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JPH0642899B2 - Deodorant for sulfur compounds - Google Patents
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JPH0642899B2 - Deodorant for sulfur compounds - Google Patents

Deodorant for sulfur compounds

Info

Publication number
JPH0642899B2
JPH0642899B2 JP63136902A JP13690288A JPH0642899B2 JP H0642899 B2 JPH0642899 B2 JP H0642899B2 JP 63136902 A JP63136902 A JP 63136902A JP 13690288 A JP13690288 A JP 13690288A JP H0642899 B2 JPH0642899 B2 JP H0642899B2
Authority
JP
Japan
Prior art keywords
particles
ferric oxide
sulfur
adsorption
gas
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 - Fee Related
Application number
JP63136902A
Other languages
Japanese (ja)
Other versions
JPH01305957A (en
Inventor
恵久 山本
是彦 西本
浩 藤田
俊治 原田
七生 堀石
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
Toda Kogyo Corp
Original Assignee
Mitsubishi Heavy Industries Ltd
Toda Kogyo Corp
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, Toda Kogyo Corp filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP63136902A priority Critical patent/JPH0642899B2/en
Publication of JPH01305957A publication Critical patent/JPH01305957A/en
Publication of JPH0642899B2 publication Critical patent/JPH0642899B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Disinfection, Sterilisation Or Deodorisation Of Air (AREA)

Description

【発明の詳細な説明】 〔産業上の用分野〕 本発明は、大気やガス中の硫化水素、メルカプタン、硫
化メチル、二硫化メチルの如き硫黄系悪臭物質や硫黄酸
化物等の硫黄化合物の吸着能、特に常温・乾式での使用
時における吸着能に優れた硫黄化合物用脱臭剤を提供す
るものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial field] The present invention is directed to the adsorption of sulfur compounds such as sulfur malodorous substances such as hydrogen sulfide, mercaptans, methyl sulfide and methyl disulfide in the atmosphere or gas and sulfur oxides. The present invention provides a deodorant for sulfur compounds, which is excellent in adsorption ability especially at room temperature and dry type.

〔従来の技術〕[Conventional technology]

大気やガス中の硫黄系悪臭物質や硫黄酸化物等の硫黄化
合物の存在は、公害として社会問題化している。
The presence of sulfur-based malodorous substances and sulfur compounds such as sulfur oxides in the atmosphere and gas has become a social problem as pollution.

特に、悪臭は生活環境を不快にするばかりでなく、「病
院設備」(Vol.27,No.6,1985年)第505頁の「……にお
いて身体に及ぼす影響については……呼吸器系、消化器
系、生殖器系、内分泌系などの各器官の働きおよび精神
状態への影響などがある……」なる記載の通り、健康に
影響する重大な問題となっている。
Especially, bad odor not only makes living environment uncomfortable, but also "Hospital equipment" (Vol.27, No.6, 1985), page 505, "... on the effects on the body ... Respiratory system, There are effects on the function of each organ such as the digestive system, reproductive system, endocrine system, and the mental state .... ”As described above, it is a serious problem affecting health.

また、近年の産業の発達に伴う燃焼炉の増大や自動車の
普及により、大量の排ガスが排出されており、種々の排
ガス対策が採られている。
In addition, a large amount of exhaust gas is being emitted due to the increase of combustion furnaces and the spread of automobiles with the development of industry in recent years, and various exhaust gas countermeasures have been adopted.

周知の通り、脱臭方法としては、アルカリ水溶液による
洗浄法、直接燃焼法、触媒酸化法、吸着法等がある。し
かし、アルカリ水溶液による洗浄法は、脱臭排液の処理
とか保守・管理が難しく、直接燃焼法、触媒酸化法は、
大量の空気を高温で燃焼する必要がある上に発生する亜
硫酸ガスの処理も必要となり有利な方法とはいえない。
As is well known, as the deodorizing method, there are a washing method using an alkaline aqueous solution, a direct combustion method, a catalytic oxidation method, an adsorption method and the like. However, the cleaning method using an alkaline aqueous solution is difficult to process and maintain the deodorizing waste liquid, and the direct combustion method and the catalytic oxidation method are
This is not an advantageous method because it requires a large amount of air to be burned at a high temperature and also requires treatment of sulfur dioxide gas generated.

それらに対して、比較的簡便で常温で用いることのでき
る吸着法が注目され、ガス中の硫黄系悪臭物質や硫黄酸
化物等の硫黄化合物の吸着能に優れた脱臭剤の開発が強
く要望されている。
Against these, an adsorption method that is relatively simple and can be used at room temperature is drawing attention, and there is a strong demand for the development of a deodorant having excellent adsorption ability for sulfur compounds such as sulfur malodorous substances and sulfur oxides in gases. ing.

脱臭剤としては、従来から活性炭、シリカゲル、ゼオラ
イト、酸化鉄等が知られている。
Activated carbon, silica gel, zeolite, iron oxide and the like have been conventionally known as deodorants.

