JPS60166033A - Desulfurizing agent - Google Patents

Desulfurizing agent

Info

Publication number
JPS60166033A
JPS60166033A JP59018430A JP1843084A JPS60166033A JP S60166033 A JPS60166033 A JP S60166033A JP 59018430 A JP59018430 A JP 59018430A JP 1843084 A JP1843084 A JP 1843084A JP S60166033 A JPS60166033 A JP S60166033A
Authority
JP
Japan
Prior art keywords
desulfurizing agent
manganese nodule
contained
manganese
regenerated
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
JP59018430A
Other languages
Japanese (ja)
Inventor
Hiroshi Ogawa
弘 小川
Yoshiaki Obayashi
良昭 尾林
Toru Seto
徹 瀬戸
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP59018430A priority Critical patent/JPS60166033A/en
Publication of JPS60166033A publication Critical patent/JPS60166033A/en
Pending legal-status Critical Current

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

Abstract

PURPOSE:To obtain a desulfurizing agent by which a sulfide contained in a reducing gas is removed effectively and which can be regenerated and used repeatedly by using manganese nodule. CONSTITUTION:A manganese nodule is used as a desulfurizing agent having excellent adsorption performance and regeneration efficiency. The manganese nodule is porous generally and an amorphous transition-metal oxide (hydroxide) and its essential component is Mn and Fe, and as a trace element, Ni, Co, Cu and Ti, etc. are contained by about 0.1-1.0% respectively. In the manganese nodule as desulfurizing agent in this method, the total of Mn and Fe is contained >=50% expressed in terms of MnO2 and Fe2O3. Since the adsorption capacity is increased and also the manganese nodule can be regenerated for a short time in comparison with conventional iron ore, manganese nodule is the desulfurizing agent having excellent adsorption performance and regeneration efficiency.

Description

【発明の詳細な説明】 本発明は、脱硫剤に関し、特に還元性ガス中に含まれる
硫化物を効率良く除去し、かつ繰返し再生・使用可能な
脱硫剤に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a desulfurization agent, and particularly to a desulfurization agent that can efficiently remove sulfides contained in reducing gas and can be repeatedly recycled and used.

原油価格の高−や輸入原油の重質化が、我が国のエネル
ギーや化学原料の将来め見通しを暗くしている。
High crude oil prices and heavier imported crude oil have darkened the outlook for Japan's energy and chemical raw materials.

この対応として原油から軽質分を蒸留した残渣分、いわ
ゆる蒸留残渣、あるいわ石炭を原料としてガス化を行な
い、そこから得られる一酸化炭素(CO)と水素(Hり
の利用が検討されている。すなわち、とのCo、H!を
直接燃料に利用する方法、このガスから液化燃料に合成
する方法、あるいわ従来石油(ナフサ)から得ていたエ
チレン、プロピレン、酢酸等々への転換を計る石油代替
エネルギー政策が打ち出されている。
As a response to this problem, the use of carbon monoxide (CO) and hydrogen (H2) obtained by gasifying the residue obtained by distilling light components from crude oil, so-called distillation residue, or coal, as a raw material, is being considered. In other words, there is a method of directly using Co and H! as fuel, a method of synthesizing this gas into liquefied fuel, and a method of converting it to ethylene, propylene, acetic acid, etc. that were conventionally obtained from petroleum (naphtha). Alternative energy policies are being launched.

重質油や石炭中のいおう化合物は、ガス化反応時に硫化
物、主としてH,8(10%程度は00B)に転化し、
coやH,の還元性ガス中に混入する。そして燃料の場
合は、いおう酸化物となシ、大気汚染源となったシ、合
成原料の場合には触媒被毒となるため、種々の精製法が
提案され、成るものは稼動中である。
Sulfur compounds in heavy oil and coal are converted into sulfides, mainly H,8 (about 10% is 00B) during gasification reactions,
It mixes into reducing gases such as co and H. In the case of fuel, sulfur oxides are a source of air pollution, and in the case of synthetic raw materials, catalysts are poisoned, so various purification methods have been proposed and some are currently in use.

その一つに湿式法があシ、硫化水素を化学吸収させて除
去するプロセスである。この方法は、溶液に硫化水素を
吸収させるためガスを冷却する必要があり、それにとも
なうエネルギー損失や、吸収液の再生、排水処理などの
課題がある。
One of them is the wet method, which is a process that chemically absorbs and removes hydrogen sulfide. This method requires cooling the gas in order to absorb hydrogen sulfide into the solution, which poses problems such as energy loss, regeneration of the absorption liquid, and wastewater treatment.

