JPS58153519A - Treatment of gas - Google Patents

Treatment of gas

Info

Publication number
JPS58153519A
JPS58153519A JP57037500A JP3750082A JPS58153519A JP S58153519 A JPS58153519 A JP S58153519A JP 57037500 A JP57037500 A JP 57037500A JP 3750082 A JP3750082 A JP 3750082A JP S58153519 A JPS58153519 A JP S58153519A
Authority
JP
Japan
Prior art keywords
gas
activated carbon
contg
nitrate
cos
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
JP57037500A
Other languages
Japanese (ja)
Other versions
JPH049573B2 (en
Inventor
Hiroshi Nishino
西野 博
Norio Aibe
紀夫 相部
Katsuya Noguchi
野口 勝也
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 JP57037500A priority Critical patent/JPS58153519A/en
Priority to US06/460,045 priority patent/US4556547A/en
Priority to GB08302308A priority patent/GB2114911B/en
Priority to DE3303039A priority patent/DE3303039C2/en
Priority to FR8301439A priority patent/FR2520635B1/en
Publication of JPS58153519A publication Critical patent/JPS58153519A/en
Priority to SG35/88A priority patent/SG3588G/en
Publication of JPH049573B2 publication Critical patent/JPH049573B2/ja
Granted legal-status Critical Current

Links

Abstract

PURPOSE:To remove efficiently H2S and COS contained in a gas, by bringing an inert gas or a reducing gas contg. no oxygen into contact with activated carbon contg. a specified metallic compd.. CONSTITUTION:An inert gas or a reducing gas contg. substantially no oxygen but contg. H2S or COS, such as beverage carbon dioxide, coke oven gas. blast furnace gas, converter gas, cracked petroleum gas, or natural gas, is brought into contact with activated carbon contg. a specified metallic compd. to remove H2S and COS by adsorption. As the specified metallic compd. in this case, sulfate, nitrate, or the like of copper; and carbonate, nitrate, borate, or the like of Li, Na, K, R6, Ca, or the like; and carbonate, sulfate, nitrate, halide, oxide, or the like of at least one of Al, Ti, V, Cr, Mn, Fe, Co, Ni, Zn, Cd, and Pb are used.

Description

【発明の詳細な説明】 本発明は、不活性ガスまえは還元性ガス中の硫化水素、
硫化力〃ボニμを除去するためのブスの処理方法に関す
る。
DETAILED DESCRIPTION OF THE INVENTION The present invention provides hydrogen sulfide in a reducing gas before an inert gas;
This article relates to a method for treating bushes to remove sulfidation power (boniμ).

飲料用の炭酸ガス、コークス炉Iス、高炉Iス、転炉ガ
ス、石油留分熱分解Xス、天然ガスなどには、硫化水素
、硫化iIl&/ボニルなどのイオウ化金物が含まれて
お多、これらイオウ化合物は、微量でも臭気中触謀毒作
用を呈するので、飲料加工、化学反応などの工程で問題
となることが多い。
Beverage carbon dioxide gas, coke oven I gas, blast furnace I gas, converter gas, petroleum fraction pyrolysis gas, natural gas, etc. contain metal sulfides such as hydrogen sulfide and IIl&/bonyl sulfide. These sulfur compounds exhibit a poisonous effect in their odor even in minute amounts, so they often pose a problem in processes such as beverage processing and chemical reactions.

これらのイオウ化合物を論夫するえめに、アルカリ液、
ア〃カッーyアミン液などによる薬液洗浄法あるいは酸
化鉄、酸化T1m、活性#l2tkどを用いる吸着法な
どが提案されているが、除去効率が悪く、特に硫化*e
’ボニpの除去は困難である。
To discuss these sulfur compounds, alkaline solution,
A chemical cleaning method using an amine solution or an adsorption method using iron oxide, T1m oxide, active #l2tk, etc., have been proposed, but the removal efficiency is poor, especially for sulfurized*e.
'Removal of Bonip is difficult.

