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JPH0460058B2 - - Google Patents
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JPH0460058B2 - - Google Patents

Info

Publication number
JPH0460058B2
JPH0460058B2 JP62116953A JP11695387A JPH0460058B2 JP H0460058 B2 JPH0460058 B2 JP H0460058B2 JP 62116953 A JP62116953 A JP 62116953A JP 11695387 A JP11695387 A JP 11695387A JP H0460058 B2 JPH0460058 B2 JP H0460058B2
Authority
JP
Japan
Prior art keywords
slag
blast furnace
iron
furnace slag
molten
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
JP62116953A
Other languages
Japanese (ja)
Other versions
JPS63285134A (en
Inventor
Akira Seki
Sukeyoshi Narita
Minoru Mita
Tsuneo Fujisawa
Toyoji Iemura
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.)
JFE Mineral Co Ltd
Original Assignee
Kawatetsu Mining Co 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 Kawatetsu Mining Co Ltd filed Critical Kawatetsu Mining Co Ltd
Priority to JP62116953A priority Critical patent/JPS63285134A/en
Publication of JPS63285134A publication Critical patent/JPS63285134A/en
Publication of JPH0460058B2 publication Critical patent/JPH0460058B2/ja
Granted legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B2400/00Treatment of slags originating from iron or steel processes
    • C21B2400/02Physical or chemical treatment of slags
    • C21B2400/022Methods of cooling or quenching molten slag
    • C21B2400/024Methods of cooling or quenching molten slag with the direct use of steam or liquid coolants, e.g. water
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B2400/00Treatment of slags originating from iron or steel processes
    • C21B2400/05Apparatus features
    • C21B2400/062Jet nozzles or pressurised fluids for cooling, fragmenting or atomising slag

Landscapes

  • Glass Compositions (AREA)
  • Manufacture Of Iron (AREA)

