JPS5824323A - Denitrating device - Google Patents

Denitrating device

Info

Publication number
JPS5824323A
JPS5824323A JP56122380A JP12238081A JPS5824323A JP S5824323 A JPS5824323 A JP S5824323A JP 56122380 A JP56122380 A JP 56122380A JP 12238081 A JP12238081 A JP 12238081A JP S5824323 A JPS5824323 A JP S5824323A
Authority
JP
Japan
Prior art keywords
catalyst
outer frame
blocks
catalyst block
block
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.)
Pending
Application number
JP56122380A
Other languages
Japanese (ja)
Inventor
Atsushi Furukawa
淳 古川
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 JP56122380A priority Critical patent/JPS5824323A/en
Publication of JPS5824323A publication Critical patent/JPS5824323A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/008Details of the reactor or of the particulate material; Processes to increase or to retard the rate of reaction
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24Stationary reactors without moving elements inside
    • B01J19/248Reactors comprising multiple separated flow channels
    • B01J19/2485Monolithic reactors
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/32Packing elements in the form of grids or built-up elements for forming a unit or module inside the apparatus for mass or heat transfer
    • B01J19/325Attachment devices therefor, e.g. hooks, consoles, brackets
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00796Details of the reactor or of the particulate material
    • B01J2208/00805Details of the particulate material
    • B01J2208/00814Details of the particulate material the particulate material being provides in prefilled containers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/322Basic shape of the elements
    • B01J2219/32203Sheets
    • B01J2219/32275Mounting or joining of the blocks or sheets within the column or vessel
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/322Basic shape of the elements
    • B01J2219/32293Cubes or cubic blocks
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/322Basic shape of the elements
    • B01J2219/32296Honeycombs
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/324Composition or microstructure of the elements
    • B01J2219/32466Composition or microstructure of the elements comprising catalytically active material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/328Manufacturing aspects

Abstract

PURPOSE:To simplify the shape of the outside frame for catalyst blocks and to assemble the blocks easily by providing means of regulating the movement among the catalyst blocks to members forming the outside frame of the catalyst block. CONSTITUTION:In a denitrating device provided with a denitration reactor wherein gases flow horizontally, the outside frame 3 of catalyst blocks 2 to be arranged in a denitration reactor 7 is formed roughly to a rectangular body by sticking plural pieces of angle steels and plural sheets of pressed corrugated plates 3C by welding, etc., wherein the plates 3C on the top side are alternately projected and recessed, and the plates on the bottom side are formed reverse from the plates on the top side. Since means for regulating the movement are provided to the members forming the outside frame of the blocks in the above- mentioned way, the shape of the outside frame is simplified and the labor and time for working are economized.

Description

【発明の詳細な説明】 本発明はガス水平流脱硝反応器を備えた脱硝装置に係〕
、特に脱硝反応器内に配列充填される触媒ブロックの外
枠構造に関するものである。
[Detailed description of the invention] The present invention relates to a denitrification device equipped with a gas horizontal flow denitrification reactor]
In particular, it relates to the outer frame structure of catalyst blocks arranged and packed in a denitrification reactor.

第1図は、パラレル触媒の最小単位である触媒風ニット
1の外観を示すものである。第2図は触媒ブロック2t
−示すもので、触媒ブロック2は外枠3と、内部仕切板
4と、外枠3内において仕切板4によって形成された各
区画部にそれぞれ組込まれた触媒ユニット1とKより構
成されている。
FIG. 1 shows the appearance of a catalyst-style knit 1, which is the smallest unit of a parallel catalyst. Figure 2 shows the catalyst block 2t.
- As shown, the catalyst block 2 is composed of an outer frame 3, an inner partition plate 4, and catalyst units 1 and K respectively incorporated in each compartment formed by the partition plate 4 in the outer frame 3. .

