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排序方式: 共有135条查询结果,搜索用时 15 毫秒
1.
基于单体硫形成原因和危害机理的分析,通过冷态-模拟试验,研究了加料方式、二次风、烟道结构等对减少物料夹带、加强烟气混合、加速烟尘粘结物沉降的作用,并由此得到了熔池熔炼炉烟气中单体硫的治理方案。 相似文献
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不同进电方式与槽膛内形的铝电解槽内流场的数值模拟 总被引:1,自引:0,他引:1
采用k-ε双方程模型封闭的Navier-stokes方程描述铝电解槽内熔体的湍流流动。对于200kA、160kA与80kA三种不同进电方式的铝电解槽以及具有不同槽膛内形的160kA槽,在磁场、热场解析的基础上,计算出相应工况下动量方程中的源项,即洛仑兹力,并对稳定状态下熔体的三维流场进行了数值计算。计算结果表明,在模拟工况条件下,铝液流动在200kA槽内呈现出四个旋涡,在160kA与80kA槽内呈现出两个旋涡;不同的进电方式与槽膛内形对熔体的运动方式均有显著影响。 相似文献
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For acquiring the details in aluminum holding furnace with bottom porous brick purging system, efforts were performed to try
to find out the potential optimal operation schemes. By adopting transient analysis scheme and constant boundary temperature,
combustion in the furnace was investigated numerically using computational fluid dynamics (CFD). The predicted gas temperature
shows good agreement with the measured results, and the predicted energy distribution of the furnace is consistent with that
obtained from energy balance experiment, which confirms the reliability of the numerical solution. The results show that as
the fuel-air mixture temperature rises up from 300 K to 500 K, the energy utilization of the furnace could increase from 34.55%
to 37.14%. However, as the excess air coefficient increases from 1.0 to 1.4, energy utilization drops from 34.55% to 29.56%.
Increasing the combustion temperature is the most effective way to improve the energy efficiency of the furnace. High reactant
temperature and medium excess air coefficient are recommended for high operation performance, and keeping the furnace jamb
sealed well for avoiding leakage has to be emphasized. 相似文献
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Considering the fact that the temperature distribution in furnace of a tangential fired pulverized coal boiler is difficult to be measured and monitored, two-stage numerical simulation method was put forward. First, multifield coupling simulation in typical work conditions was carried out off-line with the software CFX-4.3, and then the expression of temperature profile varying with operating parameter was obtained. According to real-time operating parameters, the temperature at arbitrary point of the furnace can be calculated by using this expression. Thus the temperature profile can be shown on-line and monitoring for combustion state in the furnace is realized. The simulation model was checked by the parameters measured in an operating boiler, DO130-9. 8/540. The maximum of relative error is less than 12% and the absolute error is less than 120℃, which shows that the proposed two-stage simulation method is reliable and able to satisfy the requirement of industrial application. 相似文献
6.
The standard κ-ε model was adopted to simulate the flow field of molten metal in three aluminum electrolysis cells with different anode risers. The Hartman number, Reynolds number and the turbulent Reynolds number of molten metal were calculated quantitatively. The turbulent Reynolds number is in the order of 10^3 , and Reynolds number is in the order of 104 if taking the depth of molten metal as the characteristic length. The results show that the molten metal flow is the turbulence of high Reynolds number, the turbulent Reynolds number is more appropriate than Reynolds number to be used to describe the turbulent characteristic of molten metal, and Hartman number displays very well that electromagnetic force inhibits turbulent motion of molten metal. 相似文献
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To predict three-dimensional temperature distribution of molten aluminum and its influencing factors inside an industrial
aluminum holding furnace, a fluid-solid coupled method was presented. The fluid-solid coupled mathematics models of aluminum
holding furnace in the premixed combustion processing were established based on mass conservation, moment conservation, momentum
conservation, energy conservation and chemistry species conservation. Computational results agree well with the test data
of the typical condition. The maximum combustion temperature is 1 850 K. The average temperature of the molten aluminum is
1 158 K, and the maximum temperature difference is about 240 K. The average temperature increases 0.3 °C while the temperature
of combustion air increases 1 °C. The optimal excess air ratio is 1.25–1.30. 相似文献
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应用标准k-Е双方程、低Reynolds数Jones-Launder k-Е模型与RNG k-Е模型分别对三种不同进电方式(四点进电的200kA槽、两点进电的160kA槽以及三点进电的80kA槽)的预焙阳极Al电解槽内的Al液流场进行了数值仿真,并且应用铁棒溶蚀法对相应工况下的Al液流场进行了工业测试。通过对计算结果和测试结果的比较与分析,可以得出:与标准k-Е模型相比较,低Reynolds数模型具有较小的湍流粘度;标准k-Е模型与RNG模型用于Al液流场的数值仿真时,其计算结果均有较高的可靠性。并初步得出在电流强度大于80kA的Al电解槽中,Al液流动的计算不适宜应用低Reynolds数模型。 相似文献