〔発明が解決しようとする問題点〕[Problems to be solved by the invention]

前掲の公知脱臭剤の硫化水素、メルカプタン、硫化メチ
ル、二硫化メチルの如き硫黄系悪臭物質や硫黄酸化物等
の硫黄化合物に対する吸着能は、不十分であることが指
摘されている。
It has been pointed out that the above-mentioned known deodorizers have insufficient adsorbing ability for sulfur-based malodorous substances such as hydrogen sulfide, mercaptan, methyl sulfide and methyl disulfide, and sulfur compounds such as sulfur oxides.

この事実は、例えば、「フレグランス ジャーナル」
(No.72,1985年)第75頁の「……汎用の活性炭では……
硫化水素、メルカプタンなどの酸性ガスあるいは硫化メ
チル、アルデヒドなどの中性ガスに対して吸着能は低
い。……活性炭以外のシリカ・アルミナ系吸着剤は塩基
性または極性の強い臭気物質に対して親和性を呈する
が、ガス中に同伴する水分がより強く吸着するために臭
気物質の吸着が妨害される。ゼオライトについても広範
囲な種類の臭気分子に対して分子の大きさにより異なる
吸着親和性を示すが、水分の共存下では前者と同様に脱
臭が妨害される。……」なる記載や、日本化学会発行
「日本化学会誌」(1978年)第665頁の「二酸化硫黄を
吸着除去するために、活性炭をはじめ各種の金属酸化物
質などの無機化合物が研究されてきたが、吸着能力、選
択性、再生法などになお問題があり、新しい吸着剤の開
発が望まれている。」なる記載の通りである。
This fact is, for example, the "Fragrance Journal"
(No.72, 1985) Page 75, “…… For general-purpose activated carbon ……
It has low adsorption capacity for acidic gases such as hydrogen sulfide and mercaptan, and neutral gases such as methyl sulfide and aldehyde. ...... Silica / alumina-based adsorbents other than activated carbon have an affinity for odorants with strong basicity or polarity, but the adsorption of odorants is hindered by the stronger adsorption of water entrained in the gas. . Zeolite also has different adsorption affinities for a wide variety of odor molecules depending on the size of the molecule, but in the presence of water, deodorization is disturbed as in the former case. ...... "or" Chemical Society of Japan "published by the Chemical Society of Japan (1978), p. 665," Inorganic compounds such as activated carbon and various metal oxides have been studied to adsorb and remove sulfur dioxide. " However, there are still problems with the adsorption capacity, selectivity, regeneration method, etc., and the development of new adsorbents is desired. ”

一方、含水酸化第二鉄粒子粉末が硫黄系悪臭物質や硫黄
酸化物等の硫黄化合物に対する吸着能が優れていること
が知られている。
On the other hand, it is known that ferric oxide hydroxide particles have excellent adsorption ability for sulfur compounds such as sulfur malodorous substances and sulfur oxides.

この事実は、例えば、日本化学会発行「日本化学会誌」
(1980年)第681頁の「……含水酸化鉄がSO2を化学吸着
する能力が高いことを見い出して以来、SO2吸着材料と
しての可能性を検討する目的で、燃焼炉排ガス組成に近
い混合気体からのSO2吸着実験を行ない、SO2吸着能は共
存するHOの影響ををほとんどないことを知り、…
…」なる記載の通りである。
This fact is, for example, published by the Chemical Society of Japan "Chemical Society of Japan"
(1980) Page 681 “... Since we found that hydrous iron oxide has a high ability to chemisorb SO 2 , it is close to the combustion furnace exhaust gas composition for the purpose of examining its potential as an SO 2 adsorbent material. We conducted SO 2 adsorption experiments from a mixed gas, and learned that SO 2 adsorption capacity had almost no effect of coexisting H 2 O.
... "is as described.

尚、含水酸化第二鉄粒子粉末を硫黄化合物用脱臭剤とし
て用いている先行技術文献としては、特公昭46-20688号
公報や特開昭50-60492号公報等が挙げられる。
Incidentally, as prior art documents using the ferric oxide hydroxide particles as a deodorant for sulfur compounds, there are JP-B-46-20688 and JP-A-50-60492.

ところで、脱臭剤は、硫黄系悪臭物質や硫黄酸化物等の
硫黄化合物を脱臭剤の表面に吸着させるものであるか
ら、脱臭剤の比表面積が大きくなる程吸着能が増すの
で、脱臭剤は出来るだけ微細であることが要求される。
By the way, since the deodorant adsorbs sulfur compounds such as sulfur-based malodorous substances and sulfur oxides on the surface of the deodorant, the larger the specific surface area of the deodorant, the higher the adsorption capacity, and thus the deodorant can be formed. Only fineness is required.

この事実は、例えば、前出の日本化学会発行「日本化学
会誌」(1980年)第681頁の「固体表面の気体分子吸着
の研究においては、表面積の大きい粉体を用いることが
多い。……」なる記載の通りである。
This fact is because, for example, in the study of gas molecule adsorption on a solid surface, a powder having a large surface area is often used in "Chemical Society of Japan" (1980) p. ... "is as described.

