JPH02203923A - Catalystic reduction of nitrogen oxide - Google Patents
Catalystic reduction of nitrogen oxideInfo
- Publication number
- JPH02203923A JPH02203923A JP1022133A JP2213389A JPH02203923A JP H02203923 A JPH02203923 A JP H02203923A JP 1022133 A JP1022133 A JP 1022133A JP 2213389 A JP2213389 A JP 2213389A JP H02203923 A JPH02203923 A JP H02203923A
- Authority
- JP
- Japan
- Prior art keywords
- catalyst
- nitrogen oxide
- reducing agent
- ammonium
- ammonium salt
- 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
- MWUXSHHQAYIFBG-UHFFFAOYSA-N Nitric oxide Chemical compound O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 title claims abstract description 27
- 239000003638 chemical reducing agent Substances 0.000 claims abstract description 19
- 239000003054 catalyst Substances 0.000 claims abstract description 15
- -1 amine compound Chemical class 0.000 claims abstract description 9
- 150000003863 ammonium salts Chemical class 0.000 claims abstract description 8
- 238000000034 method Methods 0.000 claims description 9
- 238000010531 catalytic reduction reaction Methods 0.000 claims description 4
- 239000007789 gas Substances 0.000 abstract description 10
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 abstract description 6
- ATRRKUHOCOJYRX-UHFFFAOYSA-N Ammonium bicarbonate Chemical compound [NH4+].OC([O-])=O ATRRKUHOCOJYRX-UHFFFAOYSA-N 0.000 abstract description 4
- 239000001099 ammonium carbonate Substances 0.000 abstract description 4
- USFZMSVCRYTOJT-UHFFFAOYSA-N Ammonium acetate Chemical compound N.CC(O)=O USFZMSVCRYTOJT-UHFFFAOYSA-N 0.000 abstract description 2
- 239000005695 Ammonium acetate Substances 0.000 abstract description 2
- 229910000013 Ammonium bicarbonate Inorganic materials 0.000 abstract description 2
- 229940043376 ammonium acetate Drugs 0.000 abstract description 2
- 235000019257 ammonium acetate Nutrition 0.000 abstract description 2
- 235000012538 ammonium bicarbonate Nutrition 0.000 abstract description 2
- 235000012501 ammonium carbonate Nutrition 0.000 abstract description 2
- 239000004202 carbamide Substances 0.000 abstract description 2
- 229910044991 metal oxide Inorganic materials 0.000 abstract description 2
- 150000004706 metal oxides Chemical class 0.000 abstract description 2
- XSQUKJJJFZCRTK-UHFFFAOYSA-N urea group Chemical group NC(=O)N XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 abstract description 2
- 239000013043 chemical agent Substances 0.000 abstract 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 10
- 238000006243 chemical reaction Methods 0.000 description 8
- 239000000126 substance Substances 0.000 description 4
- 229910000069 nitrogen hydride Inorganic materials 0.000 description 3
- 239000007864 aqueous solution Substances 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 229910004688 Ti-V Inorganic materials 0.000 description 1
- 229910010968 Ti—V Inorganic materials 0.000 description 1
- 150000003868 ammonium compounds Chemical class 0.000 description 1
- VZTDIZULWFCMLS-UHFFFAOYSA-N ammonium formate Chemical compound [NH4+].[O-]C=O VZTDIZULWFCMLS-UHFFFAOYSA-N 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 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
- 230000002939 deleterious effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 230000007096 poisonous effect Effects 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000010453 quartz Substances 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 1
- 229910052720 vanadium Inorganic materials 0.000 description 1
- LEONUFNNVUYDNQ-UHFFFAOYSA-N vanadium atom Chemical compound [V] LEONUFNNVUYDNQ-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
この発明は、排ガス中の窒素酸化物(以下、NOxと記
す)を触媒の存在下に還元剤によって選択的に接触還元
する方法に関し、さらに詳しくは還元剤の改良に関する
。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application This invention relates to a method for selectively catalytically reducing nitrogen oxides (hereinafter referred to as NOx) in exhaust gas using a reducing agent in the presence of a catalyst. Relating to improvements in reducing agents.
