JPS6161618A - Harmful gas adsorbent - Google Patents

Harmful gas adsorbent

Info

Publication number
JPS6161618A
JPS6161618A JP59181897A JP18189784A JPS6161618A JP S6161618 A JPS6161618 A JP S6161618A JP 59181897 A JP59181897 A JP 59181897A JP 18189784 A JP18189784 A JP 18189784A JP S6161618 A JPS6161618 A JP S6161618A
Authority
JP
Japan
Prior art keywords
component
gas
activated carbon
halogen
hydrogen halide
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
JP59181897A
Other languages
Japanese (ja)
Other versions
JPH0475049B2 (en
Inventor
Hiroshi Nishino
西野 博
Norio Aibe
紀夫 相部
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.)
Takeda Pharmaceutical Co Ltd
Original Assignee
Takeda Chemical Industries 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 Takeda Chemical Industries Ltd filed Critical Takeda Chemical Industries Ltd
Priority to JP59181897A priority Critical patent/JPS6161618A/en
Priority to US06/653,091 priority patent/US4594231A/en
Publication of JPS6161618A publication Critical patent/JPS6161618A/en
Publication of JPH0475049B2 publication Critical patent/JPH0475049B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Treating Waste Gases (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Carbon And Carbon Compounds (AREA)

Abstract

PURPOSE:To adsorb and remove efficiently by bringing halogen and hydrogen halide in a gas into contact with a specified adsorbent. CONSTITUTION:(1) A zinc compd. and (2) >=1 kind selected from a group consisting of (a)>=1 kind of alkali metal compd., (b)>=1 kind of an alkaline earth metal compd., and (c)>=1 kind among the compds. of Al, Ti, U, Cr, Mn, Fe, Co, Ni, Cd, and Pb are incorporated into activated carbon to obtain an adsorbent. A gas contg. halogen and/or hydrogen halide is brought into contact with the adsorbent to remove the halogen and/or hydrogen halide from the gas. Consequently, halogen and/or hydrogen halide from the gas. Consequently, halogen and hydrogen halide in the gas can be efficiently removed.

Description

【発明の詳細な説明】 本発明はハロゲンおよび/またはハロゲン化水素を除去
するための吸着剤および該水素化合物を含有する気体を
処理する方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an adsorbent for removing halogens and/or hydrogen halides and a method for treating gases containing said hydrogen compounds.

石油化学工場、化学工場のプロセスガス、 1pJ鉄所
などの副生ガス、電解水素、改質用水蒸気、その他各種
の排ガスなどにはハロゲン、ハロゲン化水素が含まれて
おシ、このハロゲン、ハロゲン化水素はg&量でも人体
tc[めて有害であり、装置女どの金属面に対して腐食
作用があ)また触V&毒作用も呈するので、化学度広な
どの工程で問題となることが多い。
Process gases from petrochemical plants and chemical plants, by-product gases from 1pJ steel plants, electrolyzed hydrogen, reforming steam, and various other exhaust gases contain halogens and hydrogen halides. Hydrogen chloride is extremely harmful to the human body, even in large amounts, and has a corrosive effect on metal surfaces of equipment and equipment.Hydrogen is also toxic to the touch, so it often becomes a problem in processes such as chemical conversion. .

ガス中のハロゲン、ハロゲン化水素を除去する方法とし
て、アルカリ性溶液などKよる薬液洗浄法あるいは活性
度などを用いる吸着法などが提案されているが、除去効
果が悪く、効率のよい吸着剤が望まれていた。
As a method for removing halogens and hydrogen halides from gases, chemical cleaning methods using K such as alkaline solutions or adsorption methods using activity etc. have been proposed, but the removal effects are poor and efficient adsorbents are desired. It was rare.

