JPS5834051A - Classification of dust - Google Patents
Classification of dustInfo
- Publication number
- JPS5834051A JPS5834051A JP13172081A JP13172081A JPS5834051A JP S5834051 A JPS5834051 A JP S5834051A JP 13172081 A JP13172081 A JP 13172081A JP 13172081 A JP13172081 A JP 13172081A JP S5834051 A JPS5834051 A JP S5834051A
- Authority
- JP
- Japan
- Prior art keywords
- zinc
- dust
- particulate substance
- slurry
- liquid cyclone
- 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
Links
Landscapes
- Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
Abstract
Description
【発明の詳細な説明】
この発明は液体サイクロンによってダスト中の亜鉛を分
級する方法の改良に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an improvement in a method for classifying zinc in dust using a hydrocyclone.
一般に高炉ダストの脱亜鉛のため、液体サイク、ロンが
使用されている。即ち液体サイクロンにより分級された
アンダーフロー側の粗粒物には亜鉛が少なく、オーバー
フロー側の微粒物には亜鉛が多く分級されていて、亜鉛
の少ない粗粒物を鉄源(焼結原料)として回収している
。Generally, a liquid cyclone is used to dezincify blast furnace dust. In other words, the coarse particles on the underflow side classified by the hydrocyclone contain less zinc, and the fine particles on the overflow side contain more zinc, and the coarse particles with less zinc are used as the iron source (sintering raw material). It is being collected.
なお高炉ダストは表1の高炉ダストの化学成分に示すよ
うに炭素分と鉄分とを多く含んでいて、亜鉛が少なけれ
ば良好な鉄源(焼結原料)となるため、効果的な脱亜鉛
法が期待されている。As shown in the chemical composition of blast furnace dust in Table 1, blast furnace dust contains a large amount of carbon and iron, and if it contains less zinc, it becomes a good source of iron (raw material for sintering), making it an effective dezincing method. is expected.
而して高炉ダストを調査してみると、大部分は装入原料
に起因する粗粒物と、高炉内で還元されて蒸発したのち
再酸化されたところの比較的少量の低融点金属(亜鉛、
アルカリ、その他)の微粒酸化物とから構成されている
。したがって前述の如く高炉ダストを分級処理すれば、
オーバーフロー側の微粒物中に亜鉛が富化されることに
なる。When blast furnace dust was investigated, it was found that most of it was coarse particles originating from the charged raw materials, and a relatively small amount of low melting point metal (zinc) that had been reduced and evaporated in the blast furnace and then reoxidized. ,
It is composed of fine oxides of alkalis, etc.). Therefore, if blast furnace dust is classified as described above,
Zinc will be enriched in the fine particles on the overflow side.
さらにこれら粒状物を詳細に調査してみると、低融点金
属の微粒酸化物が粗粒物表面へかなり強固に固着してい
ることがわかった。Furthermore, when these particles were investigated in detail, it was found that fine oxide particles of low melting point metals were quite firmly adhered to the surface of the coarse particles.
、而して脱亜鉛のため、高炉ダストを液体サイクロンで
分級処理を行う場合には、あらかじめ粗粒物に固着した
微粒状の亜鉛等を分離する工程が必要となる。そのため
従来は第1図に示す如く高炉ダストスラリーを混合攪拌
する方法が採用されているが、この方法はかなり時間を
要すほか、大きな攪拌槽を設置しなければならない欠点
があった。Therefore, when blast furnace dust is classified using a liquid cyclone for dezincing, a step is required in advance to separate fine particles of zinc etc. stuck to coarse particles. Conventionally, therefore, a method of mixing and stirring the blast furnace dust slurry as shown in FIG. 1 has been adopted, but this method requires a considerable amount of time and has the disadvantage of requiring the installation of a large stirring tank.
この発明はこれらの欠点を改善するためになされたもの
であり、粗粒物に固着した微粒状亜鉛の分離方法につい
て種々検討した結果、ダストスラリーを超音波で処理す
ると粗粒物に固着した微粒状亜鉛が容易に剥離すること
を確認した。This invention was made to improve these drawbacks, and as a result of various studies on methods for separating fine zinc particles stuck to coarse particles, it was found that when dust slurry is treated with ultrasonic waves, fine particles stuck to coarse particles are removed. It was confirmed that the shaped zinc was easily peeled off.
