JP3711045B2 - Briquette for steelmaking raw materials - Google Patents
Briquette for steelmaking raw materials Download PDFInfo
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- JP3711045B2 JP3711045B2 JP2001241024A JP2001241024A JP3711045B2 JP 3711045 B2 JP3711045 B2 JP 3711045B2 JP 2001241024 A JP2001241024 A JP 2001241024A JP 2001241024 A JP2001241024 A JP 2001241024A JP 3711045 B2 JP3711045 B2 JP 3711045B2
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- briquette
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- steelmaking
- raw material
- pure iron
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- 239000004484 Briquette Substances 0.000 title claims description 42
- 238000009628 steelmaking Methods 0.000 title claims description 22
- 239000002994 raw material Substances 0.000 title claims description 19
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 37
- 238000000227 grinding Methods 0.000 claims description 27
- 238000007711 solidification Methods 0.000 claims description 20
- 230000008023 solidification Effects 0.000 claims description 20
- 229910052742 iron Inorganic materials 0.000 claims description 17
- 229910052751 metal Inorganic materials 0.000 claims description 7
- 239000002184 metal Substances 0.000 claims description 7
- 229910000831 Steel Inorganic materials 0.000 claims description 6
- 239000012530 fluid Substances 0.000 claims description 6
- 239000010959 steel Substances 0.000 claims description 6
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 5
- 239000004115 Sodium Silicate Substances 0.000 claims description 5
- ILRRQNADMUWWFW-UHFFFAOYSA-K aluminium phosphate Chemical compound O1[Al]2OP1(=O)O2 ILRRQNADMUWWFW-UHFFFAOYSA-K 0.000 claims description 5
- 239000008119 colloidal silica Substances 0.000 claims description 5
- 238000000748 compression moulding Methods 0.000 claims description 5
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 claims description 5
- 229910052911 sodium silicate Inorganic materials 0.000 claims description 5
- 239000000463 material Substances 0.000 claims description 3
- 239000012752 auxiliary agent Substances 0.000 claims description 2
- 230000003647 oxidation Effects 0.000 claims description 2
- 238000007254 oxidation reaction Methods 0.000 claims description 2
- 239000003921 oil Substances 0.000 description 20
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 17
- 238000004519 manufacturing process Methods 0.000 description 14
- 239000000843 powder Substances 0.000 description 11
- 238000000034 method Methods 0.000 description 10
- 238000003860 storage Methods 0.000 description 6
- 239000010426 asphalt Substances 0.000 description 5
- 241000209094 Oryza Species 0.000 description 4
