JPS58202041A - Preparation of high strength iron oxide desulfurizing agent - Google Patents

Preparation of high strength iron oxide desulfurizing agent

Info

Publication number
JPS58202041A
JPS58202041A JP57085399A JP8539982A JPS58202041A JP S58202041 A JPS58202041 A JP S58202041A JP 57085399 A JP57085399 A JP 57085399A JP 8539982 A JP8539982 A JP 8539982A JP S58202041 A JPS58202041 A JP S58202041A
Authority
JP
Japan
Prior art keywords
iron oxide
molded
high strength
desulfurizing agent
mixture
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
JP57085399A
Other languages
Japanese (ja)
Inventor
Masaki Kondo
正樹 近藤
Akira Suzuki
公 鈴木
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.)
Sumitomo Heavy Industries Ltd
Original Assignee
Sumitomo Heavy 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 Sumitomo Heavy Industries Ltd filed Critical Sumitomo Heavy Industries Ltd
Priority to JP57085399A priority Critical patent/JPS58202041A/en
Publication of JPS58202041A publication Critical patent/JPS58202041A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To obtain a high strength iron oxide desulfurizing agent suitable for use in a dry desulfurizing method, by a method wherein water is added to a mixture of an iron oxide powder and clay to be kneaded therewith and the kneaded mixture is molded to be baked in an oxygen atmosphere within a range of a specific temp. CONSTITUTION:About 25-100pts.wt. clay is mixed with 100pts.wt. iron oxide powder. This mixture is kneaded in the presence of a proper amount of water while the kneaded mixture is molded into a predetermined shape with a predetermined dimension to be dried. In the next step, the dried molded one is baked in an acidic atmosphere under a temp. condition of 300-600 deg.C. By this procedure, a high strength iron oxide molded body suitable for a desulfurizing agent in a dry desulfurizing method is obtained.

Description

【発明の詳細な説明】 本発明tit硫化水素含有カスの乾式脱硫法で脱硫剤と
して使用される粒状酸化鉄の改良に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an improvement in granular iron oxide used as a desulfurization agent in a dry desulfurization method for hydrogen sulfide-containing scum.

減化水素含有カスの乾式脱伝法の一つとして粒状酸化鉄
を移動床で用いる脱硫法がカスデクニーク法の名で知ら
れている。この方法は粒状酸化鉄の移動床に連成の酸素
を共存させた硫化水素含有ガスに供給して脱硫し、脱硫
に際して硫化鉄に転化した脱硫剤を共存酸素によって再
び酸化鉄に転化させるものであって、この方法によれば
、単体硫黄を含んだ粒状酸化鉄が移動床式脱硫器から排
出されるので、単体硫黄を1去して粒状酸化鉄を再生す
ることにより、これを脱硫器に循環して+4使用するこ
とができる。
A desulfurization method using granular iron oxide in a moving bed is known as the Kasdecnik method as one of the dry detransmission methods for decomposed hydrogen-containing scum. In this method, a moving bed of granular iron oxide is desulfurized by supplying hydrogen sulfide-containing gas coexisting with coupled oxygen, and the desulfurizing agent, which has been converted to iron sulfide during desulfurization, is converted back to iron oxide by the coexisting oxygen. According to this method, granular iron oxide containing elemental sulfur is discharged from the moving bed desulfurizer, so by removing elemental sulfur and regenerating the granular iron oxide, it can be transferred to the desulfurizer. +4 can be used in circulation.

しかしながら、ガスラークニーク法で使用されている粒
状酸化鉄は、その耐摩耗性が必ずしも充分ではない。ち
なみに上記の粒状酸化鉄はセメントをバインダーに用い
て粒状に成型したものであるが、これを循環使用した場
合VC:はlザイクル毎に約lOチ程艮が消耗する。
However, the granular iron oxide used in the gas-lark sneak method does not necessarily have sufficient wear resistance. Incidentally, the above-mentioned granular iron oxide is molded into granules using cement as a binder, and when it is used repeatedly, about 100 ml of VC is consumed every 1 cycle.

而して本発明は脱誠工程ではもちろん再生工程でも移ζ
り床が採用される硫化水素含不カスの乾式脱硫法に脱硫
剤として使用して好適な高強度酸化鉄成型体の製造法を
提系するものでち一ノて、その方法は酸化鉄粉末に粘土
を混合し、この混合物を適斌の水の存在下に混#!後、
バ1望の形状と寸法に成型して乾燥し、しかる後これを
300〜600℃の温度中性でかつ酸素雰囲気で焼成す
ることからなる。
Therefore, the present invention is applicable not only to the de-faith process but also to the regeneration process.
This project proposes a method for producing a high-strength iron oxide molded body suitable for use as a desulfurization agent in the dry desulfurization process that does not contain hydrogen sulfide, in which a bed is used. Mix the clay and mix this mixture in the presence of suitable water! rear,
The bar is molded into the desired shape and dimensions, dried, and then fired at a neutral temperature of 300 to 600° C. in an oxygen atmosphere.

