Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPH0322201B2 - - Google Patents
[go: Go Back, main page]

JPH0322201B2 - - Google Patents

Info

Publication number
JPH0322201B2
JPH0322201B2 JP58035059A JP3505983A JPH0322201B2 JP H0322201 B2 JPH0322201 B2 JP H0322201B2 JP 58035059 A JP58035059 A JP 58035059A JP 3505983 A JP3505983 A JP 3505983A JP H0322201 B2 JPH0322201 B2 JP H0322201B2
Authority
JP
Japan
Prior art keywords
component
activated carbon
compounds
compound
metal compound
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.)
Expired - Lifetime
Application number
JP58035059A
Other languages
Japanese (ja)
Other versions
JPS59160584A (en
Inventor
Hiroshi Nishino
Norio Aibe
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 JP3505983A priority Critical patent/JPS59160584A/en
Publication of JPS59160584A publication Critical patent/JPS59160584A/en
Publication of JPH0322201B2 publication Critical patent/JPH0322201B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Treatment Of Liquids With Adsorbents In General (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Liquid Carbonaceous Fuels (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明はイオウ化合物を含有する液体炭化水素
の処理方法およびこの方法で用いられるイオウ化
合物の吸着剤に関する。 石油留分熱分解ガス、LNG、LPGなどの炭化
水素類などには硫化水素、硫化カルボニル、メル
カプタン類、サルフアイド類、ジサルフアイド類
などのイオウ化合物が含まれており、これらイオ
ウ化合物は、微量でも臭気や触媒毒作用を呈する
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。 これらのイオウ化合物を除去するために、気相
でアルカリ液、アルカノールアミン液などによる
薬液洗浄法あるいは酸化鉄、酸化亜鉛、活性炭な
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、除去装置が大型となるなどの欠点が
あり実用的でない。 本発明者らは、このような実情に鑑み、鋭意検
討した結果、活性炭に銅化合物とアルカリ金属、
アルカリ土類金属化合物またはAl、Ti、V、Cr、
Mn、Fe、Co、Ni、Zn、Cd、Pbの化合物を含有
せしめることによつて、液体炭化水素中の硫化水
素、硫化カルボニル、メルカプタン類、サルフア
イド類、ジサルフアイド類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。 すなわち本発明は、 (1) 活性炭に銅化合物と(a)アルカリ金属化合
物、(b)アルカリ土類金属化合物および(c)Al、
Ti、V、Cr、Mn、Fe、Co、Ni、Zn、Cd、
Pbの化合物の一種以上とを含有せしめてなる
液体炭化水素中のイオウ化合物の吸着剤、 (2) イオウ化合物を含有する液体を、活性炭に
銅化合物(以上第一成分ということもある)と
(a)アルカリ金属化合物、(b)アルカリ土類金属
化合物および(c)Al、Ti、V、Cr、Mn、Fe、
Co、Ni、Zn、Cd、Pbの化合物(以上第二成
分ということもある)の一種以上とを含有せし
めてなる吸着剤に接触させることを特徴とする
イオウ化合物含有液体炭化水素の処理方法、 である。 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り製造すること
ができる。 この場合に用いられる活性炭は、石炭、コーク
ス、木炭、ヤシガラ、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
200〜2000cm2/g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、円柱状、破
砕状、粉末状、繊維状などガスの処理方法に応じ
て適当なものが使用される。 本発明で用いられる銅化合物としては、たとえ
ば炭酸塩、塩基性炭酸塩、硝酸塩、硫酸塩、リン
酸塩、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、酢酸物、シユ
ウ酸塩などの有機酸塩などが挙げられる。 アルカリ金属化合物としては、Li、Na、K、
Rb、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
酸化物などの無機酸塩または無機化合物、ギ酸
塩、酢酸塩、シユウ酸塩、安息香酸塩、フエノー
ル類の塩、スルホン酸類の塩などの有機酸塩など
が挙げられる。 またアルカリ土類金属化合物としては、Be、
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、酢酸物、シユウ酸塩などの有機酸塩などが
Al、Ti、V、Cr、Mn、Fe、Co、Ni、Zn、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、水酸化物、アンモ
ニウム塩、酸化物などの無機酸塩または無機化合
物、ギ酸塩、酢酸塩、シユウ酸塩、安息香酸塩、
フエノール類の塩、スルホン酸類の塩などの有機
酸塩などが挙げられる。 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、V、Mn、Fe、Co、Ni、Zn、Cd、
Pbの化合物〔以下成分(c)ということもある〕単
独を含有せしめたものであつてもよいが、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)の三成
分を同時に含有せしめたものでもよい。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
二種の異なつ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の異なつた成分を含有せしめ
たものでもよい。 金属化合物含有活性炭中の第一成分の含量は活
性炭1g当り金属として0.1mg−原子〜3.0mg−原
子、好ましくは0.2mg−原子〜2.0mg−原子であ
り、第二成分の含量は活性炭1g当り金属として
0.1mg−原子〜5.0mg−原子、好ましくは0.2mg−原
子〜4.0mg−原子である。 本発明の吸着剤は活性炭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、これを残り
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。 活性炭に各成分を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
記の調製法において、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