Description

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

〔産業上の利用分野〕 本発明は高炉スラグからガラス製造に使用され
る原料を製造する方法に関するものである。 〔従来の技術〕 従来高炉スラグを用いてガラス原料とすること
は知られており例えば次のような方法がある。 1 炉から放出された溶融スラグをピツト等に流
し込んで自然冷却して固化せしめ、この際不純
物を沈降させて不純物の少ない上方のスラグの
みを取出して粉砕し、磁選機にかけて鉄分を除
去する方法(特公昭52−21003号)。 2 溶融スラグに水を噴射して水砕スラグとしそ
のまま用いるか又は磁選鉱操作により鉄分を除
去する方法。 3 高炉から放出された溶融スラグを、出滓樋の
途中に設けた溶鉄分離槽を通し、ここで鉄分を
分離した後なお溶融状態にあるスラグを水砕化
する方法(特開昭54−124013号)。 等がある。 〔発明が解決しようとする問題点〕 しかしながら上記のような従来法においては次
のような欠点がある。例えば1)、の方法におい
ては、高炉スラグが自然の徐冷スラグであるか
ら、一定の粒度を得るために充分な破砕操作が必
要であり、このため過大な破砕エネルギーを消費
し、またガラス原料として高炉スラグを使用する
場合極めて有害とされる鉄分は沈降では充分除去
されず、固結スラグ中には、なお平均してFe2O3
が1.5%程度含有されており、磁選によつて脱鉄
しても約0.8%程度にしか低減されないので、ガ
ラス原料としては満足なものとは言えない。 また2)、の方法は、粉砕する必要はないがそ
のままでは溶鉄分が多く含まれており、磁選によ
る脱鉄では充分に鉄分を除去できない。さらに、
スラグ中には高炉中の耐火物のコランダム
(Al2O3)等が通常数4ppm程度混入しており、こ
れは磁選では除去できない。したがつてガラス原
料に用いると、コランダムは融点が高い(融点
2015℃)ため溶けきらず小粒状で存在し、ガラス
に欠陥が生ずる原因となる。 なお3)、の方法は溶鉄分離の過程で高炉の耐
火物のコランダムは鉄分と共に沈降して分離され
るとしても、次いで水砕スラグとなす工程までの
間でスラグは耐火物の樋を通つて運ばれるので、
ここで混入した耐火物のコランダムは水砕スラグ
中に残留することになり、前記と同様ガラス原料
としては好ましくない。 本発明はこのような従来の問題点を解決し、鉄
その他の重金属は勿論のことコランダムも確実に
除去することにより、高炉スラグを原料として優
れたガラス原料を得る方法を提供するものであ
る。 〔問題点を解決するための手段〕 すなわち本発明は溶融高炉スラグに圧力水を噴
射して水砕スラグとなした後、比重選鉱手段を適
用して鉄分と同時にその他のガラス原料として有
害な不純物である高融点化合物を除去することを
特徴とする高炉スラグからガラス原料を製造する
方法である。 本発明において比重選鉱手段としては、乾式、
湿式いずれの比重選鉱装置も適用することができ
る。また必要に応じ該比重選鉱手段の適用前又は
後に磁力選別操作を行なう工程を付加してもよ
く、この場合鉄分の除去は一層確実となる。 以下実施例をあげて本発明を更に明らかにす
る。 実施例 1 高炉出滓樋から落下する溶融スラグ流に圧力水
を噴射し細粒化及び急冷を行ない得られた水砕ス
ラグを約20メツシで分級した後、乾式比重選鉱機
((株)原島総業社製MH−551型)にかけて比重
分離を行つた。 選鉱条件は下記のとおりである。 風速 0.7〜1.3m/sec 振動数 600rpm 振幅 5mm 前後角度 4° 左右角度 1.5° 試料は第1図に示すように矢印方向に流れ下部
に回収され、鉄鉱物、コランダム等のガラス原料
に有害なものがT、ガラス原料に使用できるもの
がCで回収される。 回収されたガラス原料Cの、Fe2O3品位、コラ
ンダム量は表−1に示すとおりであつた。この結
果から、Fe2O3の低下及びコランダムの除去効果
が確認された。 なお、コランダム量は、比重4.0〜4.1g/cm3
あるため2種の重液(比重3.23g/cm3,4.5g/cm3
で分離して求めた。 実施例 2 20メツシで分級した水砕スラグを磁場の強さを
5000ガウスで磁力選鉱を行なつた後、乾式比重選
鉱機により実施例1と同じ条件で比重選鉱を行な
つた。結果は表−1に示すとおりである。 実施例 3 水砕スラグを20メツシで分級した後、実施例1
と同じ条件で乾式比重選鉱機により比重選鉱し、
得られたものを更に磁力選鉱を磁場の強さ5000ガ
ウスで選鉱した。結果は表−1に示すとおりであ
る。 比較例 1 溶融スラグ約20tonを1.2m×1.2m×1.4m深の約
7m3ピツトに流し込んで8日間自然冷却して固化
させた。 固化後、表層より約1mまでの上層部を掘り出
し、粉砕機にて粉砕し、磁場の強さ5000ガウスの
磁選機にて鉄分を除去した。 結果を表−1に示す。 比較例 2 溶融スラグに水を噴射して水砕スラグとし、そ
の後、磁場の強さ5000ガウスの磁選機にて鉄分を
除去した。 結果を表−1に示す。 比較例 3 溶融スラグを200mlのルツボにて約1500℃で再
溶融し、その後、炉外へ取り出し、傾斜法にて、
溶融スラグの上層部だけを水砕化し回収した。 結果を表−1に示す。
[Industrial Application Field] The present invention relates to a method for producing a raw material used in glass production from blast furnace slag. [Prior Art] Conventionally, it has been known to use blast furnace slag as a raw material for glass, and for example, there are the following methods. 1 A method in which the molten slag discharged from the furnace is poured into a pit, etc., where it is naturally cooled and solidified, and at this time, the impurities are allowed to settle, and only the upper slag with fewer impurities is taken out and crushed, and then passed through a magnetic separator to remove the iron content ( Special Publication No. 52-21003). 2 A method of injecting water into molten slag and using it as granulated slag, or removing iron by magnetic separation. 3 A method in which the molten slag discharged from the blast furnace is passed through a molten iron separation tank installed in the middle of the slag gutter, where the iron content is separated and the slag still in a molten state is pulverized (Japanese Patent Application Laid-Open No. 54-124013 issue). etc. [Problems to be Solved by the Invention] However, the conventional method as described above has the following drawbacks. For example, in method 1), since the blast furnace slag is naturally slowly cooled slag, sufficient crushing operations are required to obtain a constant particle size, which consumes excessive crushing energy and also When blast furnace slag is used as iron, the iron content, which is considered extremely harmful, is not sufficiently removed by sedimentation, and the solidified slag still contains Fe 2 O 3 on average.
It contains about 1.5% of iron, and even if iron is removed by magnetic separation, the content is only reduced to about 0.8%, so it cannot be said to be satisfactory as a raw material for glass. In addition, method 2) does not require pulverization, but as it is, it contains a large amount of molten iron, and iron removal by magnetic separation cannot sufficiently remove the iron. moreover,