本発明者らは、このような実情に鑑み、鋭意検討した結
果、活性炭に亜鉛化合物とアルカリ金属化合物、アルカ
リ土類金属化合物、 Al、 Ti、 v。
In view of these circumstances, the inventors of the present invention have conducted intensive studies and found that activated carbon contains a zinc compound, an alkali metal compound, an alkaline earth metal compound, Al, Ti, and v.

Cr、 Mn、 Fe、 Co、 Ni、 Cd、 P
b  の金属化合物を含有せしめることによって、ガス
中のハロゲン、ハロゲン化水素を非常に効率よく除去で
きることを見出し、本発明を完成した。
Cr, Mn, Fe, Co, Ni, Cd, P
The present invention was completed based on the discovery that halogens and hydrogen halides in the gas can be removed very efficiently by containing the metal compound b.

すなわち本発明は、 L(1)  亜鉛化合物と (2)(a)アルカリ金属化合物の一種以上。That is, the present invention L(1) Zinc compound and (2) (a) One or more alkali metal compounds.

(b)アルカリ土類金属化合物の一種以上および (c)Al、 Ti、 V、 Or、 IJn、 F’
e、 Co、 Ni。
(b) one or more alkaline earth metal compounds and (c) Al, Ti, V, Or, IJn, F'
e, Co, Ni.

CdおよびPbの化合物の一種以上からなる群から選ば
れた(a) 、 (bl 、 (c)の一種以上とを活
性炭に含有せしめてなるハロゲンおよび/またはハロゲ
ン化水素を除去するための吸着剤Z ハロゲンおよび/
またはハロゲン化水素を含有する気体を、 (1)亜鉛化合物(以下第一成分ということもある)。
An adsorbent for removing halogen and/or hydrogen halide, comprising activated carbon containing one or more of (a), (bl, and (c)) selected from the group consisting of one or more of Cd and Pb compounds. Z halogen and/or
Or a gas containing hydrogen halide: (1) Zinc compound (hereinafter sometimes referred to as the first component).

(2)(a)アルカリ金属化合物の一種以上。(2) (a) One or more alkali metal compounds.

(b)アルカリ土類金属化合物の一種以上および (c)An、 Ti、 ’i、 Cr、 1ion、 
Fe、 Co、 Ni。
(b) one or more alkaline earth metal compounds; and (c) An, Ti, 'i, Cr, 1ion,
Fe, Co, Ni.

CdおよびPbの化合物の一種以上からなる群から選ば
れた(a) 、 (b) 、 (c)の一種以上(以下
第二成分ということもある) とを活性炭に含有せしめてなる吸着剤に接触させること
を特徴とする該気体からハロゲンおよび/またはハロゲ
ン化水素を除去する方法 である。
An adsorbent comprising activated carbon containing one or more of (a), (b), and (c) (hereinafter also referred to as the second component) selected from the group consisting of one or more of Cd and Pb compounds. This is a method for removing halogen and/or hydrogen halide from the gas, which is characterized by contacting the gas.

本発明の吸着剤は活性炭に前記第一成分および第二成分
を含有せしめることによって製造することができる。
The adsorbent of the present invention can be manufactured by incorporating the first component and the second component into activated carbon.

この場合に用いられる活性炭は、石炭、コークス、木炭
、キンガラ。樹脂などを原料として公知の方法により製
造されたもので、その比表面積が200〜2000 m
2/ 9のものであれば、いかなるものでもよく、その
形状はたとえば球状9円柱状、破砕状、粉末状、R雄状
などガスの処理方法に応じて3汐なものが使用される。
The activated carbons used in this case are coal, coke, charcoal, and Kingara. Manufactured by a known method using resin or the like as a raw material, and has a specific surface area of 200 to 2000 m
Any material with a diameter of 2/9 may be used, and its shape may be, for example, spherical, 9 cylindrical, crushed, powdered, or R-shaped, depending on the gas processing method.