従って、硫黄系悪臭物質や硫黄酸化物等の硫黄化合物を
吸着する脱臭剤として、含水酸化第二鉄粒子粉末の吸着
能、特に常温・乾式での使用時における吸着能を更に向
上させるために、粒子粉末の微粒子化が強く要求されて
いる。
Therefore, as a deodorant for adsorbing sulfur compounds such as sulfur-based malodorous substances and sulfur oxides, in order to further improve the adsorption ability of ferric oxide hydroxide particles, particularly the adsorption ability during use at room temperature and dry type, There is a strong demand for making fine particles of particles.

しかしながら、針状含水酸化第二鉄粒子粉末の場合、特
にそれが微細であればある程、粒子と粒子がくっついて
重なり合つて凝集するために、緻密で空隙率の小さなも
のとなって空気の透過性が悪くなり、大気やガス中の硫
黄系悪臭物質や硫黄酸化物等の硫黄化合物との接触面積
が小さなものとなり、吸着能が低下してしまうという問
題点がある。
However, in the case of needle-shaped ferric oxide hydroxide particles, in particular, the finer the particles are, the more particles stick to each other and agglomerate with each other. There is a problem in that the permeability becomes poor, the contact area with a sulfur-based malodorous substance in the air or gas or a sulfur compound such as sulfur oxide becomes small, and the adsorption ability decreases.

尚、前掲各公報に示されている純γ−オキシ水酸化鉄粒
子粉末やいがぐり状含水酸化第二鉄粒子粉末は、その粒
子形態に起因して硫黄化合物の吸着能に優れたものとは
考えられない。
In addition, the pure γ-iron oxyhydroxide particles powder and the urchin-shaped ferric oxide hydroxide particles shown in the above publications are considered to have excellent sulfur compound adsorption ability due to the particle morphology. I can't.

〔問題を解決する為の手段〕[Means for solving problems]

本発明者は、前記問題点の解決を技術的課題として、含
水酸化第二鉄粒子粉末の吸着能を向上させるべく、含水
酸化第二鉄粒子粉末の比表面積及び大気やガスとの接触
面積等について系統的な検討及び研究を重ねた結果、本
発明に到達したのである。
The present inventor, as a technical problem to solve the above problems, in order to improve the adsorption capacity of the ferric oxide hydroxide particles, the specific surface area of the ferric hydroxide particles powder and the contact area with the atmosphere or gas, etc. The present invention has been achieved as a result of repeated systematic examinations and studies of the above.

即ち、本発明は、スジ状の超微細構造を有している長軸
径0.2〜1.0μmで軸比(長軸径/短軸径)3〜10の笹の
葉状を呈した含水酸化第二鉄粒子粉末からなる硫黄化合
物用脱臭剤である。
That is, the present invention has a bamboo-like hydrous second oxide having a stripe-shaped ultrafine structure and having a major axis diameter of 0.2 to 1.0 μm and an axial ratio (major axis diameter / minor axis diameter) of 3 to 10. A deodorant for sulfur compounds, which is composed of iron particle powder.

〔作用〕[Action]

先ず、本発明において最も重要な点は、スジ状の超微細
構造を有している長軸径0.2〜1.0μmで軸比(長軸径/
短軸径)3〜10の笹の葉状を呈した含水酸化第二鉄粒子
粉末を脱臭剤として用いた場合には、比表面積が大き
く、且つ、大気やガスとの接触面積が大きいことに起因
して、大気やガス中の硫黄系悪臭物質や硫黄酸化物等の
硫黄化合物の吸着を効率よく、特に常温・乾式での使用
時においても効率よく行うことができるという事実であ
る。
First, the most important point in the present invention is that the axial ratio (major axis diameter / major axis diameter) is 0.2 to 1.0 μm, which has a stripe-shaped ultrafine structure.
(Short axis diameter) 3 to 10 leaves of bamboo hydroxide-like ferric oxide particles are used as a deodorant, due to their large specific surface area and large contact area with the atmosphere and gas. Then, it is a fact that the adsorption of sulfur compounds such as sulfur-based malodorous substances and sulfur oxides in the air or gas can be efficiently carried out, particularly when used at room temperature and dry type.

本発明に使用する含水酸化第二鉄微粒子粉末は、スジ状
の超微細構造を有している長軸径0.2〜1.0μmで軸比
(長軸径/短軸径)3〜10の笹の葉状を呈した粒子であ
るから比表面積が極めて大きい。
The ferric hydroxide-containing fine particle powder used in the present invention is a bamboo grass having a streaky ultrafine structure and a major axis diameter of 0.2 to 1.0 μm and an axial ratio (major axis diameter / minor axis diameter) of 3 to 10. Since the particles are leaf-shaped, the specific surface area is extremely large.

更に、本発明に使用する含水酸化第二鉄微粒子粉末は、
笹の葉状を呈して丸味を帯びている粒子であるから、粒
子と粒子がくっついて重なり合うことが少ないため、空
隙率が大きく空気の透過性もよいため、大気やガスとの
接触面積が大きい。
Furthermore, the hydrous ferric oxide fine particles used in the present invention,
Since the particles have a bamboo leaf shape and are rounded, particles are less likely to stick to each other and overlap each other, and have a large porosity and good air permeability, and thus have a large contact area with the atmosphere and gas.

