2016
DOI: 10.1002/srin.201600169
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Investigation on the Reduction Behavior of Coal Composite Pellet at Temperatures between 1373 and 1573 K

Abstract: The influence of different coal types on the reduction of composite pellet is investigated. Three Australian coals representing high volatile, medium volatile, and low volatile coal are analyzed and used for pellet preparation. High temperature behavior is investigated by Thermo‐Gravimetric Analyzer (TGA) at temperature range from 1373 K (1100 °C) to 1573 K (1300 °C). CO and CO2 gases released from the reaction measured by Infrared (IR) gas analyzer are used for kinetic analysis. Reaction rates at different te… Show more

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Cited by 6 publications
(8 citation statements)
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“…respectively, made according to the Equations (15) and (16). As can be seen from Figure 5a,b, for both the upper side nozzle and the lower side nozzle, the experimental values have a considerable linear relationship with the calculated values.…”
Section: Resultsmentioning
confidence: 81%
See 2 more Smart Citations
“…respectively, made according to the Equations (15) and (16). As can be seen from Figure 5a,b, for both the upper side nozzle and the lower side nozzle, the experimental values have a considerable linear relationship with the calculated values.…”
Section: Resultsmentioning
confidence: 81%
“…After the parameters such as the injection velocity of the upper side nozzle and the lower side nozzle are respectively substituted into Equation 14, the data of multiple linear regression are shown in the Table 6: From Table 6, the equation of the mixing time of the upper side nozzle and the lower side nozzle and the similar number of Ca, La 1 can be obtained, respectively: (16) where V us is the injection velocity of the upper side nozzle, m•s −1 , V ls is the injection velocity of the lower side nozzle, m•s −1 . Figure 5a,b shows the relationship between the experimental value and the calculated value of the dimensionless group of the mixing time of the upper side nozzle and the lower side nozzle, respectively, made according to the Equations (15) and (16). As can be seen from Figure 5a,b, for both the upper side nozzle and the lower side nozzle, the experimental values have a considerable linear relationship with the calculated values.…”
Section: Resultsmentioning
confidence: 99%
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“…Measured and model-predicted mass-loss fraction curves under different temperatures were compared, and the results are shown in Figure 3. In simulations, the briquette mass-loss fraction at time t was calculated using Equation (22).…”
Section: Briquette Mass Changementioning
confidence: 99%
“…The reaction kinetics of iron ore-carbon briquettes under inert atmosphere (nitrogen or argon) have been extensively studied, and their major features are well established [19][20][21][22]. The reduction of the briquette proceeds rapidly under high temperatures and generates a large amount of gas inside the briquette, making it more complicated than the reaction behavior of an iron ore or coal briquette.…”
Section: Introductionmentioning
confidence: 99%