本発明者らは、このよう&爽情に鑑み、鋭意検討し九結
果、活性炭に銅化金物とアルカリ金属化合物とさらにア
μミニウム、チタニウム、バナジウム、タロムニウム、
マンrye鉄sコバルト。
In view of these circumstances, the inventors of the present invention have conducted intensive studies and found that activated carbon contains copperized metals, alkali metal compounds, aluminum, titanium, vanadium, talomnium, etc.
manrye iron s cobalt.

ニッケル、亜鉛、iIドミウム、tたは鉛の化合物を含
有せしめることに、よって、ガス中の硫化水素、硫化力
μボニ〜を非常に効率よく除去できることを見出し、本
発明を完成し丸。
It was discovered that by containing a compound of nickel, zinc, iI domium, t, or lead, hydrogen sulfide and sulfuric acid μbony in the gas could be removed very efficiently, and the present invention was completed.

すなわち、本発明は、実質的に酸素を含有しない不活性
ガスまたは還元性ガス中の硫化水素および/マエは硫化
カルボ=*(以下イオウ化合物という、)を除去するに
際し、該ガスを■銅化合物、■アルカリ金属化金物およ
び■アルミニウム。
That is, in the present invention, when removing hydrogen sulfide and/or carbo sulfide (hereinafter referred to as sulfur compound) from an inert gas or reducing gas that does not substantially contain oxygen, the gas is converted into a copper compound. , ■ Alkali metalized metal objects and ■ Aluminum.

チタニウム、パナVウム、りDAミクム、マンIン、鉄
、コバ〜ト、ニッケμ、亜鉛、iIドミウムおよび鉛か
らなる群よ)選ばれえ少なくと4一種の金属の化金物(
以下第五金属化金物という)を含有する活性*(以下金
属化金物含有活性炭という、)K接触させることを特徴
とするガスの処理方法である。
Chemicals of at least four selected metals (from the group consisting of titanium, panamium, diamium, manganese, iron, cobalt, nickel, zinc, idomium, and lead)
This is a method for treating a gas, which is characterized in that it is brought into contact with active* (hereinafter referred to as metallized metal-containing activated carbon) containing K (hereinafter referred to as the fifth metallized metal substance).

本発明に使用される活性炭は、石炭、コークス、本脚、
ヤVlフ、樹meどを原料として全知の方法により製造
され丸もので、その比表面積が、200〜2000 m
”/fのものであれば、いかなるものでもよく、そ01
#状は、丸とえば球状9円柱状、破砕状、粉末状、繊維
状などガスの処理方法に応じて適当1にものが使用され
る。
Activated carbon used in the present invention includes coal, coke, main carbon,
It is a round product manufactured by an omniscient method using wood, wood, etc. as raw materials, and its specific surface area is 200 to 2000 m
”/f, any item is fine, so long as it is 01
The # shape may be round, spherical, 9 cylindrical, crushed, powdered, fibrous, etc. depending on the gas processing method.

本発明で用いられる銅化合物としては、たとえば、脚酸
塩、m基性炭鹸塩、硝酸塩、硫酸塩、す7エ、7、al
’:y(5@、@、カイ−1,イ、□。
Examples of the copper compound used in the present invention include podate, m-based carbonate, nitrate, sulfate, s7e, 7, al
':y(5@, @, chi-1, i, □.

無機酸塩tえは無機化金物、ギ酸塩、酢酸塩、Vユウ酸
塩などの有機酸塩などが挙げられる。
Examples of the inorganic acid salt include organic acid salts such as mineralized metals, formates, acetates, and V-oxalates.

Rb、 Caの丸とえば炭酸水素塩、炭酸塩、硝峻塩、
ホウ酸塩、ケイ酸撫、硫酸塩、ハロゲン化物。
Rb, Ca circles such as hydrogen carbonate, carbonate, nitrate salt,
Borates, silicates, sulfates, halides.

水酸化物などの無機酸塩tえは無機化合物、ギ酸填、酢
酸填、Vユウ酸塩、安息香酸塩、フェノ−μ類の塩、ス
ルホン酸類O填などの有機酸塩などが挙けられる。
Inorganic acid salts such as hydroxides include inorganic compounds, organic acid salts such as formic acid salts, acetic acid salts, V oxalates, benzoates, pheno-μ salts, and sulfonic acid salts. .

tえ第ミ金属化金物としては、Al、 Ti、 V。The third metallized metals include Al, Ti, and V.