乾燥した添着活性炭を不活性ガス、炭酸ガス、水
蒸気、燃焼排ガスなどの雰囲気で加熱し、金属化
合物の一部または全部を熱分解させる工程をい
う。 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をするのがよく、また第一成
分、第二成分(ただしアルカリ金属化合物を除
く)を活性炭に添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、重炭酸塩
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添着したのち熱
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、炭酸塩、重炭酸塩を用いるのがよい。 本発明において除去対象物であるイオウ化合物
としては、たとえば硫化水素、硫化カルボニル、
メルカプタン類、(たとえばメチルメルカプタン、
エチルメルカプタンなど)、サルフアイド類(た
とえば硫化メチル、硫化エチルなど)、ジサルフ
アイド類(たとえば二硫化メチル、二硫化エチル
など)があげられる。イオウ化合物を含有する液
体はいかなるものでもよいが、たとえば炭化水素
としてはたとえば液化エチレン、液化プロピレ
ン、液化天然ガス、液化石油ガスなどがあげられ
る。 本発明の方法は、前記で得られた金属化合物含
有活性炭にイオウ化合物を含む液体炭化水素を接
触させることにより行なわれる。接触方法として
は、たとえば固定層、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、
100℃以下、好ましくは0〜100℃であり、ガスの
圧力は50Kg/cm2以下、好ましくは0.1〜40Kg/cm2
であり、また液体の空間速度は25℃、1Kg/cm2
算で1/10〜20hr-1、好ましくは1/5〜10hr-1であ
る。 以下に実施例を挙げて本発明をより具体的に説
明する。 実施例 1 BET比表面積1040m2/gの16〜24meshの活性
炭Aに所定量の第一成分(硝酸銅)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Al、Ti、V、Cr、Mn、Fe、Co、
Ni、Zn、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。 得られた添着物50mlを4cmφの石英ガラス製カ
ラムに充填し、窒素ガスを線流速10cm/secで流
通しながら昇温速度5℃/minで加熱し、300℃
で30分間焼成した。 得られた吸着剤中の各金属化合物の含量は、第
1表に示すように、活性炭1g当りそれぞれ金属
として、0.2〜2.0mg−原子であつた。 なお、対照として、前述と同様の方法で、活性
炭Aに各金属の硝酸塩を単独で添着し、さらに窒
素ガス中、300℃で30分間焼成した吸着剤を調製
した。 このようにして得られた吸着剤A〜Gおよび
〜〓〓を100mesh以下に微粉砕し乾燥してその各
1.0gを100mlの共栓フラスコに入れ、これにH2S
−0.1mg/ml、cos−0.15mg/mlおよびCH3SH−
0.05mg/mlを含有する25℃のn−ヘキサン10mlを
注入し密栓して、25℃で10分間振とうし、n−ヘ
キサン中のこれらイオウ化合物濃度を測定し、除
去率を求めた。結果を第1表に示した。
The present invention relates to a method for treating liquid hydrocarbons containing sulfur compounds and an adsorbent for sulfur compounds used in this method. Hydrocarbons such as petroleum distillate pyrolysis gas, LNG, and LPG contain sulfur compounds such as hydrogen sulfide, carbonyl sulfide, mercaptans, sulfides, and disulfides, and even in trace amounts, these sulfur compounds cause odor. It often causes problems in processes such as beverage processing and chemical reactions because it exhibits catalyst poisoning effects. In order to remove these sulfur compounds, chemical cleaning methods using alkaline solutions, alkanolamine solutions, etc. in the gas phase, or adsorption methods using iron oxide, zinc oxide, activated carbon, etc., have been proposed, but the removal effects are poor; This method has drawbacks such as the large size of the removal device, making it impractical. In view of these circumstances, the inventors of the present invention have made extensive studies and found that activated carbon contains copper compounds and alkali metals.
Alkaline earth metal compounds or Al, Ti, V, Cr,
By containing compounds of Mn, Fe, Co, Ni, Zn, Cd, and Pb, hydrogen sulfide, carbonyl sulfide, mercaptans, sulfides, and disulfides in liquid hydrocarbons can be removed very efficiently. The present invention has been completed. That is, the present invention provides: (1) activated carbon with a copper compound, (a) an alkali metal compound, (b) an alkaline earth metal compound, and (c) Al;
Ti, V, Cr, Mn, Fe, Co, Ni, Zn, Cd,
(2) An adsorbent for sulfur compounds in liquid hydrocarbons containing one or more Pb compounds;
(a) alkali metal compounds, (b) alkaline earth metal compounds and (c) Al, Ti, V, Cr, Mn, Fe,
A method for treating a liquid hydrocarbon containing a sulfur compound, the method comprising bringing it into contact with an adsorbent containing one or more of Co, Ni, Zn, Cd, and Pb compounds (sometimes referred to as the second component); It is. The adsorbent of the present invention can be manufactured by incorporating the first component and the second component into activated carbon. The activated carbon used in this case is manufactured by a known method using coal, coke, charcoal, coconut shell, resin, etc. as raw materials, and its specific surface area is
