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JPS6229089B2 - - Google Patents
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JPS6229089B2 - - Google Patents

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Publication number
JPS6229089B2
JPS6229089B2 JP54046050A JP4605079A JPS6229089B2 JP S6229089 B2 JPS6229089 B2 JP S6229089B2 JP 54046050 A JP54046050 A JP 54046050A JP 4605079 A JP4605079 A JP 4605079A JP S6229089 B2 JPS6229089 B2 JP S6229089B2
Authority
JP
Japan
Prior art keywords
catalyst unit
integrated catalyst
integrated
reactor
gas
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
JP54046050A
Other languages
Japanese (ja)
Other versions
JPS55139820A (en
Inventor
Hiroshi Masutomi
Minoru Izutsu
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 JP4605079A priority Critical patent/JPS55139820A/en
Priority to US06/076,784 priority patent/US4322386A/en
Publication of JPS55139820A publication Critical patent/JPS55139820A/en
Publication of JPS6229089B2 publication Critical patent/JPS6229089B2/ja
Granted legal-status Critical Current

Links

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  • Exhaust Gas Treatment By Means Of Catalyst (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Description

【発明の詳細な説明】 この発明は触媒反応装置の構造特に触媒ユニツ
トを組付けしたときの反応ガスの短絡流れを防止
する装置の構造に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to the structure of a catalytic reaction device, and more particularly to the structure of a device for preventing short-circuit flow of reaction gas when a catalyst unit is assembled.

近時火力発電所における排ガスの脱硝の装置と
して大型の触媒反応装置が使用されている。この
場合において触媒の除塵、交換、組付け等を容易
かつ効率よくすることが要望されている。これに
伴いガス流れに対する抵抗も少く脱硝効率よくか
つ前記の要望を満すものとして板状の触媒を間隙
をもち一つの箱型枠内に収容し触媒ユニツトと
し、反応ガスの通路内に取付けする構造をとつて
いる。第1図は板状触媒1aを1部取り出した状
態を斜視図で示す触媒ユニツト1である。触媒ユ
ニツトには箱状枠1b内に板状触媒1aがその面
をガス流れに平行して収容されている。なお本発
明における触媒ユニツトに収容する触媒は板状に
限定するものではなく他の筒状、粒状の触媒であ
つてもよい。発明者等は、大型の反応ガス処理装
置における組付けと交換を更に容易にするよう箱
型枠内に複数個の触媒ユニツトを収容し形成した
集積触媒ユニツトの構造を採用した。しかしこの
場合、触媒ユニツトの枠側面相互間の隙間及び触
媒ユニツトと反応器側壁間に生ずる通路に反応ガ
スが流れ、所謂ガスの短絡流れを生じ、かつ横梁
上面にはダストが堆積し、反応ガス処理の効率低
下と横梁から集積触媒ユニツト底面へとダストの
堆積架橋を生じガス通路の閉塞による故障の機会
をもつなどの問題が生ずることとなる。
Recently, large-sized catalytic reaction devices have been used as exhaust gas denitrification devices in thermal power plants. In this case, it is desired to make dust removal, replacement, assembly, etc. of the catalyst easy and efficient. Along with this, in order to achieve high denitration efficiency with low resistance to gas flow and to meet the above requirements, a plate-shaped catalyst is housed in a single box frame with gaps, forming a catalyst unit, and installed in the reaction gas passage. It has a structure. FIG. 1 shows a catalyst unit 1 in a perspective view with a portion of the plate-shaped catalyst 1a taken out. In the catalyst unit, a plate-shaped catalyst 1a is housed in a box-shaped frame 1b with its surface parallel to the gas flow. Note that the catalyst housed in the catalyst unit in the present invention is not limited to a plate-shaped catalyst, but may be other cylindrical or granular catalysts. The inventors have adopted an integrated catalyst unit structure in which a plurality of catalyst units are housed within a box frame to facilitate assembly and replacement in a large-scale reaction gas processing apparatus. However, in this case, the reaction gas flows into the gap between the side walls of the catalyst unit frame and the passage between the catalyst unit and the side wall of the reactor, resulting in a so-called gas short-circuit flow, and dust accumulates on the upper surface of the cross beam, causing the reaction gas to This results in problems such as a reduction in processing efficiency and the possibility of failure due to the accumulation of dust from the cross beams to the bottom surface of the integrated catalyst unit due to the blockage of the gas passages.