即ち、本発明に使用する含水酸化第二鉄微粒子粉末は、
比表面積が大きく、且つ、大気やガスとの接触面積が大
きいことに起因して、大気やガス中の硫黄系悪臭物質や
硫黄酸化物等の硫黄化合物の吸着を効率よく行うことが
でき、脱臭剤として極めて優れている。
That is, the ferric oxide hydroxide fine powder used in the present invention,
Due to its large specific surface area and large contact area with air and gas, it is possible to efficiently adsorb sulfur compounds such as sulfur malodorous substances and sulfur oxides in air and gas, and to deodorize It is extremely excellent as an agent.

尚、本発明脱臭剤は、そのまま粉末状又はペレット状に
造粒成型して用いても良く、また、紙や布などに混入あ
るいは塗布し、これをハニカム構造、ラミネート構造に
成型して用いることもできる。更にハニカム構造及びラ
ミネート構造の基材に添着し、脱臭フィルターとして用
いることもできる。
The deodorant of the present invention may be used as it is by granulating it into powder or pellets, or by mixing or coating it on paper, cloth, etc., and molding it into a honeycomb structure or laminate structure for use. You can also Further, it can be attached to a substrate having a honeycomb structure or a laminated structure and used as a deodorizing filter.

後出「実施例1」の笹の葉状含水酸化第二鉄微粒子粉末
と後出「比較例1」の針状含水酸化第二鉄微粒子粉末及
び後出「比較例2」のいがぐり状含水酸化第二鉄粒子粉
末について、硫化水素の吸着能を測定した実験結果を実
験例として示す。
Bamboo leaf-shaped ferric oxide-containing ferric oxide fine powder of the following "Example 1", acicular hydrous ferric oxide fine-particle powder of the following "Comparative Example 1", and porridge-shaped hydrous hydroxide-containing fine powder of the following "Comparative Example 2". The experimental results of measuring the hydrogen sulfide adsorption capacity of the diiron particle powder are shown as experimental examples.

実験例1 前記の各含水酸化第二鉄粒子粉末のそれぞれを加圧成型
し、破砕して10〜20meshに粒度を揃えたものを試料とし
て、約0.4gをカラムに充填して循環式吸着速度評価装
置(「化学工業資料」Vol.20,No.4,(1985)第14頁記載の
評価方法)にセットし、次に濃度5ppmの硫化水素含有
の試験ガス10lの入ったテドラバックを該装置に取り付
けた。つづいて、流量5l/minの割合で試験ガスを試料
カラムに通気して循環させた。循環している試験ガスを
一定時間毎にサンプリングし、、サンプリングした試験
ガス中の硫化水素含有濃度をガスクロマトグラフィー法
で測定した値を図1に示す。
Experimental Example 1 Each of the ferric oxide hydroxide particles was pressure-molded and crushed to obtain a sample having a uniform particle size of 10 to 20 mesh. Set it on an evaluation device (Evaluation method described in “Chemical Industry Data”, Vol. 20, No. 4, (1985) page 14), and then put a tedra bag containing 10 l of a test gas containing hydrogen sulfide at a concentration of 5 ppm into the device. Attached to. Subsequently, the test gas was circulated by ventilating the sample column at a flow rate of 5 l / min. The circulating test gas is sampled at regular intervals, and the concentration of hydrogen sulfide contained in the sampled test gas is measured by gas chromatography.

図1より、後出「実施例1」の笹の葉状含水酸化第二鉄
微粒子粉末(図中の曲線A)は後出「比較例1」の針状
含水酸化第二鉄微粒子粉末(図中の曲線B)及び後出
「比較例2」のいがぐり状含水酸化第二鉄粒子粉末(図
中の曲線C)よりも、硫化水素の吸着性能が優れている
ことが確認できる。
From FIG. 1, the bamboo-leaf-shaped ferric hydroxide-containing fine particles (curve A in the figure) of “Example 1” described later are the acicular hydrous ferric-oxide fine particles of “Comparative Example 1” (see the figure). It can be confirmed that the adsorption performance of hydrogen sulfide is superior to that of the curve B) of No. 1 and the urchin-shaped ferric oxide hydroxide particles (curve C in the figure) of Comparative Example 2 described later.

実験例2 前記の各含水酸化第二鉄粒子粉末のそれぞれを実験例1
と同様10〜20meshに整粒したものを試料として、約0.4
gをカラムに充填して流通式吸着容量評価装置(講談社
サイエンティフィク発行「触媒実験ハンドブック」(触
媒学会編)(1986年)第44頁記載の評価方法)にセット
し、次に濃度10ppmの硫化水素含有の試験ガスを1l/min
の割合で試料カラムに通気した。試料カラムを通過した
試験ガスを一定時間毎にサンプリングし、サンプリング
した試験ガス中の硫化水素含有濃度をガスクロマトグラ
フィー法で測定した値を図2に示す。
Experimental Example 2 Each of the above-mentioned powders of ferric oxide hydroxide was tested in Experimental Example 1
Similar to the above, a sample that has been sized to 10 to 20 mesh is used,
The column was filled with g and set in a flow-through type adsorption capacity evaluation device (Kodansha Scientific published "Catalysis Experiment Handbook" (Catalysis Society of Japan) (1986), page 44), and then a concentration of 10 ppm Test gas containing hydrogen sulfide 1l / min
The sample column was vented at a rate of. The test gas that has passed through the sample column is sampled at regular intervals, and the concentration of hydrogen sulfide contained in the sampled test gas is measured by gas chromatography.

