Study on the Evaporation Kinetics of Zinc and Lead in Zn-Pb-Bearing Dust Pellets Mixed with Coal Powder

The study on the evaporation kinetics of zinc and lead in the pellets made of ZnPbbearing dust mixed with carbon ,in nitrogen atmosphere at the temperature range between 1 100 and 1 300 , shows that the reduction temperature has a significant effect on the evaporation rates of zinc and lead and that both the particle size of coal powder and the extra carbon content have no effect on the evaporation rates . The obtained activation energies for the evaporation of zinc and lead are 7942 kJ/mol and 8874kJ/mol respectively. The evaporation rate of zinc is controlled by the reaction between zinc oxide and CO while that of lead is controlled by lead volatilization and the diffusion of gaseous lead through gas boundary layer covering the surface of liquid lead.

Kinetics of Evaporation of Zn and Pb from Carbon-bearing Pellets Made of Dust Containing Zn-Pb-Fe Oxides

The influence of reduction temperature, size of coal powder and the carbon content on the evaporation rates of Zn and Pb in pellets made of ZnO-PbO-FeO bearing dust has been investigated between 1100-1300℃. The evaporation rate of Zn and Pb obtained from the experiments has been analyzed with kinetic models. The results show that the control step for evaporation of Zn is reduction reaction of ZnO by CO at the interface，and that the evaporation rate of Pb is controlled by the volatilization of reduction products, i.e. liquid lead. The overall apparent activation energies of Zn and Pb evaporation from the pellet are 79.42kJ/mol and 88.74kJ/mol respectively.

EVAPORATION KINETICS OF SnS FROM SnS-Cu_2S-FeS MELTS

The evaporation kinetics of SnS from SnSCu2SFeS teruary system was investigated against matte grade, tetnperature and carrier gas flow rate. It was demonstrated that the evapomtion process is controlled by gas-phase mass transport. The increases of the flow rote of carrier gas and the temperature could increase the gas-phase mass transport coefficient and the Partial pressure of SnS over the melts, respectively, and hence would appreciably promote the evaporation process. An increase of matte grade could lower the activitv coefficient of SnS in the melts, which in turn would cause the reduction of the evapomtion rate of SnS

Evaporation Kinetics of SnS from SnS-Cu_2S Melts

The kinetics of SnS evaporation from SnS-Cu2S melts was investigated by a unique experimental method. It is shown that the process is controlled by the mass transport of SnS in gas phase. The evaporation rate of SnS is significantly enhanced by increasing tempeature and carrier gas flow rate. The apparent activation energy for the process is found to be 204.67 kJ. The evaporation rate for the present system is much smaller than that for SnS-FeS system.

Rebuilding the theory of isotope fractionation for evaporation of silicate melts under vacuum condition

Isotope eff ects are pivotal in understanding silicate melt evaporation and planetary accretion processes.Based on the Hertz-Knudsen equation,the current theory often fails to predict observed isotope fractionations of laboratory experiments due to its oversimplified assumptions.Here,we point out that the Hertz-Knudsen-equation-based theory is incomplete for silicate melt evaporation cases and can only be used for situations where the vaporized species is identical to the one in the melt.We propose a new model designed for silicate melt evaporation under vacuum.Our model considers multiple steps including mass transfer,chemical reaction,and nucleation.Our derivations reveal a kinetic isotopic fractionation factor(KIFF orα)αour model=[m(^(1)species)/m(^(2)species)]^(0.5),where m(species)is the mass of the reactant of reaction/nucleation-limiting step or species of diffusion-limiting step and superscript 1 and 2 represent light and heavy isotopes,respectively.This model can eff ectively reproduce most reported KIFFs of laboratory experiments for various elements,i.e.,Mg,Si,K,Rb,Fe,Ca,and Ti.And,the KIFF-mixing model referring that an overall rate of evaporation can be determined by two steps jointly can account for the eff ects of low P_(H2)pressure,composition,and temperature.In addition,we find that chemical reactions,diffusion,and nucleation can control the overall rate of evaporation of silicate melts by using the fitting slope in ln(−ln f)versus ln(t).Notably,our model allows for the theoretical calculations of parameters like activation energy(E_(a)),providing a novel approach to studying compositional and environmental eff ects on evaporation processes,and shedding light on the formation and evolution of the proto-solar and Earth-Moon systems.

Fluoride evaporation and crystallization behavior of CaF_2–CaO–Al_2O_3–(TiO_2) slag for electroslag remelting of Ti-containing steels

To elucidate the behavior of slag films in an electroslag remelting process, the fluoride evaporation and crystallization of CaF2–CaO–Al2O3–（TiO2） slags were studied using the single hot thermocouple technique. The crystallization mechanism of TiO2-bearing slag was identified based on kinetic analysis. The fluoride evaporation and incubation time of crystallization in TiO2-free slag are found to considerably decrease with decreasing isothermal temperature down to 1503 K. Fish-bone and flower-like CaO crystals precipitate in TiO2-free slag melt, which is accompanied by CaF2 evaporation from slag melt above 1503 K. Below 1503 K, only near-spherical CaF2 crystals form with an incubation time of less than 1 s, and the crystallization is completed within 1 s. The addition of 8.1wt% TiO2 largely prevents the fluoride evaporation from slag melt and promotes the slag crystallization. TiO2 addition leads to the precipitation of needle-like perovskite（CaTiO3） crystals instead of CaO crystals in the slag. The crystallization of perovskite（CaTiO3） occurs by bulk nucleation and diffusion-controlled one-dimensional growth.