本発明において第一成分として用いられる亜鉛化合物と
しては、たとえば炭酸塩、塩基性炭酸塩、硝酸塩、硫酸
塩、リン酸塩、ケイ酸塩、ハロゲン化物、酸化物、水酸
化物などの無機酸塩または無機化合物、ギtf!l塊、
ap酸塩、シュウ酸塩などの有機酸塩などが挙げられる
Examples of the zinc compound used as the first component in the present invention include inorganic acid salts such as carbonates, basic carbonates, nitrates, sulfates, phosphates, silicates, halides, oxides, and hydroxides. Or inorganic compounds, Gitf! l lump,
Examples include organic acid salts such as ap acid salts and oxalate salts.

第二成分の一つであるアルカリ金属化合物としては、L
i、 Na、 K、 Rh、 Csのたとえば炭酸水素
塩、炭酸塩、硝酸塩、ホウ酸塩、ケイ酸塩、硫酸塩、ハ
ロゲン化物、水酸化物などの無機化合物。
As an alkali metal compound which is one of the second components, L
Inorganic compounds such as bicarbonates, carbonates, nitrates, borates, silicates, sulfates, halides, and hydroxides of i, Na, K, Rh, and Cs.

ギ酸塩、酢酸塩、シュウ酸塩、安息香酸塩、フェノ−μ
類の塊、スルホン酸類の塩などの有機酸塩などが挙げら
れる。
Formate, acetate, oxalate, benzoate, pheno-μ
and organic acid salts such as sulfonic acid salts.

またもう一つの第二成分であるアルカリ土類金属化合物
としては、Bθ、 Mg、 Ca、’SrおよびBaの
たとえば炭酸塩、硝酸塩、硫酸塩、リン酸塩、ハロゲン
化物、酸化物、水酸化物などの無機酸塩または無機化合
物、ギ酸塩、酢酸塩、シュウ酸塩などの有機酸塩などが
あげられる。
Examples of alkaline earth metal compounds that are another second component include carbonates, nitrates, sulfates, phosphates, halides, oxides, and hydroxides of Bθ, Mg, Ca, 'Sr, and Ba. Examples include inorganic acid salts or inorganic compounds such as, and organic acid salts such as formates, acetates, and oxalates.

池の第二放物であるAl、 Ti、 V、 Cr、 I
n。
The second parabola of the pond is Al, Ti, V, Cr, I
n.

F’θ、 Co、 Ni、 Cd、 Pbの化合物とし
てはこれらの金属の炭酸塩、炭酸水素塩、硝酸塩、ホウ
酸塩、ケイ酸塩、硫酸塩、リン酸塩、ハロゲン化物。
Compounds of F'θ, Co, Ni, Cd, and Pb include carbonates, hydrogen carbonates, nitrates, borates, silicates, sulfates, phosphates, and halides of these metals.

水酸化物、アンモニウム塩、酸化物など一0無機酸塩ま
たは無機化合物、ギ酸塩、酢酸塩、Vユウ酸塩、安息香
酸塩、フェノ−μ類の塩、スルホン酸類の塩などの有機
酸塩などが挙げられる。
Inorganic acid salts or inorganic compounds such as hydroxides, ammonium salts, oxides, organic acid salts such as formates, acetates, V oxalates, benzoates, salts of pheno-μ, salts of sulfonic acids, etc. Examples include.

本発明の吸着剤は活性炭に第一成分および第二成分の双
方を含有せしめたものであるが、この場合、第二成分と
して、アルカリ金属化合物〔以下成分(a)ということ
もある〕単独、アルカリ土類金属化合物〔以下成分(b
)ということもある〕単独またはAl、 Cr、 Ti
、 ’Y、 Mn、 Te、 Co、 Ni、 Cd。
The adsorbent of the present invention is one in which activated carbon contains both a first component and a second component. In this case, the second component is an alkali metal compound (hereinafter also referred to as component (a)) alone, Alkaline earth metal compound [component (b)
)] alone or Al, Cr, Ti
, 'Y, Mn, Te, Co, Ni, Cd.

