摘要：提出了"双搅拌新型高效分离萃取槽"的新概念,即在澄清室增加搅拌装置,通过选择适当的搅拌条件,提高萃取过程水相与有机相的澄清分离速率,从而达到提高萃取设备效率的目的.设计了一套双搅拌萃取水模型实验装置,采用冷态模拟手段研究不同搅拌条件下搅拌离心场及重力场耦合作用对萃取槽澄清室中水油两相分离效果的影响,并结合实验数据,建立了实验范围内的开式45°涡轮桨的澄清度与搅拌转速、离底距离、搅拌桨距溢流口距离之间的准数方程.经实验验证,计算值与实验值吻合良好.

摘要：混合澄清槽是稀土生产过程中应用最广泛的萃取设备,其单级的澄清室与混合室体积比多在2.5∶1以上,造成生产过程中占地面积大、稀土存槽量大、夹带损失高等不利影响.为解决此问题,设计了一种新型混合澄清槽,在澄清室增加搅拌圆筒,创新性采用紫外可见光分光光度法考察不同条件下的水相夹带量以衡量其澄清性能,并与实际生产线测定结果对比.结果表明:适当的搅拌转速、离底高度和环盖尺寸等条件均有利于两相分离.环盖直径30 mm、离底高度13 cm及搅拌转速低于300 r/min时,所测水相夹带量均小于实际生产线夹带量的0.50%,满足实际生产要求.

摘要：Rare earth oxide was prepared via direct pyrolysis of rare earth chloride solution. Based on this technique, a new-type jet-flow pyrolysis reactor was designed, and then the fluid dynamics (pressure and velocity) inside the reactor was numerically simulated using a computational fluid dynamics method. The self-produced pressure (p) and the fuel inlet velocity (v) satisfied a quadratic function,p=0.06v2+0.23v?4.49. To fully utilize the combustion-generated heat in pyrolysis of rare earth chloride, an appropriate external pressure p=v2+3v?4.27 should be imposed at the feed inlet. The 1.25- and 1.5-fold increase of feed inlet diameter resulted in decline of adsorption dynamic pressure, but the intake of rare earth chloride increased by more than 30% and 60%, respectively. The fluid flow in the reactor was affected by the feeding rate; the fluid flow peaked near the throat of venturi and gradually smoothed down at the jet-flow reactor’s terminal along with the sharp decline of feeding rate.

摘要：设计了精炼铜-铬合金用低氟CaF2-CaO-Al2O3-MgO-SiO2五元渣系,并研究了其粘度、密度、表面张力及熔化温度等性能.结果表明,该渣系的熔化温度在1336～1402℃之间;高温下该渣系的密度和表面张力均随温度升高而减小,且随CaF2含量和MgO含量增加逐渐降低;增加CaF2添加量可降低渣系粘度;CaF2含量较低时,MgO含量增加也可降低渣系粘度,CaF2含量较高时,渣粘度在MgO含量为6%时最小,MgO含量续增加到9%时粘度反而上升.该渣系粘度较低,表面张力较小,具有良好的精炼效果.

摘要：针对“原位热解-热法还原炼镁”海绵钛清洁生产新工艺中镁、氯循环的关键步骤——气态MgCl2与O2的气相热解反应的反应器进行研究。设计了2种反应器模型,并采用物理模拟和数值模拟的方法研究反应器模型内的浓度场和速度场。物理模拟中,在N2与CO2流量比为6∶1时,CO2采用环向四口进气方式,此时气体混合不均匀度为0.02,混合程度最佳;数值模拟结果和物理模拟结果相吻合。

摘要：针对低品位铝土矿在工业中利用率不高、赤泥中高碱高铝等问题,提出了钙化-碳化法处理低品位铝土矿和赤泥的新方法.设计了文丘里式钙化渣碳化反应器,利用商用CFD软件ANSYS13.0/Fluent对该反应器中气液固三相流动进行了模拟计算.模拟和研究了表观气速等结构参数对钙化渣碳化反应器内速度场、气含率的影响,发现增大表观气速有利于促进气液间传质和反应,但气含率不宜过大.平均气含率的模拟值与实测值吻合良好,验证了所提方法的有效性.研究结果对钙化渣碳化反应器的设计及应用具有一定的参考价值.

摘要：The improved Intermig impeller has been used in the seed precipitation tank in China, which could enhance the mixing and suspension of Al(OH)3 particles and the power consumption declined largely. The flow field, solids hold-up, cloud height, just off-bottom speed and power consumptions were investigated in solid-liquid mixing system with this new type of impeller by CFD and water experiment methods. Compared with the standard Intermig impeller, the improved one coupled with specially sloped baffles could promote the fluid circulation, create better solids suspension and consume less power. Besides lower impeller off-bottom clearance is good for solid suspension and distribution. The just-off-bottom speed was also determined by a power number criterion. Meanwhile, the predicted results were in good agreement with the experimental data.

摘要：基于海绵钛生产工艺过程中副产物氯化镁的综合利用问题,提出以钛冶炼过程中蒸馏工序段熔融氯化镁为原料,在通氧条件下,熔融态氯化镁直接热解,产物为高附加值的氧化镁和氯气.本文针对气相反应,设计主反应器文丘里管的形状与尺寸、盛装容器的形状与尺寸、电阻炉的选取及收集装置的选取与其尺寸.

摘要：利用商业CFD软件Fluent12.0和并行计算系统图形工作站,对改进的Intermig桨种分槽内部流场进行了三维数值解析.采用Realizablekε湍流模型和欧拉欧拉多相流模型对槽内不同桨叶离底距离C、桨叶直径D下的氢氧化铝颗粒悬浮规律以及搅拌桨功率消耗进行了模拟.结果显示,搅拌转速一定的条件下,桨叶直径越大,越有利于颗粒悬浮,搅拌功率越大;相对最佳桨径与槽径比为0.6;过高和过低的桨叶离底距离都不利于氢氧化铝颗粒悬浮,桨叶离底距离对功率影响较小,相对最佳离底距离与桨径比为0.55.

摘要：为了研究改进的Intermig桨的搅拌性能,在无挡板的氧化铝种分搅拌槽内,采用PC6D颗粒浓度测量仪对水-玻璃珠液-固体系在不同条件下的颗粒轴向和径向局部浓度进行了测量与分析.结果表明,较高的搅拌转速和体系粘度更有利于固体颗粒的悬浮.粘度μ=3.50×10-3Pa·s、转速n=172r/min时,实验浓度平均值是理论浓度平均值的1.011倍,可见该条件下实验浓度值与理论浓度值更接近,混合更均匀.