JPH0778259B2 - Recovery method of metal from dephosphorization slag - Google Patents
Recovery method of metal from dephosphorization slagInfo
- Publication number
- JPH0778259B2 JPH0778259B2 JP15838985A JP15838985A JPH0778259B2 JP H0778259 B2 JPH0778259 B2 JP H0778259B2 JP 15838985 A JP15838985 A JP 15838985A JP 15838985 A JP15838985 A JP 15838985A JP H0778259 B2 JPH0778259 B2 JP H0778259B2
- Authority
- JP
- Japan
- Prior art keywords
- slag
- metal
- hot metal
- crushed
- lime
- 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
Links
- 239000002893 slag Substances 0.000 title claims description 52
- 239000002184 metal Substances 0.000 title claims description 34
- 229910052751 metal Inorganic materials 0.000 title claims description 34
- 238000011084 recovery Methods 0.000 title claims description 6
- 238000000034 method Methods 0.000 title description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 10
- 235000008733 Citrus aurantifolia Nutrition 0.000 claims description 9
- 235000011941 Tilia x europaea Nutrition 0.000 claims description 9
- 239000004571 lime Substances 0.000 claims description 9
- 230000004907 flux Effects 0.000 claims description 7
- 238000010298 pulverizing process Methods 0.000 claims 1
- 238000000926 separation method Methods 0.000 claims 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 7
- 239000011574 phosphorus Substances 0.000 description 7
- 229910052698 phosphorus Inorganic materials 0.000 description 7
- 239000002245 particle Substances 0.000 description 4
- 230000002093 peripheral effect Effects 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 238000007664 blowing Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 229910004298 SiO 2 Inorganic materials 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000010494 dissociation reaction Methods 0.000 description 1
- 230000005593 dissociations Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000006703 hydration reaction Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000007885 magnetic separation Methods 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 238000010079 rubber tapping Methods 0.000 description 1
- 238000007873 sieving Methods 0.000 description 1
- 238000002791 soaking Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 1
- 229920002554 vinyl polymer Polymers 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Landscapes
- Manufacture And Refinement Of Metals (AREA)
Description
【発明の詳細な説明】 〔発明の技術分野〕 この発明は、高炉から流出する溶銑を溶銑鍋(トーピー
ドその他の容器を含む。以下同じ。) に導くための出銑樋の途中または溶銑鍋中において、溶
銑中に含有されている燐を、石灰系のフラツクスを使用
して除去する際に発生したスラグから、前記スラグ中に
含有されている地金を回収するための、脱燐スラグ中か
らの地金の回収方法に関するものである。Description: TECHNICAL FIELD OF THE INVENTION The present invention relates to hot metal flowing out of a blast furnace to a hot metal ladle (including torpedo and other containers; the same applies hereinafter) or during tapping gutter or in a hot metal ladle. In, the phosphorus contained in the hot metal, from the slag generated when removing using a lime-based flux, from the dephosphorization slag for recovering the metal contained in the slag It relates to the method of collecting bullion.
近時、高炉から流出する溶銑を溶銑鍋に導くための出銑
樋の途中または溶銑鍋中において、前記出銑樋または溶
銑鍋中の溶銑に石灰系のフラツクスを供給し、前記フラ
ツクスによつて溶銑中の燐を除去することが行なわれて
いる。Recently, in the middle of or in the hot metal ladle for guiding the hot metal flowing out of the blast furnace to the hot metal ladle, in the hot metal ladle, a lime-based flux is supplied to the hot metal in the hot metal ladle or the hot metal ladle, and by the said flux. Phosphorus in hot metal is removed.
このような溶銑中に含有されている燐の除去の際に生成
した溶融スラグ中には、地金が含有されている。この溶
融スラグ中に含有されている地金は、従来、前記溶融ス
ラグを冷却して塊状にした塊状スラグを粉砕し、粉砕し
たスラグ中の地金を、磁石により吸着することによつて
行なつていた。Metal is contained in the molten slag generated during the removal of phosphorus contained in such hot metal. The ingot contained in this molten slag is conventionally crushed by cooling the molten slag into lumps, and the ingot in the crushed slag is adsorbed by a magnet. Was there.