Pbの化合物〔以下成分(C)ということもちる〕単独
を含有せしめたものであってもよいが、これらのうち成
分(a)と成分(b)、成分(b)と成分(c)、また
は成分(c)と成分(a)のように二種の成分を含有せ
しめたものでもよく、成分(a)、成分(b)および成
分(c)の三種の成分を同時に含有せしめたものでもよ
い。
Pb compounds [hereinafter also referred to as component (C)] may be contained alone, but among these, component (a) and component (b), component (b) and component (c), Alternatively, it may contain two types of components such as component (c) and component (a), or it may contain three types of components such as component (a), component (b), and component (c) at the same time. good.

また第一成分として二種以上の化合物を含有せしめたも
のでもよく、第二成分として、たとえば成分(a)内の
二種の異なった成分を含有せしめるというように同種の
成分内の二種以上の異なった成分を含有せしめたもので
もよい。
Furthermore, the first component may contain two or more kinds of compounds, and the second component may contain two or more kinds of the same component, such as containing two different kinds of components in component (a). It may also contain different components.

金属化合物含有活性炭中の第一成分の含量は活性I#1
g当シ金属として0.1q−原子〜3.0ダー原子、好
ましくは0.2 #一原子〜20キー原子であシ、第二
成分の含量は活性炭1g当当金金属して0.1ダー原子
〜5.01’/一原子、好ましくはα2η一原子〜4.
0!一原子である。
The content of the first component in the metal compound-containing activated carbon is active I#1
The content of the second component is 0.1q to 3.0 atoms, preferably 0.2 to 20 key atoms, based on the metal per gram of activated carbon, and the content of the second component is 0.1 q-atoms to 3.0 atoms per gram of activated carbon. Atom ~ 5.01'/one atom, preferably α2η one atom ~ 4.
0! It is one atom.

本発明の吸着剤は活性度に各成分を担持もしくは添着せ
しめたものでもよく、また活性炭原料に各成分を添加し
たのち、これを賦活して得られるものでもよい。また第
一成分、第二成分の一部を活性炭原料に添加してこれを
賦活し、これに残シの成分を添着せしめたものでもよい
。各成分を活性炭に添着する場合は、添着後乾燥または
焼成するのがよい。
The adsorbent of the present invention may be one in which each component is supported or impregnated to a certain degree of activity, or it may be obtained by adding each component to an activated carbon raw material and then activating this. Alternatively, a part of the first component and the second component may be added to the activated carbon raw material to activate it, and the remaining components may be impregnated therewith. When each component is impregnated onto activated carbon, it is preferable to dry or bake it after impregnation.

活性炭に各成分t−添着する方法としては、各成分を水
(酸またはアルカリ水溶液を含む)、各種の溶媒などに
溶解または懸濁させた液を活性炭に含浸または散布する
方法が考えられる。また、前記の調製法に訃いて、乾燥
は、約130℃以下の温度で、添着活性炭中の水または
溶媒を蒸発させる工程をいい、また焼成は、約130℃
以上の温度で乾燥したm着活性炭を不活性ガス、炭酸ガ
ス、水魚9C2燃焼排ガスなどの雰囲気で加熱し、金属
化合物の一部また社会部を熱分解させる工程をいう。
A possible method for impregnating each component onto activated carbon is to impregnate or spray activated carbon with a solution in which each component is dissolved or suspended in water (including an aqueous acid or alkali solution), various solvents, or the like. In addition, in the above preparation method, drying refers to a step of evaporating water or solvent in the impregnated activated carbon at a temperature of about 130°C or less, and calcination refers to a step of evaporating water or solvent in the impregnated activated carbon at a temperature of about 130°C or less.
This is a process in which the m-adhered activated carbon dried at the above temperature is heated in an atmosphere of inert gas, carbon dioxide, waterfish 9C2 combustion exhaust gas, etc., to thermally decompose some of the metal compounds and social parts.