- 235000007164 Oryza sativa Nutrition 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 235000009566 rice Nutrition 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- 239000000839 emulsion Substances 0.000 description 3
- 235000013379 molasses Nutrition 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 2
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 2
- 229920002472 Starch Polymers 0.000 description 2
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
- 238000005520 cutting process Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 238000005498 polishing Methods 0.000 description 2
- 238000010298 pulverizing process Methods 0.000 description 2
- 239000010802 sludge Substances 0.000 description 2
- 235000019698 starch Nutrition 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 244000144725 Amygdalus communis Species 0.000 description 1
- 235000011437 Amygdalus communis Nutrition 0.000 description 1
- 229920002261 Corn starch Polymers 0.000 description 1
- 229920000742 Cotton Polymers 0.000 description 1
- 240000000111 Saccharum officinarum Species 0.000 description 1
- 235000007201 Saccharum officinarum Nutrition 0.000 description 1
- 239000003082 abrasive agent Substances 0.000 description 1
- 235000020224 almond Nutrition 0.000 description 1
- 125000000129 anionic group Chemical group 0.000 description 1
- 239000000440 bentonite Substances 0.000 description 1
- 229910000278 bentonite Inorganic materials 0.000 description 1
- SVPXDRXYRYOSEX-UHFFFAOYSA-N bentoquatam Chemical compound O.O=[Si]=O.O=[Al]O[Al]=O SVPXDRXYRYOSEX-UHFFFAOYSA-N 0.000 description 1
- 239000000292 calcium oxide Substances 0.000 description 1
- 235000012255 calcium oxide Nutrition 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 239000008120 corn starch Substances 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- -1 ferrous metals Chemical class 0.000 description 1
- 238000005470 impregnation Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 235000014593 oils and fats Nutrition 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 238000010008 shearing Methods 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 239000010902 straw Substances 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B30—PRESSES
- B30B—PRESSES IN GENERAL
- B30B9/00—Presses specially adapted for particular purposes
- B30B9/32—Presses specially adapted for particular purposes for consolidating scrap metal or for compacting used cars
- B30B9/327—Presses specially adapted for particular purposes for consolidating scrap metal or for compacting used cars for briquetting scrap metal
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Manufacture And Refinement Of Metals (AREA)
- Treatment Of Steel In Its Molten State (AREA)
- Carbon Steel Or Casting Steel Manufacturing (AREA)
Description
【0001】
【発明の属する技術分野】
この発明は、製鋼原料用のブリケットに関し、特に、鉄系金属の研削切粉を有効利用する技術に関する。
