JPS61293546A - Acidic gas removing agent - Google Patents
Acidic gas removing agentInfo
- Publication number
- JPS61293546A JPS61293546A JP60134206A JP13420685A JPS61293546A JP S61293546 A JPS61293546 A JP S61293546A JP 60134206 A JP60134206 A JP 60134206A JP 13420685 A JP13420685 A JP 13420685A JP S61293546 A JPS61293546 A JP S61293546A
- Authority
- JP
- Japan
- Prior art keywords
- acidic gas
- zeolite
- bentonite
- slaked lime
- molding
- 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
Abstract
Description
【発明の詳細な説明】
〈産業上の利用分野〉
本発明は酸性ガス除去剤、更に云えば耐水性、強度及び
酸性ガス除去率に優れた酸性ガス除去剤に関するもので
ある。DETAILED DESCRIPTION OF THE INVENTION <Industrial Application Field> The present invention relates to an acidic gas removing agent, and more particularly to an acidic gas removing agent that is excellent in water resistance, strength, and acidic gas removal rate.
〈従来の技術〉
大気汚染物質の中の代表的なものとして、亜硫酸ガス、
塩化水素ガス、フッ化水素ガス、硝酸ガス等の酸性ガス
が存在するが、従来例えば、活性炭の吸着作用を利用し
て除去する方法、あるいは、アルカリ剤で吸収除去する
方法が代表的に知られている。<Conventional technology> Typical air pollutants include sulfur dioxide gas,
Acidic gases such as hydrogen chloride gas, hydrogen fluoride gas, and nitric acid gas exist, but the typical methods known in the past include removing them by using the adsorption effect of activated carbon, or by absorbing and removing them with an alkaline agent. ing.
〈発明が解決しようとする問題点〉
しかしながら、活性炭j[HC1、HFXHNOs、等
の酸性ガスに対しては吸着能力が低く、活性炭への吸着
の飽和現象や脱着現象があり、又極く稀薄な濃度のガス
に対しては吸着容量が小さいこと等の問題点があった。<Problems to be solved by the invention> However, activated carbon [HC1, HFXHNOs, etc.] has a low adsorption capacity for acidic gases, and there are saturation phenomena and desorption phenomena of adsorption to activated carbon, and extremely dilute There were problems such as low adsorption capacity for concentrated gases.
く問題点を解決するための手段〉
本発明者は上記問題点を解決すべく研究を重ねた結果、
本発明を得た。Means for Solving the Problems〉 As a result of repeated research to solve the above problems, the inventor has found that
The present invention has been obtained.
すなわち、本発明は、ゼオライト、ベントナイト及び消
石灰に結合剤としてコロイダルシリカを配合し成型して
なる酸性ガス除去剤である。That is, the present invention is an acidic gas removing agent formed by blending colloidal silica as a binder with zeolite, bentonite, and slaked lime and molding the mixture.
本発明に適用できるゼオライトとは、結晶性のアルミノ
珪酸塩でいわゆるゼオライト結晶構造を有し、そのカチ
オン交換可能なものである。The zeolite applicable to the present invention is a crystalline aluminosilicate having a so-called zeolite crystal structure and whose cations can be exchanged.
この結晶構造はX線回折によって容易に確認され、実質
的に無定形のアルミノ珪酸塩は原体としては適さない。This crystal structure is easily confirmed by X-ray diffraction, making the substantially amorphous aluminosilicate unsuitable as a bulk material.
この種のゼオライトとしては、例えば、A型、X型、Y
型およびP型ゼオライト、モルデナイト、アナルサイト
、ソーダライト族アルミノ珪酸塩、クリノプチロライト
、エリオナイト又はチャバサイト等があげられ、またこ
れらは合成品又は天然品のいずれであってもよく、さら
に合成品について、その製法は特に限定する必要はない
。Examples of this type of zeolite include A-type, X-type, and Y-type zeolites.
and P-type zeolites, mordenite, analsite, sodalite group aluminosilicates, clinoptilolite, erionite, chabasite, etc., and these may be either synthetic or natural products, and There is no need to particularly limit the manufacturing method for synthetic products.
次に、ベントナイトとに、5iOzとAl2O3を主と
して5i02/A1zOsが約4.4〜77であるモン
モリロナイトを主成分としたもので周知の粘土鉱物であ
る。Next, bentonite is a well-known clay mineral whose main components are montmorillonite, which mainly contains 5iOz and Al2O3 and has a 5i02/A1zOs ratio of about 4.4 to 77.
さらに、消石灰としては、試薬、工業品いずれでも使用
できるが、粘度の細かいものがコロイダルシリカとの反
応性も良く好ましい。例えば工業用消石灰符号(、Tl
5R9001)などが挙げられる。なお、消石灰として
は成型時に水の存在により、水利しうる前駆体としての
生石灰も含まれる。Further, as the slaked lime, either a reagent or an industrial product can be used, but one with a fine viscosity is preferred because it has good reactivity with colloidal silica. For example, industrial slaked lime code (, Tl
5R9001), etc. Note that slaked lime also includes quicklime, which is a precursor that can be used as water due to the presence of water during molding.