また外枠3を形成する部材は平板31および山形鋼3b
であシ、これらの部材を溶接などKよp固着することに
よって外枠3の外観がはソ長方体に形成されている。外
枠3の上置側から後に詳述するストッパ5が垂直方向に
突出され、外枠3の下面には第3図に示すようにストッ
パ5がはまり込む隙間を持った2板の平板よシなるスト
ツノ<6が設けられている。
Also, the members forming the outer frame 3 are the flat plate 31 and the angle iron 3b.
By fixing these members together by welding or the like, the outer frame 3 has a rectangular parallelepiped appearance. A stopper 5, which will be described in detail later, protrudes from the upper side of the outer frame 3 in the vertical direction, and the lower surface of the outer frame 3 has two flat plates with a gap into which the stopper 5 fits, as shown in FIG. A distance <6 is provided.

第4図はガス水平流脱硝反応器7f示すもので1脱硝装
置では現場における触媒充填の作業性を良くするため、
触媒ブロック単位で脱硝反応器7内部に触媒管充填する
。す表わち、複数個の触媒ユニット1″を組込んだ触媒
ブロック2が脱硝反応器7内において垂直方向およびそ
れと直交する各水平方向に配列充填される。ガスは各図
において矢印で示すように、ひとつの水平方向に流され
、脱硝反応a+7内において各触媒ユニット1の働IK
よシガスの脱硝反応が行なわれる。第4図に示すように
多数の触媒ブロック2′t−配列充填した脱硝反応器7
では地震などによって触媒ブロック2間の位置が移動し
、触媒ブロック2が脱硝反応器7よシ外部へくずれ落ち
てしまう危険性がある。特にガスの流れる水平方向は解
放されているため、触媒ブロック2.2間の移動を規制
する必要があるO このため、従来では前述のように触媒ブロック2の外枠
上面側および下面側にストッパ5,6t−設け、触媒ブ
ロック2f:脱硝反応器7内に装填するとき、予め各触
媒ブロック2の外枠3上面側のストッパ5をその上段に
積み重ねる触媒ブロック2の外枠3下里のストッパ6の
隙間に嵌り込ませて、触媒ブロック2.2間の移動を阻
止している。
Figure 4 shows the gas horizontal flow denitrification reactor 7f.In order to improve the workability of catalyst filling in the field with one denitrification device,
Catalyst tubes are filled inside the denitrification reactor 7 in units of catalyst blocks. That is, a catalyst block 2 incorporating a plurality of catalyst units 1'' is arranged and filled in the denitrification reactor 7 in the vertical direction and in each horizontal direction orthogonal thereto.The gas flows as shown by the arrows in each figure. , the flow is carried out in one horizontal direction, and the function IK of each catalyst unit 1 in the denitrification reaction a+7 is
The denitrification reaction of Yoshigas is carried out. As shown in FIG. 4, a denitration reactor 7 packed with a large number of catalyst blocks 2't-arrayed.
In this case, there is a risk that the position between the catalyst blocks 2 may shift due to an earthquake or the like, and the catalyst blocks 2 may collapse from the denitrification reactor 7 to the outside. In particular, since the horizontal direction in which the gas flows is open, it is necessary to restrict the movement between the catalyst blocks 2 and 2. For this reason, in the past, stoppers were installed on the upper and lower sides of the outer frame of the catalyst block 2, as described above. Catalyst block 2f: A stopper at the bottom of the outer frame 3 of each catalyst block 2, in which the stopper 5 on the upper surface side of the outer frame 3 of each catalyst block 2 is stacked on top of it in advance when loading into the denitrification reactor 7. 6 to prevent movement between the catalyst blocks 2 and 2.