他の方法として、吸着剤(例えば、酸化鉄、酸化モリブ
デン等が知られている)K吸着させて、酸素でいおう酸
化物として脱着するとともに吸着剤を再生して繰シ返し
利用する、いわゆる乾式法が提案されている。 。
Another method is a so-called dry method in which K is adsorbed using an adsorbent (for example, iron oxide, molybdenum oxide, etc. are known), desorbed as an oxide with oxygen, and the adsorbent is regenerated and used repeatedly. A law is proposed. .

本発明は、この乾式法に適用する硫黄化合物の吸着剤に
関する。
The present invention relates to a sulfur compound adsorbent applied to this dry method.

従来から酸化鉄は脱硫剤としてよく知られている。酸化
鉄としては鉄鉱石自身でも脱硫性能はあるが、H,S 
+0OEIの吸着量が少なく、吸着再生に長時間を要し
、また吸着再生の繰如返しによシ粉化するという欠点が
ある。
Iron oxide has been well known as a desulfurization agent. Iron ore itself has desulfurization performance as iron oxide, but H, S
The adsorption amount of +0OEI is small, it takes a long time for adsorption and regeneration, and it has the disadvantage that it becomes powder due to repeated adsorption and regeneration.

かかる現状を鑑み、本発明者等は(1)吸着容量が大巻
く、(2)短2時間に簡便な方法で再生でき、繰シ返し
使用が可能である吸着剤の開発に鋭意努力した結果、マ
ンガン・ノジュールが同上の目的を満足する物質である
ことを見い出し、本発明に到達したものである。
In view of the current situation, the inventors of the present invention have made earnest efforts to develop an adsorbent that (1) has a large adsorption capacity, (2) can be regenerated in a simple manner in just two hours, and can be used repeatedly. The present invention was achieved by discovering that manganese nodules are a substance that satisfies the above objectives.

マンガン・ノジュールは、一般に多孔質で、はぼ無定形
の遷移金属酸化物(水酸化物)で、主成分はMnとIF
eであυ、微量成分として引。
Manganese nodules are generally porous, almost amorphous transition metal oxides (hydroxides) whose main components are Mn and IF.
e and υ as a trace component.

co、Ou、TI などがa 1〜1.0%くらいずつ
含まれている。本発明における脱硫剤としてのマンガン
・ノジュールは、Mnと′PeがMnO2及びP’92
03換算でその合計が50%以上のものである。
Co, Ou, TI, etc. are contained in a of about 1 to 1.0% each. In the manganese nodule as a desulfurization agent in the present invention, Mn and 'Pe are MnO2 and P'92
The total is 50% or more when converted to 0.03.

以下、本発明の吸着剤を実施例に従い説明する。Hereinafter, the adsorbent of the present invention will be explained according to Examples.

実施例1 試料は下表に示すマンガン・ノジュールを粉砕し、14
メツシュ〜24メツシュ釦整粒したものを用いた。
Example 1 The sample was prepared by crushing the manganese nodules shown in the table below.
The particles that had been sized with mesh to 24 mesh buttons were used.

マンガン・ノジュールの化学組成(wt%)反応管は内
径15鰭の石英管を用い、内部に試料を20ゴ充填し、
反応管上部から被処理ガスとしてN2日 0.3%、H
210%、0025%。
Chemical composition of manganese nodules (wt%) A quartz tube with an inner diameter of 15 fins was used as the reaction tube, and 20 samples were filled inside.
N2 days 0.3%, H as gas to be treated from the upper part of the reaction tube
210%, 0025%.

C013%、 H2O2%、N、59.7%からなる合
成ガスを流量601Jt/Hで送入した。反応温度は4
00℃で行ない、硫化水素の除去率を測定した。除去率
は吸着剤充填層入口、出口における硫化水素濃度の減少
率である。比較のため鉄鉱石についても測定した。
Synthesis gas consisting of 13% CO, 2% H2O, and 59.7% N was fed at a flow rate of 601 Jt/H. The reaction temperature is 4
The removal rate of hydrogen sulfide was measured at 00°C. The removal rate is the rate of decrease in hydrogen sulfide concentration at the inlet and outlet of the adsorbent packed bed. For comparison, iron ore was also measured.

この結果、硫化水素除去率が80%になるまでに吸着し
た硫化水素は、鉄鉱石及びマンガン・ノジュールで、そ
れぞれ15.7・mmot% ”五6mmotであった
As a result, the amount of hydrogen sulfide adsorbed until the hydrogen sulfide removal rate reached 80% was 15.7 mmot% (56 mmot) for iron ore and manganese nodule, respectively.