【0002】
【従来の技術】
軸受鋼や浸炭鋼等の鉄系金属を研削(以下、研磨、超仕上げ研磨及びラッピング等も含む概念として使用する)した際に生じる切粉は、水分及び油分を含有する研削液や砥粒等を含む綿状(繊維状)凝集体として回収されている。この綿状凝集体は、多量の純鉄を含むことからこれを製鋼原料として再利用することが試みられている。しかし、この綿状凝集体は多量の水分を含有していることから、これを溶鉱炉にそのまま投入すると、当該水分によって突沸(水蒸気爆発)が生じるという問題を引き起こす。そこで、綿状凝集体中の水分を遠心分離等によって除去することが考えられるが、この場合には、綿状凝集体に含まれる油分も水分とともに除去されて、綿状凝集体の自然発熱により研削切粉の成分である純鉄が酸化鉄に変質する。このため、これを製鋼原料として再利用するには還元する必要があり、還元剤の使用等によりコスト高になる。
【0003】
また、前記油分の付着した研削切粉は相互に密着し難いことから、綿状凝集体を圧縮成形しても所望の強度に固形化するのが困難である。さらに、炭素の含有量が0.2重量%以上の鉄系金属の研削切粉を多量に含む綿状凝集体については、圧縮時のスプリングバックが大きいので、これを圧縮成形しても所望の強度に固形化するのが困難である。したがって、圧縮成形した綿状凝集体を溶鉱炉に投入しても、飛散しながら舞い上がって、集塵機によって大半が回収されてしまうという問題を生じる。
さらに、前記綿状凝集体に含まれる繊維状の研削切粉は、ハンマーミル等で粉砕することが困難であるので、綿状凝集体を細かくせん断することができない。このため、綿状凝集体をブリケット等に加工することも困難である。
したがって、前記綿状凝集体は再利用することなく廃棄物処理業者に委託して埋め立て処分されているのが実状である。
【0004】
【発明が解決しようとする課題】
しかし、このような綿状凝集体の埋め立て処分は、資源の有効利用という観点から好ましくない。また、環境悪化を引き起こすとともに、廃棄コストが高くつくという問題もある。
この発明は、前記問題点に鑑みてなされたものであり、研削切粉を有効に再利用することができる製鋼原料用のブリケットを提供することを目的とする。
【0005】
【課題を解決するための手段】
前記目的を達成するためのこの発明のブリケットは、粉状の純鉄と油分とを含む乾燥したブリケットであって、鉄系金属の研削切粉と油分及び水分を含有する研削液とを含む綿状凝集体を圧縮成形して得られる余剰の水分及び油分を除去し純鉄の酸化防止用の油分を1〜5重量%保持した脆性成形体を、無機質の固形化補助剤を含浸させて固形化してなることを特徴としている(請求項1)。
このように構成された製鋼原料用のブリケットは、乾燥した固形物であるので、そのまま溶鉱炉に投入しても、突沸を生じたり舞い上がったりするおそれがないとともに、運搬、貯蔵等の取り扱いが容易なものになる。また、油分を含有するので、粉状の純鉄が酸化するのが防止される。
【0008】
前記製鋼原料用のブリケットにおいて(請求項1)、無機質の固形化補助剤はコロイダルシリカ、珪酸ソーダ、燐酸アルミニウムから選択される少なくとも1種であるのが好ましく(請求項2)、これにより、油分を含有しているにもかかわらず強固に固形化されたものになる。
【0009】
前記した製鋼原料用のブリケットは、固形化補助剤を2〜30重量%含むのが好ましく(請求項3)、これにより、より一層強固に固形化されたものになる。
前記したブリケットは、ほぼピロー形状のものであるのが好ましく(請求項4)、これにより、圧縮強度を高めることができるとともに、部分的な破損が生じ難いものになる。
【0010】
【発明の実施の形態】
以下、この発明の実施の形態について添付図面を参照しながら詳述する。
図1はこの発明の一実施形態に係る製鋼原料用のブリケットを示す一部欠截斜視図である。このブリケットAは、粉状の純鉄と油分とを含むものであり、鉄系金属の研削切粉と油分及び水分を含有する研削液とを含む綿状凝集体を微細にせん断して得られる粉体を、固形化補助剤を用いて固形化し、これを乾燥させて前記水分を除去したものである。このブリケットAの形状はほぼピロー形状に形成されている。
【0011】
図2は前記ブリケットAの製造方法を示す工程図である。このブリケットAの製造においては、まず鉄系金属を研削加工する際に発生する研削切粉の綿状凝集体B(図2(a)参照)を加圧圧縮して、当該綿状凝集体Bに含まれる研削液の成分である水分及び油分の含有量を予備的に調整する。この綿状凝集体Bの加圧圧縮は、例えばベルトコンベア1にて搬送しながら一対のロール2間に挟み込むことにより行う(図2(b)参照)。この際、綿状凝集体Bは、含水率が50重量%を超えない範囲に、含油率が10重量%を超えない範囲にそれぞれ調整するのが好ましく、これにより、綿状凝集体Bの搬送、貯蔵等の取り扱いが容易となる。
【0012】
次に、水分及び油分の含有量が調整された前記綿状凝集体Bを、成形型3を用いてプレスにより圧縮成形して脆性成形体Cを得る(図2(c)参照)。この圧縮成形によって、綿状凝集体Bに含まれるスパイラル繊維状の研削切粉が粗せん断される。また、余剰の水分及び油分が除去されて、前記脆性成形体Cの含水率が2〜12重量%に、含油率が1〜5重量%に調整される。これにより、最小限の残留油分によって研削切粉が酸化するのを効果的に防止することができる。また、前工程において綿状凝集体Bの含水率が50重量%、含油率が10重量%をそれぞれ超えない範囲に予め調整されているので、前記脆性成形体Cの水分及び油分の含有割合を圧縮成形のみによって容易かつ適正に調整することができる。
前記脆性成形体Cは、円柱形、球形、角柱形等の取り扱いの容易な形状に形成されているとともに、次工程への搬送時等に崩壊しない程度の強度に固められている。
【0013】
次いで、前記脆性成形体Cを固形化補助剤Dとともに回転刃4を備えるチョッパーミル付きミキサー(又はヘンシェル型ミキサー)5に投入して粉砕する(図2(d)参照)。これにより脆性成形体Cの研削切粉をさらに細かくせん断(仕上げせん断)して、純鉄の粉と固形化補助剤Dとを含む粉体Eを得ることができる(図2(e)参照)。前記純鉄の粉の長径は3〜1000μm程度のものである。この脆性成形体Cの粉砕に際しては、当該脆性成形体C中の繊維状の研削切粉が予め粗せん断されているので、これを支障なく仕上げせん断することができる。この脆性成形体C中の繊維状の研削切粉が粗せん断がされていない場合には、これを前記ミキサー5によって粉砕することが非常に困難であり、微細な粉体Eを得ることは不可能である。
