JPH0326318A - Waste gas treating device - Google Patents
Waste gas treating deviceInfo
- Publication number
- JPH0326318A JPH0326318A JP1162880A JP16288089A JPH0326318A JP H0326318 A JPH0326318 A JP H0326318A JP 1162880 A JP1162880 A JP 1162880A JP 16288089 A JP16288089 A JP 16288089A JP H0326318 A JPH0326318 A JP H0326318A
- Authority
- JP
- Japan
- Prior art keywords
- catalyst
- denitration catalyst
- denitration
- exhaust gas
- denitrification
- 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
Links
- 239000002912 waste gas Substances 0.000 title abstract 3
- 239000003054 catalyst Substances 0.000 claims abstract description 54
- 239000007789 gas Substances 0.000 claims abstract description 25
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims abstract description 24
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims abstract description 22
- 230000003647 oxidation Effects 0.000 claims abstract description 16
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 16
- 229910021529 ammonia Inorganic materials 0.000 claims abstract description 12
- 239000000203 mixture Substances 0.000 claims abstract description 12
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 claims abstract description 12
- 229910052697 platinum Inorganic materials 0.000 claims abstract description 11
- 238000011144 upstream manufacturing Methods 0.000 claims abstract description 8
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 7
- 229910002091 carbon monoxide Inorganic materials 0.000 claims abstract description 7
- 229910052703 rhodium Inorganic materials 0.000 claims abstract description 4
- 239000010948 rhodium Substances 0.000 claims abstract description 4
- MHOVAHRLVXNVSD-UHFFFAOYSA-N rhodium atom Chemical compound [Rh] MHOVAHRLVXNVSD-UHFFFAOYSA-N 0.000 claims abstract description 4
- 239000007800 oxidant agent Substances 0.000 claims description 6
- 239000010970 precious metal Substances 0.000 claims description 5
- 238000002347 injection Methods 0.000 claims description 4
- 239000007924 injection Substances 0.000 claims description 4
- 239000000126 substance Substances 0.000 claims description 4
- 229910000510 noble metal Inorganic materials 0.000 abstract description 4
- 239000007921 spray Substances 0.000 abstract description 4
- 239000011248 coating agent Substances 0.000 abstract description 3
- 238000000576 coating method Methods 0.000 abstract description 3
- 230000008021 deposition Effects 0.000 abstract 2
- -1 etc. Inorganic materials 0.000 abstract 1
- 239000000243 solution Substances 0.000 description 6
- 238000002485 combustion reaction Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 239000003638 chemical reducing agent Substances 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- APUPEJJSWDHEBO-UHFFFAOYSA-P ammonium molybdate Chemical compound [NH4+].[NH4+].[O-][Mo]([O-])(=O)=O APUPEJJSWDHEBO-UHFFFAOYSA-P 0.000 description 1
- 229940010552 ammonium molybdate Drugs 0.000 description 1
- 235000018660 ammonium molybdate Nutrition 0.000 description 1
- 239000011609 ammonium molybdate Substances 0.000 description 1
- UNTBPXHCXVWYOI-UHFFFAOYSA-O azanium;oxido(dioxo)vanadium Chemical compound [NH4+].[O-][V](=O)=O UNTBPXHCXVWYOI-UHFFFAOYSA-O 0.000 description 1
- 239000000969 carrier Substances 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 229910052750 molybdenum Inorganic materials 0.000 description 1
- 239000011733 molybdenum Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- PXXKQOPKNFECSZ-UHFFFAOYSA-N platinum rhodium Chemical compound [Rh].[Pt] PXXKQOPKNFECSZ-UHFFFAOYSA-N 0.000 description 1
- 230000002028 premature Effects 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 description 1
- 229910052721 tungsten Inorganic materials 0.000 description 1
- 239000010937 tungsten Substances 0.000 description 1
- 229910052720 vanadium Inorganic materials 0.000 description 1
- GPPXJZIENCGNKB-UHFFFAOYSA-N vanadium Chemical compound [V]#[V] GPPXJZIENCGNKB-UHFFFAOYSA-N 0.000 description 1
- UUUGYDOQQLOJQA-UHFFFAOYSA-L vanadyl sulfate Chemical compound [V+2]=O.[O-]S([O-])(=O)=O UUUGYDOQQLOJQA-UHFFFAOYSA-L 0.000 description 1
- 229940041260 vanadyl sulfate Drugs 0.000 description 1
- 229910000352 vanadyl sulfate Inorganic materials 0.000 description 1
Landscapes
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
- Exhaust Gas After Treatment (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は燃焼排ガス処理装置に係り、特に性能の低下し
た脱硝装置を再生するようにした燃焼排ガス処理装置に
関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a combustion exhaust gas treatment device, and more particularly to a combustion exhaust gas treatment device that regenerates a denitrification device whose performance has deteriorated.