この発明はこのうな問題の発生を防止し反応ガ
ス漏洩短絡がなくかつ横梁上面にダストの堆積の
ない触媒反応装置の構造を提案することを目的と
する。
It is an object of the present invention to prevent the occurrence of such problems and to propose a structure of a catalytic reaction device that is free from reaction gas leakage and short circuits and free from dust accumulation on the upper surface of the cross beam.

要するにこの発明は集積触媒ユニツトの底面の
一辺には固定のシールプレートを設け、その組付
けにより集積触媒ユニツト相互間のガスの短絡流
れを防止し、容器壁面との間には壁面シールプレ
ートとブリツジプレートを設けてガスの短絡流れ
を防止し、横梁上面にはダスト堆積防止部材を設
けた構造をもつ触媒反応装置であることを特徴と
する。
In short, this invention provides a fixed seal plate on one side of the bottom surface of the integrated catalyst unit, and by assembling the fixed seal plate, short-circuit flow of gas between the integrated catalyst units is prevented. The catalytic reaction device is characterized by having a structure in which a joint plate is provided to prevent short-circuit flow of gas, and a dust accumulation prevention member is provided on the upper surface of the cross beam.

この発明にかかる装置の構造を以下図面により
説明する。触媒反応装置3には第3図に示すごと
く反応ガスの入口ダクト3aが上端に取付けされ
反応ガスは下方に流れ、出口ダクト3bより排出
される。触媒反応装置3内には集積触媒ユニツト
2が複数段、図面では二段に取付け配置される。
更にその上方の最上段には小型の集積触媒ユニツ
ト2′を載置してもよい。このような集積触媒ユ
ニツトは組付けしたときは無駄な空間を生ずるこ
とがない。しかし一つの集積触媒ユニツトの重量
は約600Kgもありその取扱いと組付けには労力と
安全上より特別の配慮を必要とする。
The structure of the device according to the present invention will be explained below with reference to the drawings. As shown in FIG. 3, the catalytic reaction device 3 has an inlet duct 3a for the reaction gas attached to the upper end thereof, and the reaction gas flows downward and is discharged from the outlet duct 3b. In the catalytic reaction device 3, integrated catalyst units 2 are installed in multiple stages, two stages in the drawing.
Furthermore, a small integrated catalyst unit 2' may be placed on the uppermost stage. Such an integrated catalyst unit does not occupy any wasted space when assembled. However, each integrated catalyst unit weighs approximately 600 kg, and its handling and assembly requires labor and special consideration for safety.

第4図は発明者等がさきに提案した組付け用台
車を使用して組付けをしている状態を模式に示す
ものである。集積触媒ユニツト2は組付け用台車
4に載置され、ウインチ5に接続するワイヤ6の
力により定位置に運ばれる。定位置での下しは油
圧装置4′によつてもよく、天井レール7に組付
けした手動ホイスト8によつてもよい。この場
合、先に述べたごとく集積触媒ユニツト相互間の
隙間のシールのため第2図第7図に示すごとくシ
ールプレート9を集積触媒ユニツトの底面の一辺
に取付けしておくときは組付けただけでシールが
され反応ガスの短絡流れは防止される。なお集積
触媒ユニツト2の枠2aの上端面側には補強を兼
ねた整流バー2bを複数個設けておく。
FIG. 4 schematically shows the assembly process using the assembly trolley proposed earlier by the inventors. The integrated catalyst unit 2 is placed on an assembly trolley 4 and is carried into position by the force of a wire 6 connected to a winch 5. Lowering at a fixed position may be done by a hydraulic device 4' or by a manual hoist 8 assembled to the ceiling rail 7. In this case, as mentioned above, if the seal plate 9 is attached to one side of the bottom surface of the integrated catalyst unit as shown in FIG. 2 and FIG. The reactor gas is sealed to prevent short-circuit flow of the reactant gas. Incidentally, a plurality of rectifying bars 2b are provided on the upper end surface side of the frame 2a of the integrated catalyst unit 2, which also serves as reinforcement.

