The available studies in the literature on mathematical modeling of the vacuum circulation (RH) refining process of molten steel have briefly been reviewed. The latest advances obtained by the author with his research...The available studies in the literature on mathematical modeling of the vacuum circulation (RH) refining process of molten steel have briefly been reviewed. The latest advances obtained by the author with his research group have been summarized. On the basis of the mass and momentum balances in the system, a new mathematical model for decarburization and degassing during the RH and RH KTB refining processes of molten steel was proposed and developed. The refining roles of the three reaction sites, i.e. the up snorkel zone, the droplet group and steel bath in the vacuum vessel, were considered in the model. It was assumed that the mass transfer of reactive components in the molten steel is the rate control step of the refining reactions. And the friction losses and drags of flows in the snorkels and vacuum vessel were all counted. The model was applied to the refining of molten steel in a multifunction RH degasser of 90 t capacity. The decarburization and degassing processes in the degasser under the RH and RH KTB operating conditions were modeled and analyzed using this model. Besides, proceeded from the two resistance mass transfer theory and the mass balance of sulphur in the system, a kinetic model for the desulphurization by powder injection and blowing in the RH refining of molten steel was developed. Modeling and predictions of the process of injecting and blowing the lime based powder flux under assumed operating modes with the different initial contents of sulphur and amounts of powder injected and blown in a RH degasser of 300 t capacity were carried out using the model. It was demonstrated that for the RH and RH KTB refining processes, and the desulphurization by powder injection and blowing in the RH refining, the results predicted by the models were all in good agreement respectively with data from industrial experiments and practice. These models may be expected to offer some useful information and a reliable basis for determining and optimizing the technologies of the RH and RH KTB refining and desulphurization by powder injection and blowing in the RH refining and for controlling the processes.展开更多
100 t RH真空炉外精炼设备,备有RH-WPB水冷顶枪喷粉系统,该套喷粉系统一次最大喷吹量2 000kg,理论最大喷吹速度250 kg/min,采用的喷粉脱硫剂为80CaO/20CaF_2。14MnSV钢、30CrMnSi钢和27CrMo27Vs钢的RH-WPB处理结果表叫,经过RH喷粉处理后...100 t RH真空炉外精炼设备,备有RH-WPB水冷顶枪喷粉系统,该套喷粉系统一次最大喷吹量2 000kg,理论最大喷吹速度250 kg/min,采用的喷粉脱硫剂为80CaO/20CaF_2。14MnSV钢、30CrMnSi钢和27CrMo27Vs钢的RH-WPB处理结果表叫,经过RH喷粉处理后,钢水中的硫含量分别从42×10、28×10^(-6)和39×10^(-6)降至28×10^(-6)、15×10^(-6)和22×10~,脱硫效果显著。展开更多
文摘The available studies in the literature on mathematical modeling of the vacuum circulation (RH) refining process of molten steel have briefly been reviewed. The latest advances obtained by the author with his research group have been summarized. On the basis of the mass and momentum balances in the system, a new mathematical model for decarburization and degassing during the RH and RH KTB refining processes of molten steel was proposed and developed. The refining roles of the three reaction sites, i.e. the up snorkel zone, the droplet group and steel bath in the vacuum vessel, were considered in the model. It was assumed that the mass transfer of reactive components in the molten steel is the rate control step of the refining reactions. And the friction losses and drags of flows in the snorkels and vacuum vessel were all counted. The model was applied to the refining of molten steel in a multifunction RH degasser of 90 t capacity. The decarburization and degassing processes in the degasser under the RH and RH KTB operating conditions were modeled and analyzed using this model. Besides, proceeded from the two resistance mass transfer theory and the mass balance of sulphur in the system, a kinetic model for the desulphurization by powder injection and blowing in the RH refining of molten steel was developed. Modeling and predictions of the process of injecting and blowing the lime based powder flux under assumed operating modes with the different initial contents of sulphur and amounts of powder injected and blown in a RH degasser of 300 t capacity were carried out using the model. It was demonstrated that for the RH and RH KTB refining processes, and the desulphurization by powder injection and blowing in the RH refining, the results predicted by the models were all in good agreement respectively with data from industrial experiments and practice. These models may be expected to offer some useful information and a reliable basis for determining and optimizing the technologies of the RH and RH KTB refining and desulphurization by powder injection and blowing in the RH refining and for controlling the processes.
文摘100 t RH真空炉外精炼设备,备有RH-WPB水冷顶枪喷粉系统,该套喷粉系统一次最大喷吹量2 000kg,理论最大喷吹速度250 kg/min,采用的喷粉脱硫剂为80CaO/20CaF_2。14MnSV钢、30CrMnSi钢和27CrMo27Vs钢的RH-WPB处理结果表叫,经过RH喷粉处理后,钢水中的硫含量分别从42×10、28×10^(-6)和39×10^(-6)降至28×10^(-6)、15×10^(-6)和22×10~,脱硫效果显著。