従来技術およびその問題点
排ガス中のNOxの処理方法としては、すでに多くの提
案がなされているが、そのうち、還元剤としてNH3を
用い、触媒の存在下に所定温度で操作して、NOxをN
2に還元無害化するいわゆる接触還元脱硝法は、排ガス
中に酸素が共存していても上記反応が選択的に進行する
ので、排ガス脱硝プロセスとして有効な方法である。PRIOR ART AND THEIR PROBLEMS Many proposals have already been made for the treatment of NOx in exhaust gas. Among them, NOx is reduced by using NH3 as a reducing agent and operating at a predetermined temperature in the presence of a catalyst.
The so-called catalytic reduction denitrification method, which reduces and renders the exhaust gas harmless, is an effective method as an exhaust gas denitrification process because the above reaction proceeds selectively even if oxygen coexists in the exhaust gas.
しかしながら、この脱硝法で還元剤として使用されるN
H3は、各種法規において毒物、劇物、悪臭物質などに
指定されており、その取扱い、輸送、貯蔵などに特別注
意を払う必要があるものである。そのためNH3に関す
る専門的知識を有する取扱い者、および安全を確保する
ための特殊な設備などが必要となり、この還元剤の使用
は実用的でなかった。However, the N used as a reducing agent in this denitrification method
H3 is designated as a poisonous substance, a deleterious substance, a malodorous substance, etc. under various laws and regulations, and special care must be taken when handling, transporting, storing, etc. Therefore, a handler with specialized knowledge of NH3 and special equipment to ensure safety are required, making the use of this reducing agent impractical.
この発明の目的は、上記の如き実情に鑑み、取扱い、輸
送、貯蔵などにおいて安全性に問題のない化合物を還元
剤として使用する脱硝方法を提供するにある。In view of the above-mentioned circumstances, an object of the present invention is to provide a denitrification method that uses a compound as a reducing agent that poses no safety problems in handling, transportation, storage, etc.
問題点の解決手段
この発明によるNOxの接触還元方法は、窒素酸化物を
触媒の存在下に還元剤によって選択的に還元するに当た
り、還元剤として、アンモニウム塩またはアミン化合物
を用いることを特徴とする。A method for catalytic reduction of NOx according to the present invention is characterized in that an ammonium salt or an amine compound is used as a reducing agent in selectively reducing nitrogen oxides with a reducing agent in the presence of a catalyst. .
触媒としては、担体担持型、非担持型、ラネー型など公
知の脱硝触媒が使用できるが、とりわけアナターゼ型の
チタニアにv205のような金属酸化物を担持させたも
のが優れた脱硝性能を示す。As the catalyst, known denitrification catalysts such as carrier-supported, non-supported, and Raney-type catalysts can be used, but in particular, anatase-type titania supported with a metal oxide such as V205 exhibits excellent denitrification performance.
還元剤としてのアンモニウム塩の例としては、炭酸アン
モニウム、炭酸水素アンモニウム、蟻酸アンモニウム、
酢酸アンモニウムなどが挙げられる。またアミノ化合物
の例としては尿素が挙げられる。Examples of ammonium salts as reducing agents include ammonium carbonate, ammonium bicarbonate, ammonium formate,
Examples include ammonium acetate. Moreover, urea is mentioned as an example of an amino compound.
アンモニウム化合物およびアミン化合物は、排ガス中に
そのまま粉末で注入されても溶液状で注入されてもよい
。またこれらを予め分解ガス化しておき、生じた分解ガ
スを排ガスに注入することもできる。The ammonium compound and the amine compound may be injected directly into the exhaust gas in the form of a powder or in the form of a solution. Alternatively, these may be decomposed and gasified in advance, and the resulting decomposed gas may be injected into the exhaust gas.