しかしながら、上述のような方法では、スラグと地金と
の分離が不十分であり、回収した地金の品位が悪い問題
があつた。However, the above-mentioned method has a problem that the slag and the ingot are not sufficiently separated and the quality of the recovered ingot is poor.
また、特開昭59−123706号公報には、溶滓鍋に収容され
た溶滓中に注水して冷却し、この冷却された溶滓を屋外
に払い出して乾燥させた後、この乾燥滓をふるい分け
し、磁選および破砕処理することによつて地金を回収す
る方法が開示されている。しかしながらこの方法は、溶
滓鍋中に注水するものであるから危険を伴い、工程が複
雑である等の問題を有している。Further, in JP-A-59-123706, water is poured into a slag contained in a slag pan to cool it, and the cooled slag is discharged to the outside to be dried, and then the dried slag is dried. A method of recovering the metal by sieving, magnetic separation and crushing treatment is disclosed. However, this method is problematic in that it involves pouring water into the slag ladle and that the process is complicated.
従つて、この発明の目的は、石灰系のフラツクスを使用
して、溶銑中の燐を除去する際に生成したスラグ中か
ら、地金を簡単に且つ効率よく分離回収するための脱燐
スラグ中からの地金の回収方法を提供することにある。Therefore, an object of the present invention is to use a lime-based flux to remove the phosphorus in the hot metal from the slag produced when the phosphorus is removed from the slag to easily and efficiently separate and recover the metal. The purpose is to provide a method of collecting bullion from.
この発明は、石灰系のフラツクスを使用して溶銑の脱燐
を行なう際に生成したスラグを粗砕し、次いで、粗砕さ
れたスラグ中に散水または水蒸気を吹き込んで、スラグ
中のCaOを予備消和し、次いで、予備消和されたスラグ
をクラツシヤーにより微粉砕し、このように微粉砕され
たスラグ中の地金を磁石に吸着させて分離回収すること
に特徴を有するものである。This invention coarsely crushes the slag produced when performing dephosphorization of hot metal using a lime-based flux, and then sprays water or steam into the crushed slag to reserve CaO in the slag. It is characterized in that the slag that has been soaked and then preliminarily soaked is finely pulverized by a crusher, and the metal in the slag thus finely pulverized is adsorbed by a magnet to be separated and recovered.
第1表は石灰系のフラツクスを使用して溶銑中の燐を除
去する際に生成したスラグの成分組成の一例である。第
1表からわかるように、スラグは遊離石灰を主成分とし
ているため、大気中に放置しても膨張崩壊するほど活性
(不安定)である。Table 1 is an example of the component composition of the slag produced when phosphorus in the hot metal is removed using a lime-based flux. As can be seen from Table 1, since slag contains free lime as a main component, it is so active (unstable) that it expands and collapses even if left in the atmosphere.
上記スラグは、顕微鏡観察の結果、遊離石灰のマトリツ
クス中に構成鉱物であるβ−2CaO.SiO2,Ca5F(PO4)3,C
aF2が分散された構造であり、鉄分は約20μmの大きさ
の微粒錠から数cmの大きさの扁平状のものまで、上記ス
ラグ中に取りこまれた状態で含有されている。 As a result of microscopic observation, the above-mentioned slag is a constituent mineral β-2CaO.SiO 2 , Ca 5 F (PO 4 ) 3 , C in the matrix of free lime.
It has a structure in which aF 2 is dispersed, and the iron content is contained in the above slag in a state of being incorporated, from a fine tablet having a size of about 20 μm to a flat tablet having a size of several cm.
