロック、7,7A・・・取付金具、8・・・メンブレン
ライニング、9,9A・・・目地材、10・・・挿入固
体、11・・・器壁。 第1図 第2図 第3図 第4図 第5図
Fig. 1 is a cutaway perspective view showing how a conventional brick mounting bracket is installed in the throw section of the flue gas desulfurization equipment; Fig. 2 is a sectional view of the inner wall of the throw slot of the flue gas desulfurization equipment in Fig. The figure is a cutaway view of the vicinity of the throw part of a flue gas desulfurization equipment using the dust separation method, FIG. 4 is a cross-sectional view showing the lining structure of the throw part showing an embodiment of the present invention, and FIG. FIG. 3 is a cutaway perspective view showing the mounting state of the mounting fittings in the embodiment. 1... Dust removal tower, 4... Throw section, 6, 6A... Brick block, 7, 7A... Mounting bracket, 8... Membrane lining, 9, 9A... Joint material, 10... Insertion Solid, 11... vessel wall. Figure 1 Figure 2 Figure 3 Figure 4 Figure 5

Claims (1)

【特許請求の範囲】[Claims] 1 脱硫装置の内壁に取付金具を介して煉瓦を取付け、
煉瓦間の空隙を目地材で充填したものにおいて、前記取
付金具を連続した長片で形成し、かつ、この取付金具の
周囲を連続したメンブレンライニングで内張したことを
特徴とする排煙脱硫装置。
1. Attach the brick to the inner wall of the desulfurization equipment via the mounting bracket,
A flue gas desulfurization device in which the gaps between the bricks are filled with a joint material, characterized in that the mounting bracket is formed of a continuous long piece, and the periphery of the mounting bracket is lined with a continuous membrane lining. .
JP55061224A 1980-05-10 1980-05-10 Flue gas desulfurization equipment Expired JPS601046B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP55061224A JPS601046B2 (en) 1980-05-10 1980-05-10 Flue gas desulfurization equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP55061224A JPS601046B2 (en) 1980-05-10 1980-05-10 Flue gas desulfurization equipment

Publications (2)

Publication Number Publication Date
JPS56157784A JPS56157784A (en) 1981-12-05
JPS601046B2 true JPS601046B2 (en) 1985-01-11

Family

ID=13165016

Family Applications (1)

Application Number Title Priority Date Filing Date
JP55061224A Expired JPS601046B2 (en) 1980-05-10 1980-05-10 Flue gas desulfurization equipment

Country Status (1)

Country Link
JP (1) JPS601046B2 (en)

Also Published As

Publication number Publication date
JPS56157784A (en) 1981-12-05

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