上記方法において、第一成分、第二成分(ただしアルカ
リ金属化合物を除く)として酸化物以外のものを活性炭
に添着した場合は、添着後乾燥または焼成など熱処理す
るのがよく、また第一成分、第二成分(ただしアルカリ
金ハ化合物を除く)を活性度にm着して熱処理をしない
ときは、第一成分、第二成分(ただしアルカリ金属化合
物を除く)は酸化物を用いるのがよい。第二成分として
アルカリ金属の水酸化物、炭酸塩、Ti次酸塩以外のア
ルカリ金属化合物を活性炭に添着した場合には添着後乾
燥または焼成などの熱処理をするのがよく、アルカリ金
属化合物をf!At/?したのち熱処理をしない場合に
はアルカリ金属化合物として水酸化物1次酸塩、!!炭
酸塩を用いるのがよい。
In the above method, when substances other than oxides are impregnated onto activated carbon as the first component and second component (excluding alkali metal compounds), it is preferable to heat-treat the activated carbon by drying or firing after impregnation. When the second component (excluding the alkali metal compound) is not heat-treated with high activity, it is preferable to use an oxide as the first component and the second component (excluding the alkali metal compound). When an alkali metal compound other than an alkali metal hydroxide, carbonate, or Ti subacid is impregnated onto activated carbon as a second component, it is recommended to perform heat treatment such as drying or calcination after impregnation. ! At/? If no heat treatment is performed after that, the primary acid salt of hydroxide is used as an alkali metal compound,! ! It is better to use carbonate.

本発明において、ハロゲンとはF2.C1□、 Br2
および工2であシ、ハロゲン化水素とはHF’、 HC
I、 HBr  および■工である。
In the present invention, halogen refers to F2. C1□, Br2
and 2, hydrogen halides are HF', HC
I, HBr and ■Eng.

本発明を用いてガス中のハロゲン、ハロゲン化水素を除
去するには、ハロゲン、ハロゲン化水素を含有するガス
と吸着剤とを接触させればよい。
In order to remove halogen and hydrogen halide from a gas using the present invention, it is sufficient to bring the gas containing halogen and hydrogen halide into contact with an adsorbent.

接触方法としては、たとえば固定層、移*[。Examples of contact methods include fixed layer, transfer*[.

流動層などの公知の手段が用いられる。この場合の接触
温度は、600℃以下、好ましくは0〜300℃であり
、圧力は3001177cm2以下、好ましくは0.1
〜250 kO/ ctx2である。また接触時間は2
5℃、1に97−換算で1710〜100秒、好ましく
は175〜80秒である。
Known means such as a fluidized bed can be used. In this case, the contact temperature is 600°C or less, preferably 0 to 300°C, and the pressure is 3001177cm2 or less, preferably 0.1
~250 kO/ctx2. Also, the contact time is 2
5° C., 1710 to 100 seconds, preferably 175 to 80 seconds, based on 1:97.

以下に実施例を挙げて本発明をよ)具体的に説明する。EXAMPLES The present invention will be explained in more detail below with reference to Examples.

実施例I BET比表面積1150 m2/9016〜24mes
hの活性炭AQに所定量の第一成分(硝酸亜鉛)と第二
成分(アルカリ金属の硝酸塩、アルカリ土類金属の硝酸
塩、およびAユ、 Ti、 V、 Cr。
Example I BET specific surface area 1150 m2/9016~24mes
A predetermined amount of the first component (zinc nitrate) and second component (alkali metal nitrate, alkaline earth metal nitrate, and A, Ti, V, and Cr) are added to the activated carbon AQ of h.

In、 Fa、 Co、 Hl、 Cd、 Pbの硝酸
塩(vのみは硫酸塩))とを溶解した水溶液を均一に散
布した。
An aqueous solution containing In, Fa, Co, Hl, Cd, and Pb nitrates (v is a sulfate) was uniformly sprayed.