図2より、後出「実施例1」の笹の葉状含水酸化第二鉄
微粒子粉末(図中の曲線A)は後出「比較例1」の針状
含水酸化第二鉄微粒子粉末(図中の曲線B)及び後出
「比較例2」のいがぐり状含水酸化第二鉄粒子粉末(図
中の曲線C)よりも、硫化水素の吸着容量が大きいこと
が確認できる。
From FIG. 2, the bamboo-leaf-shaped ferric hydroxide-containing fine particles of the bamboo (curve A in the figure) of “Example 1” described later are the needle-shaped ferric-hydroxide-containing fine particles of the powder of “Comparative Example 1” (see the figure). It can be confirmed that the adsorption capacity of hydrogen sulfide is larger than that of the curve B) of No. 1 and the urchin-shaped ferric oxide hydroxide particles (curve C in the figure) of Comparative Example 2 below.

次に、本発明実施にあたっての諸条件について述べる。Next, various conditions for carrying out the present invention will be described.

本発明に使用する含水酸化第二鉄微粒子粉末は、スジ状
の超微細構造を有している長さ0.2〜1.0μmで軸比(長
軸径/短軸径)3〜10の笹の葉状を呈した含水酸化第二
鉄粒子からなる粉末である。
The ferric hydroxide-containing fine particle powder used in the present invention has a striped ultrafine structure, has a length of 0.2 to 1.0 μm, and has an axial ratio (major axis diameter / minor axis diameter) of 3 to 10 It is a powder consisting of ferric oxide hydroxide particles exhibiting the above.

長軸径が1.0μmを越える粒子は、比表面積が小さくな
り不適当であり、長軸径が0.2μm未満の粒子は、あま
りに微細なため粒子間の凝集が生じて好ましくない。
Particles having a major axis diameter of more than 1.0 μm are unsuitable because they have a small specific surface area, and particles having a major axis diameter of less than 0.2 μm are undesirably agglomerated between particles because they are too fine.

また、軸比が3未満の粒子は、スジ状の超微細構造を有
している笹の葉状を呈するという粒子の特徴が小さくな
り、軸比が10を越える粒子は、針状の形状に近くなり好
ましくない。
In addition, particles with an axial ratio of less than 3 have a smaller characteristic that the particles have a bamboo-like shape with a stripe-shaped ultrafine structure, and particles with an axial ratio of more than 10 have a needle-like shape. It is not preferable.

本発明に使用する含水酸化第二鉄微粒子粉末は、次の通
りの製造法によって容易に得られる。
The ferric oxide hydroxide fine particle powder used in the present invention can be easily obtained by the following production method.

即ち、第一鉄塩水溶液に第一鉄塩に対して1当量以上の
炭酸アルカリ水溶液を加え、反応させてFeCO3を得、得
られたFeCO3を含む懸濁液中に酸素含有ガスを通気し
て、酸化反応することにより得られる。
That is, 1 equivalent or more of an aqueous solution of an alkali carbonate with respect to the ferrous salt is added to the ferrous salt aqueous solution and reacted to obtain FeCO 3 , and an oxygen-containing gas is passed through the obtained suspension containing FeCO 3 . Then, it is obtained by an oxidation reaction.

上記製造法において、第一鉄塩水溶液としては、硫酸第
一鉄水溶液、塩化第一鉄水溶液等が用いられる。第一鉄
塩水溶液に炭酸アルカリ水溶液又は炭酸アルカリ・水酸
化アルカリ水溶液を加えFeCO3又はFe含有沈澱物を得る
場合、炭酸アルカリの一部を炭酸アルカリに対し50%以
下の範囲で水酸化アルカリで置換して使用してもよい。
炭酸アルカリとしては、炭酸ナトリウム、炭酸カリウ
ム、炭酸水素アンモニウム等を単独で、又は、これらと
水酸化アルカリを併用して使用する場合は、水酸化ナト
リウム、水酸化カリウム、水酸化アンモニウム等が用い
られる。また、場合により非酸化性雰囲気下で熟成して
もよい。
In the above production method, as the aqueous ferrous salt solution, an aqueous ferrous sulfate solution, an aqueous ferrous chloride solution, or the like is used. When an aqueous solution of ferrous salt or an aqueous solution of alkali carbonate or an alkali hydroxide is added to an aqueous solution of ferrous salt to obtain FeCO 3 or Fe-containing precipitate, a part of the alkali carbonate is treated with alkali hydroxide within a range of 50% or less with respect to the alkali carbonate. You may replace and use it.
As the alkali carbonate, sodium carbonate, potassium carbonate, ammonium hydrogen carbonate or the like is used alone, or when these are used in combination with alkali hydroxide, sodium hydroxide, potassium hydroxide, ammonium hydroxide or the like is used. . Further, in some cases, it may be aged under a non-oxidizing atmosphere.