Or、 Mn、 Fe、 Co、 lli、 Zn、 
Cd、 Pbの一種以上の金属の廣酸塩、硝酸塩、硫酸
樵、リン酸填、ハロゲン化物、アン毫ニウム填、酸化物
、水酸化物などの無機酸塩を走は無機化合物、ギ酸塩。
Or, Mn, Fe, Co, lli, Zn,
Inorganic compounds such as Cd, Pb, chloride, nitrate, sulfuric acid, phosphoric acid, halide, anhydride, oxide, hydroxide, etc. are inorganic compounds, formates.

酢酸塩、Vユウ酸塩などの有機酸塩などが挙げられる。Examples include organic acid salts such as acetate and V-oxalate.

本発明の金属化合物含有活性炭は、九とえばっぎOよう
な方法で調製される。
The metal compound-containing activated carbon of the present invention is prepared by a method similar to Kutobagi O.

(1)活性炭原料に■銅化合“轡、■アルカリ金属化合
物、■ム1.〒1.マ、 Or、 Mn、 Fe、 C
o、 Ni、 Kn、 C(1,Pb ()化金物を添
加し、通常の方法で炭化・賦活する。
(1) Activated carbon raw materials include ■copper compound, ■alkali metal compound, ■mu1.〒1.Ma, Or, Mn, Fe, C
o, Ni, Kn, C(1,Pb()) are added and carbonized and activated using a conventional method.

(2)活性炭原料に■銅化合物を添加し、通常の方法で
炭化・賦活する。得られ九活性炭に■アルカリ金属化合
物と■ム1.〒i、 Y、 Cr、 Mn、 Fe。
(2) ■ Add a copper compound to the activated carbon raw material and carbonize and activate it using a normal method. 1. Add an alkali metal compound and 1. to the obtained nine activated carbon. 〒i, Y, Cr, Mn, Fe.

Co、 Ni、 Zn、 Cd、 Pb ()化合物と
を同時を九は別個に添着し必要に応じて乾燥i九は焼成
する。
Co, Ni, Zn, Cd, Pb (2) compounds are simultaneously and separately applied, dried and fired as necessary.

(3)活性#!原料に■アルカリ金属化合物を添加し、
通常の方法で炭化・賦活する。得られ友活性脚に■銅化
合物と■ムl、 Ti、 Y、 Cr、 Mn、 re
、 G。
(3) Active #! ■ Adding an alkali metal compound to the raw material,
Carbonize and activate using normal methods. The obtained active leg was treated with ■copper compound and ■mul, Ti, Y, Cr, Mn, re
, G.

、 lii、 Zn、 Cd、 Pisの化合物とを同
時まえは別個に添着し、−要に応じて、乾燥を九は焼成
する。
.

(4)活性炭原料に■Al、 Ti、 V、 Cr、 
Mn、 F’e、 Go、 Ni、 Zn、 Cd、 
Pb C)化合物を添加し、通常の方法で炭化・賦活す
る。得られえ活性炭に■銅化合物と■アルカリ金属化合
物とを同時を丸は別個に添着し、必要に応じて乾燥ま九
は焼成する。
(4) Activated carbon raw materials ■Al, Ti, V, Cr,
Mn, F'e, Go, Ni, Zn, Cd,
Pb C) compound is added and carbonized and activated in a conventional manner. 1) Copper compound and 2) alkali metal compound are impregnated simultaneously and separately on the obtained activated carbon, and if necessary, they are dried and fired.

(5)  活性炭に■銅化金物、■アルカリ金属化合物
、■Al、Ti、V、Cr、Mn、T@、Go、lii
、Zn、 Cd、 Pb  の化金物を同時に添着し、
必要に応じて乾燥を九は焼成する。
(5) Activated carbon with ■copper metal compound, ■alkali metal compound, ■Al, Ti, V, Cr, Mn, T@, Go, lii
, Zn, Cd, and Pb are simultaneously attached,
Dry and bake if necessary.