得られた添着物50ytlを4cxφの石英ガラス製カ
ラムに充填し、窒素ガスを線流速10em/secで流
通しなから昇温速度5℃7’ win  で加熱し、3
00℃で30分tIJJ焼成した。
50 ytl of the obtained impregnated material was packed into a 4cxφ quartz glass column, and heated at a temperature increase rate of 5°C 7'win while flowing nitrogen gas at a linear flow rate of 10em/sec.
It was baked at 00° C. for 30 minutes.

得られ九吸着剤中の各金属化合物の含量は、第1表に示
すように、活!l:AW1g当シそれぞれ金属として0
.2〜2.01N−原子であった。
The content of each metal compound in the nine adsorbents obtained is as shown in Table 1. l: AW1g each as metal 0
.. It was 2 to 2.01 N-atoms.

なお、対照として、前述と同様の方法で活性炭AQ に
各金属の硝酸塩を単独で添着し、さらに窒素ガス中、3
00℃で30分間焼成した吸着剤を調製した。
As a control, activated carbon AQ was impregnated with nitrate of each metal alone in the same manner as described above, and further impregnated with nitrate of each metal in nitrogen gas for 30 minutes.
An adsorbent was prepared which was calcined at 00°C for 30 minutes.

このようにして得られた吸着剤の各15ゴを1,6aφ
のガフス製カラムに充填し、IlICl−20ppおよ
びC:B2−10 P 1) m含有のガス(N2−9
7.5vo1%、 H2O−Z、 5 vo1%)を線
流速40w/sec (30℃換算)、温度200℃で
流通し、HCl−Cl2(全C1換X)の除去率の経時
変化を調べ結果を第1表に示した。
Each 15 pieces of the adsorbent thus obtained was divided into 1.6aφ
A gas (N2-9
7.5vo1%, H2O-Z, 5vo1%) was passed at a linear flow rate of 40w/sec (30℃ conversion) and a temperature of 200℃, and the change in removal rate of HCl-Cl2 (total C1 conversion are shown in Table 1.

実施例2 実施例1の吸着剤A□、 AI、 A3. Ag、 B
2゜B3・B4・C19C6・C9・Dl、B2・B3
・B6・DBおよびDloの各15dをL61Jφのガ
ラス製カフムに充填し、HHCl−20ppおよびCC
12−1Qpp含有の30℃のガス(B2−8 vo1
%。
Example 2 Adsorbents A□, AI, A3. of Example 1. Ag, B
2゜B3・B4・C19C6・C9・Dl, B2・B3
・Fill 15d each of B6, DB and Dlo into a L61Jφ glass cuff, and add 20pp of HHCl and CC.
30°C gas containing 12-1Qpp (B2-8 vol.
%.

N292VO1%)を線流速40em/sea  で流
通し、HCl−Cl2(全C1換算)の除去率の経時変
化を調べ結果を第2表に示した。
N292VO1%) was passed through the tube at a linear flow rate of 40 em/sea, and the change over time in the removal rate of HCl-Cl2 (in terms of total C1) was investigated. The results are shown in Table 2.

第2表 実施例3 実施例1の吸治剤A□、 Al、 A3. B2. C
6゜B3およびDloの各15gttl−1.6c肩φ
のガラス製カラムに充填し、HHCl−20pp、0O
12−10pp含有のガス(N2−97.5vo1%、
H2O−15vo1%) 、HHBr−20pp、BB
r2−1Opp含有のガス([2−97,5vo1%、
 Tl2O−Z5vo1%)1.およびHI  −20
ppm 、HI2−10pp含有のガス(B2−97.
5vo1%。
Table 2 Example 3 Absorption agent A□ of Example 1, Al, A3. B2. C
6゜B3 and Dlo each 15gttl-1.6c shoulder φ
Filled a glass column with HHCl-20pp, 0O
Gas containing 12-10pp (N2-97.5vo1%,
H2O-15vo1%), HHBr-20pp, BB
r2-1Opp-containing gas ([2-97,5vo1%,
Tl2O-Z5vo1%)1. and HI-20
ppm, HI2-10pp containing gas (B2-97.
5vo1%.