上述した成分組成のスラグを、例えばジヨークラツシヤ
ーを使用してその粒径が約50mm以下(好ましくは15mm以
下)になるように粗砕する。次いで、このように粗砕さ
れたスラグに十分に水がゆきわたるように散水し、更に
スラグ中の遊離石灰の水和反応を促進するために、必要
により水蒸気を吹き込む。この結果、スラグ中のCaOは
予備消和されてCa(OH)2となり、膨張し破砕されやすく
なる。なお、上記予備消和は、散水することなく、水蒸
気の吹込みのみにより行なつてもよい。The slag having the above-mentioned component composition is roughly crushed by using, for example, a Diyoke crusher so that the particle size thereof becomes about 50 mm or less (preferably 15 mm or less). Then, water is sprayed so that water is sufficiently spread over the slag thus roughly crushed, and steam is blown in if necessary in order to accelerate the hydration reaction of free lime in the slag. As a result, CaO in the slag is pre-sorted to Ca (OH) 2 and expands and is easily broken. The preliminary slaking may be performed only by blowing steam without sprinkling water.
次いで、この予備消和されたスラグを、例えば高速で回
転するインパクトクラツシヤーによつて破砕することに
より、スラグは微粉砕される。従つて、この微粉砕され
たスラグ中の地金を、磁石により吸着することによつ
て、地金を効率的に回収することができる。The slag is then finely crushed by crushing the pre-swaged slag with, for example, an impact crusher rotating at a high speed. Therefore, the metal in the finely pulverized slag is adsorbed by the magnet, so that the metal can be efficiently recovered.
下記は、スラグの予備消和を効率的に行なうための条件
の一例である。The following is an example of conditions for efficiently performing pre-swapping of slag.
スラグの含水率:5〜15% 散水量または水蒸気の吹込み量:85〜170kg/t・スラグ 温度:20℃以上好ましくは60℃以上 時間:数時間〜1週間 〔発明の実施例〕 実施例1 粒径50mm以下に粗砕した脱燐スラグ200kgを図面に示す
ような容器1に入れ、導管2を通して100℃の水蒸気
を、20kg/Hrの流量で約1時間吹き込んだ。図面におい
て、3は圧力計、4は流量計、5は網である。このよう
な水蒸気の吹き込みにより予備消和されたスラグを、供
給量10T/Hr、ローター周速20m/secの条件でインパクト
クラツシヤに装入し微粉砕した。次いで、この微粉砕さ
れたスラグ中の地金を磁石により吸着することによつ
て、地金を回収した。第2表は上記により回収された地
金の回収率と品位である。Moisture content of slag: 5 to 15% Amount of sprinkling water or injection of steam: 85 to 170 kg / t-Slag temperature: 20 ° C or higher, preferably 60 ° C or higher Time: several hours to one week [Examples of the invention] Examples 1. 200 kg of dephosphorized slag roughly crushed to a particle size of 50 mm or less was placed in a container 1 as shown in the drawing, and steam at 100 ° C. was blown into the container 1 through a conduit 2 at a flow rate of 20 kg / Hr for about 1 hour. In the drawing, 3 is a pressure gauge, 4 is a flow meter, and 5 is a mesh. The slag preliminarily neutralized by the blowing of water vapor was charged into an impact crusher under the conditions of a supply rate of 10 T / Hr and a rotor peripheral speed of 20 m / sec, and pulverized. Then, the metal in the finely pulverized slag was adsorbed by a magnet to recover the metal. Table 2 shows the recovery rate and quality of the bullion collected above.
比較例1 粒径50mm以下に粗砕した脱燐スラグ200kgを、予備消和
することなく、供給量10T/Hr、ローター周速40m/secの
条件でインパクトクラツシヤに装入し微粉砕した。次い
で、この微粉砕されたスラグ中の地金を磁石により吸着
することによつて、地金を回収した。第3表は、上記に
より回収された地金の回収率と品位である。 Comparative Example 1 200 kg of dephosphorized slag coarsely crushed to a particle size of 50 mm or less was charged into an impact crusher under the conditions of a supply amount of 10 T / Hr and a rotor peripheral speed of 40 m / sec without crushing, and pulverized. . Then, the metal in the finely pulverized slag was adsorbed by a magnet to recover the metal. Table 3 shows the recovery rate and quality of the bullion collected above.
上記第2表と第3表とを比較すれば明らかなように、本
発明方法によつて予備消和した場合の地金回収率は極め
て高い。As is clear from the comparison between Tables 2 and 3, the bullion recovery rate is extremely high in the case of preliminary slaking by the method of the present invention.