(6)  活性炭に■銅化合物を添着し、乾燥または焼
成し、さらに■アルカリ金属化合物と■ムl、Ti。
(6) A copper compound is impregnated on activated carbon, dried or fired, and an alkali metal compound and Ti are added.

V、 Cr、 Mn、 We、 Go、 Ml、 Zn
、 Cd、 Pbの化金物とを同時または別個に添着し
、必要に応じて乾燥を九紘焼處する。
V, Cr, Mn, We, Go, Ml, Zn
, Cd, and Pb are applied simultaneously or separately, and if necessary, drying and baking are performed.

(7)活性炭に■ア#*l金属化合物な添着し、乾燥を
九は焼成し、さらに■銅化合物と■Al、Ti。
(7) A metal compound is impregnated on activated carbon, dried and calcined, and then a copper compound and Al and Ti are added.

V、Cr、 Mn、 Fe、 Co、 Ni、 Zn、
 Cd、 Pbの化合物とを同時を九は別11に添着し
、必要に応じて乾燥または焼成する。
V, Cr, Mn, Fe, Co, Ni, Zn,
Compounds of Cd and Pb are simultaneously attached to the substrate and dried or fired as required.

(8)活性炭に■ムl、 Ti、 V、 Cr、 Mn
、 1’@。
(8) Activated carbon with ■Mul, Ti, V, Cr, Mn
, 1'@.

Co、 Mi、 Zn、 Cd、 Pb の化合物な添
着し、乾燥または焼成し、さらに■銅化合物と■アルカ
リ金属化合物とを同時または別個に添着し、必要に応じ
て乾燥i先は焼成する。
Compounds of Co, Mi, Zn, Cd, and Pb are impregnated and dried or fired, and (1) a copper compound and (2) an alkali metal compound are applied simultaneously or separately, and if necessary, the first part is fired after drying.

これら調製において、活性炭に金属化金物を添着する方
法として杜、金属化合物を水(酸ま九はアルカリ水溶液
を含む)、各種の溶V&などに溶解ま九は懸濁させ丸液
を活性炭に含浸を丸は散布する方法が考えられる。
In these preparations, the method for impregnating activated carbon with metallized metals is to dissolve the metal compound in water (including alkaline aqueous solutions), various types of solutions, etc., and then impregnate the activated carbon with the liquid. One possible method is to scatter the circles.

また、前記の調製において、乾燥とは、約13−U−℃
以下の温度で、添着活性炭中の水を丸は溶媒を蒸発させ
る工程をいい、を丸焼成とは、約130℃以上の温度で
乾燥しえ添着活性炭を不活性ガス、脚酸Xス、水S駕、
燃焼排Iスなどの雰囲気で加熱し、金属化合物の一部i
えは全部を熱分解させる工程をいう。
In addition, in the above preparation, drying means about 13-U-℃
The process of evaporating the water in the impregnated activated carbon at the following temperature is the process of evaporating the solvent, and firing is the process of evaporating the water in the impregnated activated carbon at a temperature of about 130°C or higher. S-Kan,
Some of the metal compounds are heated in an atmosphere such as combustion exhaust gas.
E refers to the process of thermally decomposing the entire material.

上記方法において、銅化合物、第三金属化合物として酸
化物以外の4のを活性炭に添着し丸場合は、添着後乾燥
まえは焼成などの熱処理をするのがよく、また銅化合物
、第三金属化合物を活性炭に添着して熱処理をしないと
きは、銅化合物、第三金属化合物は酸化物を用いるのが
よい。またアルカリ金属化合物としてその水酸化物、廣
酸塩。
In the above method, if a copper compound or a third metal compound other than an oxide is impregnated onto activated carbon, heat treatment such as firing is preferably performed after impregnation and before drying. When impregnated with activated carbon and not subjected to heat treatment, it is preferable to use an oxide as the copper compound and third metal compound. Also, as alkali metal compounds, its hydroxides and hydrochlorides.

