JPS63285134A - Production of glass raw material from blast furnace slag - Google Patents
Production of glass raw material from blast furnace slagInfo
- Publication number
- JPS63285134A JPS63285134A JP62116953A JP11695387A JPS63285134A JP S63285134 A JPS63285134 A JP S63285134A JP 62116953 A JP62116953 A JP 62116953A JP 11695387 A JP11695387 A JP 11695387A JP S63285134 A JPS63285134 A JP S63285134A
- Authority
- JP
- Japan
- Prior art keywords
- blast furnace
- raw material
- slag
- furnace slag
- glass raw
- 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.)
- Granted
Links
- 239000002893 slag Substances 0.000 title claims abstract description 42
- 239000011521 glass Substances 0.000 title claims abstract description 19
- 239000002994 raw material Substances 0.000 title claims abstract description 17
- 238000004519 manufacturing process Methods 0.000 title claims description 5
- 230000005484 gravity Effects 0.000 claims abstract description 18
- 239000012535 impurity Substances 0.000 claims abstract description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 7
- 238000000034 method Methods 0.000 claims description 15
- 238000007885 magnetic separation Methods 0.000 claims description 6
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 abstract description 36
- 229910052742 iron Inorganic materials 0.000 abstract description 18
- 239000010431 corundum Substances 0.000 abstract description 11
- 229910052593 corundum Inorganic materials 0.000 abstract description 11
- 238000000926 separation method Methods 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 3
- 239000006148 magnetic separator Substances 0.000 description 3
- 230000008018 melting Effects 0.000 description 3
- 238000002844 melting Methods 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 229910001608 iron mineral Inorganic materials 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 239000010410 layer Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 239000004071 soot Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002344 surface layer Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B2400/00—Treatment of slags originating from iron or steel processes
- C21B2400/02—Physical or chemical treatment of slags
- C21B2400/022—Methods of cooling or quenching molten slag
- C21B2400/024—Methods of cooling or quenching molten slag with the direct use of steam or liquid coolants, e.g. water
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B2400/00—Treatment of slags originating from iron or steel processes
- C21B2400/05—Apparatus features
- C21B2400/062—Jet nozzles or pressurised fluids for cooling, fragmenting or atomising slag
Landscapes
- Glass Compositions (AREA)
- Manufacture Of Iron (AREA)
Abstract
Description
【発明の詳細な説明】
〔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。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a method for producing a raw material used in glass production from blast furnace slag.
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。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)炉から放出されり溶融スラグをピット等に流し込ん
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52−210
03号]。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. At this time, impurities are allowed to settle, and only the upper slag with fewer impurities is taken out and crushed, and the iron content is removed by applying it to a magnetic separator. (Tokuko Sho 52-210
No. 03].
2I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。A method of injecting water into 2I molten slag and using it as granulated slag, or removing the iron content by magnetic separation.
3)高炉から放出され+g融ススラグ、出滓樋の途中に
設はり溶鉄分離槽を通し、ここで鉄分を分離した後なお
溶融状態にあるスラグ全水砕化する方法(特開昭54−
124013号)。3) A method in which the +g molten soot 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 completely pulverized (Japanese Patent Application Laid-Open No. 1983-
No. 124013).
等がある。etc.
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ノ、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Fe2O
3が1.5%程度含有されており、磁選によって脱鉄し
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。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, a sufficient crushing operation is 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 extremely harmful, is not sufficiently removed by sedimentation, and the solidified slag still contains an average of Fe2O.
The content of 3 is about 1.5%, 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.
まり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(At203)等が通常数4 pp
m程度混入しており、これは磁選では除去できない。し
たがっ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℃)ため晦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。In the method of [Mari 2], it is not necessary to crush the iron, but as it is, it contains a large amount of molten iron, and the iron cannot be removed sufficiently by magnetic separation. In addition, corundum (At203), a refractory used in blast furnaces, is usually contained in the slag at a concentration of 4 ppp.
m, 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°C), so it does not burn out and exists in the form of small particles.
This causes defects in the glass.
なお3)、の方法は耐融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
樋を通って運ばれるので、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。In addition, in method 3), even though the corundum of the blast furnace refractory settles and is separated together with iron in the process of melting and separation, the slag passes through the refractory gutter before the process of making it into granulated slag. Since the refractory corundum mixed therein remains in the granulated slag, it is not preferable as a raw material for glass as described above.
本発明はこのよう力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。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.
すなわち本発明は容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ガラス原
料として有害な不純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。That is, the present invention involves injecting pressurized water into molten blast furnace slag to form granulated slag, and then applying a specific gravity beneficiation method to remove harmful impurities as a glass raw material. This is a method of manufacturing.
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。In the present invention, either a dry type or a wet type gravity concentrator can be applied as the gravity concentrator. 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.
以下実施例をあげて本発明を更に明らかにする。The present invention will be further clarified with reference to Examples below.