実施例2 粒径25mm以下に粗砕した脱燐スラグ800kgを、幅1m、長
さ2m、高さ20cmに均し、このように均された脱燐スラグ
上に約140kgの水を均等に散水した後、ビニールシート
で覆つて1週間放置し予備消和した。次いで、このよう
にして予備消和されたスラグを、供給量10T/Hr、ロータ
ー周速20m/secの条件でインパクトクラツシヤに装入し
微粉砕した。次いで、この微粉砕されたスラグ中の地金
を磁石により吸着することによつて、地金を回収した。
第4表は上記により回収された地金の回収率と品位であ
る。 Example 2 800 kg of dephosphorized slag roughly crushed to a particle size of 25 mm or less is leveled to a width of 1 m, a length of 2 m and a height of 20 cm, and about 140 kg of water is evenly sprayed on the dephosphorized slag thus leveled. After that, it was covered with a vinyl sheet and left for 1 week for preliminary sterilization. Then, the slag thus preliminarily soaked was charged into an impact crusher under the conditions of a supply amount of 10 T / Hr and a rotor peripheral speed of 20 m / sec, and pulverized. Then, the metal in the finely pulverized slag was adsorbed by a magnet to recover the metal.
Table 4 shows the recovery rate and quality of the bullion collected above.
〔発明の効果〕 以上述べたように、この発明によれば、CaOの予備消和
によつて、スラグを容易に微粉砕することができるか
ら、スラグ中の地金を磁力によつて効率的に分離回収す
ることができ、回収された地金への燐の付着量は微量で
その品質は優れている等、工業上優れた効果がもたらさ
れる。 [Effects of the Invention] As described above, according to the present invention, the slag can be easily finely pulverized by the preliminary soaking of CaO, so that the metal in the slag can be efficiently magnetized. It can be separated and recovered, and the amount of phosphorus adhering to the recovered metal is very small and its quality is excellent.
図面は予備消和のための装置の一例を示す概略縦断面図
である。図面において、 1……容器、2……導管 3……圧力計、4……流量計 5……網The drawing is a schematic vertical cross-sectional view showing an example of an apparatus for preliminary dissociation. In the drawing, 1 ... container, 2 ... conduit, 3 ... pressure gauge, 4 ... flow meter, 5 ... mesh
Claims (1)
を行なう際に生成したスラグを粗砕し、次いで、粗砕さ
れたスラグ中に散水または水蒸気を吹き込んで、スラグ
中のCaOを予備消和し、次いで、予備消和されたスラグ
をクラツシヤーにより微粉砕し、このように微粉砕され
たスラグ中の地金を磁石に吸着させて分離回収すること
を特徴とする脱燐スラグ中からの地金の回収方法。1. A slag produced during dephosphorization of hot metal using a lime-based flux is crushed, and then water or steam is blown into the crushed slag to remove CaO in the slag. In the dephosphorization slag, which is characterized by preliminarily slagging and then pulverizing the slag preliminarily slagging with a crusher and adsorbing the metal contained in the slag thus pulverized to a magnet for separation and recovery. How to collect the bullion from.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15838985A JPH0778259B2 (en) | 1985-07-19 | 1985-07-19 | Recovery method of metal from dephosphorization slag |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15838985A JPH0778259B2 (en) | 1985-07-19 | 1985-07-19 | Recovery method of metal from dephosphorization slag |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6220839A JPS6220839A (en) | 1987-01-29 |
| JPH0778259B2 true JPH0778259B2 (en) | 1995-08-23 |
Family
ID=15670656
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15838985A Expired - Lifetime JPH0778259B2 (en) | 1985-07-19 | 1985-07-19 | Recovery method of metal from dephosphorization slag |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0778259B2 (en) |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS53721B2 (en) * | 1973-03-20 | 1978-01-11 |
-
1985
- 1985-07-19 JP JP15838985A patent/JPH0778259B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6220839A (en) | 1987-01-29 |
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