また、かかる三成分に結合剤として配合するコロイダル
シリカというのは、シリカゾルとして平均粒子径30m
μ以下のシリカ成分を8102として5〜50重量憾、
通常10〜30重量%をコロイド状に水中分散させたも
のである。In addition, the colloidal silica that is blended as a binder with these three components is a silica sol with an average particle diameter of 30 m.
5 to 50 weight as 8102 silica component less than μ,
Usually 10 to 30% by weight is colloidally dispersed in water.
本発明にかかる酸性ガス除去剤は、その使用目的や汚染
ガスの態様によってその組成は適宜可変しうるものであ
るが、多くの場合、ゼオライトが10〜2[]wt4、
ベントナイトが10として1〜20wt4配合し成型し
てなるものである。The composition of the acidic gas removing agent according to the present invention can be varied depending on the purpose of use and the type of pollutant gas, but in most cases, zeolite is 10 to 2 [wt4],
It is made by blending 1 to 20 wt4 of bentonite as 10 and molding it.
この理由は、上記組成の範囲外では、ガスの除去作用、
成型性および成型物の耐水性など酸性ガス除去剤として
の筒品質のものを得ることが雉かしいことによる。The reason for this is that outside the above composition range, the gas removal effect,
This is because it is difficult to obtain a cylinder quality product that is suitable for use as an acidic gas remover, such as moldability and water resistance of molded products.
例えば、ベントナイトが10wt4未満の場合は、可塑
性が小さくて成型性に欠け、逆に30wt4を越えると
成型物の空孔容積が小さくなる傾向を示して性能を劣化
するし、また、ゼオライトがI O’Wt4以下では、
他の成分を変えても性能的に劣る。これは恐らく、ゼオ
ライト自体の吸着力とゼオライト水の機能が影響してい
るものと思われる。For example, if bentonite is less than 10wt4, it has low plasticity and lacks moldability, whereas if it exceeds 30wt4, the pore volume of the molded product tends to decrease, degrading the performance. 'Wt4 and below,
Even if other ingredients are changed, the performance is inferior. This is probably due to the adsorption power of zeolite itself and the function of zeolite water.
更に、消石灰が50wt4以下では、ガス除去剤として
のライフが短かく、逆に80wt4以上の場合には同様
に空孔容積が小さく酸性ガスとの反応速度が低下する傾
向にあって、いずれも上記範囲外は品質的に劣る。Furthermore, if the slaked lime is less than 50wt4, its life as a gas removal agent will be short, and if it is more than 80wt4, the pore volume will be small and the reaction rate with acidic gas will tend to decrease. Outside the range, the quality is poor.
本発明に係わる酸性ガス除去剤は上記各成分を所定量配
合し、要すれば水を添加して十分に混合、混練した後、
造粒機で造粒する成型したものである。造粒後はそのま
ま使用することもできるが、多くの場合50〜150C
の温度で乾燥させる方が好ましい。The acidic gas removing agent according to the present invention is prepared by blending the above-mentioned components in predetermined amounts, adding water if necessary, thoroughly mixing and kneading, and then
It is a molded product that is granulated using a granulator. After granulation, it can be used as is, but in most cases it is heated at 50 to 150C.
It is preferable to dry at a temperature of .
又、上記造粒物の形状は、球状、円筒状、針状、塊状、
礫状等いずれでも差し支えなく特に制限はない。In addition, the shape of the above granules may be spherical, cylindrical, acicular, lumpy,
There is no particular restriction, as it may be in the form of gravel or the like.
成型したものであるが、高温度下の使用においても造粒
が崩壊せず、長期的に使用に耐える程の耐水性があるが
、これは恐らく、消石灰の一非晶質又は結晶質珪酸カル
シウムを生成せしめこれが、吸着能力を向上させると共
に結合作用を発揮させることによるものと思われる。Although it is molded, the granules do not collapse even when used at high temperatures and are water resistant enough to withstand long-term use, but this is probably due to slaked lime, amorphous or crystalline calcium silicate. This is thought to be due to the fact that the adsorption capacity is improved and the binding effect is exerted.
〈実施例〉
実施例1
ゼオライト :10fi量部
ベントナイト :20
消石灰 =70
コロイダルシリカ : 7
(8102304含有)
上記の配合比の各成分に水52重量部を加えて混合、混
練した後、押し出し成型機で6珊径に造粒し、乾燥して
酸性ガス除去剤100重量部得た。<Example> Example 1 Zeolite: 10 fi parts Bentonite: 20 Slaked lime = 70 Colloidal silica: 7 (Contains 8102304) After adding 52 parts by weight of water to each component in the above blending ratio, mixing and kneading, extrusion molding machine The granules were granulated to a size of 6 mm and dried to obtain 100 parts by weight of an acidic gas removing agent.
