JPH09122483A - Absorbent for nitrogen oxide and sulfur oxide - Google Patents

Absorbent for nitrogen oxide and sulfur oxide

Info

Publication number
JPH09122483A
JPH09122483A JP7282759A JP28275995A JPH09122483A JP H09122483 A JPH09122483 A JP H09122483A JP 7282759 A JP7282759 A JP 7282759A JP 28275995 A JP28275995 A JP 28275995A JP H09122483 A JPH09122483 A JP H09122483A
Authority
JP
Japan
Prior art keywords
gypsum
calcium hydroxide
absorbent
acidic gas
potassium carbonate
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
JP7282759A
Other languages
Japanese (ja)
Inventor
Tetsuo Ikehata
徹男 池端
Akira Hashimoto
彰 橋本
Junjiro Awano
順二郎 粟野
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial Co Ltd
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 Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP7282759A priority Critical patent/JPH09122483A/en
Publication of JPH09122483A publication Critical patent/JPH09122483A/en
Pending legal-status Critical Current

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  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Abstract

PROBLEM TO BE SOLVED: To produce an acidic gas absorbent to be reproduced several times to scores of times by impregnating a honeycomb-shaped material formed by active carbon, calcium hydroxide and gypsum with calcium hydroxide solution. SOLUTION: A bonding force is decreased by the variation of structure caused by the reaction of gypsum as an aggregate with potassium carbonate in an acidic gas absorbing material heretofore available. Also, for instance, calcium hydroxide is turned into calcium nitrite through the reaction with nitrogen dioxide and becomes water-soluble and its shape is broken. To avoid the above trouble, potassium carbonate is removed and the required shape is formed, and then impregnation with potassium hydroxide water solution is carried out to control the change of gypsum, and an acidic gas absorption material to be reproduced several times can be manufactured without lowering the absorption performance. Also the number of the reproductions can be improved up to scores of times by adding an inorganic bonding material producing no chemical change.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、大気中の硫黄酸化
物や窒素酸化物の吸収剤として用いられるもので家庭用
空気清浄器や自動車の排気ガスで充満するトンネル内の
ガス中における前記硫黄酸化物や窒素酸化物を除去する
装置等に用いられる。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention is used as an absorbent for sulfur oxides and nitrogen oxides in the atmosphere, and the sulfur contained in the gas in a tunnel filled with exhaust gas from a domestic air cleaner or an automobile. It is used in equipment for removing oxides and nitrogen oxides.

【0002】[0002]

【従来の技術】従来、特開平1−176449号公報や
特開平1−176450号公報に見られるように活性
炭、水酸化カルシウムを主成分とする酸性ガス吸収剤は
提案されているが、石膏が結合剤として用いられてお
り、吸収剤中に混合されている炭酸カリウムや水酸化カ
リウムが高い吸収性を有するために必要であった。
2. Description of the Related Art Conventionally, as disclosed in JP-A-1-176449 and JP-A-1-176450, there have been proposed activated carbon and an acidic gas absorbent mainly containing calcium hydroxide, but gypsum is used. It was used as a binder and was necessary because potassium carbonate and potassium hydroxide mixed in the absorbent have high absorbency.

【0003】また、特公昭58−5699号公報には、
水硬性セメント材やベントナイト等の硬化材を用いた窒
素酸化物除去剤が考案されているが、炭酸塩を含むもの
である。
Further, Japanese Patent Publication No. 58-5699 discloses that
A nitrogen oxide removing agent using a hardening material such as hydraulic cement material or bentonite has been devised, but it contains a carbonate.

【0004】[0004]

【発明が解決しようとする課題】上記、従来技術にみら
れる吸収剤は一度最後まで酸性ガスを吸収すると吸収剤
中に水溶性成分が主体となる。特に炭酸カリウムや水酸
化カリウムを吸収剤中に含む場合、骨剤となるべき石膏
が硫酸カリウムに変化するためさらに、水溶性成分が増
える。そのため吸収したNO2ガスやSO2ガス成分を取
り除くために水に漬けると形状が崩れ再使用することが
できなかった。
SUMMARY OF THE INVENTION In the above-described absorbents of the prior art, once the acidic gas is absorbed to the end, the water-soluble components are mainly contained in the absorbents. In particular, when potassium carbonate or potassium hydroxide is contained in the absorbent, the gypsum to be used as the bone agent is changed to potassium sulfate, which further increases the water-soluble component. Therefore, when it was soaked in water to remove the absorbed NO 2 gas and SO 2 gas components, its shape collapsed and it could not be reused.