酸化反応時の溶液のpHは7〜11である。pH7未満、又
は、pH11を越える場合には、笹の葉状を呈した含水酸化
第二鉄粒子を得ることはできない。
The pH of the solution during the oxidation reaction is 7-11. When the pH is less than 7 or more than 11, the bamboo-leaf-shaped ferric oxide hydroxide particles cannot be obtained.

酸化時における反応温度は、30〜80℃である。30℃未満
では、笹の葉状を呈した含水酸化第二鉄粒子を得ること
ができず、80℃を越える場合には、粒状の黒色沈澱が
混在してくる。
The reaction temperature during oxidation is 30 to 80 ° C. Below 30 ° C, bamboo-leaf-shaped ferric oxide hydroxide particles cannot be obtained, and above 80 ° C, granular black precipitates are mixed.

酸化手段は、酸素含有ガス(例えば、空気)を液中に通
気することにより行い、また、当該通気ガスや機械的操
作等により撹拌しながら行う。
The oxidizing means is performed by aerating an oxygen-containing gas (for example, air) in the liquid, and is performed while stirring by the aeration gas or mechanical operation.

〔実施例〕〔Example〕

次に、実施例並びに比較例により本発明を説明する。以
下の実施例並びに比較例における粒子径、軸比(長軸径
/短軸径)は、いずれも電子顕微鏡写真から測定した数
値の平均値で示したものであり、比表面積はBET法によ
り測定した値で示した。また、硫化水素の吸着性能は、
前出実験例1の方法で評価した値であり、硫化水素の吸
着容量は、前出実験例2の方法で評価した値である。
Next, the present invention will be described with reference to Examples and Comparative Examples. The particle diameters and axial ratios (major axis diameter / minor axis diameter) in the following examples and comparative examples are all shown as the average value of the numerical values measured from electron micrographs, and the specific surface area is measured by the BET method. It was shown by the value. Also, the adsorption performance of hydrogen sulfide is
It is the value evaluated by the method of the above-mentioned Experimental Example 1, and the adsorption capacity of hydrogen sulfide is the value evaluated by the method of the above-mentioned Experimental Example 2.

実施例1 反応容器中に3.53mol/lのNaCO3水溶液20lを入れ、次い
で、1.0mol/lのFeSO4水溶液30lを添加、混合し、温度4
0℃においてFeCO3を得た。得られたFeCO3を含む水溶液
中に温度40℃において、毎分150lの空気を4.0時間通気
して酸化反応を行い、黄褐色沈澱粒子を生成させた。
尚、空気通気中の反応溶液のpHは9.6であった。
Example 1 20 l of a 3.53 mol / l aqueous solution of NaCO 3 was placed in a reaction vessel, and then 30 l of a 1.0 mol / l aqueous solution of FeSO 4 was added and mixed to obtain a temperature of 4
FeCO 3 was obtained at 0 ° C. At a temperature of 40 ° C., 150 l of air per minute was passed for 4.0 hours in the obtained aqueous solution containing FeCO 3 to carry out an oxidation reaction to generate yellowish brown precipitate particles.
The pH of the reaction solution during aeration with air was 9.6.

生成した黄褐色沈澱粒子を常法により、別、水洗、乾
燥、粉砕して黄褐色粒子粉末2.61kgを得た。
The produced yellowish brown precipitate particles were separated, washed with water, dried and pulverized by a conventional method to obtain 2.61 kg of yellowish brown particle powder.

得られた黄褐色粒子粉末は、X線回折の結果、含水酸化
第二鉄であることが確認できた。その結果を図3にす。
また、得られた黄褐色粒子粉末は、図4に示す電子顕微
鏡写真(×30,000)及び図5に示すその拡大写真(×15
0,000)の通り、平均値で長軸径0.25μm、軸比(長軸
径/短軸径)8、比表面積106m2/gのスジ状の超微細構
造を有している笹の葉状を呈した含水酸化第二鉄粒子か
らなっていることが確認できた。
As a result of X-ray diffraction, the obtained yellowish brown particle powder could be confirmed to be hydrous ferric oxide. The result is shown in FIG.
Also, the obtained yellowish brown particle powder is an electron micrograph (× 30,000) shown in FIG. 4 and an enlarged photograph (× 15) shown in FIG.
(0,000), the average value of the major axis diameter is 0.25 μm, the axial ratio (major axis diameter / minor axis diameter) is 8, and the surface area is 106 m 2 / g. It was confirmed that the particles were composed of ferric oxide hydroxide particles.

上記笹の葉状含水酸化第二鉄微粒子粉末の硫化水素の吸
着性能は、15分間通気後の試験ガスの濃度が0.16ppm、
吸着容量は、120分間通気した後の試験ガスの濃度が0.2
0ppmであった。
The adsorption performance of hydrogen sulfide of the bamboo leaf-shaped ferric oxide hydroxide particles as described above, the concentration of the test gas after aeration for 15 minutes is 0.16 ppm,
The adsorption capacity is such that the concentration of the test gas after aeration for 120 minutes is 0.2.
It was 0 ppm.