Any material may be used as long as it has a density of 200 to 2000 cm 2 /g, and its shape may be spherical, cylindrical, crushed, powdered, fibrous, etc. depending on the gas processing method. Examples of the copper compound used in the present invention include inorganic acid salts or inorganic compounds such as carbonates, basic carbonates, nitrates, sulfates, phosphates, halides, oxides, and hydroxides, formates, and acetic acid. and organic acid salts such as oxalates. Alkali metal compounds include Li, Na, K,
Rb, Cs such as bicarbonate, carbonate, nitrate,
Inorganic acid salts or inorganic compounds such as borates, silicates, sulfates, halides, hydroxides, formates, acetates, oxalates, benzoates, salts of phenols, salts of sulfonic acids, etc. Examples include organic acid salts of In addition, examples of alkaline earth metal compounds include Be,
Mg, Ca, Sr and Ba such as carbonates, nitrates, sulfates, phosphates, halides, oxides,
Inorganic acid salts or inorganic compounds such as hydroxides, organic acid salts such as formates, acetates, oxalates, etc.
Al, Ti, V, Cr, Mn, Fe, Co, Ni, Zn, Cd,
Pb compounds include inorganic acid salts of these metals such as carbonates, hydrogen carbonates, nitrates, borates, silicates, sulfates, phosphates, halides, hydroxides, ammonium salts, and oxides. or inorganic compounds, formates, acetates, oxalates, benzoates,
Examples include organic acid salts such as phenol salts and sulfonic acid salts. 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 [hereinafter sometimes referred to as component (b)] alone or Al, Cr, V, Mn, Fe, Co, Ni, Zn, Cd,
It may contain a single Pb compound [hereinafter also referred to as component (c)], but among these, component (a) and component (b), component (b) and component (c), Alternatively, it may contain two components, such as component (c) and component (a), or it may contain three components, component (a), component (b), and component (c), at the same time. Moreover, the first component may contain two or more kinds of compounds, and the second component may contain two or more kinds of compounds in the same kind of component, for example, two different kinds of components in component (a). It may also contain different components. The content of the first component in the activated carbon containing a metal compound is from 0.1 mg-atom to 3.0 mg-atom, preferably from 0.2 mg-atom to 2.0 mg-atom, as metal per gram of activated carbon, and the content of the second component is from 0.2 mg-atom to 2.0 mg-atom per gram of activated carbon. as metal
0.1 mg-atom to 5.0 mg-atom, preferably 0.2 mg-atom to 4.0 mg-atom. The adsorbent of the present invention may be one in which each component is supported or impregnated on activated carbon, 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 with this. When each component is impregnated onto activated carbon, it is preferable to dry or bake it after impregnation. Possible methods for impregnating activated carbon with each component include impregnating or spraying activated carbon with a solution in which each component is dissolved or suspended in water (including acid or alkaline aqueous solutions), various solvents, or the like. In the above preparation method, drying refers to the step of evaporating the water or solvent in the impregnated activated carbon at a temperature of about 130°C or lower, and calcination refers to the step of evaporating the impregnated activated