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i原島総業社
製MH−551型Jにかけて比重分離を行った。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 about 20 meters. Specific gravity separation was performed using MH-551 Model J manufactured by Sogyosha.
選鉱条件は下記のとおりである。The beneficiation conditions are as follows.
風速 0.7〜1.3 rn/ sec振動数
60 Q rpm
振幅 5m
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
T1ガラス原料に使用できるものがCで回収される。Wind speed 0.7-1.3 rn/sec Frequency
60 Q rpm Amplitude 5m Anteroposterior angle 4° Lateral angle 1.5° The sample flows in the direction of the arrow as shown in Figure 1 and is collected at the bottom, and substances harmful to glass raw materials such as iron minerals and corundum are collected in the T1 glass raw material. Usable materials are collected at C.
回収されたガラス原料Cの、Fe2O3品位、コランダ
ム量は表−1に示すとおりであった。この結果から、F
e2O3の低下及びコランダムの除去効果が確認された
。The Fe2O3 grade and amount of corundum of the recovered glass raw material C were as shown in Table-1. From this result, F
The effect of reducing e2O3 and removing corundum was confirmed.
なお、コランダム量は、比重4.0〜4,1り/−であ
るため2種の重液(比重3.23 f/m、 4.5
f/eta )で分離して求めた。In addition, since the amount of corundum has a specific gravity of 4.0 to 4.1/-, two types of heavy liquids (specific gravity 3.23 f/m, 4.5
f/eta).
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500
0ガウスで磁力選鉱を行なった後、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った。結果は表
−1に示すとおりである。Example 2 Granulated slag classified with 20 mesh was subjected to magnetic field strength of 500
After performing magnetic beneficiation at 0 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.
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。Example 3 After granulated slag was classified with 20 mesh, it was subjected to gravity beneficiation using a dry type gravity separator under the same conditions as in Example 1, and the resulting material was further beneficent by magnetic force at a magnetic field strength of 5000 Gauss. The results are shown in Table-1.
比較例1
溶融スラグ約20 ton f 1.2 m X 1.
2 mX1.4m深の約7?F/ビツトに流し込んで8
日間自然冷却して固化させた。Comparative Example 1 Molten slag approximately 20 tons f 1.2 m x 1.
2 m x 1.4 m deep, about 7? Pour into F/bit 8
It was naturally cooled and solidified for several days.
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。After solidification, the upper layer up to about 1 m from the surface layer was excavated, crushed with a crusher, and iron content was removed with a magnetic separator with a magnetic field strength of 5000 Gauss.
結果を表−1に示す。The results are shown in Table-1.
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。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.
結果を表−1に示す。The results are shown in Table-1.
比較例3
溶融スラグを200−のルッゼにて約1500℃で再溶
融し、その後、炉外へ取シ出し、傾斜法にて、溶融スラ
ブの上#蔀だけを水砕化し回収した。Comparative Example 3 The molten slag was remelted at about 1500° C. in a 200° Rusze, and then taken out of the furnace, and only the upper hem of the molten slab was pulverized and recovered using a tilting method.
結果を表−1に示す。The results are shown in Table-1.
表−1
〔発明の効果〕
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っ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
。Table 1 [Effects of the Invention] As described above, according to the method of the present invention, not only iron but also harmful contents, especially corundum, which could not be removed conventionally, can be efficiently removed from blast furnace slag as a raw material for glass with a simple operation. This is extremely beneficial for the use of blast furnace slag.
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)
した後、比重選鉱手段を適用して、ガラス原料として有
害な不純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. Blast furnace slag characterized in that after injecting pressurized water into molten blast furnace slag to form granulated slag, a specific gravity beneficiation method is applied to remove impurities harmful to glass raw materials. A method for producing raw glass from. 2. The method according to claim 1, wherein a magnetic separation operation is performed before or after the gravity beneficiation treatment.
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 true JPS63285134A (en) | 1988-11-22 |
JPH0460058B2 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) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113087546A (en) * | 2021-04-02 | 2021-07-09 | 陕西科技大学 | Iron-based artistic black glaze and preparation method thereof |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5221003A (en) * | 1975-08-07 | 1977-02-17 | Exxon Research Engineering Co | Method of liquefying coal |
JPS54124013A (en) * | 1978-03-20 | 1979-09-26 | Nippon Steel Corp | Production of glass raw material from blast furnace slag |
-
1987
- 1987-05-15 JP JP62116953A patent/JPS63285134A/en active Granted
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5221003A (en) * | 1975-08-07 | 1977-02-17 | Exxon Research Engineering Co | Method of liquefying coal |
JPS54124013A (en) * | 1978-03-20 | 1979-09-26 | Nippon Steel Corp | Production of glass raw material from blast furnace slag |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113087546A (en) * | 2021-04-02 | 2021-07-09 | 陕西科技大学 | Iron-based artistic black glaze and preparation method thereof |
Also Published As
Publication number | Publication date |
---|---|
JPH0460058B2 (en) | 1992-09-25 |
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