第5図は第3図のD−D断面視図で、この図面
により集積触媒ユニツトの組付けに際し触媒反応
装置の柱10の存在のため壁面11との間に相当
の隙間fを生ずることが判る。このため集積触媒
ユニツト2の組付けに際し自動的にこの隙間f部
を反応ガスが流れることを防止する壁面シールプ
レート12を壁面11に取付ける必要がある。第
8図は集積触媒ユニツト2を壁面側に組付けした
状態を示す部分断面図である。ストツパ13は台
車の停止位置決めに使用するもので壁面11に取
付けされる。この場合前記隙間f部へのダストの
堆積防止とガス阻止をするため第9図に示すごと
く集積触媒ユニツト2の上端辺と壁11との面間
を架橋するブリツジプレート14を設ける。
FIG. 5 is a sectional view taken along the line DD in FIG. 3, and this drawing shows that when the integrated catalyst unit is assembled, it can be seen that due to the presence of the column 10 of the catalytic reaction device, a considerable gap f will be created between the pillar 10 and the wall surface 11. I understand. Therefore, when assembling the integrated catalyst unit 2, it is necessary to automatically attach a wall seal plate 12 to the wall surface 11 to prevent the reaction gas from flowing through the gap f. FIG. 8 is a partial sectional view showing the integrated catalyst unit 2 assembled on the wall side. The stopper 13 is used for determining the stop position of the cart and is attached to the wall surface 11. In this case, in order to prevent dust from accumulating in the gap f and to block gas, a bridge plate 14 is provided to bridge the surface between the upper end of the integrated catalyst unit 2 and the wall 11, as shown in FIG.

触媒反応装置3の横梁15で集積触媒ユニツト
2の底面に近く位置するのは、一般にその上面が
平坦なI型部材を使用するので、反応ガス中に含
まれるダストが集積触媒ユニツトの底面と架橋し
て、条件によつてはこれを根として増大する機会
をもつものである。従つて第10図に示すごとく
ダストの安息角より大なる底角をもつ斜面を形成
する折り曲げ部材即ち横断面山形状の長手部材を
I型部材の上面に取付けダスト堆積防止部材16
とするときは、ダストの堆積がなく装置の連続運
転に貢献するものである。
The cross beam 15 of the catalytic reaction device 3 located close to the bottom of the integrated catalyst unit 2 is generally an I-shaped member with a flat top surface, so that dust contained in the reaction gas can cross-link with the bottom of the integrated catalyst unit. Therefore, depending on the conditions, there is an opportunity to increase based on this. Therefore, as shown in FIG. 10, a folded member that forms a slope with a base angle larger than the angle of repose of the dust, that is, a longitudinal member having a mountain-shaped cross section, is attached to the upper surface of the I-shaped member to prevent dust accumulation 16.
This contributes to continuous operation of the device without dust accumulation.

この発明を実施することによりガスの短絡流れ
による漏れがなくガス中に含まれる有害成分除去
の効率は増大し、かつダストの堆積による架橋事
故を生ずることなく装置の連続運転が可能とな
り、しかも集積触媒ユニツトの交換は容易である
等種々の効果を奏するものである。
By implementing this invention, there will be no leakage due to gas short-circuit flow, the efficiency of removing harmful components contained in gas will be increased, and continuous operation of the device will be possible without causing bridging accidents due to dust accumulation. The catalyst unit can be easily replaced, and various other effects can be achieved.