【0005】[0005]

【課題を解決するための手段】上記欠点を解消するた
め、炭酸カリウムを除いた状態、あるいは比較的低温で
結合力を有する無機結合剤を用いた状態で、従来の炭酸
カリウムを混合する代わりに水酸化カリウム水溶液をハ
ニカム体形成後に含浸させることで、数回から十数回の
再生が可能な酸性ガス吸収剤を得ることができる。ここ
で、水酸化カルシウムは100℃以上で構造水をなくし
はじめ、580℃以上では完全に酸化カルシウムに変化
するため、比較的低温で製造または使用することが好ま
しい。
In order to solve the above-mentioned drawbacks, instead of mixing conventional potassium carbonate in a state where potassium carbonate is removed or an inorganic binder having a binding force at a relatively low temperature is used, By impregnating the aqueous potassium hydroxide solution after forming the honeycomb body, it is possible to obtain an acidic gas absorbent that can be regenerated several times to ten times or more. Here, since calcium hydroxide begins to lose structural water at 100 ° C. or higher and completely changes to calcium oxide at 580 ° C. or higher, it is preferable to manufacture or use it at a relatively low temperature.

【0006】[0006]

【発明の実施の形態】従来の酸性ガス吸収剤では、骨材
である石膏が炭酸カリウムと反応し硫酸カリウムと炭酸
カルシウムとなり構造の変化により結合力が小さくな
る。また、例えば二酸化窒素との反応吸収において、主
材である水酸化カルシウムも亜硝酸カルシウムに変化
し、水溶性となるため吸収使用後に水に漬けると形状が
崩れる。
BEST MODE FOR CARRYING OUT THE INVENTION In the conventional acid gas absorbent, gypsum as an aggregate reacts with potassium carbonate to form potassium sulfate and calcium carbonate, and the binding force becomes small due to the change in structure. In addition, for example, upon absorption by reaction with nitrogen dioxide, calcium hydroxide, which is the main material, also changes to calcium nitrite and becomes water-soluble, so that the shape collapses when immersed in water after absorption and use.

【0007】そのため、炭酸カリウムを除き必要な形状
を形成後、水酸化カリウム水溶液を含浸させることで石
膏(硫酸カルシウム)の変化を抑え数回の再生が可能な
酸性ガス吸収材を吸収性能を低下させることなく作るこ
とができる。この数回の再生後においては、酸性ガスの
吸収性能の低下よりも形状の崩壊が先に起こる。
[0007] Therefore, after the potassium carbonate is formed into a required shape and then impregnated with an aqueous solution of potassium hydroxide, the change of gypsum (calcium sulfate) is suppressed and the acid gas absorbent which can be regenerated several times is deteriorated in absorption performance. Can be made without After the regeneration of several times, the shape collapse occurs before the acid gas absorption performance deteriorates.

【0008】このことから、さらに化学変化を起こさな
い無機結合材を加えることにより、その再生回数を十数
回にまで高めることも可能になった。
From the above, it has become possible to increase the number of times of regeneration to a dozen or more by adding an inorganic binder which does not cause a chemical change.

【0009】[0009]

【実施例】以下に本発明の実施例について説明する。Embodiments of the present invention will be described below.

【0010】(実施例1)活性炭20wt%・水酸化カ
ルシウム40wt%・石膏40wt%に成型助剤を混合
し1.5mm角の穴がピッチ2.0mmで縦×横に並ん
だハニカム形状に押し出した後、乾燥・不活性雰囲気で
の熱処理を行ってハニカム体を得た。このハニカム体を
15wt%の水酸化カリウム水溶液中に1分間浸して本
発明のハニカム体を得た。
(Example 1) 20 wt% of activated carbon, 40 wt% of calcium hydroxide and 40 wt% of gypsum were mixed with a molding aid, and a 1.5 mm square hole was extruded into a honeycomb shape in which the pitch was 2.0 mm and the holes were arranged vertically and horizontally. After that, heat treatment was performed in a dry / inert atmosphere to obtain a honeycomb body. This honeycomb body was immersed in a 15 wt% potassium hydroxide aqueous solution for 1 minute to obtain a honeycomb body of the present invention.

【0011】このハニカム体の形状を図1に示す。同様
な方法で(表1)に示すハニカム体を製作し、それぞれ
浄化性能・使用可能再生回数に関するデータを取得し
た。その結果を(表2)に示す。
The shape of this honeycomb body is shown in FIG. Honeycomb bodies shown in (Table 1) were manufactured in the same manner, and data regarding the purification performance and the usable number of recycles were obtained for each. The results are shown in (Table 2).

【0012】評価については、全て窒素酸化物の内のN
2を用いた。硫黄酸化物については、化学反応性の面
からも実際にもNO2以上に除去し易いため、浄化率と
して影響の出やすいNO2を用いた。
Regarding the evaluation, all of the nitrogen oxides N
O 2 was used. Regarding sulfur oxides, NO 2 is used because it is easy to remove more than NO 2 actually from the viewpoint of chemical reactivity, so NO 2 which is likely to affect the purification rate was used.

