JPS6034743A - Regeneration of used denitration catalyst - Google Patents

Regeneration of used denitration catalyst

Info

Publication number
JPS6034743A
JPS6034743A JP58143666A JP14366683A JPS6034743A JP S6034743 A JPS6034743 A JP S6034743A JP 58143666 A JP58143666 A JP 58143666A JP 14366683 A JP14366683 A JP 14366683A JP S6034743 A JPS6034743 A JP S6034743A
Authority
JP
Japan
Prior art keywords
catalyst
catalytic activity
denitration catalyst
contg
water
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.)
Granted
Application number
JP58143666A
Other languages
Japanese (ja)
Other versions
JPH0446621B2 (en
Inventor
Isato Morita
勇人 森田
Yoshiro Inagaki
稲垣 芳郎
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 JP58143666A priority Critical patent/JPS6034743A/en
Publication of JPS6034743A publication Critical patent/JPS6034743A/en
Publication of JPH0446621B2 publication Critical patent/JPH0446621B2/ja
Granted legal-status Critical Current

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  • Exhaust Gas Treatment By Means Of Catalyst (AREA)

Abstract

PURPOSE:To obtain regenerated denitration catalyst having high performance by a simple process wherein used denitration catalyst is washed in a solution contg. component having catalytic activity. CONSTITUTION:Used denitration catalyst is washed with a soln. contg. components having catalytic activity instead of washing with water. Such components having catalytic activity are compd. contg. at least one among V, Fe, Ni, Mo, Co, Cu, Cr, Sn, W, U. These compds. are usually available in the form of oxides, however, it is preferred to use solution of these metallic compds. in water or in mineral acid such as H2SO4. By the washing in accordance with this invention, satisfactory regeneration effect of catalytic activity is recognized in regenerated catalyst, and same degree of catalytic performance as high as fresh catalyst is obtd.

Description

【発明の詳細な説明】 本発明は、使用済脱硝触媒体の再生処理方法に関し、特
にアンモニア接触還元による排煙脱硝装置に用いられた
使用済触媒体の簡便な再生処理方法に関するものである
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for regenerating a used denitrification catalyst, and more particularly to a simple method for regenerating a spent catalyst used in a flue gas denitrification device using ammonia catalytic reduction.

従来、特にボイラーなどの排気ガス中に含まれる窒素酸
化物(NOx)を除去するために、N。
Conventionally, N has been used to remove nitrogen oxides (NOx) contained in exhaust gas, particularly from boilers.

Xを含む排気ガスにアンモニアを加え、金属酸化物触媒
体と接触させて、排気ガス中に含まれるNOxを接触還
元し、これを人体に無害な窒素にまで還元する方法が知
られている。この方法に用いられる金属酸化物触媒体は
、例えば活性金属酸化物触媒を筒状、ハニカム状、板状
等に成形した担体に付着させたものからなる。
A known method is to add ammonia to exhaust gas containing X and bring it into contact with a metal oxide catalyst to catalytically reduce NOx contained in the exhaust gas, reducing it to nitrogen that is harmless to the human body. The metal oxide catalyst body used in this method consists of, for example, an active metal oxide catalyst adhered to a carrier formed into a cylinder, honeycomb, plate, or the like.

従来、このような触媒体を使用した後の簡便な再生処理
方法としては、水洗いによる方法が提案されていたが、
この方法では活性の回復が完全ではなく、使用時の排ガ
スの性状によってはほとんど活性の回復が認められない
場合がある等の問題があった。
Conventionally, a method of washing with water was proposed as a simple reprocessing method after using such a catalyst body.
This method has problems such as incomplete recovery of activity and, depending on the properties of the exhaust gas during use, almost no recovery of activity may be observed.

本発明の目的は、上記した従来技術の欠点をなくし、簡
単な処理により高性能な再生脱硝触媒を得る方法を提供
することにある。
An object of the present invention is to eliminate the drawbacks of the prior art described above and to provide a method for obtaining a high-performance regenerated denitrification catalyst through simple processing.

要するに本発明は、使用済脱硝触媒体を水により洗浄す
る方法の代わりに、バナジウム、鉄、等の活性成分を含
有する溶液により洗浄するようにしたものである。
In short, in the present invention, instead of washing a used denitrification catalyst with water, it is washed with a solution containing active ingredients such as vanadium and iron.

本発明において、触媒活性成分としては、バナジウム、
鉄、ニッケル、モリブデン、コバルト、銅、クロム、タ
ングステン、スズ、ウランのうちの一種以上を含む化合
物があげられる。これらの化合物は一般に酸化物の形で
得られるが、本発明の洗浄においては、これらの金属化
合物を水(温湯を含む)、硫酸等の鉱酸に溶解させた溶
液が好適に用いられる。
In the present invention, the catalytically active components include vanadium,
Examples include compounds containing one or more of iron, nickel, molybdenum, cobalt, copper, chromium, tungsten, tin, and uranium. These compounds are generally obtained in the form of oxides, but in the cleaning of the present invention, solutions in which these metal compounds are dissolved in water (including hot water) or mineral acids such as sulfuric acid are preferably used.