第5図は、このストッパ5とストツノ<6の保合状態を
詳細に示す図である0下段の触媒ブロック21の仕切板
41に固着され外枠31上面側より垂直方向に突出した
ストツノ<51は上段の触媒ブロック22の外枠32下
面に固着された2枚のストッパー61m 、61b O
91間8にさし込まれている。また第2図および第3図
に示すように、このようなストッパの保合が上段、下段
の各触媒プルツク間の4個所で行われるOしたがって、
第5図ではガスの流れる水平方向の上下触媒ブロック間
の移動は下段の触媒ブロック21のストツノ々51と上
段の触媒ブロック22の外枠32が干渉することにより
規制され、ガスの流れ方向と直交する水平方向の上下触
媒ブロック間の移動は下段の触媒ブロック21のストン
/(21と上段の触媒  、。
FIG. 5 is a diagram showing in detail the engagement state of the stopper 5 and the stop horn <6. are two stoppers 61m and 61b O fixed to the lower surface of the outer frame 32 of the upper catalyst block 22.
It is inserted between 91 and 8. Furthermore, as shown in FIGS. 2 and 3, such stoppers are secured at four locations between the upper and lower catalyst pulls.
In FIG. 5, the movement between the upper and lower catalyst blocks in the horizontal direction of gas flow is restricted by interference between the stop horns 51 of the lower catalyst block 21 and the outer frame 32 of the upper catalyst block 22, and is perpendicular to the gas flow direction. The movement between the upper and lower catalyst blocks in the horizontal direction is as follows: the lower catalyst block 21 and the upper catalyst block.

ブロック22のストツノ<61が干渉することによって
規制される。このようにして触媒ブロック2を積み重ね
脱硝反応器内に配列充填することによって触媒ブロック
間の移動が防止されるようになっている。
This is regulated by the interference of the block 22's stroke angle <61. By stacking the catalyst blocks 2 and packing them in an array in the denitrification reactor in this way, movement between the catalyst blocks is prevented.

しかしながら、脱硝装置における脱硝反応器内に配列充
填される触媒ブロック2の数は実際には数百側もある。
However, in reality, the number of catalyst blocks 2 arranged and packed in the denitrification reactor of the denitrification device is on the order of several hundred.

各触媒ブロック2の所定位置にストッパ5.6vc取付
ける必要があるから、ストッパの材料費および加工費が
多くなシ、またストッパの位置合せと溶接作業には多大
の手間と時間がかかるため非常に不経済である。
Since it is necessary to install a stopper 5.6vc at a predetermined position on each catalyst block 2, the material and processing costs for the stopper are high, and the positioning and welding of the stopper requires a great deal of effort and time, making it extremely expensive. It is uneconomical.

本発明は上記に鑑み正なされたもので、ストッパーf触
媒ブロックに設けることなく、各触媒ブロック間の移動
を規制できる触媒ブロックを提供することを目的とする
The present invention has been made in view of the above, and an object of the present invention is to provide a catalyst block that can restrict movement between each catalyst block without providing a stopper f in the catalyst block.

この目的を達成するため本発明は、触媒ブロックの外枠
を形成する部材自身に各触媒ブロック間の移動を規制す
る手段を持たせたこと全特徴とするO 以下第6図反型第8図によシ、本発明の一実施例を説明
する。各図において第1図反型第5図と同符号のものは
同一のものもしくは均等物を示す。
In order to achieve this object, the present invention is characterized in that the member forming the outer frame of the catalyst block itself has a means for regulating movement between each catalyst block. Now, one embodiment of the present invention will be described. In each figure, the same reference numerals as those in FIG. 1 and FIG. 5 indicate the same or equivalent items.

第6図を参照するに1触媒ブロツク2の外枠3は複数枚
の山形鋼31と複数枚のプレス加工した波形状板5cL
vt:溶接などによって固着することによシ外観はy長
方体に形成されている。外枠3の上面にはガス流れ水平
方向に直交する長手方向を有する波形状板3cがはソ等
しい間隔で三枚設けられ、ガス流れ方向に対して前側と
後側の二枚の波形状板3aがその凸部會外枠3の上面よ
り突出するように取付けられ、また中間の波形状板3c
はその凹部が外枠3の上面に開口するように取付けられ
ている。外枠30下面には、図示しないが、外枠3の上
面と同様に三枚の波形状板3cが設けられ、ガス流れ方
向に対して前側と後側の二枚の波形状板3cがその凹部
を下面に開口し、中間の波形状板3cがその凸部を下面
よシ突出するように取付けられている。
Referring to FIG. 6, the outer frame 3 of one catalyst block 2 consists of a plurality of angle irons 31 and a plurality of pressed corrugated plates 5cL.
vt: By being fixed by welding or the like, the external appearance is formed into a y rectangular shape. On the upper surface of the outer frame 3, three corrugated plates 3c having a longitudinal direction perpendicular to the horizontal gas flow direction are provided at equal intervals, and two corrugated plates are provided on the front side and the rear side with respect to the gas flow direction. 3a is attached so as to protrude from the upper surface of the convex outer frame 3, and the intermediate corrugated plate 3c
is attached so that its concave portion opens on the upper surface of the outer frame 3. Although not shown, three corrugated plates 3c are provided on the lower surface of the outer frame 30 in the same way as on the upper surface of the outer frame 3, and the two corrugated plates 3c on the front and rear sides with respect to the gas flow direction are provided on the lower surface of the outer frame 30. The concave portion is opened on the lower surface, and the intermediate corrugated plate 3c is attached so that the convex portion thereof protrudes from the lower surface.

