JPH0623413B2 - Resin coated reduced iron pellets - Google Patents
Resin coated reduced iron pelletsInfo
- Publication number
- JPH0623413B2 JPH0623413B2 JP60122144A JP12214485A JPH0623413B2 JP H0623413 B2 JPH0623413 B2 JP H0623413B2 JP 60122144 A JP60122144 A JP 60122144A JP 12214485 A JP12214485 A JP 12214485A JP H0623413 B2 JPH0623413 B2 JP H0623413B2
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- Prior art keywords
- reduced iron
- pellets
- resin
- iron pellets
- water absorption
- 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.)
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Description
【発明の詳細な説明】 産業上の利用分野 本発明は樹脂被覆還元鉄ペレットに関する。TECHNICAL FIELD The present invention relates to resin-coated reduced iron pellets.
従来技術 還元ガスを用いて鉄鉱石を直接還元する直接還元製鋼法
としては、ミドレックス法、ヒル法、フィオール法等が
広く知られている。ミドレックス法およびヒル法は、塊
状または粉状の鉄鉱石を直径5〜20mm程度のペレット
状に固め、これを還元炉中に投入し、還元ガスを導入す
ることにより還元鉄を得る方法である。この還元鉄ペレ
ットは通常空隙率約50%程度のものであり、ペレット
どうしの摩擦により、比較的微粉化し易く、また、吸水
による酸化を起こし易い欠点がある。2. Description of the Related Art The Midrex method, the Hill method, the Fior method, and the like are widely known as direct reduction steelmaking methods for directly reducing iron ore using a reducing gas. The Midrex method and the Hill method are methods for obtaining reduced iron by solidifying massive or powdery iron ore into pellets having a diameter of about 5 to 20 mm, introducing this into a reducing furnace, and introducing a reducing gas. . The reduced iron pellets usually have a porosity of about 50%, and have a drawback that they are relatively easily pulverized by friction between the pellets and that they are easily oxidized by water absorption.
一方、フィオール法等の製鋼法では、天然の塊状又は粉
状の鉱石をそのまま使用するため、安価である一面、生
成物が粉状並びにスポンジ状であるため、吸湿、酸化を
起こし易い。従って、この方法では生成した還元鉄を再
度熱間(例えば770〜780℃)圧縮し、空隙率20〜
30%のブリケットとして、保管または搬送等に供して
いる。このブリケットは外観は鉄様の均一な表面をして
いるが、なお吸水率が3〜5%あり、これが酸化、腐蝕
および溶融時の突沸等の原因となっている。この吸水現
象を防止するため、米国特許3,573,959号明細
書では、このブリケット細孔に樹脂を含浸せしめて、ブ
リケット自体の熱で樹脂を硬化させ、細孔を封ずる方法
が記載されている。ここに用いられている樹脂は、脂環
式オレフィン、環状オレフィン、ジオレフィン、トリオ
レフィン等であり、シクロポリエンのオリゴマーを含む
混合物が特に好ましい旨記載され、特に蒸気分解サフサ
残査が適当である旨述べられている。これらは一般に、
粘度の低いものであり、ブリケット細孔中でブリケット
自体の熱により重合し、封孔するものと考えられる。On the other hand, in the steel manufacturing method such as the fior method, since natural lump or powdery ore is used as it is, it is inexpensive, but on the other hand, the product is powdery or sponge-like, so that moisture absorption and oxidation are easily caused. Therefore, in this method, the reduced iron produced is hot-compressed again (for example, 770 to 780 ° C.) to obtain a porosity of 20 to
Used as a 30% briquette for storage or transportation. Although this briquette has an iron-like uniform surface in appearance, it still has a water absorption rate of 3 to 5%, which causes oxidation, corrosion, and bumping during melting. In order to prevent this water absorption phenomenon, US Pat. No. 3,573,959 describes a method of impregnating the briquette pores with a resin and curing the resin by the heat of the briquette itself to seal the pores. ing. The resin used here is an alicyclic olefin, a cyclic olefin, a diolefin, a triolefin, etc., and it is described that a mixture containing an oligomer of cyclopolyene is particularly preferable, and a steam cracking suffer residue is particularly suitable. Is stated. These are generally
It has a low viscosity and is considered to be polymerized and sealed by the heat of the briquette itself in the briquette pores.