本発明に於て、酸化鉄粉末としては硫化水素含有ガスの
脱硫剤に従来から使用されている酸化鉄の粉末がいずれ
も使用できる。酸化鉄粉末に混合される粘土はバインダ
ーとして機能するものであるが、この粘土の混合割合は
酸化鉄粉末11J O重:1部当−t> 25〜l 0
0 X、1itstyJ範囲にすることが好ましい。粘
土の混合割合が少なすぎる場合は焼成後の成型体に充分
な強度を付与することができず、多すぎる場合は脱硫剤
としての性能が低下してしまうからである。つ洩り、本
発明で使用される粘土は、上記の゛混合割合で焼成後の
成型体に充分なる強度を与え得るものでなければならず
、この棟の粘土としては、本節粘土、蛙目粘土なとが挙
げられる。もし焼成しなければ、被処理ガス中すミスト
により崩壊ノーるおそれがある。
In the present invention, any iron oxide powder conventionally used as a desulfurizing agent for hydrogen sulfide-containing gas can be used as the iron oxide powder. The clay mixed with the iron oxide powder functions as a binder, and the mixing ratio of this clay is iron oxide powder 11 J O weight: 1 part - t > 25 ~ l 0
It is preferable to set it in the range of 0x, 1itstyJ. This is because if the mixing ratio of clay is too small, it will not be possible to impart sufficient strength to the molded body after firing, and if it is too large, the performance as a desulfurizing agent will deteriorate. However, the clay used in the present invention must be able to provide sufficient strength to the molded body after firing at the above-mentioned mixing ratio. Examples include clay. If it is not fired, there is a risk of collapse due to mist in the gas to be treated.

酸化鉄粉末と粘土の混合物は適微の水の存在下に混練後
、所望の形状と寸法に成型して乾燥され、しかる後30
0〜600℃の温度で焼成される。成型体の形状と寸法
は任意に選ぶことができるが、焼成温疫は300〜60
0°ICc)範囲としなければならない。300℃以下
では焼成物に充分な強度を期待することができず、60
0℃以上の焼成温度では酸化鉄が焼結してしまうからで
ある。
The mixture of iron oxide powder and clay is kneaded in the presence of an appropriate amount of water, then molded into the desired shape and dimensions, dried, and then dried for 30 minutes.
It is fired at a temperature of 0 to 600°C. The shape and dimensions of the molded body can be chosen arbitrarily, but the firing temperature is 300 to 60
0°ICc) range. If the temperature is below 300℃, the fired product cannot be expected to have sufficient strength;
This is because iron oxide will be sintered at a firing temperature of 0° C. or higher.

次に実施例により本発明の構成と効果を具捧的に説明す
る。
Next, the configuration and effects of the present invention will be specifically explained using examples.

実施例 酸化鉄粉末65重量部に粘土35重東部を混合し、過員
の水の存在下に混練後、直径約6.2龍、長さ1511
jの円柱状に成型し、しかる後これをioo℃で乾燥し
た。次いでこの乾煉成!ψ体を様々な温度で焼成し、焼
成成型体の単位圧壊強度及びマイクロ強度と焼成温度と
の関保全求めた。
Example: 65 parts by weight of iron oxide powder was mixed with 35 parts by weight of clay, and after kneading in the presence of an excess of water, the resulting mixture was approximately 6.2 parts in diameter and 1511 parts in length.
It was molded into a cylindrical shape, and then dried at io0°C. Next is this dry cultivation! The ψ body was fired at various temperatures, and the relationship between the unit crushing strength and micro strength of the fired molded body and the firing temperature was determined.

単位圧壊強度は本屋式強度計を用いて画定した。またマ
イクロ強度は25AX300闘の一゛iに試料5.0g
と・8鰭φの鋼球10個を入れて宥の両端を封じ、管内
の試料と鋼球が管の両端を往復するように、銅管を2 
Orpmで20分間回転させ、しかる後供試試料を9メ
ツシユの篩にかけ、篩上の試料残留率にて定義されるも
のである。
The unit crushing strength was determined using a Honya type strength meter. In addition, the micro strength is 5.0g of sample for 25AX300
Insert 10 steel balls of 8 fin diameter, seal both ends of the tube, and insert the copper tube into two tubes so that the sample inside the tube and the steel balls reciprocate at both ends of the tube.
The test sample was rotated for 20 minutes at Orpm, and then passed through a 9-mesh sieve, and was defined by the percentage of sample remaining on the sieve.

結果を添付図面に示すが、これから明らかなよりに本発
明の方法によれば、萬強度の酸化鉄脱硫剤を得ることが
できる。
The results are shown in the attached drawings, and it is clear from the results that according to the method of the present invention, an iron oxide desulfurization agent with ten-proof strength can be obtained.

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

図面は酸化鉄脱硫剤の単位圧壊強度及びマイクロ強度と
焼成温度との関係を示すグラフである。
The drawing is a graph showing the relationship between unit crushing strength and micro strength of an iron oxide desulfurizing agent and firing temperature.