B20−Z5vo1%)をそれぞれ纏流速4Qem/s
ea (30℃換算)、温度250℃で流通し、HCl
−Cl2(全C1換算) HBr Br2 (全Br換
算)および)II−工2(全Ia算)がカラムからリー
クするまでの時間(それぞれの除去率が95%に達する
までの時間)を求め、結果を第3表にまとめた。
B20-Z5vo1%) respectively at a flow rate of 4Qem/s
ea (30℃ conversion), distributed at a temperature of 250℃, HCl
-Cl2 (total C1 conversion) HBr Br2 (total Br conversion) and )II-Cl2 (total Ia calculation) to find the time until it leaks from the column (time until each removal rate reaches 95%), The results are summarized in Table 3.

第3表Table 3

Claims (1)

【特許請求の範囲】 1、(1)亜鉛化合物と (2)(a)アルカリ金属化合物の一種以上、 (b)アルカリ土類金属化合物の一種以上 および (c)Al、Ti、V、Cr、Mn、Fe、Co、Ni
、CdおよびPbの化合物の一種以上からなる群から選
ばれた(a)、(b)、(c)の一種以上とを活性炭に
含有せしめてなるハロゲンおよびまたはハロゲン化水素
を除去するための吸着剤2、ハロゲンおよび/またはハ
ロゲン化水素を含有する気体を、 (1)亜鉛化合物と (2)(a)アルカリ金属化合物の一種以上、 (b)アルカリ土類金属化合物の一種以上 および (c)Al、Ti、V、Cr、Mn、Fe、Co、Ni
、CdおよびPbの化合物の一種以上からなる群から選
ばれた(a)、(b)、(c)の一種以上とを活性炭に
含有せしめてなる吸着剤に接触させることを特徴とする
該気体からハロゲンおよび/またはハロゲン化水素を除
去する方法
[Claims] 1. (1) a zinc compound and (2) (a) one or more alkali metal compounds, (b) one or more alkaline earth metal compounds, and (c) Al, Ti, V, Cr, Mn, Fe, Co, Ni
Adsorption for removing halogen and/or hydrogen halide, comprising activated carbon containing one or more of (a), (b), and (c) selected from the group consisting of one or more of Cd and Pb compounds. Agent 2, a gas containing halogen and/or hydrogen halide, (1) a zinc compound, (2) (a) one or more alkali metal compounds, (b) one or more alkaline earth metal compounds, and (c) Al, Ti, V, Cr, Mn, Fe, Co, Ni
The gas is brought into contact with an adsorbent made of activated carbon containing one or more of (a), (b), and (c) selected from the group consisting of one or more of the following compounds: , Cd, and Pb. Method for removing halogen and/or hydrogen halide from
JP59181897A 1983-09-22 1984-08-30 Harmful gas adsorbent Granted JPS6161618A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP59181897A JPS6161618A (en) 1984-08-30 1984-08-30 Harmful gas adsorbent
US06/653,091 US4594231A (en) 1983-09-22 1984-09-21 Method for removal of poisonous gases

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59181897A JPS6161618A (en) 1984-08-30 1984-08-30 Harmful gas adsorbent

Publications (2)

Publication Number Publication Date
JPS6161618A true JPS6161618A (en) 1986-03-29
JPH0475049B2 JPH0475049B2 (en) 1992-11-27

Family

ID=16108793

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59181897A Granted JPS6161618A (en) 1983-09-22 1984-08-30 Harmful gas adsorbent

Country Status (1)