【0014】
前記固形化補助剤Dとしては、米糠(米糠の精)、サトウキビ等の廃糖蜜、芋澱粉やコーンスターチ等の澱粉類、生石灰、コロイダルシリカ、珪酸ソーダ、燐酸アルミニウム、酢酸ビニル汚泥、アスファルト乳剤、ベントナイトのうちから選択される1種又は2種以上が好適に使用される。このような固形化補助剤Dは2〜30重量%含有するのが好ましい。特に、前記米糠及び廃糖蜜については、粉体E中に多量に含まれる純鉄の粉が変質するのを効果的に防止できるとともに、その価格も安いことから固形化補助剤Dとしてきわめて好適である。また、アスファルト乳剤は混練後、アスファルトと水に分離すると粘結性が生じ、強度が発現する。このアスファルト乳剤としては、アニオン系アスファルトが好適に使用される。
【0015】
次に、所定量の前記粉体Eを、成形型6を用いてプレスにより圧縮成形して(図2(f)参照)、多量の純鉄を含有するほぼピロー形状の含水ブリケットFを得る。この粉体Eの圧縮成形に際しては、前記固形化補助剤Dと粉体E中の水分とによって、油脂が付着した純鉄の粉どうしを強固に結合して固形化することができる。特に、粉体Eとして水分5〜6重量%、米糠4重量%及び廃糖蜜2重量%含むもの、並びに水分7〜15重量%、酢酸ビニル汚泥2〜10重量%含むものを用いる場合には、より強固に固形化された含水ブリケットFを得ることができる。
なお、前記「ほぼピロー形状」とは、周縁部に丸みを有し、周縁部から中央部に向かって肉厚が漸次厚くなる形状であって、卵形、アーモンド形、ラグビーボール形等を含む形状であり、このような形状に成形することにより、圧縮荷重に強く崩壊し難いとともに、角部等における部分的な破損が生じ難いブリケットAを得ることができる。
【0016】
そして、圧縮成形直後の含水ブリケットFに常温又は冷却されたエアーを吹き付けてこれを急速冷却する(図2(g)参照)。これにより、当該含水ブリケットFを容易且つ安定的に固形化することができる。その後、含水ブリケットFを養生(乾燥)してその含有水分を除去することにより(図2(h)参照)、製鋼原料用のブリケットAを得ることができる(図2(i)参照)。この養生は2日間程度行うのが含有水分を確実に除去することができるので好ましい。
【0017】
以上により得られたブリケットAは、粉体Eを固形化した多孔質のものであるので、養生によって含有水分を容易且つ確実に除去することができる。このため、そのまま溶鉱炉に投入しても突沸が生じたり舞い上がって排出されたりするおそれがない。また、研削液の油分の一部を常に保持した状態で加工しているので、純鉄の酸化が効果的に防止されている。例えば軸受鋼(SUJ−2)の研削切粉を含む綿状凝集体Bを用いて製造されたブリケットAについては、84〜95重量%の純鉄を含むことが確認されている。したがって、溶解歩留まりが90%以上と非常に高く、高品質の製鋼原料として製鋼メーカに有償で提供することができる。しかも、固形にて運搬その他の取り扱いが容易である。
【0018】
図3はこの発明のブリケットAの他の製造方法を示す工程図である。この製造方法が図1に示す製造方法と主に異なる点は、脆性成形体Cの粉砕工程を省略した点である。すなわち、この製造方法においては、図1に示す製造方法と全く同様にして、綿状凝集体Bから脆性成形体Cを得ている(図3(a)〜(c)参照)。
【0019】
そして、これらの工程を経て得られた脆性成形体Cに、液状の固形化補助剤Dを含浸させる。この固形化補助剤Dの含浸は、例えば脆性成形体Cをベルトコンベア7にて搬送しながら、タンク8に注入した前記固形化補助剤Dに浸漬させることにより行う(図3(d)参照)。この製造方法に用いる固形化補助剤Dとしては、コロイダルシリカ、珪酸ソーダ、燐酸アルミニウムから選択される少なくとも1種を用いるのが好ましく、これにより、脆性成形体Cを容易且つ強固に固形化することができる。
【0020】
次に、前記固形化補助剤Dを含浸させた脆性成形体Cを(図3(e)参照)養生(乾燥)して(図3(f)参照)、製鋼原料用のブリケットAを得る(図3(g)参照)。
以上により得られたブリケットAは、図1に示す製造方法により得られるブリケットAと同じ作用を奏することができる。また、図3に示す製造方法は、脆性成形体Cを粉砕する工程を省略しているので、ブリケットAをより能率よく製造することができる。
【0021】
前記した各ブリケットの製造方法は、炭素を0.2重量%以上含む研削切粉を再利用するのに特に好適に適用される。このような研削切粉は、スプリングバックが大きく、固形化が困難であるが、この発明の製造方法を適用することにより、当該スプリングバックの影響を排除して強固に固形化されたブリケットAを容易に得ることができる。なお、炭素を0.2重量%以上含む研削切粉の代表例としては、軸受鋼の研削切粉を挙げることができる。
【0022】
【発明の効果】
以上のように、請求項1記載の製鋼原料用のブリケットは、水分が除去された固形のものであるので、そのまま溶鉱炉に投入しても、突沸を生じたり舞い上がったりするおそれがないとともに、運搬、貯蔵等の取り扱いが容易なものになる。また、油分を含有するので、粉状の純鉄が酸化するのが防止される。したがって、高品質の製鋼原料として再利用が可能であり、環境保全に役立つとともに、切削切粉の廃棄コストを削減することができる。
【0025】
請求項2記載の製鋼原料用のブリケットによれば、前記無機質の固形化補助剤がコロイダルシリカ、珪酸ソーダ、燐酸アルミニウムから選択される少なくとも1種であるので、油分を含むにもかかわらず強固に固形化されたものになる。このため、運搬、貯蔵等の取り扱いがさらに容易になる。
請求項3記載の製鋼原料用のブリケットによれば、固形化補助剤を2〜30重量%混合するので、粉体をさらに強固に固形化することができる。このため、運搬、貯蔵等の取り扱いがさらに容易になる。
請求項4記載の製鋼原料用のブリケットによれば、ほぼピロー形状のものであるので、圧縮強度を高めることができるとともに、部分的な破損が生じ難いものになる。このため、運搬、貯蔵等の取り扱いがさらに容易になる。
【図面の簡単な説明】
【図1】ブリケットの一部欠截斜視図である。
【図2】この発明のブリケットの製造方法を示す工程図である。