Claims (1)

【特許請求の範囲】[Claims] 1、#1化鉄粉末に粘土を混合し、この混合物を適竜の
水の存在下に混線後、所望の形状と寸法に成型して乾燥
し、しかる後これを300〜600℃の温度条件でがっ
酸81囲気で焼成することからなる高強度酸化鉄脱硫剤
の製造法。
1. Mix #1 iron chloride powder with clay, mix this mixture in the presence of water, mold it into the desired shape and size, dry it, and then heat it at a temperature of 300 to 600°C. A method for producing a high-strength iron oxide desulfurization agent, which comprises firing in an atmosphere of degaric acid.
JP57085399A 1982-05-19 1982-05-19 Preparation of high strength iron oxide desulfurizing agent Pending JPS58202041A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57085399A JPS58202041A (en) 1982-05-19 1982-05-19 Preparation of high strength iron oxide desulfurizing agent

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57085399A JPS58202041A (en) 1982-05-19 1982-05-19 Preparation of high strength iron oxide desulfurizing agent

Publications (1)

Publication Number Publication Date
JPS58202041A true JPS58202041A (en) 1983-11-25

Family

ID=13857696

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57085399A Pending JPS58202041A (en) 1982-05-19 1982-05-19 Preparation of high strength iron oxide desulfurizing agent

Country Status (1)

Country Link
JP (1) JPS58202041A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02265645A (en) * 1989-04-04 1990-10-30 Kawasaki Heavy Ind Ltd Desulfurizing and dust removing agent and its manufacture
WO1991003422A1 (en) * 1989-08-30 1991-03-21 Irwin Fox Disposable oxide carrier for scavenging hydrogen sulfide
US5320992A (en) * 1989-08-30 1994-06-14 Irwin Fox Disposable oxide carrier for scavenging hydrogen sulfide
JP2007516817A (en) * 2003-12-05 2007-06-28 アイヤー,ジャヤルクシュミ Catalysts useful for removing H2S from gas streams, methods for their preparation, and uses thereof

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02265645A (en) * 1989-04-04 1990-10-30 Kawasaki Heavy Ind Ltd Desulfurizing and dust removing agent and its manufacture
WO1991003422A1 (en) * 1989-08-30 1991-03-21 Irwin Fox Disposable oxide carrier for scavenging hydrogen sulfide
AU641931B2 (en) * 1989-08-30 1993-10-07 M-I L.L.C. Disposable oxide carrier for scavenging hydrogen sulfide
US5320992A (en) * 1989-08-30 1994-06-14 Irwin Fox Disposable oxide carrier for scavenging hydrogen sulfide
JP2007516817A (en) * 2003-12-05 2007-06-28 アイヤー,ジャヤルクシュミ Catalysts useful for removing H2S from gas streams, methods for their preparation, and uses thereof

Similar Documents

Publication Publication Date Title
CN102049179B (en) Method for preparing supported iron oxide series desulfurizing agent
JPH06279774A (en) Method of removing hydrogen sulfide from gaseous stream
CN112295395B (en) Flue gas desulfurizer as well as preparation method and application thereof
US5360468A (en) Sulfur absorbents
DE69727038T2 (en) METHOD FOR THE DIRECT OXIDATION OF SULFUR COMPOUNDS TO ELEMENTAL SULFUR WITH A CATALYST CONTAINING COPPER
CN115814580A (en) Carbide slag modified desulfurizer composition, desulfurizer, preparation method and application thereof
JPS58202041A (en) Preparation of high strength iron oxide desulfurizing agent
JP2001294414A (en) Manufacturing method of activated coke having high strength and high adsorpability
ATE54128T1 (en) SILICATE-BONDED ZEOLITE GRANULES, PROCESS FOR THEIR PRODUCTION AND USE.
JPH08206443A (en) Acidic gas absorbent and production thereof
FI64790B (en) FOERFARANDE FOER ROSTNING AV SELENHALTIGT MATERIAL
JPH05261279A (en) Production of desulfurizing agent
JPH02153818A (en) Production of zeolite moldings
JPS5481188A (en) Method of producing catalyst for oxidizing carbon monoxide
HU182040B (en) Method and apparatus first for hardening preparations serving for producing of moulds and cores
US2008953A (en) Gas purifying mass
JPH11349319A (en) Production of activated carbon
US4144312A (en) Desulfurization of fluorite ores
CN101906345B (en) Method for preparing oxygen carrier particles for restraining release of sulfur-containing gas
US2479520A (en) Gas-absorbing material and process of making same
JPH0159008B2 (en)
RU2142335C1 (en) Method of preparing sorbent for removing sulfur compounds from gases
JPS62258742A (en) Preparation of adsorbent for metal ion and offensive smell
JPS5895551A (en) Desulfurizer for fluidized bed
SU1617019A1 (en) Charge for nodulizing sulfite-sulfate calcium slurry