実 施 例 つぎに、この発明を実施例によって具体的に説明する。Example Next, the present invention will be specifically explained using examples.
まず、つぎの操作によってTi−V系触媒を調製した。First, a Ti-V catalyst was prepared by the following operation.
所要量のβチタン酸を400℃で5時間焼成して酸化チ
タンを得、これを粒径的21に破砕した。この破砕物を
メタバナジン酸アンモニウムの飽和水溶液中に室温で3
時間浸漬し、120°Cで乾燥し、400℃で3時間焼
成した。得られた触媒において、バナジウムの担持率は
4重量%であった。A required amount of β-titanic acid was calcined at 400° C. for 5 hours to obtain titanium oxide, which was crushed to 21 particles in size. This crushed material was added to a saturated aqueous solution of ammonium metavanadate at room temperature for 3 hours.
It was soaked for an hour, dried at 120°C, and fired at 400°C for 3 hours. In the obtained catalyst, the vanadium loading rate was 4% by weight.
つぎに、上記触媒を用い、表2に示す各還元剤について
それぞれNOxの反応率を測定した。Next, using the above catalyst, the NOx reaction rate was measured for each reducing agent shown in Table 2.
すなわち、直径30mIIlの円筒状の石英製反応管に
上記触媒を2.25111充填し、この反応管に、通常
の流通系において、温度調節を行ないながら、表1に示
す組成の試験用調製排ガスを流量1. 51/分(0℃
、1気圧)で流通した。この状態で、還元剤として表2
に示す各種化合物の水溶液を、NH2+NH4/NO比
で1.2モル1モルの量で、反応管の頂部に注入し、脱
硝反応を行なわせた。That is, a cylindrical quartz reaction tube with a diameter of 30 ml was filled with 2.25111 parts of the above catalyst, and a prepared exhaust gas for testing having the composition shown in Table 1 was poured into the reaction tube while controlling the temperature in a normal flow system. Flow rate 1. 51/min (0℃
, 1 atm). In this state, as a reducing agent Table 2
Aqueous solutions of various compounds shown in the figure were injected into the top of the reaction tube in an amount of 1.2 mol 1 mol (NH2+NH4/NO ratio) to carry out a denitrification reaction.
各還元剤について、温度200℃、250℃、300℃
、350℃および400°CにおけるNOxの反応率を
求めた。その結果を表2に示す。For each reducing agent, the temperature is 200℃, 250℃, 300℃
, the NOx reaction rate at 350°C and 400°C was determined. The results are shown in Table 2.
表 (以下余白) 表 林 アンモニアガスをNH3/No比1゜ 2で調製排ガスに混入した。table (Margin below) table Hayashi Ammonia gas at NH3/No ratio of 1° It was mixed into the flue gas prepared in step 2.
表2から明らかなように、還元剤としてアンモニウム塩
またはアミン化合物を使用した場合にも、アンモニアガ
スを使用した場合と比べて遜色のない高い反応率か得ら
れた。As is clear from Table 2, even when an ammonium salt or an amine compound was used as the reducing agent, a high reaction rate comparable to that when ammonia gas was used was obtained.
発明の効果
この発明のNOx触媒還元方法では、還元剤としてアン
モニウム塩またはアミン化合物を使用するので、本書冒
頭で述べたようなアンモニアガスの使用に起因する諸問
題、すなわち薬剤の取扱い、輸送、貯蔵などにおいて危
険が伴い、安全を確保するための専門取扱い者および特
種設備などが必要となるといった問題を一挙に解消する
ことができる。Effects of the Invention Since the NOx catalytic reduction method of this invention uses an ammonium salt or an amine compound as a reducing agent, it does not solve the problems caused by the use of ammonia gas as mentioned at the beginning of this book, namely, the handling, transportation, and storage of chemicals. It is possible to solve the problem of the need for specialized operators and special equipment to ensure safety due to the danger involved in such operations.