【図3】この発明のブリケットの他の製造方法を示す工程図である。
【符号の説明】
A ブリケット
B 綿状凝集体
C 脆性成形体
D 固形化補助剤
E 粉体[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a briquette for a steelmaking raw material, and more particularly to a technique for effectively using ferrous metal ground chips.
[0002]
[Prior art]
Chips generated when grinding ferrous metals such as bearing steel and carburized steel (hereinafter used as concepts including polishing, super-finish polishing, lapping, etc.) are grinding fluids and abrasives containing moisture and oil. It is recovered as a cotton-like (fibrous) agglomerate containing. Since this flocculent aggregate contains a large amount of pure iron, attempts have been made to reuse it as a raw material for steelmaking. However, since this flocculent agglomerate contains a large amount of moisture, if it is put into a blast furnace as it is, it causes a problem that bumping (steam explosion) occurs due to the moisture. Therefore, it is conceivable to remove the water in the flocculent aggregate by centrifugation or the like. In this case, the oil contained in the flocculent aggregate is also removed together with the water, and the flocculent aggregate spontaneously generates heat. Pure iron, which is a component of grinding chips, is transformed into iron oxide. For this reason, in order to reuse this as a steelmaking raw material, it is necessary to reduce it, and the use of a reducing agent increases the cost.
[0003]
Moreover, since the grinding chips to which the oil is attached are difficult to adhere to each other, it is difficult to solidify to a desired strength even if the cotton-like aggregate is compression-molded. Furthermore, for cotton-like aggregates containing a large amount of iron-based metal grinding chips having a carbon content of 0.2% by weight or more, the spring back during compression is large. It is difficult to solidify strongly. Therefore, even if the compression-molded cotton-like aggregate is put into the blast furnace, it flies up while being scattered and the problem is that the majority is collected by the dust collector.
Furthermore, since the fibrous grinding chips contained in the cotton-like aggregates are difficult to grind with a hammer mill or the like, the cotton-like aggregates cannot be finely sheared. For this reason, it is also difficult to process cotton-like aggregates into briquettes or the like.
Therefore, the actual condition is that the flocculent aggregates are disposed of in a landfill outsourced to a waste disposal company without being reused.
[0004]
[Problems to be solved by the invention]
However, landfill disposal of such flocculent aggregates is not preferable from the viewpoint of effective use of resources. There are also problems of causing environmental degradation and high disposal costs.