しかしながら、このブリケットの細孔が封じ吸水を防ぐ
技術は、還元鉄ペレットの吸水防止ならびに微粉化防止
には有用でない。その理由は、還元鉄ペレットがブリケ
ットに比べ著しく大きい空隙率を有し、かつブリケット
に比べ脆く、また一般に、樹脂含浸後のペレット自体の
温度がポリエン類を重合するのに十分高くないことが多
い。However, the technique in which the pores of the briquette seal the pores and prevent water absorption is not useful for preventing water absorption and reducing pulverization of the reduced iron pellets. The reason is that reduced iron pellets have significantly higher porosity than briquette and are more brittle than briquette, and in general, the temperature of the pellet itself after resin impregnation is not high enough to polymerize polyenes. .
米国特許第3,573,959号明細書に記載のごとき
樹脂を還元鉄ペレットの被覆に用いると、重合可能な温
度では樹脂の含浸量が著しく増加し、採算性がない。ま
た、ペレット表面の被覆厚が薄くなり、耐摩耗性が低下
する。また、温度が低いと、ポリエン類の重合を促進す
るための別の加熱工程が必要であったり、元素的に好ま
しくない金属塩等のドライヤーを必要とする。When a resin as described in U.S. Pat. No. 3,573,959 is used for coating reduced iron pellets, the impregnated amount of the resin is significantly increased at a temperature at which polymerization is possible, which is not profitable. In addition, the coating thickness on the surface of the pellet becomes thin, and the wear resistance decreases. Further, when the temperature is low, a separate heating step for accelerating the polymerization of polyenes is required, and a dryer for elementally unfavorable metal salts is required.
また英国特許第2129708号明細書には、パラフィ
ンワックスによる方法が記載されているが、パラフィン
ワックスは強度的に問題があり、必ずしも微粉化防止に
有用でない。British Patent No. 2129708 describes a method using paraffin wax, but paraffin wax has a problem in strength and is not necessarily useful for preventing pulverization.
発明が解決しようとする問題点 本発明は、還元鉄ペレットが有する前記問題点、即ち、
微粉化し易く、吸水により錆び易いと云った問題点、お
よび吸水した還元鉄ペレットを電気炉等に投入すると水
の突沸を生じ極めて危険である等の問題点を解決するこ
とを目的とする。またパラフィワックス等に比べ、より
高い強度の被覆の被覆剤を用いて達成する。DISCLOSURE OF THE INVENTION Problems to be Solved by the Invention The present invention provides the above-mentioned problems of reduced iron pellets, namely,
It is an object of the present invention to solve the problems that it is easily pulverized and that it easily rusts due to water absorption, and that it is extremely dangerous when water-absorbed reduced iron pellets are thrown into an electric furnace or the like to cause bumping of water. Further, it is achieved by using a coating agent having a higher strength than that of paraffin wax.
問題点を解決するための手段 本発明は、200℃における粘度が1〜10000cp
sであり、軟化温度が60〜195℃であるポリオレフ
ィン樹脂製被覆層を有する還元鉄ペレットに関する。Means for Solving Problems The present invention has a viscosity at 200 ° C. of 1 to 10000 cp.
s, and a reduced iron pellet having a polyolefin resin coating layer having a softening temperature of 60 to 195 ° C.
本発明で用いられる還元鉄ペレットはミドレックス法や
ヒル法等から得られるものであって、通常、空隙率約5
0〜60容量%、吸水量12〜15重量%(水中浸漬飽
和)、見掛け比重3〜4程度のものであり、粒径約5〜
20mm程度の実質上球形のペレットである。これらは鉄
鉱石をペレット化して得られた未還元鉄ペレットを還元
炉中、還元ガスと接触させることにより得られる。The reduced iron pellet used in the present invention is obtained from the Midrex method, the Hill method, etc., and usually has a porosity of about 5
0-60% by volume, water absorption 12-15% by weight (saturated in water), apparent specific gravity 3-4, particle size 5
It is a substantially spherical pellet of about 20 mm. These are obtained by bringing unreduced iron pellets obtained by pelletizing iron ore into contact with a reducing gas in a reducing furnace.
還元鉄ペレットを被覆するために用いる樹脂は特定の粘
度を有するポリオレフィン樹脂である。ポリオレフィン
樹脂としては、ポレチレン、ポリプロピレン、変性ポリ
エチレン等であり、ポリエチレン、特に分子量1000
以上のポリエチレンが適している。The resin used to coat the reduced iron pellets is a polyolefin resin having a specific viscosity. Examples of the polyolefin resin include polyethylene, polypropylene, modified polyethylene, and the like.