第7図は、上記のように外枠3を形成する各触媒ブロッ
ク2t−脱硝反応器7内に配列充填した状態の一部と所
間で示すもので、第8図にその一部の詳細を示す評段の
触媒ブロック2の外枠31上面に設けられた前後側の波
形状板31cの凸部が上段の触媒ブロック2の外枠32
下面に設けられた前後側の波形状板32cの凹部に嵌シ
込んでいる。また、下段の触媒ブロック2の外枠31上
面に設けられた中間の波形状板(図示せず)の凹部に上
段の触媒ブロック2の外枠32下面に設けられた中間の
波形状板(図示せず)の凸部かは−1)込んでいる。し
たがって、この上段の触媒ブロック2と下段の触媒ブロ
ック2は各凹凸部の係合によってガス流れ水平方向の移
動が規制されている。
FIG. 7 shows a part of each catalyst block 2t forming the outer frame 3 as described above, arranged and packed in the denitrification reactor 7, and FIG. 8 shows the details of a part. The outer frame 32 of the catalyst block 2 in the upper stage has the convex portions of the front and rear corrugated plates 31c provided on the upper surface of the outer frame 31 of the catalyst block 2 in the rating stage.
It is fitted into a recess in the front and rear corrugated plates 32c provided on the lower surface. Further, an intermediate corrugated plate (not shown) provided on the lower surface of the outer frame 32 of the upper catalyst block 2 is inserted into a recessed portion of an intermediate corrugated plate (not shown) provided on the upper surface of the outer frame 31 of the lower catalyst block 2. The convex part (not shown) is -1) crowded. Therefore, the movement of the gas flow in the horizontal direction of the upper catalyst block 2 and the lower catalyst block 2 is restricted by the engagement of the respective uneven portions.

またガス流れ方向と直交する水平方向の上下触媒ブロッ
ク2.2間の移動は上段触媒ブロック2の外枠32下面
および下段融媒ブロック2の外枠31上面の波形状板3
1.,32cの凸部と下段触媒ブロック2の外枠31の
山形鋼31bおよび上段触媒ブロック2の外枠32の山
形鋼32bとが干渉することによって規制されている。
In addition, movement between the upper and lower catalyst blocks 2.2 in the horizontal direction perpendicular to the gas flow direction is caused by the lower surface of the outer frame 32 of the upper catalyst block 2 and the corrugated plate 3 on the upper surface of the outer frame 31 of the lower melting medium block 2.
1. , 32c interfere with the angle iron 31b of the outer frame 31 of the lower catalyst block 2 and the angle iron 32b of the outer frame 32 of the upper catalyst block 2.

上記本発明の実施例によれば次の効果を奏するものであ
る。
According to the embodiment of the present invention described above, the following effects are achieved.

(1)、プレス加工によって簡単に凹凸部を形成した波
形状板を触媒ブロック外枠を形成する部材として用いる
こ′とによって、脱硝反応器内に配列充填された各触媒
ブロック間の移動t−規制することができるので、新た
表ストッパーを取付ける必要がなく触媒ブロックの構造
が簡単になる。
(1) By using a corrugated plate with concave and convex portions easily formed by press working as a member forming the outer frame of the catalyst block, movement between each catalyst block arranged and packed in the denitrification reactor is reduced. Since it can be controlled, there is no need to install a new front stopper and the structure of the catalyst block is simplified.