This invention is made | formed in view of the said problem, and it aims at providing the briquette for the steelmaking raw materials which can recycle | grind cutting chips effectively.
[0005]
[Means for Solving the Problems]
In order to achieve the above object, a briquette of the present invention is a dry briquette containing powdered pure iron and an oil component, and includes a ferrous metal grinding chip and a cotton containing a grinding fluid containing oil and moisture. The brittle molded body, which is obtained by removing excess water and oil content obtained by compression molding of the aggregates and retaining 1 to 5% by weight of pure iron oxidation-preventing oil, is impregnated with an inorganic solidification aid. (Claim 1).
Since the briquette for steelmaking raw material constituted in this way is a dry solid, there is no risk of bumping or rising even if it is put into the blast furnace as it is, and handling such as transportation and storage is easy. Become a thing. Moreover, since oil content is contained, it is prevented that powdery pure iron oxidizes.
[0008]
In the steelmaking raw material briquette (Claim 1 ), the inorganic solidification aid is preferably at least one selected from colloidal silica, sodium silicate, and aluminum phosphate (Claim 2 ). In spite of containing, it becomes solidified firmly.
[0009]
Briquettes for steelmaking raw material described above is preferably to include a solidification assistant 2-30 wt% (claim 3), which makes it more those more firmly solidified.
Wherein the blanking Ricketts is preferably those substantially pillow-shaped (claim 4), by which, it is possible to increase the compressive strength, partial damage is what hardly occurs.
[0010]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, embodiments of the present invention will be described in detail with reference to the accompanying drawings.
FIG. 1 is a partially broken perspective view showing a briquette for a steelmaking raw material according to an embodiment of the present invention. This briquette A contains powdery pure iron and oil, and is obtained by finely shearing a cotton-like aggregate containing iron-based metal grinding chips and oil and water-containing grinding fluid. The powder is solidified by using a solidification auxiliary agent and dried to remove the moisture. The briquette A is formed in a substantially pillow shape.
[0011]
FIG. 2 is a process diagram showing a manufacturing method of the briquette A. In the production of this briquette A, first, the cotton-like aggregate B (see FIG. 2 (a)) of the grinding chips generated when grinding the ferrous metal is pressed and compressed, and the cotton-like aggregate B is then compressed. The contents of water and oil, which are the components of the grinding fluid contained in, are preliminarily adjusted. The pressure-compression of the cotton-like aggregate B is performed, for example, by being sandwiched between a pair of rolls 2 while being conveyed by the belt conveyor 1 (see FIG. 2B). At this time, the flocculent aggregate B is preferably adjusted so that the moisture content does not exceed 50 wt% and the oil content does not exceed 10 wt%. Handling such as storage becomes easy.
[0012]
Next, the flocculent aggregate B whose water and oil contents are adjusted is compression-molded by a press using the mold 3 to obtain a brittle molded body C (see FIG. 2 (c)). By this compression molding, the spiral fibrous grinding chips contained in the cotton-like aggregate B are roughly sheared. Further, excess water and oil are removed, and the moisture content of the brittle shaped body C is adjusted to 2 to 12% by weight, and the oil content is adjusted to 1 to 5% by weight. Thereby, it is possible to effectively prevent the grinding chips from being oxidized by the minimum residual oil. In addition, since the moisture content of the cotton-like aggregate B is adjusted in advance in a range that does not exceed 50% by weight and the oil content does not exceed 10% by weight, respectively, the moisture and oil content of the brittle molded body C is adjusted. It can be adjusted easily and appropriately only by compression molding.
The brittle molded body C is formed in a shape that is easy to handle, such as a cylindrical shape, a spherical shape, and a prismatic shape, and is hardened to such an extent that it does not collapse during transportation to the next process.