【0013】[0013]

【表1】 [Table 1]

【0014】比較品は、原料混合時に炭酸カリウムを1
0%混合したもので従来の製品である。
The comparative product contains 1% potassium carbonate when the raw materials are mixed.
It is a conventional product with a mixture of 0%.

【0015】使用可能再生回数は、以下の方法により確
認した。 1.サンプルに50ppmのNO2を吸収させる(浄化
率が20%以下になるまで約3時間) 2.1のサンプルを水に1時間漬け水溶性成分を取り除
く 3.2のサンプルを乾燥し15%KOH水溶液を1分間
含浸しサンプルとする1〜3のサイクルをn=5のサン
プルについて確認し、上記2において崩れるまでの回数
を平均化した。
The usable number of times of reproduction was confirmed by the following method. 1. Absorb 50 ppm of NO 2 into the sample (about 3 hours until the purification rate becomes 20% or less) Soak the 2.1 sample in water for 1 hour to remove water-soluble components 3.2 Dry the sample to 15% KOH The cycles of 1 to 3 in which the sample was impregnated with the aqueous solution for 1 minute were confirmed for the sample of n = 5, and the number of times until collapse in 2 was averaged.

【0016】(表2)に上記サンプルの評価結果を示
す。NO2浄化性能は、NO2ガスを湿度が60%になる
ように調整したコンプレッサエアーで希釈しNO2濃度
約10ppmとしたガスを、縦横約10mm長さ20m
mに切断したサンプルに通し、前後の濃度差より浄化率
として表した。測定の空間速度は50,000h-1で行
った。
Table 2 shows the evaluation results of the above samples. The NO 2 purification performance is obtained by diluting NO 2 gas with compressor air adjusted to have a humidity of 60% to give a NO 2 concentration of about 10 ppm, and measuring about 10 mm in length and width and 20 m in length.
It was passed through the sample cut into m and expressed as the purification rate from the difference in concentration before and after. The space velocity of the measurement was 50,000 h -1 .

【0017】[0017]

【表2】 [Table 2]

【0018】上記結果より活性炭が増加すると(No.
1〜4)浄化性能も良くなるが、相対的に他の材料が減
少するため再生回数が減少する傾向にある。但し上記範
囲においては、比較品に比べ再生回数が大きく延びる。
7では、石膏が10%となっているため再生回数が少な
くなっている。また、水酸化カリウム水溶液への浸し時
間が長くなりすぎても浄化性能に影響するが、再生回数
には影響が少ない。
From the above results, when the activated carbon increased (No.
1 to 4) The purification performance is improved, but the number of times of regeneration tends to decrease because other materials decrease relatively. However, in the above range, the number of times of reproduction is greatly increased as compared with the comparative product.
In No. 7, since the gypsum is 10%, the number of times of regeneration is small. Further, if the immersion time in the aqueous potassium hydroxide solution is too long, the purification performance is affected, but the regeneration frequency is not significantly affected.

【0019】(実施例2)実施例1と同様の方法で無機
結合材として含水珪酸マグネシウムアルミニウムを結合
材として追加したハニカムを試作した。この含水珪酸マ
グネシウムアルミニウムはシリカ分60から80wt
%、アルミナ分5から20wt%、マグネシア5から2
0wt%からなる材料であり、300℃〜400℃にお
いて結合力を発揮する材料である。(表3)に各種試作
配合を示す。
(Example 2) In the same manner as in Example 1, a honeycomb was experimentally manufactured by adding hydrous magnesium aluminum silicate as a binder as an inorganic binder. This hydrous magnesium aluminum silicate has a silica content of 60 to 80 wt.
%, Alumina content 5 to 20 wt%, magnesia 5 to 2
It is a material composed of 0 wt% and exhibits a binding force at 300 ° C to 400 ° C. Table 3 shows various trial formulations.

【0020】[0020]

【表3】 [Table 3]

【0021】(表4)に上記サンプルの評価結果を示
す。サンプル及び評価ガス条件等は、実施例1と同じと
した。
Table 4 shows the evaluation results of the above samples. The sample and evaluation gas conditions were the same as in Example 1.

【0022】[0022]

【表4】 [Table 4]

【0023】上記テスト結果より前記結合材を配合する
ことにより再生回数が大きく延びることが明らかであ
る。但し従来の結合材石膏を減少させると浄化性能に大
きく影響がでる。そのため、5〜30wt%の結合材を
使用することが望ましい。
From the above test results, it is clear that the number of times of regeneration is greatly increased by adding the binder. However, if the conventional binder gypsum is reduced, the purification performance will be greatly affected. Therefore, it is desirable to use 5 to 30 wt% of binder.