以下、本発明を実施例により具体的に説明する。Hereinafter, the present invention will be specifically explained with reference to Examples.

実施例1〜12 市浦焚ボイラ排ガスの排煙脱硝に使用され、その所要性
能を失なった使用済の板状触媒体を第1表に示す条件に
より洗浄を行った後、恒温乾燥器中にて180℃で2時
間乾燥を行った。なお再生効果の確認のため、第1表中
に水のみの洗浄を行った場合を比較例として示した。こ
のようにして管)1られた再生触媒の触媒活性を以下に
示す条件で測定した。
Examples 1 to 12 A used plate-shaped catalyst body that was used for exhaust gas denitration of Ichiura-fired boiler exhaust gas and had lost its required performance was cleaned under the conditions shown in Table 1, and then placed in a constant temperature dryer. and dried at 180° C. for 2 hours. In order to confirm the regeneration effect, Table 1 shows a comparative example in which cleaning was performed with only water. The catalytic activity of the regenerated catalyst thus obtained was measured under the conditions shown below.

触媒活性測定条件 AV:15m/h。Catalytic activity measurement conditions AV: 15m/h.

温度:350°C ガス組成:NOx=200ppm、SO2=500pp
m、02 =3%、CO2− 12%、H20=12%、N2=残 (NH3)/ (NOX): 1.2 その結果を第2表に示したが、比較例で示す従来技術と
比較し、本実施例による再生触媒は良好な再生効果が認
められ、新品と同等の性能が得られることがわかった。
Temperature: 350°C Gas composition: NOx = 200ppm, SO2 = 500ppm
m, 02 = 3%, CO2- 12%, H20 = 12%, N2 = remainder (NH3)/(NOX): 1.2 The results are shown in Table 2, and compared with the conventional technology shown in the comparative example. However, it was found that the regenerated catalyst according to this example had a good regeneration effect, and the same performance as a new catalyst could be obtained.

以下余白 第1表 由師第腎呼ルと対する浅n晰斡■責の比率第2表 実施例13〜17 実施例1〜12において使用したものと同一の使用済板
状触媒体を第3表に示す条件により洗浄した後、恒温乾
燥器中にて180 ”cにて2時間乾燥を行った。この
ようにして得られた再生触媒の脱硝性能を前述の方法に
より測定したところ、第4表に示す結果が得られ、本実
施例による再生触媒の性能は、新品触媒と同等であるこ
とが確認された。
The following is a blank space: Table 1: Ratio of Asa n Lucidity to Responsibility Table 2: Examples 13 to 17 The same used plate-shaped catalyst body as that used in Examples 1 to 12 was After washing under the conditions shown in the table, it was dried in a constant temperature dryer at 180"C for 2 hours.The denitrification performance of the regenerated catalyst thus obtained was measured by the method described above. The results shown in the table were obtained, and it was confirmed that the performance of the regenerated catalyst according to this example was equivalent to that of a new catalyst.

第4表 実施例18 実施例1〜12において使用したものと同一の使用済板
状触媒体を触媒容量の10倍の15°C149g VO
3O4/ 11 HzOの溶液によりスプレー法により
洗浄した後、180°Cにて2時間乾燥した。このよう
にして得られた再生触媒の性能を前述の条件により測定
したところ、97%であり、新品と同等の性能であった
Table 4 Example 18 The same used plate catalyst as used in Examples 1 to 12 was heated at 15°C, 149g VO, which is 10 times the catalyst capacity.
After washing with a solution of 3O4/11 HzO by spraying, it was dried at 180°C for 2 hours. The performance of the thus obtained regenerated catalyst was measured under the conditions described above and was found to be 97%, which was equivalent to a new catalyst.

以上、本発明によれば、従来の再生技術上の問題であっ
た、活性回復の不完全さが除去、軽減され、新品触媒と
同等の性能を有する再生触媒を簡便な方法で得ることが
できる。
As described above, according to the present invention, the incompleteness of activity recovery, which was a problem with conventional regeneration techniques, is removed and reduced, and a regenerated catalyst having the same performance as a new catalyst can be obtained by a simple method. .

代理人 弁理士 川 北 武 長Agent: Patent Attorney Kawakita Takecho

Claims (1)