The above polyethylenes are suitable.
本発明に好適なポリオレフィン樹脂の粘度は200℃に
おいて1〜10000cps 、特に10〜7000cps が
好ましく、軟化温度が60〜195℃、特に80〜120
℃であるのが好ましい。The viscosity of the polyolefin resin suitable for the present invention at 200 ° C. is 1 to 10000 cps, particularly 10 to 7000 cps, and the softening temperature is 60 to 195 ° C., especially 80 to 120.
It is preferably in ° C.
ポリオレフィン樹脂の粘度が10000cps より大きい
と、還元鉄ペレット表面への樹脂被覆が不均一となり、
吸水防止のためにより多くの樹脂を必要とすることにな
る。これは極めて不経済である。If the viscosity of the polyolefin resin is greater than 10,000 cps, the resin coating on the surface of the reduced iron pellets will be uneven,
More resin is required to prevent water absorption. This is extremely uneconomical.
また、樹脂粘度が1cps より小さいと、樹脂を適正な粘
度に維持することが困難となり、還元鉄ペレットの細孔
内部に浸透し、また、ペレットは空隙率約50%と多孔
性であり、従ってこれを溶融ポリオレフィン等に浸漬し
て被覆するとポリオレフィンがペレットの細孔内部に浸
透し細孔の封鎖に消費されるため、ペレット表面への樹
脂の付着量が減少する。その結果、処理ペレットの耐摩
耗性や耐微粉化性が低下する。また、本発明ではペレッ
トの表面被覆が目的であり、細孔および空隙の封鎖は必
ずしも必要でない。Further, if the resin viscosity is less than 1 cps, it becomes difficult to maintain the resin at an appropriate viscosity, the resin penetrates into the pores of the reduced iron pellets, and the pellets are porous with a porosity of about 50%. When this is dipped in molten polyolefin or the like for coating, the polyolefin penetrates into the inside of the pores of the pellet and is consumed for blocking the pores, so that the amount of resin adhering to the pellet surface is reduced. As a result, the abrasion resistance and pulverization resistance of the treated pellets are reduced. Further, the purpose of the present invention is to coat the surface of the pellet, and it is not always necessary to block the pores and voids.
従って、経済的には樹脂が細孔の奥まで浸入しないよう
な粘度を選定するのが望ましい。Therefore, it is economically desirable to select a viscosity that does not allow the resin to penetrate deep into the pores.
ポリオレフィンの使用により、パラフィン類より少量の
使用で高い強度の被膜を形成することができる。The use of polyolefin enables formation of a high-strength coating with a smaller amount than paraffins.
ポリオレフィンは望ましくは無溶媒下、その効果溶融点
以上、好ましくは軟化溶融点より2〜3℃以上高くなる
ように還元鉄ペレットと接触させ、かつ、接触時の粘度
が少なくとも80〜90cps 以上を保持させるのが望ま
しく、ポリオレフィンまたは還元鉄ペレットの温度を調
整することにより可能である。The polyolefin is preferably brought into contact with the reduced iron pellets in the absence of a solvent so as to be higher than its effective melting point, preferably 2 to 3 ° C. higher than the softening melting point, and the viscosity at the time of contact is kept at least 80 to 90 cps It is desirable to adjust the temperature of the polyolefin or the reduced iron pellets.
ポリオレフィンと還元鉄ペレットの接触は浸漬、スプレ
ー等が可能であるが、浸漬は均一な反面、付着量が多
く、スプレーは均一性に欠けるためポリオレフィンの一
定量をスプレー、またはそのまま投入し前記条件に保持
した後、回転等により混練する。Although contact between the polyolefin and the reduced iron pellets can be performed by dipping, spraying, etc., the dipping is uniform, but the amount of adhesion is large and the spray lacks uniformity. After holding, kneading is performed by rotation or the like.
ポリオレフィン樹脂て被覆した還元鉄ペレットの製造法
の一例を第1図〜第4図に示す。An example of a method for producing reduced iron pellets coated with a polyolefin resin is shown in FIGS. 1 to 4.