比較例1 反応容器中に0.68mol/lのFeSO4/g水溶液80lを入れ、次
いで、4.32mol/lのNaOH水溶液10lを添加、混合し、続
いて、温度40℃において、毎分130lの割合で空気を通
気しながら、4時間反応を行い、黄褐色沈澱粒子を生成
させた。尚、空気通気中の反応溶液のpHは5.8〜4.0であ
った。
Comparative Example 1 80 l of 0.68 mol / l FeSO 4 / g aqueous solution was placed in a reaction vessel, then 10 l of 4.32 mol / l NaOH aqueous solution was added and mixed, and subsequently, at a temperature of 40 ° C., a rate of 130 l / min. The reaction was carried out for 4 hours while air was blown through to produce yellowish brown precipitate particles. The pH of the reaction solution during aeration was 5.8 to 4.0.

生成した黄褐色沈澱粒子を常法により、別、水洗、乾
燥、粉砕して黄褐色粒子粉末1.83kgを得た。
The produced yellowish brown precipitate particles were separated, washed with water, dried and pulverized by a conventional method to obtain 1.83 kg of yellowish brown particle powder.

得られた黄褐色粒子粉末は、X線回折の結果、含水酸化
第二鉄であることが確認できた。その結果を図6に示
す。また、得られた黄褐色粒子粉末は、図7に示す電子
顕微鏡写真(×30,000)及び図8に示すその拡大写真
(×100,000)の通り、平均値で長軸径0.3μm、軸比
(長軸径/短軸径)10、比表面積95m2/gの針状含水酸
化第二鉄粒子からなっていることが確認できた。
As a result of X-ray diffraction, the obtained yellowish brown particle powder could be confirmed to be hydrous ferric oxide. The result is shown in FIG. The obtained yellowish brown particle powder has an average long axis diameter of 0.3 μm and an axial ratio (long axis) as shown in an electron micrograph (× 30,000) shown in FIG. 7 and an enlarged photograph (× 100,000) shown in FIG. It was confirmed that the particles consisted of acicular hydrous iron oxide particles having a shaft diameter / minor axis diameter of 10 and a specific surface area of 95 m 2 / g.

上記針状含水酸化第二鉄粒子粉末の硫化水素の吸着性能
は、15分間通気後の試験ガスの濃度が0.42ppm、吸着容
量は、120分間通気した後の試験ガスの濃度が0.90ppmで
あった。
The adsorption performance of hydrogen sulfide of the acicular hydrous ferric oxide particles is 0.42 ppm for the test gas after aeration for 15 minutes, and the adsorption capacity is 0.90 ppm for the test gas after aeration for 120 minutes. It was

比較例2 反応容器中に1.57mol/lのFeSO4水溶液5lを加え、温
度を30℃に調節した。次いで、毎分20lの割合で空気を
吹き込みながら、4mol/lのアンモニア水溶液0.2l
(アンモニアの量は全Fe量に対し5.0%に該当する。)
で中和し、黄褐色の種子を含む水溶液を得た。この時の
pHは約3であった。
Comparative Example 2 5 l of a 1.57 mol / l FeSO 4 aqueous solution was added to the reaction vessel, and the temperature was adjusted to 30 ° C. Then, while blowing air at a rate of 20 liters per minute, 0.2 liter of a 4 mol / l aqueous ammonia solution
(The amount of ammonia corresponds to 5.0% of the total Fe amount.)
Was neutralized with to obtain an aqueous solution containing yellowish brown seeds. At this time
The pH was about 3.

引き続き、毎分201の割合で空気を通気しながら、反応
温度を80℃に調節し、4mol/lのアンモニア水溶液をpH
2.5〜4.0の範囲に保持するように加え、酸化反応を5時
間反応を行った。
Then, while aerating air at a rate of 201 per minute, the reaction temperature was adjusted to 80 ° C and the pH of the 4 mol / l aqueous ammonia solution was adjusted.
The addition was carried out so as to maintain the range of 2.5 to 4.0, and the oxidation reaction was carried out for 5 hours.

生成した黄褐色沈澱粒子を常法により、別、水洗、乾
燥、粉砕して黄褐色粒子粉末629gを得た。
The produced yellowish brown precipitate particles were separated, washed with water, dried and pulverized by a conventional method to obtain 629 g of yellowish brown particle powder.

得られた黄褐色粒子粉末は、電子顕微鏡観察の結果、い
がぐり状含水酸化第二鉄粒子からなっていることが確認
できた。
As a result of electron microscopic observation, it was confirmed that the obtained yellowish brown particle powder was composed of porcelain ferric hydroxide particles.

また、この粒子粉末は、平均値で直径が0.9μm、比表
面積85m2/gであった。
The particle powder had an average diameter of 0.9 μm and a specific surface area of 85 m 2 / g.

上記いがぐり状含水酸化第二鉄粒子粉末の硫化水素の吸
着性能は、15分間通気後の試験ガスの濃度が0.27ppm、
吸着容量は、120分間通気した後の試験ガスの濃度が0.6
5ppmであった。
The hydrogen sulfide adsorption performance of the above-mentioned burdock-shaped ferric hydroxide particles, the concentration of the test gas after aeration for 15 minutes is 0.27 ppm,
The adsorption capacity was such that the test gas concentration after aeration for 120 minutes was 0.6.
It was 5 ppm.