[0013]
Next, the brittle shaped body C is put into a mixer (or Henschel type mixer) 5 with a chopper mill equipped with a rotating blade 4 together with the solidification auxiliary D and pulverized (see FIG. 2 (d)). Thereby, the grinding chips of the brittle shaped body C can be further finely sheared (finished shear) to obtain a powder E containing pure iron powder and a solidification auxiliary D (see FIG. 2 (e)). . The major axis of the pure iron powder is about 3 to 1000 μm. When the brittle shaped body C is pulverized, the fibrous grinding chips in the brittle shaped body C are coarsely sheared in advance, and can be finished and sheared without any trouble. When the fibrous grinding chips in the brittle shaped body C are not coarsely sheared, it is very difficult to pulverize them with the mixer 5, and it is impossible to obtain a fine powder E. Is possible.
[0014]
Examples of the solidifying aid D include rice bran (rice bran spirit), molasses such as sugarcane, starches such as straw starch and corn starch, quicklime, colloidal silica, sodium silicate, aluminum phosphate, vinyl acetate sludge, asphalt emulsion, bentonite One or more selected from among these are preferably used. Such a solidification auxiliary D is preferably contained in an amount of 2 to 30% by weight. In particular, the rice bran and molasses can be effectively prevented from changing the quality of pure iron powder contained in a large amount in the powder E, and the price thereof is also low, which makes it extremely suitable as a solidification aid D. is there. Further, when the asphalt emulsion is kneaded and then separated into asphalt and water, caking occurs and strength is developed. As this asphalt emulsion, an anionic asphalt is preferably used.
[0015]
Next, a predetermined amount of the powder E is compression-molded by a press using the molding die 6 (see FIG. 2 (f)) to obtain a substantially pillow-shaped water-containing briquette F containing a large amount of pure iron. When the powder E is compression-molded, the solidification aid D and the moisture in the powder E can solidify the powder of pure iron to which oils and fats adhere to each other. In particular, when using powder E containing 5 to 6% by weight of water, 4% by weight of rice bran and 2% by weight of molasses, and 7 to 15% by weight of water and 2 to 10% by weight of vinyl acetate sludge, The water-containing briquette F solidified more firmly can be obtained.
The “substantially pillow shape” is a shape having a rounded periphery and gradually increasing in thickness from the periphery to the center, and includes an egg shape, an almond shape, a rugby ball shape, and the like. By forming into such a shape, it is possible to obtain briquette A that is not easily disintegrated strongly against a compressive load and that is difficult to cause partial breakage at corners and the like.
[0016]
Then, normal temperature or cooled air is blown onto the water-containing briquette F immediately after compression molding to rapidly cool it (see FIG. 2 (g)). Thereby, the said water-containing briquette F can be solidified easily and stably. Then, the briquette A for steelmaking raw materials can be obtained (refer FIG.2 (i)) by curing (drying) the water-containing briquette F and removing the water content (refer FIG.2 (h)). This curing is preferably performed for about 2 days because the contained water can be removed reliably.
[0017]
Since the briquette A obtained as described above is a porous material obtained by solidifying the powder E, the contained moisture can be easily and reliably removed by curing. For this reason, there is no possibility that bumping will occur or it will rise and be discharged even if it is put into the blast furnace as it is. Further, since the processing is performed in a state where a part of the oil of the grinding fluid is always held, oxidation of pure iron is effectively prevented. For example, it has been confirmed that briquette A manufactured using cotton-like aggregate B containing grinding chips of bearing steel (SUJ-2) contains 84 to 95% by weight of pure iron. Therefore, the melting yield is very high at 90% or more, and can be provided to steel makers as a high-quality steelmaking raw material for a fee. In addition, it is easy to transport and handle in solid form.
[0018]
FIG. 3 is a process diagram showing another method for manufacturing the briquette A of the present invention. This manufacturing method is mainly different from the manufacturing method shown in FIG. 1 in that the pulverizing step of the brittle shaped body C is omitted. That is, in this manufacturing method, the brittle molded body C is obtained from the cotton-like aggregate B in exactly the same manner as the manufacturing method shown in FIG. 1 (see FIGS. 3A to 3C).
[0019]
And the brittle molded object C obtained through these processes is impregnated with the liquid solidification auxiliary D. The impregnation of the solidification auxiliary D is performed, for example, by immersing the brittle molded body C in the solidification auxiliary D injected into the
[0020]
Next, the brittle molded body C impregnated with the solidification aid D is cured (see FIG. 3 (e)) and dried (see FIG. 3 (f)) to obtain a briquette A for a steelmaking raw material ( (See FIG. 3 (g)).