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

第1図は触媒ユニツトの斜視図、第2図は集積
触媒ユニツトの斜視図、第3図はこの発明にかか
る触媒反応装置の部分切欠き側面図、第4図は台
車を使用する集積触媒ユニツト組付け作業を説明
する装置の部分側面図、第5図は第3図のD−D
断面図、第6図は第5図のE−E断面図、第7図
はシールプレート9と集積触媒ユニツトとの関係
を示す横断面図、第8図は第3図A部の詳細図、
第9図はB部の詳細図、第10図はC部の詳細図
である。 1……触媒ユニツト、2……集積触媒ユニツ
ト、2a……枠、3……触媒反応装置、4……台
車、5……ウインチ、7……天井レール、8……
手動ホイスト、9……シールプレート、10……
柱、11……壁面、12……壁面シールプレー
ト、13……ストツパ、14……ブリツジプレー
ト、15……横梁、16……ダスト堆積防止部
材。
FIG. 1 is a perspective view of a catalyst unit, FIG. 2 is a perspective view of an integrated catalyst unit, FIG. 3 is a partially cutaway side view of a catalytic reaction apparatus according to the present invention, and FIG. 4 is an integrated catalyst unit using a truck. A partial side view of the device to explain the assembly work, FIG. 5 is taken from D-D in FIG. 3.
6 is a sectional view taken along the line EE in FIG. 5, FIG. 7 is a cross-sectional view showing the relationship between the seal plate 9 and the integrated catalyst unit, and FIG. 8 is a detailed view of part A in FIG. 3.
FIG. 9 is a detailed view of section B, and FIG. 10 is a detailed view of section C. DESCRIPTION OF SYMBOLS 1...Catalyst unit, 2...Integrated catalyst unit, 2a...Frame, 3...Catalytic reaction device, 4...Dolly, 5...Winch, 7...Ceiling rail, 8...
Manual hoist, 9... Seal plate, 10...
Column, 11... Wall surface, 12... Wall seal plate, 13... Stopper, 14... Bridge plate, 15... Cross beam, 16... Dust accumulation prevention member.

Claims (1)

【特許請求の範囲】[Claims] 1 箱型枠内に触媒部材を収容する触媒ユニツト
の複数個を収容した集積触媒ユニツトの複数個を
そのガス通路内に組付けした反応器において、隣
接する集積触媒ユニツトの側面との間の隙間のシ
ールについては集積触媒ユニツト底面の一辺に設
けたシールプレートにより、集積触媒ユニツト側
面と反応器壁面との間の隙間のシールについては
反応器壁面より展出する壁面シールプレートによ
り、集積触媒ユニツト上端辺と壁面間を架橋する
ブリツジプレートにより夫々処理ガスの短絡流れ
を防止し、反応器の梁の上面にダスト堆積防止部
材を設けてダスト堆積を防止することを特徴とす
る触媒反応装置。
1. In a reactor in which a plurality of integrated catalyst units each containing a plurality of catalyst units containing catalyst members housed in a box frame are assembled in its gas passage, the gap between adjacent integrated catalyst units A seal plate provided on one side of the bottom of the integrated catalyst unit is used to seal the integrated catalyst unit, and a wall seal plate extending from the reactor wall is used to seal the gap between the side surface of the integrated catalyst unit and the reactor wall. A catalytic reaction apparatus characterized in that bridge plates that bridge sides and walls prevent short-circuit flows of processing gases, and dust accumulation prevention members are provided on the upper surfaces of beams of the reactor to prevent dust accumulation.
JP4605079A 1978-09-19 1979-04-17 Catalytic reaction apparatus Granted JPS55139820A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP4605079A JPS55139820A (en) 1979-04-17 1979-04-17 Catalytic reaction apparatus
US06/076,784 US4322386A (en) 1978-09-19 1979-09-18 Catalytic apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4605079A JPS55139820A (en) 1979-04-17 1979-04-17 Catalytic reaction apparatus

Publications (2)

Publication Number Publication Date
JPS55139820A JPS55139820A (en) 1980-11-01
JPS6229089B2 true JPS6229089B2 (en) 1987-06-24

Family

ID=12736187

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4605079A Granted JPS55139820A (en) 1978-09-19 1979-04-17 Catalytic reaction apparatus

Country Status (1)

Country Link
JP (1) JPS55139820A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5993642U (en) * 1982-12-06 1984-06-25 三菱重工業株式会社 Denitration reactor
JP2587422B2 (en) * 1987-05-11 1997-03-05 バブコツク日立株式会社 Internally heated vertical flow denitration reactor
JP4535416B2 (en) * 2001-02-20 2010-09-01 三菱重工環境・化学エンジニアリング株式会社 Exhaust gas treatment device having a honeycomb catalyst filled pallet

Also Published As

Publication number Publication date
JPS55139820A (en) 1980-11-01

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