1[脚酸塩以外のものを活性炭に添着し九場合は、添着
後乾燥または焼成などの熱処理をするのがよく、tえア
ルカリ金属化合物を活性炭に添着し先後熱処理をしない
ときはアルカリ金属化合物としては水酸化物、*酸塩ま
九は重炭酸塩を用いるのがよい。
1 [When impregnating activated carbon with something other than podate, it is best to carry out heat treatment such as drying or calcination after impregnation, and when impregnating activated carbon with an alkali metal compound without prior heat treatment. It is best to use hydroxide for the acid, and bicarbonate for the *acid.

金属化合物含有活性炭中の銅化合物の含量は、鋼として
、活性炭1f@、90.IIIIg−原子〜3゜O〜−
原子、好ましくは0.2〜一原子〜2.0岬−原子で、
アルカリ金属化合物の含量は、金属として活性炭1g当
クシ0.1岬−原子3.θ〜一原子、好ましくは0.2
1L−原子〜2.O1F−原子で、また第三金属化合物
の含量は活性炭1g当J)0.111g−原子〜5.0
”f−原子、好ましくtie、2q−原子〜460■〜
原子である。
The content of the copper compound in the metal compound-containing activated carbon is as follows: activated carbon 1f@90. IIIg-atom ~3゜O~-
atoms, preferably from 0.2 to 1 to 2.0 cap-atoms,
The content of the alkali metal compound is 0.1 cap - 3 atoms per gram of activated carbon as metal. θ~1 atom, preferably 0.2
1L-atom ~2. O1F-atom, and the content of the third metal compound is J) 0.111 g-atom to 5.0 per gram of activated carbon.
"f-atom, preferably tie, 2q-atom~460■~
It is an atom.

本発明において用いられる実質的に酸素を含有しない不
活性ガスま九は還元性ガスは、酸素濃度が2v01%以
下のもので、水蒸気濃度がイオウ化合物と等七ル以上の
ものである。これらOガスとして、九とえば廣酸ガメー
、コークス炉Iス、高炉ガス、転炉ガス、石油留分熱分
解ガス、天然ガスなどが挙げられる。
The substantially oxygen-free inert gas or reducing gas used in the present invention has an oxygen concentration of 2% or less and a water vapor concentration of 7% or more, equivalent to that of a sulfur compound. Examples of these O gases include hydrogen gas, coke oven gas, blast furnace gas, converter gas, petroleum fraction pyrolysis gas, and natural gas.

本発明の方法は、前記、で得られた金属化合吻合1 有活性巌にイオウ化合物を含むガスを接触させるととに
よシ行なわれる。接触方法としては、九とえば固定層、
移動層、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、250℃以下、好ましくは0〜150
℃であり、ガスの圧力は50kg/(−一下、好ましく
紘0,1〜40−/lであり、またガスの接触時間は2
5℃、1kgj層算で1/10〜100秒、好ましくは
175〜80秒である。
The method of the present invention is carried out by bringing a gas containing a sulfur compound into contact with the active metal compound anastomosis 1 obtained in the above. As for the contact method, for example, fixed layer,
Known means such as a moving bed and a fluidized bed are used. The contact temperature in this case is 250°C or less, preferably 0 to 150°C.
℃, the pressure of the gas is 50 kg/(-1, preferably 0.1 to 40-40), and the contact time of the gas is 2
The heating time is 1/10 to 100 seconds, preferably 175 to 80 seconds at 5°C and 1 kgj layer count.

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

実施N/ BLOT比表面積1065清27/7の16〜24鳳e
sh (2)活性度ムに所定量の硝酸鋼とアルカリ金属
の硝酸塩とムl、 Cr、 Mn、 Fe、 Co、 
lli、 Zn。
Implementation N/BLOT specific surface area 1065 27/7 16-24
sh (2) Predetermined amounts of nitric acid steel and alkali metal nitrate and mulch, Cr, Mn, Fe, Co,
lli, Zn.

Cd、Pbの硝酸填、硫酸チタンおよび硫酸バナジルと
を溶解しえ水溶液を拘−に散布し良。
Cd and Pb can be filled with nitric acid, titanium sulfate and vanadyl sulfate can be dissolved and an aqueous solution can be widely sprayed.