〔発明の効果〕〔The invention's effect〕

本発明に係る硫黄化合物用脱臭剤は、大気やガス中の硫
黄系悪臭物質や硫黄酸化物等の硫黄化合物の吸着能、特
に常温・乾式での使用時における吸着能に優れている
為、硫黄化合物用脱臭剤として最適である。
The deodorant for sulfur compounds according to the present invention is excellent in adsorption ability of sulfur compounds such as sulfur malodorous substances and sulfur oxides in the air or gas, especially since it is excellent in adsorption ability at the time of use at room temperature and dry type. Most suitable as a deodorant for compounds.

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

図1は実験例1で求めた含水酸化第二鉄粒子粉末の硫化
水素の吸着性能の評価結果を示すものである。 図2は実験例2で求めた含水酸化第二鉄粒子粉末の硫化
水素の吸着容量の評価結果を示すものである。 図1及び図2の図中の曲線Aは実施例1で得られた含水
酸化第二鉄微粒子粉末、曲線Bは比較例1で得られた含
水酸化第二鉄微粒子粉末及び曲線Cは比較例2で得られ
た含水酸化第二鉄粒子粉末である。 図3は、実施例1で得られた含水酸化第二鉄微粒子粉末
のX線回折図であり、図中のピークはα-FeOOHである。
図4は、実施例1で得られた含水酸化第二鉄微粒子粉末
の粒子構造を示す電子顕微鏡写真(×30,000)であり、
図5は、その拡大写真(×150,000)である。 図6は、比較例1で得られた含水酸化第二鉄微粒子粉末
のX線回折図であり、図中のピークはα-FeOOHである。
図7は、比較例1で得られた含水酸化第二鉄微粒子粉末
の粒子構造を示す電子顕微鏡写真(×30,000)であり、
図8は、その拡大写真(×100,000)である。
FIG. 1 shows the evaluation results of the hydrogen sulfide adsorption performance of the ferric oxide hydroxide particles obtained in Experimental Example 1. FIG. 2 shows the evaluation results of the hydrogen sulfide adsorption capacity of the ferric oxide hydroxide powder obtained in Experimental Example 2. In FIGS. 1 and 2, a curve A is a ferric oxide hydroxide fine particle powder obtained in Example 1, a curve B is a ferric hydroxide fine particle powder obtained in Comparative Example 1, and a curve C is a comparative example. It is the ferric oxide hydroxide particle powder obtained in 2. FIG. 3 is an X-ray diffraction pattern of the ferric oxide-containing fine iron oxide powder obtained in Example 1, and the peak in the figure is α-FeOOH.
FIG. 4 is an electron micrograph (× 30,000) showing the particle structure of the ferric oxide hydroxide fine powder obtained in Example 1.
FIG. 5 is an enlarged photograph (× 150,000). FIG. 6 is an X-ray diffraction pattern of the ferric oxide-containing fine iron oxide powder obtained in Comparative Example 1, and the peak in the figure is α-FeOOH.
FIG. 7 is an electron micrograph (× 30,000) showing the particle structure of the ferric hydroxide-containing fine particle powder obtained in Comparative Example 1.
FIG. 8 is an enlarged photograph (× 100,000).

───────────────────────────────────────────────────── フロントページの続き (72)発明者 堀石 七生 広島県広島市東区牛田東3丁目29―5 審査官 川端 修 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Nansei Horiishi 29-5 Ushidahigashi, Higashi-ku, Hiroshima City, Hiroshima Prefecture Examiner Osamu Kawabata

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】スジ状の超微細構造を有している長軸径0.
2〜1.0μmで軸比(長軸径/短軸径)3〜10の笹の葉状
を呈した含水酸化第二鉄粒子粉末からなる硫黄化合物用
脱臭剤。
1. A major axis diameter of 0.1 which has a stripe-shaped ultrafine structure.
A deodorant for sulfur compounds, which comprises a powder of ferric oxide hydroxide particles in the form of bamboo leaves having an axial ratio (major axis diameter / minor axis diameter) of 3 to 10 at 2 to 1.0 μm.
JP63136902A 1988-06-02 1988-06-02 Deodorant for sulfur compounds Expired - Fee Related JPH0642899B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63136902A JPH0642899B2 (en) 1988-06-02 1988-06-02 Deodorant for sulfur compounds

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63136902A JPH0642899B2 (en) 1988-06-02 1988-06-02 Deodorant for sulfur compounds

Publications (2)

Publication Number Publication Date
JPH01305957A JPH01305957A (en) 1989-12-11
JPH0642899B2 true JPH0642899B2 (en) 1994-06-08

Family

ID=15186240

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63136902A Expired - Fee Related JPH0642899B2 (en) 1988-06-02 1988-06-02 Deodorant for sulfur compounds

Country Status (1)

Country Link
JP (1) JPH0642899B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3174565B2 (en) * 1990-03-22 2001-06-11 三菱重工業株式会社 Deodorizing filter
JP5017779B2 (en) * 2005-01-11 2012-09-05 東洋紡績株式会社 Organic compound adsorption remover and method for producing the same

Also Published As

Publication number Publication date
JPH01305957A (en) 1989-12-11

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