書誌事項
- タイトル別名
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- Reduction of Sintered Ore in Fixed Bed with CO Gas
- ショウケツコウ ノ コテイソウ ニ オケル CO ガス カンゲン
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抄録
<p>The reduction processes of sintered ore in the fixed bed with CO gas have been studied.</p> <p>The reduction rates of sintered ore in the temperature range from 800 to 1000℃ have been measured by analysing the waste gas composition or by weighing the bed weight continuously ; the following results are obtained.</p> <p>(1) The reduction curves obtained by gas analysis are in good agreement with those by the thermobalance in the same experimental conditions.</p> <p>(2) At a constant ratio of the bed weight to the gas flow rate (M/V), the same reduction curves were obtained at different gas flow rates (4.6, 9.1 and 36 Nl/min) ; the gas film resistance seems to be unimportant.</p> <p>(3) The analysis based on the unreacted core model for a single pellet applied to the reduction of sintered ore with CO gas gives the following expression for the calculated chemical reaction rate constant ks=exp(5.23-14000/RT). As the calculated constant F defind as r0ks/De is dependent of the diameter of sintered ore, it is considered that the reduction process is controlled by the chemical reaction rate for small sizes (Dp=3 mm), but is controlled by mixed rates of the chemical reaction and the gas diffusion through ash layer for large sizes (Dp=7-13 mm).</p>
収録刊行物
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- 鉄と鋼
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鉄と鋼 60 (10), 1425-1431, 1974-09-01
一般社団法人 日本鉄鋼協会
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詳細情報 詳細情報について
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- CRID
- 1390001288150449664
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- NII論文ID
- 110001871663
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- NII書誌ID
- AN00151251
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- ISSN
- 18832954
- 00211575
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- NDL書誌ID
- 7582967
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- 本文言語コード
- ja
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- データソース種別
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- JaLC
- NDL
- Crossref
- CiNii Articles
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- 抄録ライセンスフラグ
- 使用不可