第1図は本発明ポリオレフィン被覆還元鉄ペレット製造
用装置の模式的断面図であり、第2図は第1図の装置の
左側面図、第3図はI−I断面図および第4図は右側面
図を示す。回転ドラム(1)はモーター(2)によって回転
する回転支持台(3)によって回転可能に設置されてお
り、ドラム外側面に設けられたヒーター(4)により加熱
される。ドラム左側面にはドラムの回転に際して、ヒー
ターに通電し得るようカーボンリング(5)が配設され、
ブラシ(6)により電源と接続されている。ヒーターに供
給される電力はスライダックス(7)により、ドラム内部
温度に対応してコントロールされる。この温度と供給電
力の調節は手動でもよいがコンピューターにより容易に
管理し得る。(10)は絶縁体、Aは電流計、Vは電圧計
を示す。ドラム右側面には還元鉄ペレットを供給するた
めの供給口(8)と蓋(9)および不活性ガス(例えば、窒素
ガス)供給用バルブ(10)が設けられている。ドラム内
部に羽根(11)が設けられている。FIG. 1 is a schematic sectional view of an apparatus for producing a polyolefin-coated reduced iron pellet of the present invention, FIG. 2 is a left side view of the apparatus of FIG. 1, FIG. 3 is an II sectional view and FIG. The right side view is shown. The rotary drum (1) is rotatably installed by a rotary support base (3) which is rotated by a motor (2), and is heated by a heater (4) provided on the outer surface of the drum. A carbon ring (5) is installed on the left side of the drum so that the heater can be energized when the drum rotates.
It is connected to the power supply by the brush (6). The electric power supplied to the heater is controlled by the slider box (7) according to the temperature inside the drum. The adjustment of the temperature and the supplied power may be manual, but can be easily managed by a computer. (10) indicates an insulator, A indicates an ammeter, and V indicates a voltmeter. A supply port (8) for supplying reduced iron pellets, a lid (9), and an inert gas (for example, nitrogen gas) supply valve (10) are provided on the right side surface of the drum. A blade (11) is provided inside the drum.
還元鉄ペレットとこれを被覆するためのポリオレフィン
樹脂を供給口から仕込み、不活性ガスでドラム内部の空
気を完全に置換した後、バルブ(10)および蓋(9)を完
全に密閉し、ドラムを回転させながら、ヒーターで加熱
する。ペレットは羽根によって回転が邪魔されるため、
お互いによく接触し、加熱により溶融した樹脂が均一に
付着する。樹脂融点および内部温度を調節することによ
り、樹脂の粘度を適当な範囲に選定することが可能であ
り、樹脂が還元鉄ペレットの内部に浸入することなく、
表面に均一に付着させることができる。After charging reduced iron pellets and a polyolefin resin for coating the pellets from the supply port and completely replacing the air inside the drum with an inert gas, the valve (10) and lid (9) were completely sealed and the drum was closed. Heat with a heater while rotating. Since the rotation of the pellets is obstructed by the blades,
The resins that are in good contact with each other and melted by heating adhere uniformly. By adjusting the resin melting point and the internal temperature, it is possible to select the viscosity of the resin in an appropriate range, without the resin penetrating inside the reduced iron pellets,
It can be evenly attached to the surface.
還元鉄ペレットに対するポリオレフィンの付着量は、還
元鉄ペレット100重量部当り、ポリオレフィン0.1
〜4重量部、特に0.3〜3重量部が適当である。0.
1重量部より少ないと被膜厚さが不十分となり、逆に4
重量部より多く用いても不経済になるだけである。The amount of polyolefin adhering to the reduced iron pellets was 0.1% of polyolefin per 100 parts by weight of reduced iron pellets.
-4 parts by weight, especially 0.3-3 parts by weight are suitable. 0.
If it is less than 1 part by weight, the coating thickness becomes insufficient, and conversely 4
It is only uneconomical to use more than parts by weight.
以上の如く、本発明により多孔性還元鉄ペレット表面に
吸い込みを極力おさえつつ均一に塗布することが可能と
なり、また、酸化、粉化、破れ等を生じない樹脂被覆還
元鉄ペレットの供給が可能となるものである。尚、本発
明はブリケットにも適用できる。As described above, according to the present invention, it becomes possible to apply uniformly to the surface of the porous reduced iron pellets while suppressing suction as much as possible, and it is possible to supply the resin-coated reduced iron pellets that do not cause oxidation, pulverization, breakage, or the like. It will be. The present invention can also be applied to briquettes.
以下、実施例を挙げて本発明を説明する。Hereinafter, the present invention will be described with reference to examples.