The briquette A obtained as described above can exhibit the same action as the briquette A obtained by the manufacturing method shown in FIG. Moreover, since the manufacturing method shown in FIG. 3 omits the step of pulverizing the brittle molded body C, the briquette A can be manufactured more efficiently.
[0021]
The manufacturing method of each briquette described above is particularly preferably applied to recycle grinding chips containing 0.2 wt% or more of carbon. Such grinding chips have a large spring back and are difficult to solidify. By applying the manufacturing method of the present invention, the briquette A solidified by eliminating the influence of the spring back can be obtained. Can be easily obtained. In addition, as a representative example of the grinding chips containing 0.2 wt% or more of carbon, there can be mentioned grinding chips of bearing steel.
[0022]
【The invention's effect】
As described above, briquette for steelmaking material according to
[0025]
According to the briquette for steelmaking raw material according to claim 2 , the inorganic solidification aid is at least one selected from colloidal silica, sodium silicate, and aluminum phosphate. It becomes solidified. For this reason, handling such as transportation and storage is further facilitated.
According to the briquette for a steelmaking raw material according to claim 3 , since the solidification aid is mixed in an amount of 2 to 30% by weight, the powder can be solidified more firmly. For this reason, handling such as transportation and storage is further facilitated.
According to the briquette for a steelmaking raw material described in claim 4 , since it is substantially in the shape of a pillow, the compressive strength can be increased and partial breakage hardly occurs. For this reason, handling such as transportation and storage is further facilitated.
[Brief description of the drawings]
FIG. 1 is a perspective view of a briquette partially cut away.
FIG. 2 is a process diagram showing a briquette manufacturing method according to the present invention.
FIG. 3 is a process diagram showing another method for manufacturing a briquette according to the present invention.
[Explanation of symbols]
A Briquette B Cotton-like aggregate C Brittle shaped body D Solidification aid E Powder
Claims (5)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2001241024A JP3711045B2 (en) | 2000-08-10 | 2001-08-08 | Briquette for steelmaking raw materials |
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2000-243458 | 2000-08-10 | ||
| JP2000243458 | 2000-08-10 | ||
| JP2001241024A JP3711045B2 (en) | 2000-08-10 | 2001-08-08 | Briquette for steelmaking raw materials |
Related Child Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2005034271A Division JP2005163187A (en) | 2000-08-10 | 2005-02-10 | Briquette as raw material for steel making |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2002121625A JP2002121625A (en) | 2002-04-26 |
| JP3711045B2 true JP3711045B2 (en) | 2005-10-26 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2001241024A Expired - Fee Related JP3711045B2 (en) | 2000-08-10 | 2001-08-08 | Briquette for steelmaking raw materials |
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| Country | Link |
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| JP (1) | JP3711045B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2008081750A1 (en) | 2006-12-28 | 2008-07-10 | Jtekt Corporation | Iron-based powder material, method for producing the same, and briquette for steelmaking material |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1454996B1 (en) | 2003-03-07 | 2010-01-20 | JTEKT Corporation | Briquette for raw material for iron manufacture and briquette for introduction into slag generating apparatus |
| JP2005256116A (en) * | 2004-03-12 | 2005-09-22 | Koyo Seiko Co Ltd | Briquette for metal raw material and its producing method |
| KR101215039B1 (en) | 2005-03-18 | 2012-12-24 | 가부시키가이샤 제이텍트 | Compression molding machine for metal material briquette, manufacturing apparatus for metal material briquette, and compression molding method for metal material briquette |
| JP4828848B2 (en) * | 2005-03-23 | 2011-11-30 | 日新製鋼株式会社 | Method for producing waste briquette for smelting furnace and waste briquette for smelting furnace produced by the method |
| BRPI0821263B8 (en) * | 2007-12-17 | 2018-04-03 | Posco | binderless briquette manufacturing equipment and method |
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2001
- 2001-08-08 JP JP2001241024A patent/JP3711045B2/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2008081750A1 (en) | 2006-12-28 | 2008-07-10 | Jtekt Corporation | Iron-based powder material, method for producing the same, and briquette for steelmaking material |
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| JP2002121625A (en) | 2002-04-26 |
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