(2)、従来に比べて材料費、加工費が低減できるとと
もにストッパーを取付けるための位置合せ、連接作業に
必1’+を手間と時間管全く必要としないの−で極めて
経済的である。
(2) Material costs and processing costs can be reduced compared to the conventional method, and the positioning and connecting work for attaching the stopper does not require any extra effort or time, making it extremely economical.

(3)、外枠を形成する部材として所間が波形の板を用
いたので外枠の座屈強度が増し、軽量の部材管採用でき
るのでさらに経済性が向上する。
(3) Since a corrugated plate is used as a member forming the outer frame, the buckling strength of the outer frame is increased, and since a lightweight member tube can be used, economical efficiency is further improved.

なお、上記実施例では各触媒ブロックの外枠上面および
下面のそれぞれに三枚の波形状板を設けるとともに、そ
の下面において前後側の二枚の波形状板がその凹部を下
面に開口し、中間の波形状板がその凸面を下面より突出
するように取付けたが、下面の波形状板が三枚とも凹部
tその下面に開口して、上下段の各触媒プレツク関が前
後二個所で凹凸部上係合するようにしても良い。
In addition, in the above embodiment, three corrugated plates are provided on the upper and lower surfaces of the outer frame of each catalyst block, and the two corrugated plates on the front and rear sides have their recesses opened to the lower surface, and the intermediate The corrugated plates were installed so that their convex surfaces protruded from the lower surface, but all three of the corrugated plates on the lower surface were opened at the bottom of the concave portions, and each of the upper and lower catalyst plectanes had concave and convex portions at two locations, front and rear. It is also possible to engage the upper part.

また外枠上面の波形状板がすべて凸部を上面より突出し
、外枠下面の波形状板がすべて凹部を下wK開口して三
個所で凹凸部を係合しても良い。
Alternatively, all of the corrugated plates on the upper surface of the outer frame may have convex portions protruding from the upper surface, and all of the corrugated plates on the lower surface of the outer frame may have concave portions opened downward wK, and the convex and convex portions may be engaged at three locations.

外枠の上面と下面の凹凸を逆にしても良い。さらに上下
段の各触媒ブロックが少なくとも一個所において、各触
媒ブロックの上面と下面とで係合されるように波形状板
を設けても良い。
The unevenness on the upper and lower surfaces of the outer frame may be reversed. Further, a corrugated plate may be provided in at least one location of each of the upper and lower catalyst blocks so that the upper and lower surfaces of each catalyst block are engaged with each other.

第9図は本発明の他の実施例を示すもので、上下段の各
触媒ブロックの保合状態の一部を表わす亀のである。下
段の触媒ブロックの外枠31上面に設けた溝形鋼31d
 と上段の触媒ブロックの外枠32下面に設けた溝形鋼
32dが位置を少しずらした状態で取付けられており、
溝形鋼31dの凸部と溝形鋼32dの凹部および溝形鋼
31dの効果を奏するとともに市販の溝形鋼を用いれば
良いのそ、プレス加工の必要もカ<、より加工費を低減
できる。溝形鋼の代りに工形鋼を用いても同様である。
FIG. 9 shows another embodiment of the present invention, and is a turtle representing a part of the engagement state of each of the upper and lower catalyst blocks. Channel steel 31d provided on the upper surface of the outer frame 31 of the lower catalyst block
and the channel steel 32d provided on the lower surface of the outer frame 32 of the upper catalyst block are installed with their positions slightly shifted,
The convex part of the channel steel 31d and the concave part of the channel steel 32d produce the effects of the channel steel 31d, and since commercially available channel steel can be used, there is no need for press working, and processing costs can be further reduced. . The same effect can be obtained even if engineered shaped steel is used instead of channel steel.