実施例1 還元鉄ペレット(空隙率55%、吸水率15%)100kg
をドラムに入れ、窒素ガス雰囲気下で50℃に加熱し、
これに分子量1400、軟化点83℃のポイレチレン樹
脂2kgを入れ、昇温しポリエチレンの温度を120℃に
保ち、3分間ドラムを40rpmで回転させた。得られた
ポリエチレン被覆ペレットを屋外に1ケ月放置し、金属
化率の変化、降雨時の吸水率、回転強度、落下強度を観
察した。結果を表−1に示す。Example 1 100 kg of reduced iron pellets (porosity 55%, water absorption 15%)
In a drum and heated to 50 ° C under a nitrogen gas atmosphere,
2 kg of a polyethylene resin having a molecular weight of 1400 and a softening point of 83 ° C. was put into this, and the temperature of polyethylene was kept at 120 ° C. to rotate the drum at 40 rpm for 3 minutes. The obtained polyethylene-coated pellets were left outdoors for one month, and changes in metallization rate, water absorption rate during rainfall, rotational strength, and drop strength were observed. The results are shown in Table-1.
金属化率:JIS−M−8202に基づく湿式分析によ
り測定。Metallization rate: Measured by wet analysis based on JIS-M-8202.
吸水率:平均降雨量2mm/Hrの降雨時に試料100g
を5時間曝露し、表面付着水分を紙に吸収後、直ちに
秤量して算出。Water absorption rate: 100g of sample when it rains with an average rainfall of 2mm / hr
Was exposed for 5 hours, the water adhering to the surface was absorbed by the paper, and then weighed immediately and calculated.
回転強度:JIS−M−8712に基づき測定。Rotational strength: Measured based on JIS-M-8712.
落下強度:JIS−M−8711に基づき測定。Drop strength: Measured based on JIS-M-8711.
実施例2 還元鉄ペレット(空隙率55%、吸水率15%)100kg
をドラムに入れ、窒素ガス雰囲気下で50℃に加熱し、
これに分子量5000、軟化点110℃のポリエチレン
樹脂2.5kgを130℃に保ち、3分間ドラムを40rp
m で回転させた。得られたポリエチレン被覆ペレットを
実施例1と同様にして金属化率の変化、降雨時の吸水率
および回転強度、落下強度を観察した。結果を表−1に
示す。Example 2 100 kg of reduced iron pellets (porosity 55%, water absorption 15%)
In a drum and heated to 50 ° C under a nitrogen gas atmosphere,
2.5 kg of polyethylene resin with a molecular weight of 5000 and a softening point of 110 ° C is kept at 130 ° C for 3 minutes and the drum is rotated at 40 rp.
Rotated at m. The obtained polyethylene-coated pellets were observed in the same manner as in Example 1 for changes in metallization rate, water absorption rate during rainfall, rotational strength, and drop strength. The results are shown in Table-1.
比較例1 未塗布還元鉄ペレット100kgを1ケ月屋外に曝露し、
金属化率変化を調べるとともに、降雨時の吸水、回転強
度、落下強度を観察した。結果を表−1に示す。Comparative Example 1 100 kg of uncoated reduced iron pellets were exposed outdoors for 1 month,
In addition to investigating changes in metallization rate, water absorption, rotational strength, and drop strength during rainfall were observed. The results are shown in Table-1.
比較例2 還元鉄ペレット(空隙率55%、吸水率15%)100kg
に液状ジオレフィン(商品名:QUINTOL MW5
00)100重量部にシクロペンタジエン8重量部を加
えたもの5kgを常温で3分間回転塗布したが、30分後
も粘着性大であり、乾燥のため200℃まで昇温したと
ころ、処理剤は全てペレット内部に吸収されてしまい被
覆効果は殆んど認められなかった。Comparative Example 2 Reduced iron pellets (porosity 55%, water absorption 15%) 100 kg
Liquid diolefin (trade name: QUINTOL MW5
00) 5 kg of 100 parts by weight plus 8 parts by weight of cyclopentadiene was spin-coated at room temperature for 3 minutes, but after 30 minutes it was still tacky and the temperature was raised to 200 ° C. for drying. All were absorbed inside the pellets and almost no coating effect was observed.