Slag usually contains about 4 ppm of corundum (Al 2 O 3 ), a refractory used in blast furnaces, which cannot be removed by magnetic separation. Therefore, when used as a raw material for glass, corundum has a high melting point (melting point
(2015℃), it is not completely melted and exists in the form of small particles, causing defects in the glass. In addition, in method 3), even though the corundum of the refractory in the blast furnace settles and is separated with iron in the process of separating molten iron, the slag passes through the refractory troughs until the next process to form granulated slag. Because it is carried
Corundum, which is a refractory mixed here, remains in the granulated slag, and is not preferable as a raw material for glass as described above. The present invention solves these conventional problems and provides a method for obtaining an excellent glass raw material from blast furnace slag by reliably removing not only iron and other heavy metals but also corundum. [Means for Solving the Problems] That is, the present invention injects pressure water into molten blast furnace slag to form granulated slag, and then applies gravity beneficiation to eliminate iron and other harmful impurities as raw materials for glass. This is a method for producing glass raw material from blast furnace slag, which is characterized by removing high melting point compounds. In the present invention, the specific gravity beneficiation means include dry type,
Any type of wet type gravity beneficiation equipment can be applied. Furthermore, if necessary, a step of performing magnetic separation may be added before or after application of the specific gravity separation means, and in this case, iron content can be removed even more reliably. The present invention will be further clarified with reference to Examples below. Example 1 Pressure water was injected into the molten slag flow falling from the blast furnace slag to refine the particles and rapidly cool the resulting granulated slag, which was then classified by approximately 20 meters. Specific gravity separation was performed using a Sogyosha model MH-551). The beneficiation conditions are as follows. Wind speed: 0.7 to 1.3 m/sec Frequency: 600 rpm Amplitude: 5 mm Front-to-back angle: 4° Right-to-left angle: 1.5° The sample flows in the direction of the arrow as shown in Figure 1 and is collected at the bottom, containing substances harmful to glass raw materials such as iron minerals and corundum. is recovered as T, and that which can be used as glass raw material is recovered as C. The Fe 2 O 3 grade and amount of corundum of the recovered glass raw material C were as shown in Table 1. From this result, the effect of reducing Fe 2 O 3 and removing corundum was confirmed. In addition, since the amount of corundum has a specific gravity of 4.0 to 4.1 g/cm 3 , two types of heavy liquids (specific gravity 3.23 g/cm 3 and 4.5 g/cm 3 ) are used.
It was determined by separating. Example 2 The strength of the magnetic field was
After performing magnetic beneficiation at 5000 Gauss, gravity beneficiation was performed using a dry gravity separator under the same conditions as in Example 1. The results are shown in Table-1. Example 3 After classifying granulated slag with 20 meshes, Example 1
Gravity beneficiation is carried out using a dry type gravity separator under the same conditions as
The obtained material was further subjected to magnetic beneficiation with a magnetic field strength of 5000 Gauss. The results are shown in Table-1. Comparative Example 1 Approximately 20 tons of molten slag was poured into an approximately 7 m 3 pit with a depth of 1.2 m x 1.2 m x 1.4 m, and was naturally cooled and solidified for 8 days. After solidification, the upper layer up to about 1 m below the surface layer was excavated, crushed using a crusher, and iron content was removed using a magnetic separator with a magnetic field strength of 5000 Gauss. The results are shown in Table-1. Comparative Example 2 Water was injected into molten slag to obtain granulated slag, and then iron was removed using a magnetic separator with a magnetic field strength of 5000 Gauss. The results are shown in Table-1. Comparative Example 3 Molten slag was remelted at approximately 1500℃ in a 200ml crucible, then taken out of the furnace and tilted using the tilting method.
Only the upper layer of the molten slag was pulverized and recovered. The results are shown in Table-1.