(酸性ガス除去試験)
実施例1で得た除去剤を充填カラムに所定量充填し、除
去すべき酸性ガスを一定流量で通過させ、カラムの入口
および出口の酸性ガス濃度を測定して酸性ガスの除去率
を求めた結果を表1に示す。(Acidic gas removal test) A predetermined amount of the removal agent obtained in Example 1 is packed into a packed column, the acidic gas to be removed is passed through at a constant flow rate, and the acidic gas concentration at the inlet and outlet of the column is measured. Table 1 shows the results of determining the removal rate.
表1
(耐水性試験)
実施例1で得た除去剤約11を1001ネスラー管に入
れ、これに水1001Ltを加え、時々液を動かして、
−ケ月間放置したが崩壊は全く見られなかった。Table 1 (Water resistance test) Approximately 11 of the remover obtained in Example 1 was placed in a 1001 Nessler tube, 1001 Lt of water was added thereto, and the liquid was moved occasionally.
- Although it was left for several months, no collapse was observed.
く効 果〉
本発明に係る酸性ガス除去剤は、塩化水素ガス、フッ化
水素ガス、硝酸ガス等の酸性ガスに対して非常に効果的
に高い吸収吸着性能を示すとともに、耐水性に優れ、か
つ粉塵発生のない取扱い容易な一粒強度の大きい工業的
に有用なものである。Effect> The acidic gas removal agent according to the present invention exhibits highly effective absorption and adsorption performance against acidic gases such as hydrogen chloride gas, hydrogen fluoride gas, and nitric acid gas, and has excellent water resistance. Moreover, it is industrially useful because it does not generate dust, is easy to handle, and has a high single-grain strength.
Claims (1)
としてコロイダルシリカを配合し成型してなる酸性ガス
除去剤(1) An acidic gas remover made by blending zeolite, bentonite, and slaked lime with colloidal silica as a binder and molding the mixture.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60134206A JPS61293546A (en) | 1985-06-21 | 1985-06-21 | Acidic gas removing agent |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60134206A JPS61293546A (en) | 1985-06-21 | 1985-06-21 | Acidic gas removing agent |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS61293546A true JPS61293546A (en) | 1986-12-24 |
Family
ID=15122897
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP60134206A Pending JPS61293546A (en) | 1985-06-21 | 1985-06-21 | Acidic gas removing agent |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS61293546A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1999061373A1 (en) * | 1998-05-26 | 1999-12-02 | S.A. Lhoist Recherche Et Developpement | Extrusion product based on hydrated lime |
WO2002016027A1 (en) * | 2000-08-23 | 2002-02-28 | Molecular Products Limited | Improvements in or relating to carbon dioxide absorbent formulations |
WO2002032493A1 (en) * | 2000-10-19 | 2002-04-25 | Intersurgical Limited | Chemical absorbent |
KR100357344B1 (en) * | 2000-03-14 | 2002-10-19 | ||
JP2008289955A (en) * | 2007-05-22 | 2008-12-04 | Nippon Pure Tec Kk | Humidity-conditioning gas-absorbing agent and humidity-conditioning gas-absorbing implement |
US10500541B2 (en) | 2014-10-28 | 2019-12-10 | Intersurgical Ag | Chemical absorbent |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS54152661A (en) * | 1978-05-24 | 1979-12-01 | Taisei Corp | Air pollutant removing method |
JPS60827A (en) * | 1983-06-20 | 1985-01-05 | Nippon Chem Ind Co Ltd:The | Manufacture of air purifying agent |
-
1985
- 1985-06-21 JP JP60134206A patent/JPS61293546A/en active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS54152661A (en) * | 1978-05-24 | 1979-12-01 | Taisei Corp | Air pollutant removing method |
JPS60827A (en) * | 1983-06-20 | 1985-01-05 | Nippon Chem Ind Co Ltd:The | Manufacture of air purifying agent |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1999061373A1 (en) * | 1998-05-26 | 1999-12-02 | S.A. Lhoist Recherche Et Developpement | Extrusion product based on hydrated lime |
BE1011935A3 (en) * | 1998-05-26 | 2000-03-07 | Lhoist Rech & Dev Sa | Extrusion product hydrated lime based. |
KR100357344B1 (en) * | 2000-03-14 | 2002-10-19 | ||
WO2002016027A1 (en) * | 2000-08-23 | 2002-02-28 | Molecular Products Limited | Improvements in or relating to carbon dioxide absorbent formulations |
WO2002032493A1 (en) * | 2000-10-19 | 2002-04-25 | Intersurgical Limited | Chemical absorbent |
US7476641B2 (en) | 2000-10-19 | 2009-01-13 | Intersurgical Ag | Chemical absorbent |
JP2008289955A (en) * | 2007-05-22 | 2008-12-04 | Nippon Pure Tec Kk | Humidity-conditioning gas-absorbing agent and humidity-conditioning gas-absorbing implement |
US10500541B2 (en) | 2014-10-28 | 2019-12-10 | Intersurgical Ag | Chemical absorbent |
GB2531738B (en) * | 2014-10-28 | 2020-08-19 | Intersurgical Ag | Chemical absorbent |
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