以上説明した本発明によれば、触媒ブロックの外枠を形
成する部材自身に脱硝反応器内に配列充填された各触媒
ブロック間の移動を規制する手段を持たせたので、触媒
ブロックの外枠形状が簡単にカシ、かつ触媒ブロックの
外枠の材料費、加工費を低減できるとともにストッパー
の位置合せ、溶接作業の手間と時間を全く必要とせず極
めて経済的である。
According to the present invention described above, since the member forming the outer frame of the catalyst block itself is provided with a means for regulating the movement between the catalyst blocks arranged and packed in the denitrification reactor, the outer frame of the catalyst block The shape is simple, and the material cost and processing cost for the outer frame of the catalyst block can be reduced, and the time and effort of positioning the stopper and welding work are not required at all, making it extremely economical.

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

第1図は脱硝反応器内に充填される触媒ユニットの外観
図、第2図は従来の触媒ブロックの一部を切欠いた斜視
図、第3図はその触媒ブロックの底面図、第4図は脱硝
反応器内に触媒ブロックを充填した状態を示す図、第5
図は従来のストッパーによシ各触媒ブロックを係合した
状態の一部を拡大し九斜視図、第6図は本発明の一実施
例による触媒ブロックの一部を切欠いた斜視図、g7図
はその触媒ブロックを脱硝反応器内に充填【7た状態を
示す図、第8図は第7図の要部詳細を示す斜夜間、菖9
図は本発明の他の実施例を示す各触媒ブロックの係合し
た状態の一部を拡大した斜視図である。 1・・・・・・触媒ユニット、2・・・・・・触媒ブロ
ック゛、3・・・・・・触媒ブロックの外枠、3& I
 ”b * 36@ 3d・・・・・・触媒ブロックの
外枠金形成する部材、7・・・・・・脱硝反応器。 第1図 第4図 第5図 第7図 第8図 第9図
Figure 1 is an external view of a catalyst unit packed in a denitrification reactor, Figure 2 is a partially cutaway perspective view of a conventional catalyst block, Figure 3 is a bottom view of the catalyst block, and Figure 4 is Figure 5 showing the state in which catalyst blocks are packed in the denitrification reactor.
Figure 6 is an enlarged perspective view of a part of each catalyst block engaged with a conventional stopper; Figure 6 is a partially cutaway perspective view of a catalyst block according to an embodiment of the present invention; Figure g7; Figure 8 shows the details of the main parts of Figure 7.
The figure is a partially enlarged perspective view showing another embodiment of the present invention in which each catalyst block is in an engaged state. 1...Catalyst unit, 2...Catalyst block, 3...Outer frame of catalyst block, 3&I
"b * 36 @ 3d... Member forming the outer frame of the catalyst block, 7... Denitrification reactor. Figure 1 Figure 4 Figure 5 Figure 7 Figure 8 Figure 9 figure

Claims (1)

【特許請求の範囲】 1、複数個の触媒ユニツ)1−組み込んだ触媒ブロック
と、この触媒ブロックを垂直方向およびそれと直交する
各水平方向に配列充填した脱硝反応器とを備え、この脱
硝反応器に対してひとつの水平方向にガスを流すことに
よシガスの脱硝管行う脱硝装置において、前記脱硝反応
器内に配列充填された各触媒ブロックの外枠を形成する
部材に各触媒ブロック間の移動を規制する手段を持たせ
たことを特徴とする脱硝装置。 2、前記各触媒ブロックの外枠を形成する部材が外枠の
上面および下面のそれぞれにおいて少くとも1個所に凹
凸部のいずれか一方を有し、脱硝反応器内に配列充填さ
れた各触媒ブロックの外枠上面とその上段に位置する触
媒ブロックの外枠下面とが前記凹凸部で係合して各触媒
ブロック間のガス流れ水平方向の移動を規制することを
特徴とする特許請求の範囲第1項記載の脱硝装置。
[Claims] 1. A plurality of catalyst units) 1- A denitrification reactor comprising an incorporated catalyst block and a denitrification reactor in which the catalyst blocks are arranged and packed in a vertical direction and each horizontal direction perpendicular thereto. In a denitrification device that performs denitrification of gas by flowing gas in one horizontal direction, the member forming the outer frame of each catalyst block arranged and packed in the denitrification reactor is moved between each catalyst block. A denitrification device characterized by having a means for regulating. 2. The members forming the outer frame of each of the catalyst blocks have at least one uneven portion on each of the upper and lower surfaces of the outer frame, and the catalyst blocks are arranged and packed in the denitrification reactor. The upper surface of the outer frame of the catalytic converter and the lower surface of the outer frame of the catalyst block positioned above the catalytic converter engage with each other at the uneven portion to restrict horizontal movement of gas flow between the catalyst blocks. The denitrification device according to item 1.
JP56122380A 1981-08-06 1981-08-06 Denitrating device Pending JPS5824323A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56122380A JPS5824323A (en) 1981-08-06 1981-08-06 Denitrating device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56122380A JPS5824323A (en) 1981-08-06 1981-08-06 Denitrating device