ボイラからの排ガスや、ガスタービンからの排ガスには
、使用する燃料や燃焼装置の状態の良否によって多少の
変動はあるが、一酸化炭素(CO)などの未燃燃料(以
下、未燃分と略称する)とともに、NoやNO2などの
窒素酸化物(以下、NOxという)が存在する。これら
の排ガス量は膨大なものであるので、COやNOxをそ
のまま排出すれば大気を汚染し、公害問題が生じる。Exhaust gas from boilers and gas turbines fluctuates to some extent depending on the fuel used and the condition of the combustion equipment, but unburned fuel such as carbon monoxide (CO) There are nitrogen oxides (hereinafter referred to as NOx) such as No and NO2. Since the amount of these exhaust gases is enormous, if CO and NOx are emitted as they are, they will pollute the atmosphere and cause pollution problems.
したがって、このような場合は、従来はGOなどの未燃
分を燃焼させてCO2などの無害ガスにするため、燃焼
促進用の触媒(以下、燃焼触媒という)を備えた酸化装
置と、NOxを還元剤としてのアンモニアにより脱硝触
媒の存在下でN2とH20に還元するための脱硝装置と
を併置することが行われていた。Therefore, in such cases, conventionally, an oxidizer equipped with a catalyst for promoting combustion (hereinafter referred to as a combustion catalyst) and an oxidizer to combust unburned substances such as GO and turn them into harmless gases such as CO2 and NOx are used. It has been practiced to co-locate a denitrification device for reducing N2 and H20 in the presence of a denitrification catalyst using ammonia as a reducing agent.
酸化触媒としては、流れに平行な多数の溝孔をハニカム
状に形威した担体の表面に白金、ロジウム、白金ロジウ
ムなどの貰金属触媒をコーティングしたものが使われて
いる。The oxidation catalyst used is a carrier having a honeycomb-like structure with many slots parallel to the flow, coated with a metal catalyst such as platinum, rhodium, or platinum-rhodium.
また、脱硝触媒としては、チタン、バナジウム、モリブ
デン、タングステン、鉄などの酸化物をl種以上含む触
媒組威物をハニカム状、あるいは板状に形或したもの、
またはハニカム、板状の担体にそれら触媒組成物を含浸
もしくは塗布して担持させたものが多く使われている。Further, as a denitrification catalyst, a catalyst composition containing one or more types of oxides such as titanium, vanadium, molybdenum, tungsten, iron, etc. is shaped into a honeycomb shape or a plate shape,
Alternatively, honeycomb or plate-shaped carriers impregnated or coated with these catalyst compositions are often used.
上記した排ガス処理装置においては、酸化装置を高温の
排ガス上流側に、脱硝装置を下流側に配置している。こ
れは高価な貴金属触媒を高温の上流側に排ガス中に配置
して活性を高くすれば、使用する貴金属触媒量を節減で
きるためである。また酸化装置で燃焼する排ガス中の未
燃分によって排ガス温度が上昇し、脱硝装置で処理され
る際の触媒活性が向上する効果もある。In the above-mentioned exhaust gas treatment device, the oxidizing device is arranged on the upstream side of the high temperature exhaust gas, and the denitrification device is arranged on the downstream side. This is because the amount of precious metal catalyst used can be reduced by placing an expensive precious metal catalyst in the exhaust gas upstream of high temperature to increase its activity. Furthermore, the temperature of the exhaust gas increases due to unburned components in the exhaust gas burned in the oxidizer, which has the effect of improving catalyst activity when treated in the denitrification device.
上記従来装置を長期間運転すると、原因は不明であるが
、脱硝装置の性能が最初予測していた値よりもかなり急
速に低下する現象が発生した。When the above-mentioned conventional device was operated for a long period of time, a phenomenon occurred in which the performance of the denitrification device decreased much more rapidly than initially expected, although the cause was unknown.
この結果、法令で規定される排ガスNOx総量を守るこ
とができず、ボイラやガスタービンの出力を下げて運転
するとか、還元剤としてのアンモニア使用量を増加して
残留アンモニア量を多くしたり、さらには脱硝触媒の交
換を早期に行うなどの対策をどらざるを得す、根本的な
解決は見出されていなかった。本発明は上記した従来技
術の問題点を解決するためになされたものである。As a result, the total amount of exhaust gas NOx stipulated by law cannot be complied with, and the output of boilers and gas turbines may be reduced, or the amount of ammonia used as a reducing agent may be increased to increase the amount of residual ammonia. Furthermore, no fundamental solution had been found, forcing the company to take measures such as replacing the denitrification catalyst early. The present invention has been made to solve the problems of the prior art described above.