【表】【table】

〔発明の効果〕〔Effect of the invention〕

以上のように本発明の方法によれば、簡単な操
作で高炉スラグからガラス原料として鉄分はもと
より有害な含有物特に従来除去し得なかつたコラ
ンダムを効率よく除去することができ、高炉スラ
グの利用上極めて有益である。
As described above, according to the method of the present invention, it is possible to efficiently remove iron as a glass raw material from blast furnace slag, as well as harmful contents, especially corundum, which could not be removed conventionally, from blast furnace slag. Above all, it is extremely beneficial.

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

図面は乾式比重選鉱の概要を示す説明図であ
る。
The drawing is an explanatory diagram showing an overview of dry specific gravity beneficiation.

Claims (1)

【特許請求の範囲】 1 溶融高炉スラグに圧力水を噴射して水砕スラ
グとなした後、比重選鉱手段を適用して、鉄分と
同時にその他のガラス原料として有害な不純物で
ある高融点化合物を除去することを特徴とする高
炉スラグからガラス原料を製造する方法。 2 比重選鉱処理の前又は後に磁力選別操作を施
す特許請求の範囲第1項に記載の方法。
[Claims] 1. After injecting pressurized water into molten blast furnace slag to form granulated slag, a specific gravity beneficiation method is applied to remove high melting point compounds, which are harmful impurities as other glass raw materials, along with iron. A method for producing glass raw material from blast furnace slag, which comprises removing blast furnace slag. 2. The method according to claim 1, wherein a magnetic separation operation is performed before or after the gravity beneficiation treatment.
JP62116953A 1987-05-15 1987-05-15 Production of glass raw material from blast furnace slag Granted JPS63285134A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62116953A JPS63285134A (en) 1987-05-15 1987-05-15 Production of glass raw material from blast furnace slag

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62116953A JPS63285134A (en) 1987-05-15 1987-05-15 Production of glass raw material from blast furnace slag

Publications (2)

Publication Number Publication Date
JPS63285134A JPS63285134A (en) 1988-11-22
JPH0460058B2 true JPH0460058B2 (en) 1992-09-25

Family

ID=14699823

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62116953A Granted JPS63285134A (en) 1987-05-15 1987-05-15 Production of glass raw material from blast furnace slag

Country Status (1)

Country Link
JP (1) JPS63285134A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113087546B (en) * 2021-04-02 2022-12-13 陕西科技大学 A kind of iron series art black glaze and preparation method thereof

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4179352A (en) * 1975-08-07 1979-12-18 Exxon Research & Engineering Co. Coal liquefaction process
JPS54124013A (en) * 1978-03-20 1979-09-26 Nippon Steel Corp Production of glass raw material from blast furnace slag

Also Published As

Publication number Publication date
JPS63285134A (en) 1988-11-22

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