2021
DOI: 10.1016/j.clet.2021.100345
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Clean iron production through direct reduction of mineral iron carbonate with low-grade hydrogen sources; the effect of reduction feed gas composition on product and exit gas composition

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Cited by 15 publications
(11 citation statements)
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“…[ 13 ] The utilization of hydrogen as the reducing agent has the great advantage that gaseous water is the sole by‐product. [ 14 ] In this view it is easy to establish the real effect of hydrogen as substitute of carbon monoxide in the direct reduction relating its usage to the carbon consumption and carbon dioxide emissions reduction during ironmaking. [ 15 ] The hydrogen‐based direct reduction process includes multiple types of chemical reactions, solid‐state and defect‐mediated diffusion (of oxygen and hydrogen species), several phase transformations, as well as massive volume shrinkage and mechanical stress buildup.…”
Section: Introductionmentioning
confidence: 99%
“…[ 13 ] The utilization of hydrogen as the reducing agent has the great advantage that gaseous water is the sole by‐product. [ 14 ] In this view it is easy to establish the real effect of hydrogen as substitute of carbon monoxide in the direct reduction relating its usage to the carbon consumption and carbon dioxide emissions reduction during ironmaking. [ 15 ] The hydrogen‐based direct reduction process includes multiple types of chemical reactions, solid‐state and defect‐mediated diffusion (of oxygen and hydrogen species), several phase transformations, as well as massive volume shrinkage and mechanical stress buildup.…”
Section: Introductionmentioning
confidence: 99%
“…The experimental studies in the lab-scale fixed-bed tubular reactor have shown that complete FeCO 3 conversion from siderite and ankerite is possible with a degree of metallization of > 80 % at a temperature of 873 K (reduction time of 5.6 h). The remaining iron was present as partially reduced wu ¨stite (Fe 1-x O) [26]. Increasing the reduction temperature above 873 K resulted in an increase of the degree of metallization up to 92 % at 1023 K, while the reduction time decreased to 2.5 h. The reduction was stopped when the process gas composition at the reactor exit (j Process gas ) was indistinguishable from the feed gas composition (j Feed ).…”
Section: Results -Direct Siderite Reductionmentioning
confidence: 99%
“…High flexibility concerning the availability of the reducing agent hydrogen is crucial to establish a technology concept for the production of iron through direct reduction of siderite ore with hydrogen. The flexibility of the direct reduction process regarding the hydrogen concentration in the feed gas stream was investigated by Loder et al [26] through variation of the feed gas ratio of hydrogen to nitrogen (H 2 /N 2 ) from 90:10 to 55:45 (v/v), and the admixture of methane (15-80 vol %) and CO 2 (27-63 vol %) to the feed gas stream. The degree of metallization did not vary significantly with varying hydrogen concentration and methane admixture, implying a high flexibility of the process for fluctuating hydrogen availability.…”
Section: Results -Direct Siderite Reductionmentioning
confidence: 99%
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