carbon that has been dried at a temperature of about 130°C or higher. A process in which part or all of a metal compound is thermally decomposed by heating in an atmosphere of active gas, carbon dioxide, steam, combustion exhaust gas, etc. In the above method, if a substance other than an oxide is impregnated onto activated carbon as the first component or second component (excluding alkali metal compounds), it is recommended to heat-treat the activated carbon by drying or firing after impregnation. , when a second component (excluding alkali metal compounds) is impregnated with activated carbon and no heat treatment is performed,
It is preferable to use oxides for the first component and the second component (excluding alkali metal compounds). When an alkali metal compound other than alkali metal hydroxide, carbonate, or bicarbonate is impregnated onto activated carbon as a second component, it is recommended to perform heat treatment such as drying or calcination after impregnation. If no heat treatment is to be carried out later, it is preferable to use hydroxide, carbonate, or bicarbonate as the alkali metal compound. Examples of the sulfur compounds to be removed in the present invention include hydrogen sulfide, carbonyl sulfide,
Mercaptans (e.g. methyl mercaptan,
ethyl mercaptan, etc.), sulfides (eg, methyl sulfide, ethyl sulfide, etc.), and disulfides (eg, methyl disulfide, ethyl disulfide, etc.). Any liquid containing a sulfur compound may be used, and examples of hydrocarbons include liquefied ethylene, liquefied propylene, liquefied natural gas, and liquefied petroleum gas. The method of the present invention is carried out by contacting the metal compound-containing activated carbon obtained above with a liquid hydrocarbon containing a sulfur compound. As the contacting method, known means such as a fixed bed, a moving bed, a fluidized bed, etc. can be used. The contact temperature in this case is
The temperature is 100℃ or less, preferably 0 to 100℃, and the gas pressure is 50Kg/ cm2 or less, preferably 0.1 to 40Kg/cm2 .
The space velocity of the liquid is 1/10 to 20 hr -1 , preferably 1/5 to 10 hr -1 at 25° C. in terms of 1 kg/cm 2 . EXAMPLES The present invention will be explained in more detail with reference to Examples below. Example 1 A predetermined amount of the first component (copper nitrate) and second component (alkali metal nitrate, alkaline earth metal nitrate, and Al, Ti, and V , Cr, Mn, Fe, Co,
Nitrate of Ni, Zn, Cd, Pb (only V is sulfate)
An aqueous solution containing the above was evenly dispersed. 50ml of the obtained impregnated material was packed into a 4cmφ quartz glass column, heated at a temperature increase rate of 5°C/min while flowing nitrogen gas at a linear flow rate of 10cm/sec, and heated to 300°C.
Baked for 30 minutes. As shown in Table 1, the content of each metal compound in the obtained adsorbent was 0.2 to 2.0 mg atoms per gram of activated carbon. As a control, an adsorbent was prepared by impregnating activated carbon A with a nitrate of each metal alone and calcining it at 300° C. for 30 minutes in nitrogen gas in the same manner as described above. The adsorbents A to G and ~〓〓 obtained in this way are finely ground to 100 mesh or less and dried.
Put 1.0g into a 100ml stoppered flask and add H 2 S to it.
-0.1mg/ml, cos-0.15mg/ml and CH3SH-
10 ml of n-hexane at 25° C. containing 0.05 mg/ml was injected, the tube was tightly stoppered, and the mixture was shaken at 25° C. for 10 minutes. The concentration of these sulfur compounds in n-hexane was measured to determine the removal rate. The results are shown in Table 1.