また、第1図に硫化水素除去率の経時変化を示す。第1
図からH2S除去率が90%以上維持できる時間は、鉄
鉱石(B) 88分に対してマンガン・ノジヱールヘ)
は138分と大巾に向上していることが判明した。
Furthermore, Fig. 1 shows the change over time in the hydrogen sulfide removal rate. 1st
From the figure, the time for which the H2S removal rate can be maintained at 90% or more is 88 minutes for iron ore (B), compared to 88 minutes for manganese nodile).
It turned out that the time was 138 minutes, a huge improvement.

実施例2 実施例1による吸収操作が終了してから、N2ガスパー
ン後、直ちに031%と残部N!とからなるキャリヤガ
スを流量b o mt/Hで反応器に流通しながら、反
応温度を400℃に保持して、吸着剤に吸収された硫黄
分を吸着剤から803として脱離させ、吸着剤充填層の
出ロSO,濃度を測定し、脱離量をめた。
Example 2 Immediately after the absorption operation according to Example 1 was completed and the N2 gas was turned off, the remaining N! While a carrier gas consisting of The output SO and concentration of the packed bed were measured, and the amount of desorption was calculated.

この結果は第2図に示す過多であシ、硫黄の脱離量は鉄
鉱石及びマンガン・ノジュールで、それぞれ149 m
mot、 21.2 mmotであり、脱離に要する時
間は同じ程度で完了することが判明した。こうして硫黄
分を脱離して吸着剤を再生した。
This result is excessive as shown in Figure 2, and the amount of sulfur desorbed is 149 m for each of iron ore and manganese nodules.
mot, 21.2 mmot, and it was found that the time required for desorption was approximately the same. In this way, the sulfur content was desorbed and the adsorbent was regenerated.

以上実施例で示す如く、マンガン・ノジュールは従来の
鉄鉱石に比較して、吸着容量を増大させると共に、はぼ
同じ時間で再生できることから、吸着性能及び再生効率
の良い脱硫剤であることが実証された。
As shown in the examples above, manganese nodules have increased adsorption capacity and can be regenerated in approximately the same time compared to conventional iron ore, proving that it is a desulfurization agent with good adsorption performance and regeneration efficiency. It was done.

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

第1図及び第2図は本発明脱硫剤の性能試験結果を示す
図である。 復代理人 内 1) 明 復代理人 萩 原 亮 −
FIG. 1 and FIG. 2 are diagrams showing the performance test results of the desulfurizing agent of the present invention. Sub-agents 1) Meifuku agent Ryo Hagiwara -

Claims (1)

【特許請求の範囲】[Claims] マンガン・ノジュールからなる還元性ガス中硫化物除去
用脱硫剤。
A desulfurizing agent for removing sulfides in reducing gases consisting of manganese nodules.
JP59018430A 1984-02-06 1984-02-06 Desulfurizing agent Pending JPS60166033A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59018430A JPS60166033A (en) 1984-02-06 1984-02-06 Desulfurizing agent

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59018430A JPS60166033A (en) 1984-02-06 1984-02-06 Desulfurizing agent

Publications (1)

Publication Number Publication Date
JPS60166033A true JPS60166033A (en) 1985-08-29

Family

ID=11971427

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59018430A Pending JPS60166033A (en) 1984-02-06 1984-02-06 Desulfurizing agent

Country Status (1)

Country Link
JP (1) JPS60166033A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2318309A (en) * 1996-10-21 1998-04-22 Dytech Corp Ltd Desulphurisation
EP1404445A2 (en) * 2001-06-15 2004-04-07 M-I L.L.C. Process and composition for increasing the reactivity of sulfur scavenging oxides
CN107694321A (en) * 2017-10-27 2018-02-16 常州大学 A kind of normal temperature support type manganese hydrogen sulfide essence scavenger, its preparation method and application

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2318309A (en) * 1996-10-21 1998-04-22 Dytech Corp Ltd Desulphurisation
GB2318309B (en) * 1996-10-21 2001-05-16 Dytech Corp Ltd Desulphurisation
EP1404445A2 (en) * 2001-06-15 2004-04-07 M-I L.L.C. Process and composition for increasing the reactivity of sulfur scavenging oxides
EP1404445A4 (en) * 2001-06-15 2006-07-26 Mi Llc Process and composition for increasing the reactivity of sulfur scavenging oxides
CN107694321A (en) * 2017-10-27 2018-02-16 常州大学 A kind of normal temperature support type manganese hydrogen sulfide essence scavenger, its preparation method and application
CN107694321B (en) * 2017-10-27 2020-05-26 常州大学 Normal-temperature loaded manganese hydrogen sulfide fine remover, and preparation method and application thereof

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