得られ九添着物50dを4csφの石英ガラス製カフム
に充填し、窒素ガスを線流速10cm/seaで流通し
ながら、昇温速度5tl;/winで加熱し、300℃
で30分間焼成し九。
50 d of the obtained nine impregnated materials were filled into a quartz glass cuff of 4 csφ, heated at a temperature increase rate of 5 tl/win while flowing nitrogen gas at a linear flow rate of 10 cm/sea, and heated to 300°C.
Bake for 30 minutes.

得られ丸触縄中の銅化金物、アpカリ金属化合物および
Al、 Cr、 Mn、 re、 Go、 Ni、 Z
n、 Cd。
Copper metals, alkali metal compounds, and Al, Cr, Mn, re, Go, Ni, and Z in the obtained round rope.
n, Cd.

Pb、 Ti、 V化合物の含量は、第1表に示すよう
に活性炭1g当りいずれも金属として、0.2〜2、O
1l−原子であつ九。
As shown in Table 1, the content of Pb, Ti, and V compounds is 0.2 to 2 as metals per 1 g of activated carbon, and O
1l-atom and nine.

なお、対照として前記と同様な方法で硝酸鋼。As a control, nitric acid steel was prepared in the same manner as above.

アルカリ金属の硝酸塩およびムl、 Cr、 Mn、 
F’s。
Alkali metal nitrates and mul, Cr, Mn,
F's.

Go、 Ni、 Zn、 Cd、 Pb、〒1.v(以
下表中で第三金属という)の化合物の二種類を組合せて
添着し、さらに窒素ガス中、300℃で30分間焼成し
先触縄を調製し丸。
Go, Ni, Zn, Cd, Pb, 〒1. A combination of two types of compounds of V (hereinafter referred to as the third metal in the table) was impregnated and fired at 300°C for 30 minutes in nitrogen gas to prepare a tip rope.

このようにして得られ先触11B−Mの各16sZを1
.6CIlφのガフス製カブ五に充填し、CO5−12
,5ppm含有の50℃のガス(N2−97.5v01
%、 H2O−2,5マロ1%)を線流40cm/ae
cで流通し、COSの破過吸着テメートを行なつ九。結
果は、第1表に示す通)である。
Each 16sZ of the precursors 11B-M obtained in this way was 1
.. Fill a 6CIlφ Kabu 5 made by Gaffs and add CO5-12
, 5ppm containing gas (N2-97.5v01
%, H2O-2,5 malo 1%) at a linear flow of 40 cm/ae
9, which circulates in c and performs breakthrough adsorption temate of COS. The results are shown in Table 1).

実施例λ 実施例1の触媒B−MO各12mgを1.6CIlφの
ガラス製カフムに充填し、HH2S−10pp 含有の
25℃O:If) (N297.5VOIg6. N2
02.5VOI、1 )を線流速40cm/secで流
通し、H,Sノ破過吸着テストを行なつ九。結果は、第
2表に示した。
Example λ 12 mg each of Catalyst B-MO of Example 1 was packed into a 1.6 CIlφ glass cuff, and 25°C O: If) containing HH2S-10pp (N297.5VOIg6.N2
02.5 VOI, 1) was passed at a linear flow rate of 40 cm/sec, and a H, S breakthrough adsorption test was conducted. The results are shown in Table 2.

実施例3 ヤシガフ原料に所定量のLi2CO3,1Ia2804
゜[2804,Rb2804. C82804,HCO
OIIa、 CH3GOOK、  (COOIIa)2
を添加し、混合粉砕し先後、ピッチ類、水などを加えて
練会し、4mwφの円柱状に成型した。このベレットを
650℃で炭化【7さらに900℃で水蒸気賦活し九。
Example 3 Predetermined amount of Li2CO3,1Ia2804 in coconut guff raw material
゜ [2804, Rb2804. C82804, HCO
OIIa, CH3GOOK, (COOIIa)2
was added, mixed and pulverized, and then pitches, water, etc. were added and kneaded, and the mixture was molded into a cylindrical shape of 4 mwφ. This pellet was carbonized at 650°C [7] and then activated with steam at 900°C.