即ち第2図に示す如くこの発明に係るダストの分級方法
は、スラリー化したダストを超音波処理したのち、液体
サイクロンを通して分級することを特徴とするものであ
る。That is, as shown in FIG. 2, the method for classifying dust according to the present invention is characterized in that the slurry of dust is subjected to ultrasonic treatment and then classified through a liquid cyclone.
而して高炉ダストスラリーを従来の攪拌槽による混合攪
拌処理と、この発明による超音波処理と別々に事前処理
を行ない、それぞれ液体サイ゛クロンで分級して得られ
た粗粒物の亜鉛量を分析し、表2で示される結果を得た
。The blast furnace dust slurry was pre-treated separately by mixing and stirring in a conventional stirring tank and by ultrasonication according to the present invention, and the amount of zinc in the coarse particles obtained by classifying each with a hydrocyclone was determined. The results were analyzed and shown in Table 2.
なお供試料として表1に示された成分の高炉ダストを用
い、分級条件は全く同一(フィード圧力s O,95k
q/cd 、サイフオン圧力;O肩wHq)にして3回
の繰り返し実験を行った。Blast furnace dust with the components shown in Table 1 was used as the sample, and the classification conditions were exactly the same (feed pressure sO, 95k
q/cd, siphon pressure; O shoulder wHq), and the experiment was repeated three times.
表2 事前処理決別の粗粒物中の亜鉛量即ち表2に示す
如くこの発明方法によれば、粗粒物中の亜鉛量が従来方
法の権となり、高炉ダストの処理による粗粒物を介して
高炉へ装入される鉄諒中の1++<船間を従来の卦に低
減することが由来た。Table 2 The amount of zinc in the coarse particles of the pre-treatment separation, that is, as shown in Table 2, according to the method of this invention, the amount of zinc in the coarse particles is the control over the conventional method, and the amount of zinc in the coarse particles by the treatment of blast furnace dust is The origin of this idea was to reduce the distance between 1++ and the ship to the conventional value in the amount of iron that is charged into the blast furnace.
而して超音波処理は、超音波発振器を液体サイクロンの
供給側スラリー配管に設置するのみで超音波処理が可能
なため、攪拌槽の如き処理槽は不安であり、しかも剥離
分散処理に要する別途処理時間を必要としない利点があ
る。However, since ultrasonic treatment can be carried out simply by installing an ultrasonic oscillator in the slurry piping on the supply side of the liquid cyclone, a treatment tank such as a stirring tank is not reliable, and additionally, it requires separate processing for stripping and dispersion treatment. It has the advantage of not requiring processing time.
第1図は従来のダストの分級方法を示すフローノート、
第2図はこの発明のダストの分級方法を示すフローシー
トである。Figure 1 is a flow note showing the conventional dust classification method.
FIG. 2 is a flow sheet showing the dust classification method of the present invention.
Claims (1)
クロンを通して分級することを特徴とするダストの分級
方法。、A dust classification method characterized by subjecting slurry-formed dust to ultrasonic treatment and then classifying it through a liquid cyclone. ,
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13172081A JPS5834051A (en) | 1981-08-21 | 1981-08-21 | Classification of dust |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13172081A JPS5834051A (en) | 1981-08-21 | 1981-08-21 | Classification of dust |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS5834051A true JPS5834051A (en) | 1983-02-28 |
Family
ID=15064619
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP13172081A Pending JPS5834051A (en) | 1981-08-21 | 1981-08-21 | Classification of dust |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5834051A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7673516B2 (en) | 2006-12-28 | 2010-03-09 | Kimberly-Clark Worldwide, Inc. | Ultrasonic liquid treatment system |
US7740666B2 (en) | 2006-12-28 | 2010-06-22 | Kimberly-Clark Worldwide, Inc. | Process for dyeing a textile web |
US9421504B2 (en) | 2007-12-28 | 2016-08-23 | Kimberly-Clark Worldwide, Inc. | Ultrasonic treatment chamber for preparing emulsions |
-
1981
- 1981-08-21 JP JP13172081A patent/JPS5834051A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7673516B2 (en) | 2006-12-28 | 2010-03-09 | Kimberly-Clark Worldwide, Inc. | Ultrasonic liquid treatment system |
US7740666B2 (en) | 2006-12-28 | 2010-06-22 | Kimberly-Clark Worldwide, Inc. | Process for dyeing a textile web |
US9421504B2 (en) | 2007-12-28 | 2016-08-23 | Kimberly-Clark Worldwide, Inc. | Ultrasonic treatment chamber for preparing emulsions |
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