【特許請求の範囲】 (1)使用済脱硝触媒体を触媒活性成分の溶液中で洗浄
することを特徴とする使用済脱硝触媒体の再生処理方法
。 (2、特許請求の範囲第1項において、触媒活性成分が
バナジウム、鉄、ニッケル、モリブデン、コバルト、銅
、クロム、タング久テン、スズ、ウランのうちの一種以
上の化合物であることを特徴とする使用済脱硝触媒体の
再生処理方法。 (3)特許請求の範囲第1項において、処理前に使用済
触媒体を水または酸溶液により一回以上洗浄することを
特徴とする使用済脱硝触媒体の再生処理方法。
[Scope of Claims] (1) A method for regenerating a used denitrification catalyst, which comprises washing the used denitrification catalyst in a solution of a catalytically active component. (2. Claim 1, characterized in that the catalytic active component is a compound of one or more of vanadium, iron, nickel, molybdenum, cobalt, copper, chromium, tungsten, tin, and uranium. (3) The used denitrification catalyst according to claim 1, characterized in that the spent catalyst is washed one or more times with water or an acid solution before treatment. Media playback processing methods.
JP58143666A 1983-08-08 1983-08-08 Regeneration of used denitration catalyst Granted JPS6034743A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58143666A JPS6034743A (en) 1983-08-08 1983-08-08 Regeneration of used denitration catalyst

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58143666A JPS6034743A (en) 1983-08-08 1983-08-08 Regeneration of used denitration catalyst

Publications (2)

Publication Number Publication Date
JPS6034743A true JPS6034743A (en) 1985-02-22
JPH0446621B2 JPH0446621B2 (en) 1992-07-30

Family

ID=15344106

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58143666A Granted JPS6034743A (en) 1983-08-08 1983-08-08 Regeneration of used denitration catalyst

Country Status (1)

Country Link
JP (1) JPS6034743A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4847054A (en) * 1986-12-06 1989-07-11 Metallgesellschaft Ag Process for catalytically reducing NO contained in a gas
WO2000012211A1 (en) * 1998-08-26 2000-03-09 Integral Umwelt- Und Anlagentechnik Gesellschaft Mbh METHOD FOR REGENERATING USED DeNOx OR DeDIOXIN CATALYTIC CONVERTERS
US6395665B2 (en) * 1998-07-24 2002-05-28 Mitsubishi Heavy Industries, Ltd. Methods for the regeneration of a denitration catalyst
WO2005028103A1 (en) * 2003-09-18 2005-03-31 Hitachi Zosen Corporation Method of regenerating deteriorated catalyst
JP2012210599A (en) * 2011-03-31 2012-11-01 Babcock Hitachi Kk Regeneration method of used denitration catalyst
CN112642496A (en) * 2020-11-18 2021-04-13 苏州西热节能环保技术有限公司 Regenerated catalyst capable of realizing synchronous denitration and VOCs and CO removal and preparation method thereof

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS51129888A (en) * 1975-05-06 1976-11-11 Asahi Glass Co Ltd Process for generating catalists havingbeen used for removing nitorge oxides
JPS5410294A (en) * 1977-06-27 1979-01-25 Mitsubishi Chem Ind Ltd Regenerating method for used vanadium-titania catalyst
JPS58247A (en) * 1981-06-26 1983-01-05 Ngk Insulators Ltd Regenerating method for denitrating catalyst

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS51129888A (en) * 1975-05-06 1976-11-11 Asahi Glass Co Ltd Process for generating catalists havingbeen used for removing nitorge oxides
JPS5410294A (en) * 1977-06-27 1979-01-25 Mitsubishi Chem Ind Ltd Regenerating method for used vanadium-titania catalyst
JPS58247A (en) * 1981-06-26 1983-01-05 Ngk Insulators Ltd Regenerating method for denitrating catalyst

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4847054A (en) * 1986-12-06 1989-07-11 Metallgesellschaft Ag Process for catalytically reducing NO contained in a gas
US6395665B2 (en) * 1998-07-24 2002-05-28 Mitsubishi Heavy Industries, Ltd. Methods for the regeneration of a denitration catalyst
WO2000012211A1 (en) * 1998-08-26 2000-03-09 Integral Umwelt- Und Anlagentechnik Gesellschaft Mbh METHOD FOR REGENERATING USED DeNOx OR DeDIOXIN CATALYTIC CONVERTERS
EP1107824B1 (en) * 1998-08-26 2001-12-05 INTEGRAL UMWELT- UND ANLAGENTECHNIK GESSELLSCHAFT m.b.H. METHOD FOR REGENERATING USED DeNOx OR DeDIOXIN CATALYTIC CONVERTERS
US6484733B2 (en) * 1998-08-26 2002-11-26 Integral Umwelt-Und Anlangentechnik Gesellschaft M.B.H Process for regenerating used deNOx or dedioxin catalytic converters
WO2005028103A1 (en) * 2003-09-18 2005-03-31 Hitachi Zosen Corporation Method of regenerating deteriorated catalyst
JP2012210599A (en) * 2011-03-31 2012-11-01 Babcock Hitachi Kk Regeneration method of used denitration catalyst
CN112642496A (en) * 2020-11-18 2021-04-13 苏州西热节能环保技术有限公司 Regenerated catalyst capable of realizing synchronous denitration and VOCs and CO removal and preparation method thereof
CN112642496B (en) * 2020-11-18 2023-11-10 苏州西热节能环保技术有限公司 Regenerated catalyst capable of realizing synchronous denitration and VOCs (volatile organic compounds) and CO and preparation method thereof

Also Published As

Publication number Publication date
JPH0446621B2 (en) 1992-07-30

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