得られ九活性廣は、第3表に示すようにIIIT比表面
積が950〜1150−99で、アルカリ金属化合物の
含量が活性炭1g当当金金属して0゜4〜(16#一原
子であり九。
As shown in Table 3, the obtained nine activated carbon has a IIIT specific surface area of 950 to 1150-99, and the content of alkali metal compound is 0°4 to (16# one atom and .

これら活性炭を16〜24 mashに破砕整粒して、
所定量の硫酸鋼とムl、 Cr、 Mn、 Fs、 C
o。
These activated carbons are crushed and sized to 16-24 mash,
Predetermined amount of sulfuric acid steel and mulch, Cr, Mn, Fs, C
o.

Ni、 Zn、 Cd、 PbO硝鹸填、硫酸チタ7お
よび硫酸バナジ〜を溶解し2九2%の一一水溶液を散布
した。
Ni, Zn, Cd, PbO, titanium sulfate, and vanadium sulfate were dissolved and a 292% aqueous solution was sprayed.

得られた添着物50mを4cvaφの石英ガラス製カラ
ムに充填し、窒素Iスを線流速10cm/sea第1表 第2表 鼻鰺1111[kffAH*8瞼去畠(%)″で流通し
ながら、昇温速度5℃/winで加熱し、350℃で3
0分間焼成し友。触媒中の銅化合物の含量は、活性脚i
f当に金属として1.0111一原子で、ムl、 Or
、 Mn、 re、 Co、 Ml、 Zn、 Cd。
50 m of the obtained impregnated material was packed into a 4 cvaφ quartz glass column, and nitrogen gas was passed through the column at a linear flow rate of 10 cm/sea (Table 1, Table 2). , heated at a temperature increase rate of 5°C/win, and heated at 350°C
A friend who baked for 0 minutes. The content of copper compounds in the catalyst is determined by the active leg i
f is 1.0111 one atom as a metal, ml, Or
, Mn, re, Co, Ml, Zn, Cd.

Pb、 TiおよびV化合物の含量は、活性炭1g当当
金金属して0.5〜一原子であつ九。
The content of Pb, Ti and V compounds is 0.5 to 1 atom per gram of activated carbon.

このようにして得られ先触KN−Uの各15sJを1.
6CIlφのガラス製カフムに充填し、CO3−12,
5pp1m含有の50℃のガス(t12−97.5vO
1%、 H2O−2,5vo1g )を線流速40cs
/aecで流通し、COS破過吸着テストを行ない、結
果を第3表に示した。
Each 15 sJ of the precursor KN-U thus obtained was 1.
Filled with 6CIlφ glass cuff, CO3-12,
Gas at 50℃ containing 5pp1m (t12-97.5vO
1%, H2O-2,5vol 1g) at a linear flow rate of 40cs
/aec, and a COS breakthrough adsorption test was conducted, and the results are shown in Table 3.

実施例刹 実施例1の触媒G7およびH3の各15mを1゜6C膳
φのガフス製カヲムに充填し、008−12.5ppm
含有のガス(Mg−97,5vO1帽a2o−z、 5
vo1g )ヲ25 、60’、 80オ!ヒl 20
℃l’流通し、COSの破過吸着テストを実施し友。な
お、いずれの場合もガス線流速は、25℃換算で40c
a/sea であった。テスト結果を第4表に示した。
Example: 15 m each of catalysts G7 and H3 of Example 1 were packed into a 1°6C diameter kaom made of Gaffs, and 008-12.5 ppm.
Containing gas (Mg-97,5vO1 cap a2oz, 5
vo1g) wo25, 60', 80o! hill 20
℃1' distribution, COS breakthrough adsorption test was carried out. In both cases, the gas linear flow velocity is 40c at 25°C.
It was a/sea. The test results are shown in Table 4.