Country Link
JP (1) JPS6161618A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH05103946A (en) * 1990-08-03 1993-04-27 Internatl Business Mach Corp <Ibm> Combination structure of housing means and chemical filter assembly, magnetic writing storage device and single material
JPH09267027A (en) * 1996-03-29 1997-10-14 Japan Pionics Co Ltd Purifying agent for harmful gas
WO2000016881A1 (en) * 1998-09-22 2000-03-30 Japan Pionics Co., Ltd. Purifying agent and purification method for halogen-containing exhaust gas
JP2000157836A (en) * 1998-09-22 2000-06-13 Japan Pionics Co Ltd Cleaning agent for halogen series exhaust gas and its cleaning method
JP2001338910A (en) * 2000-05-26 2001-12-07 Showa Denko Kk Abatement agent for halogen type gas, abatement method and its use
JP2014502208A (en) * 2010-11-08 2014-01-30 スリーエム イノベイティブ プロパティズ カンパニー Filter medium containing zinc oxide and method for forming the same
JP2020515403A (en) * 2017-05-17 2020-05-28 インテグリス・インコーポレーテッド Fluidized granule absorption bed filter

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH05103946A (en) * 1990-08-03 1993-04-27 Internatl Business Mach Corp <Ibm> Combination structure of housing means and chemical filter assembly, magnetic writing storage device and single material
JPH09267027A (en) * 1996-03-29 1997-10-14 Japan Pionics Co Ltd Purifying agent for harmful gas
WO2000016881A1 (en) * 1998-09-22 2000-03-30 Japan Pionics Co., Ltd. Purifying agent and purification method for halogen-containing exhaust gas
JP2000157836A (en) * 1998-09-22 2000-06-13 Japan Pionics Co Ltd Cleaning agent for halogen series exhaust gas and its cleaning method
US6325841B1 (en) * 1998-09-22 2001-12-04 Japan Pionics., Ltd. Purifying agent and purification method for halogen-containing exhaust gas
JP2001338910A (en) * 2000-05-26 2001-12-07 Showa Denko Kk Abatement agent for halogen type gas, abatement method and its use
JP2014502208A (en) * 2010-11-08 2014-01-30 スリーエム イノベイティブ プロパティズ カンパニー Filter medium containing zinc oxide and method for forming the same
JP2020515403A (en) * 2017-05-17 2020-05-28 インテグリス・インコーポレーテッド Fluidized granule absorption bed filter

Also Published As

Publication number Publication date
JPH0475049B2 (en) 1992-11-27

Similar Documents

Publication Publication Date Title
EP0121339B1 (en) Method for removal of poisonous gases
US4594231A (en) Method for removal of poisonous gases
US4210628A (en) Removal of nitrogen oxides
JPH0424094B2 (en)
JPH02303539A (en) Production method of carrier catalyser to oxidize co, carrier catalyser and co-oxidation by contacting method
JPS59160534A (en) Adsorbent for mercury vapor and treatment of mercury vapor-containing gas
JPS6161618A (en) Harmful gas adsorbent
JPH03106419A (en) Treatment process for gas containing fluorocarbon and catalyst for decomposing fluorocarbon
JPH0464734B2 (en)
JPH0424093B2 (en)
JPH0424092B2 (en)
JPH0857323A (en) Catalyst for decomposition of volatile organic halogen compound and production thereof
JPH049573B2 (en)
JPS6120330B2 (en)
JPH049574B2 (en)
JPS58132085A (en) Treatment of gas
JP3362918B2 (en) Exhaust gas purification method
JPH0153087B2 (en)
JPH0457368B2 (en)
EP3984623A1 (en) Nitrogen oxide absorbent slurry, preparation method therefor and use method thereof
JPS62193633A (en) Reducing agent for nitrogen oxide
JPS62286525A (en) Method for purifying exhaust gas
RU2088563C1 (en) Method of refining 1,1,1,2-tetrafluoroethane from unsaturated halogen-containing impurity
JPS58156345A (en) Adsorbent for mercury vapor
JPH0238255B2 (en) FUHOWATANKASUISOKYUSHUBUNRIZAINOSEIZOHO

Legal Events

Date Code Title Description
EXPY Cancellation because of completion of term