【表】【table】

【表】【table】

Claims (1)

【特許請求の範囲】 1 活性炭に銅化合物と(a)アルカリ金属化合
物、(b)アルカリ土類金属化合物および(c)Al、Ti、
V、Cr、Mn、Fe、Co、Ni、Zn、Cd、Pbの化合
物の一種以上とを含有せしめてなる液体炭化水素
中のイオウ化合物の吸着剤。 2 イオウ化合物を含有する液体を、活性炭に
銅化合物と(a)アルカリ金属化合物、(b)アルカリ
土類金属化合物および(c)Al、Ti、V、Cr、Mn、
Fe、Co、Ni、Zn、Cd、Pbの化合物の一種以上
とを含有せしめてなる吸着剤に接触させることを
特徴とするイオウ化合物含有液体炭化水素の処理
方法。
[Claims] 1. Activated carbon containing a copper compound, (a) an alkali metal compound, (b) an alkaline earth metal compound, and (c) Al, Ti,
An adsorbent for sulfur compounds in liquid hydrocarbons containing one or more of the following compounds: V, Cr, Mn, Fe, Co, Ni, Zn, Cd, and Pb. 2 A liquid containing a sulfur compound is added to activated carbon with a copper compound, (a) an alkali metal compound, (b) an alkaline earth metal compound, and (c) Al, Ti, V, Cr, Mn,
A method for treating a liquid hydrocarbon containing a sulfur compound, which comprises bringing it into contact with an adsorbent containing one or more of Fe, Co, Ni, Zn, Cd, and Pb compounds.
JP3505983A 1983-03-02 1983-03-02 Adsorbent for sulfur compound and process for treating liquid containing sulfur compound Granted JPS59160584A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3505983A JPS59160584A (en) 1983-03-02 1983-03-02 Adsorbent for sulfur compound and process for treating liquid containing sulfur compound

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3505983A JPS59160584A (en) 1983-03-02 1983-03-02 Adsorbent for sulfur compound and process for treating liquid containing sulfur compound

Publications (2)

Publication Number Publication Date
JPS59160584A JPS59160584A (en) 1984-09-11
JPH0322201B2 true JPH0322201B2 (en) 1991-03-26

Family

ID=12431452

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3505983A Granted JPS59160584A (en) 1983-03-02 1983-03-02 Adsorbent for sulfur compound and process for treating liquid containing sulfur compound

Country Status (1)

Country Link
JP (1) JPS59160584A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1248307A1 (en) * 2001-04-03 2002-10-09 Hitachi, Ltd. Lead-acid battery

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS513128A (en) * 1974-06-26 1976-01-12 Hitachi Ltd

Also Published As

Publication number Publication date
JPS59160584A (en) 1984-09-11

Similar Documents

Publication Publication Date Title
JP3009309B2 (en) Methods for removing hydrogen sulfide from gas streams
US4990318A (en) Selective removal of hydrogen sulfide over a nickel-promoted absorbing composition
CA1290552E (en) Selective removal of hydorgen sulfide over zinc titanate and alumina
US6514907B2 (en) Bromine-impregnated activated carbon and process for preparing the same
US5146039A (en) Process for low level desulfurization of hydrocarbons
ES2295059T3 (en) PROCEDURE FOR THE PRODUCTION OF AN ABSORBENT COMPOSITION AND USE IN DESULFURATION.
US4532115A (en) Method for removal of poisonous gases
TWI526428B (en) Lower reactivity adsorbent and higher oxygenate capacity for removal of oxygenates from olefin streams
US4001375A (en) Process for the desulfurization of flue gas
AU625032B1 (en) A process for removing trialkyl arsines from fluids
JP2004500978A (en) Desulfurization and sorbent for desulfurization
US20020052291A1 (en) Low temperature sorbents for removal of sulfur compounds from fluid feed streams
JP2923711B2 (en) Catalyst for removing sulfur compounds from industrial gas, method for producing the same and use thereof
KR20020080331A (en) Desulfurization and novel sorbents for same
KR20020047307A (en) Desulfurization and novel sorbents for same
US5094996A (en) Nickel-promoted absorbing compositions for selective removal of hydrogen sulfide
CA2120046C (en) Separately removing mercaptans and hydrogen sulfide from gas streams
JPH0322201B2 (en)
JPH0475049B2 (en)
US5145815A (en) Regeneration of zeolitic molecular sieves with sulfur oxide absorption on soda-lime bed
JPH049574B2 (en)
JPH049573B2 (en)
JPH0768528B2 (en) Method for removing carbonyl sulfide in gas
JPH0424092B2 (en)
JPS5814363B2 (en) Activated carbon processing method