Claims (1)

【特許請求の範囲】 賓質的に酸素を含有しない不活性ガスtえは還元性ガス
中の硫化水素および/ま丸は硫化カルボニμを診夫する
に際し、#Iスを■鋼化金物、■アμオリ壺属化舎物お
よび■ア々ミニクふ、チタニウム、バナジウム、ターム
ミウム、マンIン。 鉄、コバ〜ト、ニッケ*、li鉛、カドミウムおよび鉛
からなる群よ)選ばれえ少なくとも一種の金属O化合物
を含有する活性炭と接触させることを特徴とするIスO
処瑠方法。
[Claims] When examining hydrogen sulfide and/or carbonyl sulfide in a reducing gas, an inert gas that does not contain oxygen is ■A μ Ori pot belonging to the building and ■ Aminikufu, titanium, vanadium, termium, man I. IO, characterized in that it is brought into contact with activated carbon containing at least one metal O compound selected from the group consisting of iron, cobate, nickel*, li lead, cadmium and lead.
Shoruru method.
JP57037500A 1982-02-01 1982-03-09 Treatment of gas Granted JPS58153519A (en)

Priority Applications (6)

Application Number Priority Date Filing Date Title
JP57037500A JPS58153519A (en) 1982-03-09 1982-03-09 Treatment of gas
US06/460,045 US4556547A (en) 1982-02-01 1983-01-21 Process for treatment of gases
GB08302308A GB2114911B (en) 1982-02-01 1983-01-27 Treating sulpher-containing gases
DE3303039A DE3303039C2 (en) 1982-02-01 1983-01-29 Process for the removal of hydrogen sulfide and / or carbonyl sulfide from gases
FR8301439A FR2520635B1 (en) 1982-02-01 1983-01-31 PROCESS FOR THE TREATMENT OF GASES AND PRODUCTS USED THEREFOR
SG35/88A SG3588G (en) 1982-02-01 1988-01-08 Treatment of sulfur-containing gases

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57037500A JPS58153519A (en) 1982-03-09 1982-03-09 Treatment of gas

Publications (2)

Publication Number Publication Date
JPS58153519A true JPS58153519A (en) 1983-09-12
JPH049573B2 JPH049573B2 (en) 1992-02-20

Family

ID=12499240

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57037500A Granted JPS58153519A (en) 1982-02-01 1982-03-09 Treatment of gas

Country Status (1)

Country Link
JP (1) JPS58153519A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63251496A (en) * 1987-04-08 1988-10-18 Kawasaki Steel Corp Method of purifying gas mainly composed of carbon monoxide
JPS63251497A (en) * 1987-04-08 1988-10-18 Kawasaki Steel Corp Method of purifying gas mainly composed of carbon monoxide
JP2005324155A (en) * 2004-05-17 2005-11-24 Japan Pionics Co Ltd Refining agent and refining method for inert gas
JP2006143788A (en) * 2004-11-17 2006-06-08 National Institute Of Advanced Industrial & Technology Method and system for refining gas
JP2011513061A (en) * 2008-03-12 2011-04-28 ジョンソン、マッセイ、パブリック、リミテッド、カンパニー Desulfurization substance

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4861360A (en) * 1971-10-08 1973-08-28
JPS5348984A (en) * 1976-10-15 1978-05-02 Aichi Prefecture Removing agent of aldehydes* hydrocarbon derivative gases* nitrogen oxides or sulfur compounds in exhaust gases

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4861360A (en) * 1971-10-08 1973-08-28
JPS5348984A (en) * 1976-10-15 1978-05-02 Aichi Prefecture Removing agent of aldehydes* hydrocarbon derivative gases* nitrogen oxides or sulfur compounds in exhaust gases

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63251496A (en) * 1987-04-08 1988-10-18 Kawasaki Steel Corp Method of purifying gas mainly composed of carbon monoxide
JPS63251497A (en) * 1987-04-08 1988-10-18 Kawasaki Steel Corp Method of purifying gas mainly composed of carbon monoxide
JP2005324155A (en) * 2004-05-17 2005-11-24 Japan Pionics Co Ltd Refining agent and refining method for inert gas
JP2006143788A (en) * 2004-11-17 2006-06-08 National Institute Of Advanced Industrial & Technology Method and system for refining gas
JP2011513061A (en) * 2008-03-12 2011-04-28 ジョンソン、マッセイ、パブリック、リミテッド、カンパニー Desulfurization substance

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