以上that's all
Claims (1)
元するに当たり、還元剤として、アンモニウム塩または
アミン化合物を用いることを特徴とする、窒素酸化物の
接触還元方法。A method for catalytic reduction of nitrogen oxides, which comprises using an ammonium salt or an amine compound as a reducing agent in selectively reducing nitrogen oxides with a reducing agent in the presence of a catalyst.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1022133A JPH02203923A (en) | 1989-01-30 | 1989-01-30 | Catalystic reduction of nitrogen oxide |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1022133A JPH02203923A (en) | 1989-01-30 | 1989-01-30 | Catalystic reduction of nitrogen oxide |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH02203923A true JPH02203923A (en) | 1990-08-13 |
Family
ID=12074395
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1022133A Pending JPH02203923A (en) | 1989-01-30 | 1989-01-30 | Catalystic reduction of nitrogen oxide |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH02203923A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5139754A (en) * | 1989-09-12 | 1992-08-18 | Fuel Tech, Inc. | Catalytic/non-catalytic combination process for nitrogen oxides reduction |
| JP2006028235A (en) * | 2004-07-13 | 2006-02-02 | Japan Automobile Research Inst Inc | Fuel and NOx removal method |
| JP2010517767A (en) * | 2007-02-15 | 2010-05-27 | ケミラ オユイ | Method for preparing reducing agent composition |
| US7744837B2 (en) | 2004-08-04 | 2010-06-29 | Kemira Oyj | Reducing Agent Composition |
| JP4798453B2 (en) * | 2003-02-04 | 2011-10-19 | ケミラ オーワイジェイ | Contact method and reducing agent composition for reducing nitrogen oxides in flue gas |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5290461A (en) * | 1976-01-26 | 1977-07-29 | Toray Ind Inc | Removal of nitrogen oxides |
| JPS54110165A (en) * | 1978-02-17 | 1979-08-29 | Babcock Hitachi Kk | Removing method for nitrogen oxides in exhaust gas |
| JPS62262729A (en) * | 1986-05-09 | 1987-11-14 | Mitsubishi Heavy Ind Ltd | Method for removing nitrogen oxide contained in exhaust gas |
| JPS6447427A (en) * | 1987-08-17 | 1989-02-21 | Mitsubishi Heavy Ind Ltd | Method for reducing nitrogen oxides in exhaust gas of internal combustion engine |
-
1989
- 1989-01-30 JP JP1022133A patent/JPH02203923A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5290461A (en) * | 1976-01-26 | 1977-07-29 | Toray Ind Inc | Removal of nitrogen oxides |
| JPS54110165A (en) * | 1978-02-17 | 1979-08-29 | Babcock Hitachi Kk | Removing method for nitrogen oxides in exhaust gas |
| JPS62262729A (en) * | 1986-05-09 | 1987-11-14 | Mitsubishi Heavy Ind Ltd | Method for removing nitrogen oxide contained in exhaust gas |
| JPS6447427A (en) * | 1987-08-17 | 1989-02-21 | Mitsubishi Heavy Ind Ltd | Method for reducing nitrogen oxides in exhaust gas of internal combustion engine |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5139754A (en) * | 1989-09-12 | 1992-08-18 | Fuel Tech, Inc. | Catalytic/non-catalytic combination process for nitrogen oxides reduction |
| JP4798453B2 (en) * | 2003-02-04 | 2011-10-19 | ケミラ オーワイジェイ | Contact method and reducing agent composition for reducing nitrogen oxides in flue gas |
| JP2006028235A (en) * | 2004-07-13 | 2006-02-02 | Japan Automobile Research Inst Inc | Fuel and NOx removal method |
| US7744837B2 (en) | 2004-08-04 | 2010-06-29 | Kemira Oyj | Reducing Agent Composition |
| JP2010517767A (en) * | 2007-02-15 | 2010-05-27 | ケミラ オユイ | Method for preparing reducing agent composition |
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