【0024】(実施例3)実施例2と同様の方法で無機
結合材としてアルミン酸石灰を結合材として追加したハ
ニカムを試作した。このアルミン酸石灰は、アルミナ分
70wt%以上、シリカ0.5wt%以下の材料であ
り、水和反応において結合力を発揮するセメント材料で
ある。(表5)に各種試作配合を示す。
(Example 3) In the same manner as in Example 2, a honeycomb was prepared by adding lime aluminate as a binder as an inorganic binder. This lime aluminate is a material having an alumina content of 70 wt% or more and silica of 0.5 wt% or less, and is a cement material that exhibits a binding force in a hydration reaction. Table 5 shows various trial formulations.

【0025】[0025]

【表5】 [Table 5]

【0026】(表6)に上記サンプルの評価結果を示
す。サンプル及び評価ガス条件等は、実施例1と同じと
した。
Table 6 shows the evaluation results of the above samples. The sample and evaluation gas conditions were the same as in Example 1.

【0027】[0027]

【表6】 [Table 6]

【0028】実施例2の結果とほぼ同様の結果を得た。
このように、比較的低温、すなわち400℃以下で結合
力を有する無機結合材を用いると有効であった。
Results similar to those of Example 2 were obtained.
As described above, it was effective to use an inorganic binder having a binding force at a relatively low temperature, that is, 400 ° C. or lower.

【0029】[0029]

【発明の効果】以上の結果より本発明によれば、NO2
浄化性能を低下させることなくアルカリによる再生使用
が可能なハニカム状吸収剤を得ることが出来る。
From the above results, according to the present invention, NO 2
It is possible to obtain a honeycomb-shaped absorbent that can be reused with an alkali without deteriorating the purification performance.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明の試験に使用したサンプルの斜視図FIG. 1 is a perspective view of a sample used in a test of the present invention.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 活性炭、水酸化カルシウム、石膏から形
成されたハニカム状素材に水酸化カリウム水溶液を含浸
させた窒素酸化物・硫黄酸化物吸収剤。
1. A nitrogen oxide / sulfur oxide absorbent obtained by impregnating a honeycomb material formed of activated carbon, calcium hydroxide, and gypsum with an aqueous solution of potassium hydroxide.
【請求項2】 活性炭、水酸化カルシウム、石膏と無機
結合材とから形成されたハニカム状素材に水酸化カリウ
ム水溶液を含浸させた窒素酸化物・硫黄酸化物吸収剤。
2. A nitrogen oxide / sulfur oxide absorbent obtained by impregnating a honeycomb-shaped material formed of activated carbon, calcium hydroxide, gypsum and an inorganic binder with an aqueous solution of potassium hydroxide.
【請求項3】 無機結合材がアルミン酸石灰、含水珪酸
マグネシウムアルミニウム、あるいはこれらの混合物で
ある請求項2記載の窒素酸化物・硫黄酸化物吸収剤。
3. The nitrogen oxide / sulfur oxide absorbent according to claim 2, wherein the inorganic binder is lime aluminate, hydrous magnesium aluminum silicate, or a mixture thereof.
JP7282759A 1995-10-31 1995-10-31 Absorbent for nitrogen oxide and sulfur oxide Pending JPH09122483A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7282759A JPH09122483A (en) 1995-10-31 1995-10-31 Absorbent for nitrogen oxide and sulfur oxide

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7282759A JPH09122483A (en) 1995-10-31 1995-10-31 Absorbent for nitrogen oxide and sulfur oxide

Publications (1)

Publication Number Publication Date
JPH09122483A true JPH09122483A (en) 1997-05-13

Family

ID=17656702

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7282759A Pending JPH09122483A (en) 1995-10-31 1995-10-31 Absorbent for nitrogen oxide and sulfur oxide

Country Status (1)

Country Link
JP (1) JPH09122483A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4851436A (en) * 1985-08-05 1989-07-25 Merck & Co., Inc. HMG-CoA reductase inhibitors
JP2007222799A (en) * 2006-02-24 2007-09-06 Mitsubishi Heavy Ind Ltd Production method of acidic gas adsorbent
JP2009154047A (en) * 2007-12-25 2009-07-16 Panasonic Corp Acidic gas absorption removal agent, cleaning performance recovering method thereof and acidic gas absorption treatment device or fuel cell system

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4851436A (en) * 1985-08-05 1989-07-25 Merck & Co., Inc. HMG-CoA reductase inhibitors
JP2007222799A (en) * 2006-02-24 2007-09-06 Mitsubishi Heavy Ind Ltd Production method of acidic gas adsorbent
JP2009154047A (en) * 2007-12-25 2009-07-16 Panasonic Corp Acidic gas absorption removal agent, cleaning performance recovering method thereof and acidic gas absorption treatment device or fuel cell system

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