共查询到19条相似文献,搜索用时 93 毫秒
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降膜结晶过程的数值模拟 总被引:5,自引:0,他引:5
本文采用数值方法对在工业上有着广泛应用前景的降膜结晶分离过程进行了模拟,提出了一套描述降膜结晶过程的降膜流动、传热、传质及结晶相变相互耦合的以控制容积为基础的有限差分的湍流数值计算模型和算法。本模型的计算结果与以前简化模型的计算结果相比,更符合实验值. 相似文献
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降膜结晶过程传热传质简化积分模型模拟计算 总被引:6,自引:0,他引:6
本文在对降膜结晶分离过程进行传热传质分析的基础上,建立了简化数学模型。文中按时间先后次序分成若干时间流股,并对每一流股按随体坐标自上而下对传热和传质方程进方积分,其中利用稳态充分发展的传热传质公式计算局部、即时的结晶量,进一步将不同时间流股所得结晶量叠加即得到结晶在空间和时间上的分布。文中将计算结果与所作的实验结果进行了比较,二者吻合较好。最后利用本文的计算模型进一步对广泛的影响因素进行了研究,获得一系列有益的结果。 相似文献
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本文对气流床煤气化炉内高温合成气和壁面渣层的流动与传热传质过程进行了分析,建立了渣层流动、传热传质和相变数理模型,采用VOF方法对渣层和气体之间自由界面进行追踪,采用射线追踪方法(DTRM)计算辐射换热,采用焓法计算渣层相变,熔融态渣滴在渣层表面的沉积通过源项引入.应用所建立的数学模型对实验室规模的Texaco煤气化炉进行了模拟.结果表明:气化炉壁面换热系数从上到下先增加再减少最后再增加;炉膛温度升高,固态渣层厚度减少;壁面温度升高,固态渣层厚度减少. 相似文献
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蒸发式冷凝器管外流体流动与传热传质强化 总被引:3,自引:0,他引:3
蒸发式冷凝器是一种高效散热设备,能源危机和水环保促进了它的应用.提出了扭曲管强化管外水和空气流动及传热传质,测试了圆管、椭圆管、扭曲管等三种水平管蒸发式冷凝器的流动与传热传质性能,结果表明,扭曲管间为有序的可控制水流,分布均匀,脱落速度快,更易形成柱状流,管表面水膜厚度比现有圆管和椭圆管小;传热传质系数随冷却水喷淋密度及风速的增大而增大,但冷却水喷淋密度增大至一定值后,对传热传质系数基本没有影响;扭曲管的传热传质系数高于椭圆管,特别是圆管,总结了扭曲管传热传质系数经验式. 相似文献
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本文在气固流动、煤粉燃烧和NO生成数学模型的基础上,对水泥回转窑内物料烧成过程的物理化学反应热效应采用分区段拟合的方法,建立了一套描述水泥回转窑窑内过程的数学模型。并对某3000吨/天生产能力的带四通道燃烧器的水泥回转窑进行了数值模拟,得到了回转窑内气体速度场、气体温度和组分浓度沿窑长的变化规律,对窑内NO生成进行了深入研究。研究结果表明:水泥回转窑内NO生成按机理可分为热力型NO和燃料型NO,由于窑内存在着高温、富氧环境,热力型NO为主要生成方式;热力型NO和燃料型NO生成过程存在着相互抑制作用。 相似文献
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Luis M. Gonzalez Joaquim J. B. Romero 《Particle & Particle Systems Characterization》2005,22(2):119-132
A new approach is proposed to model the bulk movement of solids in rotary drums operating at low rotation speeds, in slumping and rolling regimes. The model yields an equation similar to Saeman's equation, but which is valid also for the slumping regime and active area in the rolling regime. The model was developed for constant depth using a control surface containing the steepest descent direction, so that any contribution from sliding particles to flow rate can be neglected. By considering an appropriate virtual kiln, the model is extended to the more general, variable depth situation. 相似文献
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Of the various commercially successful processes for direct reduction of iron ore, rotary kiln processes have been found to be the most promising under the Indian context. Reduction of iron ore by coal in a rotary kiln takes place in two stages: (a) reduction of iron ore by carbon monoxide: Fe2O3+3CO=2Fe+3CO2; (b) gasification of carbon of coal by CO2:C+CO2=2CO. In the present paper, kinetic equations have been developed for reduction of iron oxide by carbon monoxide and gasification of coal char by carbon dioxide. These kinetic equations have been used to develop a mathematical model for reduction of iron ore with coal char in a rotary kiln. The model can predict the degree of reduction () with time (t) at a given temperature of solid (Ts) and the ratio of fixed carbon to total iron content in the charge (Cfix/Fe(T)) for reduction of iron ore with coal char of known reducibility and reactivity, respectively. The values of the degree of reduction predicted by the model have been compared with the results of the experiments conducted in a laboratory rotary kiln. 相似文献
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Sy-Chyi Lin James T. Richardson Dan Luss 《Physica C: Superconductivity and its Applications》1996,260(3-4):321-326
Continuous synthesis of YBa2Cu3O6+x superconductor was conducted in a rotary kiln. Dense pellets or loose powder of a stoichiometric mixture of copper, barium peroxide, and yttrium oxide were fed into a heated rotary kiln causing ignition on the whole outer surface followed by an inward movement of a combustion front. Following this thermal explosion, the pellet was post-treated (sintered) at 900 to 985°C as it moved along the kiln, and a product containing about 95 wt% YBa2Cu3O6+x was obtained. The impact of the thermal-explosion temperature, the post-treatment temperature, the pellet density, and the total residence time in the kiln on the product quality were studied. The best thermal-explosion temperature was found to be 800°C, the best post-treatment temperature was 985°C, and the total residence time in the kiln of 100 minutes was sufficient for the pellet to reach equilibrium. 相似文献
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本文对圆管内超临界状态下乙烷的湍流传热过程进行了数值模拟,分析了乙烷高温裂解对壁面热流密度、平均温度以及对流换热Nusselt数的影响。计算结果表明:考虑乙烷高温裂解吸热反应,管内平均温度会降低,出口处温度降低可达135 K;壁面热流密度则会显著增加,热出口处可增加近2倍;热裂解反应改善了超临界对流换热效果,Nusselt数可提高约20%。在本文计算条件下,经典的对流换热关系式可准确适用于不考虑热裂解反应的情况,而对于考虑裂解吸热反应的超临界乙烷传热情况则误差较大。 相似文献