Publications (1)

Publication Number Publication Date
JPS5824323A true JPS5824323A (en) 1983-02-14

Family

ID=14834387

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56122380A Pending JPS5824323A (en) 1981-08-06 1981-08-06 Denitrating device

Country Status (1)

Country Link
JP (1) JPS5824323A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62191026A (en) * 1986-02-15 1987-08-21 Babcock Hitachi Kk Denitration equipment
JPS6335426U (en) * 1986-08-26 1988-03-07
WO2015128658A1 (en) * 2014-02-27 2015-09-03 Johnson Matthey Catalysts (Germany) Gmbh Catalyst module, receiving unit for such a catalyst module and method for manufacturing such a catalyst module
JP2017518163A (en) * 2014-02-27 2017-07-06 ジョンソン マッセイ キャタリスツ (ジャーマニー) ゲゼルシャフト ミット ベシュレンクテル ハフツングJohnson Matthey Catalysts (Germany) GmbH Catalyst module, receiving unit for such a catalyst module, and method for manufacturing such a catalyst module

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62191026A (en) * 1986-02-15 1987-08-21 Babcock Hitachi Kk Denitration equipment
JPS6335426U (en) * 1986-08-26 1988-03-07
JPH0450889Y2 (en) * 1986-08-26 1992-12-01
WO2015128658A1 (en) * 2014-02-27 2015-09-03 Johnson Matthey Catalysts (Germany) Gmbh Catalyst module, receiving unit for such a catalyst module and method for manufacturing such a catalyst module
CN106030067A (en) * 2014-02-27 2016-10-12 庄信万丰催化剂(德国)有限公司 Catalyst module, receiving unit for such a catalyst module and method for manufacturing such a catalyst module
JP2017507777A (en) * 2014-02-27 2017-03-23 ジョンソン マッセイ キャタリスツ (ジャーマニー) ゲゼルシャフト ミット ベシュレンクテル ハフツングJohnson Matthey Catalysts (Germany) GmbH Catalyst module, receiving unit for such a catalyst module, and method for producing such a catalyst module
JP2017518163A (en) * 2014-02-27 2017-07-06 ジョンソン マッセイ キャタリスツ (ジャーマニー) ゲゼルシャフト ミット ベシュレンクテル ハフツングJohnson Matthey Catalysts (Germany) GmbH Catalyst module, receiving unit for such a catalyst module, and method for manufacturing such a catalyst module
US9803531B2 (en) 2014-02-27 2017-10-31 Johnson Matthey Catalysts (Germany) Gmbh Catalyst module, receiving unit for such a catalyst module and method for manufacturing such a catalyst module
CN106030067B (en) * 2014-02-27 2018-11-09 庄信万丰催化剂(德国)有限公司 Photocatalyst module and its manufacturing method, the receiving unit for the photocatalyst module
RU2709208C2 (en) * 2014-02-27 2019-12-17 Джонсон Мэтти Каталистс (Джермани) Гмбх Catalytic module, installation unit for such catalytic module and method of producing such catalytic module

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