〔課題を解決するための手段]
上記した従来技術の問題点は、一酸化炭素などの未燃分
と窒素酸化物とを含有する排ガスil路の上流域に白金
、ロジウムまたはこれらの1種以上の貴金属酸化触媒を
備えた酸化装置、および前記通路の下流域に脱硝触媒を
備えた脱硝装置とアンモニア注入装置とを有する排ガス
処理装置において、前記酸化装置から飛散した貴金属酸
化触媒の付着により性能の劣下した脱硝触媒表面を脱硝
触媒組威物で塗布する装置を設けたことを特徴とする排
ガス処理装置により解決される。[Means for Solving the Problems] The problem with the prior art described above is that platinum, rhodium, or one or more of these is present in the upstream region of the exhaust gas line containing unburned substances such as carbon monoxide and nitrogen oxides. In an exhaust gas treatment device having an oxidation device equipped with a noble metal oxidation catalyst, a denitration device equipped with a denitration catalyst downstream of the passage, and an ammonia injection device, performance may be degraded due to adhesion of the precious metal oxidation catalyst scattered from the oxidation device. The problem is solved by an exhaust gas treatment device characterized by being provided with a device for coating the deteriorated surface of the denitrification catalyst with a denitrification catalyst composition.
従来装置を長期間運転すると、脱硝装置の性能が予定以
上に低下する原因について、発明者らが種々の試験と検
討を重ねた結果、酸化触媒として使用されている白金な
どの貴金属触媒が、温度変化を伴う負荷変化などにより
ハニカム担体から剥がれたり、あるいは気相化して下流
に飛散して、脱硝装置の触媒上に付着するためであろう
と推定された。すなわち、脱硝触媒上に白金等が付着す
ると、白金はNOxを還元するために脱硝装置にて使用
するアンモニアを酸化してNOxとする触媒としての作
用をするため、脱硝装置の見かけ上の性能が低下するも
のと考えられた。本発明は以上の知見に基づいてなされ
たもので、以下図面により発明の内容を具体的に説明す
る。The inventors conducted various tests and studies to find out why the performance of the denitration equipment deteriorates more than expected when conventional equipment is operated for a long period of time. It was presumed that this was due to peeling off from the honeycomb carrier due to changes in load, or becoming gaseous and scattering downstream, and depositing on the catalyst of the denitrification equipment. In other words, if platinum or the like adheres to the denitration catalyst, platinum acts as a catalyst to oxidize the ammonia used in the denitration equipment to reduce NOx to NOx, so the apparent performance of the denitration equipment will deteriorate. It was thought that this would decrease. The present invention has been made based on the above knowledge, and the content of the invention will be specifically explained below with reference to the drawings.
第l図は、本発明の実施例図であり、COなとの未燃分
とNOxをともに含有する排ガス通路1内には排ガス上
流側に白金などの酸化触媒を有する酸化装置2が設けら
れ、下流側には脱硝触媒を備えた脱硝装N3が設けられ
ている。脱硝装置より上流側の排ガス通路内にはアンモ
ニア注入ノズル4が設けられ、これにアンモニア供給管
5より必要量のアンモニアが供給され、排ガスに混合さ
れる。9はメタバナジン酸アンモニウム、硫酸バナジル
あるいはモリブデン酸アンモニウムなどの触媒組威物溶
液であり、圧縮空気供給管7からの圧縮空気と混合器8
で混合され、脱硝装置3の上流に設置した噴霧ノズル6
により噴霧される。噴霧された触媒組戒物は脱硝触媒表
面に塗布され、触媒上に付着していた白金などを被覆し
て酸化触媒機能を発揮させないようにする。このように
して、脱硝触媒を初期の性能に近く復元することができ
る。FIG. 1 is a diagram showing an embodiment of the present invention, in which an oxidizer 2 having an oxidation catalyst such as platinum is provided on the upstream side of the exhaust gas in an exhaust gas passage 1 containing both unburned components such as CO and NOx. A denitrification unit N3 equipped with a denitrification catalyst is provided on the downstream side. An ammonia injection nozzle 4 is provided in the exhaust gas passage upstream of the denitrification device, and a required amount of ammonia is supplied to this from an ammonia supply pipe 5 and mixed with the exhaust gas. 9 is a catalyst compound solution such as ammonium metavanadate, vanadyl sulfate or ammonium molybdate, which is mixed with compressed air from the compressed air supply pipe 7 and mixer 8
The mixture is mixed in the spray nozzle 6 installed upstream of the denitrification device 3.
sprayed by. The sprayed catalyst mixture is applied to the surface of the denitrification catalyst, covering platinum and other substances adhering to the catalyst to prevent it from exerting its oxidation catalytic function. In this way, the denitrification catalyst can be restored to close to its initial performance.