比較例3 還元鉄ペレット(空隙率55%、吸水率15%)100kg
を90℃に加熱し、これを金網に保持し、溶融パラフィ
ンワックス(液温120℃;軟化点68℃)に5秒間浸漬
後、回転強度および落下高度を測定した。結果を表−1
に示す。塗布量は5.8%であった。Comparative Example 3 Reduced iron pellets (porosity 55%, water absorption 15%) 100 kg
Was heated to 90 ° C., held in a wire net, immersed in molten paraffin wax (liquid temperature 120 ° C .; softening point 68 ° C.) for 5 seconds, and the rotational strength and drop height were measured. The results are shown in Table-1
Shown in. The coating amount was 5.8%.
比較例4 還元鉄ペレット(空隙率55%、吸水率15%)100kg
を50℃に加熱し、これに軟化点68℃のパラフィンワ
ックス2kgを100℃に保ち、3分間ドラムを40rpm
で回転させた。得られたパラフィンワックス被覆ペレッ
トについて回転強度および落下強度を測定した。結果を
表−1に示す。Comparative Example 4 Reduced iron pellets (porosity 55%, water absorption 15%) 100 kg
Is heated to 50 ° C., 2 kg of paraffin wax having a softening point of 68 ° C. is kept at 100 ° C., and the drum is rotated at 40 rpm for 3 minutes.
I rotated it. The rotation strength and the drop strength of the obtained paraffin wax-coated pellets were measured. The results are shown in Table-1.
発明の効果 本発明樹脂被覆還元鉄ペレットは酸化を受け難く、吸水
量が少なく、しかも粉塵化し難い。従って還元鉄ペレッ
トの保存、搬送が容易となる。またパラフィンワック
ス、被覆ペレットに比べ、少量の使用で高い摩耗強度が
得られる。 EFFECTS OF THE INVENTION The resin-coated reduced iron pellets of the present invention are less susceptible to oxidation, have a smaller water absorption amount, and are less likely to be dusted. Therefore, the reduced iron pellets can be easily stored and transported. Also, compared with paraffin wax and coated pellets, high wear strength can be obtained with a small amount of use.
第1図は本発明還元鉄ペレット製造装置の模式的断面
図、第2図は第1図装置の左側面図、第3図はI−I断
面図および第4図は右側面図を示す。 (1)……回転ドラム、(2)……モーター (3)……回転支持台、(4)……ヒーター (5)……カーボンリング、(6)……ブラシ (7)……スライダックス、(8)……供給口 (9)……蓋、(11)……羽根 (10)……不活性ガス供給バルブ。FIG. 1 is a schematic sectional view of a reduced iron pellet manufacturing apparatus of the present invention, FIG. 2 is a left side view of the apparatus of FIG. 1, FIG. 3 is a sectional view taken along line I-I, and FIG. 4 is a right side view. (1) …… Rotary drum, (2) …… Motor (3) …… Rotary support, (4) …… Heater (5) …… Carbon ring, (6) …… Brush (7) …… Sliderax , (8) …… Supply port (9) …… Lid, (11) …… Vane (10) …… Inert gas supply valve.
Claims (3)
psであり、軟化温度が60〜195℃であるポリオレ
フィン樹脂製被覆層を有する還元鉄ペレット。1. A viscosity at 200 ° C. of 1 to 10000 c
ps and reduced iron pellets having a coating layer made of polyolefin resin having a softening temperature of 60 to 195 ° C.
のポリエチレン樹脂である第1項記載のペレット。2. The pellet according to claim 1, wherein the polyolefin resin is a polyethylene resin having a molecular weight of 1000 or more.
ット100重量部当り0.1〜4重量部である第1項記
載のペレット。3. The pellet according to claim 1, wherein the coating amount of the polyolefin resin is 0.1 to 4 parts by weight per 100 parts by weight of reduced iron pellets.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60122144A JPH0623413B2 (en) | 1985-06-04 | 1985-06-04 | Resin coated reduced iron pellets |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60122144A JPH0623413B2 (en) | 1985-06-04 | 1985-06-04 | Resin coated reduced iron pellets |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61279635A JPS61279635A (en) | 1986-12-10 |
| JPH0623413B2 true JPH0623413B2 (en) | 1994-03-30 |
Family
ID=14828698
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60122144A Expired - Lifetime JPH0623413B2 (en) | 1985-06-04 | 1985-06-04 | Resin coated reduced iron pellets |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0623413B2 (en) |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4547920A (en) * | 1983-10-19 | 1985-10-22 | Sears Manufacturing Company | Process for developing porosity in air impervious film and articles produced by the process |
-
1985
- 1985-06-04 JP JP60122144A patent/JPH0623413B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61279635A (en) | 1986-12-10 |
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