触媒&11或物溶液の塗布は、脱硝率を測定して初期値
より、例えば3%程度低下したときに行うが、脱硝触媒
の表面に付着している白金などの量によって、塗布する
溶液の濃度および塗布量は左右されるが、上記噴霧塗布
を2〜3回繰返すことにより実施する。なお、脱硝触媒
上に付着した白金等は簡単には除去できないが、本発明
のように脱硝触媒組威物を塗布して被覆することにより
簡単に無害化することができる。Catalyst & 11 A certain solution is applied when the denitrification rate is measured and has decreased by about 3% from the initial value, but the concentration of the solution applied depends on the amount of platinum etc. attached to the surface of the denitrification catalyst. Although the amount of application depends on the amount of application, the above spray application is repeated 2 to 3 times. Although platinum and the like attached to the denitrification catalyst cannot be easily removed, it can be easily rendered harmless by coating it with a denitrification catalyst composition as in the present invention.
なお、白金の付着した触媒を脱硝触媒組或物で塗布、被
覆する方法としては、上記実施例とは別に、触媒自体を
触媒組威物溶液中に浸漬して行うこともできるが、噴霧
塗布のほうが簡便である。In addition, as a method for applying and covering the catalyst with platinum attached with the denitrification catalyst composition, it is possible to immerse the catalyst itself in the catalyst composition solution, apart from the above-mentioned example, but spray coating is also possible. is more convenient.
本発明によれば、従来その原因が不明で、適切な処理が
とれなかった、脱硝触媒の性能劣下を簡単に回復するこ
とができ、排ガス法規をクリヤーにするためにボイラや
ガスタービンの負荷を落゜として運転したり、脱硝触媒
の早期交換を行うことを防止できる。According to the present invention, it is possible to easily recover from deterioration in the performance of the denitrification catalyst, for which the cause was previously unknown and appropriate treatment could not be taken. It is possible to prevent operation at a reduced temperature or premature replacement of the denitrification catalyst.
第1図は、本発明の実施例説明図である。
■・・・排ガス通路、2・・・酸化装置、3・・・脱硝
装置、4・・・アンモニア注入ノズル、5・・・アンモ
ニア供給管、6・・・噴霧ノズル、7・・・圧縮空気供
給管、8・・・・・・混合器、9・・・触媒組威物溶液
。FIG. 1 is an explanatory diagram of an embodiment of the present invention. ■... Exhaust gas passage, 2... Oxidizer, 3... Denitration device, 4... Ammonia injection nozzle, 5... Ammonia supply pipe, 6... Spray nozzle, 7... Compressed air Supply pipe, 8...Mixer, 9...Catalyst composition solution.
Claims (1)
る排ガス通路の上流域に白金、ロジウムまたはこれらの
1種以上の貴金属酸化触媒を備えた酸化装置、および前
記通路の下流域に脱硝触媒を備えた脱硝装置とアンモニ
ア注入装置とを有する排ガス処理装置において、前記酸
化装置から飛散した貴金属酸化触媒の付着により性能の
劣下した脱硝触媒表面を脱硝触媒組成物で塗布する装置
を設けたことを特徴とする排ガス処理装置。(1) An oxidizer equipped with platinum, rhodium, or a precious metal oxidation catalyst of one or more of these in the upstream region of an exhaust gas passage containing unburned substances such as carbon monoxide and nitrogen oxides, and the downstream region of the passage. In an exhaust gas treatment device having a denitrification device equipped with a denitrification catalyst and an ammonia injection device, the device applies a denitration catalyst composition to the surface of the denitration catalyst whose performance has deteriorated due to the adhesion of precious metal oxidation catalysts scattered from the oxidation device. An exhaust gas treatment device characterized by being provided with.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1162880A JPH0326318A (en) | 1989-06-26 | 1989-06-26 | Waste gas treating device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1162880A JPH0326318A (en) | 1989-06-26 | 1989-06-26 | Waste gas treating device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0326318A true JPH0326318A (en) | 1991-02-04 |
Family
ID=15763020
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1162880A Pending JPH0326318A (en) | 1989-06-26 | 1989-06-26 | Waste gas treating device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0326318A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006021142A (en) * | 2004-07-08 | 2006-01-26 | Babcock Hitachi Kk | Regenerated denitrification catalyst and production method therefor |
-
1989
- 1989-06-26 JP JP1162880A patent/JPH0326318A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006021142A (en) * | 2004-07-08 | 2006-01-26 | Babcock Hitachi Kk | Regenerated denitrification catalyst and production method therefor |
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