Solid-phase Decarburization Kinetics of High-carbon Ferromanganese Powders by Microwave Heating

Solid-phase decarburization of high-carbon ferromanganese powders （HCFPs） was conducted using calcium carbonate powders （CCPs） as a decarburizer by microwave heating. Solid-phase decarburization kinelSics was investi- gated by isothermal method. The results show that the HCFPs show excellent microwave absorption at a higher av- erage heating rate of 80 ℃/min, while CCPs exhibit poor microwave absorption at a lower heating rate of 5--20 ℃/min; the heating characteristics are in-between when HCFPs and CCPs are mixed. The average heating rates of the mix- ture are 32.14, 31.25, 31.43, and 30.77 ℃/rain when the mixture is heated up to 900, 1000, 1100, and 1200 ℃, respectively. The good microwave absorption property of the mixed material lays the foundation for the solid-phase decarburization of HCFPs containing CCPs. Solid-phase decarburization of HCFPs containing CCPs is a first-order reaction by microwave heating. Apparent activation energy of solid-phase decarburization is 55.07 kJ/mol, which is far less than that of ordinary carbon gasification reaction and that of solid-phase decarburization under the same de- carburization condition by conventional heating. It indicates that microwave heating not only produces thermal effect, but also has non-thermal effect.

Numerical simulation of metal evaporation based on the kinetic model equation and the direct simulation Monte Carlo method

Metal evaporation on the basis of the kinetic model equations(BGK and S-model) and the direct simulation Monte Carlo(DSMC) method was investigated computationally under the circumstances of collimators existing or not. Numerical data of distributions of number density, bulk velocity and temperature were reported over a wide range of evaporation rate.It was shown that these results reached a good agreement for the case of small evaporation rate, while the deviations became increasingly obvious with the increase of evaporation rate, especially when the collimators existed. Moreover, the deposition thickness over substrate obtained from the kinetic model equations were inaccurate even though the evaporation rate was small. All of the comparisons showed the reliability of the kinetic model equations, which require less computational cost at small evaporation rate and simple structure.

Modeling and simulation of urea-water-solution droplet evaporation and thermolysis processes for SCR systems

A reliable mathematical model of urea-water-solution(UWS) droplet evaporation and thermolysis is developed.The well known Abramzon–Sirignano evaporation model is corrected by introducing an adjustment coefficient considering the different evaporation behaviors of UWS droplet at different ambient temperatures. A semidetailed kinetic scheme of urea thermolysis is developed based on Ebrahimian's work. Sequentially, the evaporation characteristics, decomposition efficiency of a single UWS droplet and deposit formation are simulated. As a result, the relation of evaporation time, relative velocity, exhaust temperature and droplet initial diameter is presented. Synchronously, it indicates that temperature is the decisive factor for urea thermolysis. Different temperatures result in different deposit components, and deposit yield is significantly influenced by temperature and decomposition time. The current work can provide guidance for designing urea injection strategy of SCR systems.

Kinetics of Al Evaporation from Liquid U-Al Alloys in Vacuum Induction Melting

A research on kinetics of Al evaporation from liquid U—Al alloys was made in a vacuum induction melting（VIM） furnace at 1673—1843 K.The evaporation rate of Al was found to be first order with respect to Al content in the melt.The overall mass transfer coefficient of Al was determined and it was found that the evaporation rate of Al increased with increasing temperatures.The apparent activation energy of Al evaporation at 1673-1843 K was 171.5 kJ mol-1.The value of mass transfer coefficient of Al in the liquid phase was estimated to be 3.77 × 10-6,7.41×10-6,and 9.40 × 10-6m s-1at 1673,1753,and 1843 K,respectively.Meanwhile,rate determining steps were discussed and it was concluded that the evaporation rate of Al is mainly controlled by liquid phase mass transfer.

Changes in color and rheological behavior of pineapple concentrate through various evaporation methods

The objective of this study was to investigate the effect of various concentration methods namely microwave vacuum evaporation(MVE),microwave heating evaporation(MHE),and rotary vacuum evaporation(RVE)on the concentrate change,the kinetic of color degradation,and the rheological behavior of pineapple juice.The concentrated behavior of pineapple juice from the experimental data of concentration rate was fitted with three types of exponential models for evaluating a suitable prediction.The four-parameter exponential model was found to agreeably explain the concentrated change of pineapple juice during each concentration methods.The Kinetics of color change during concentration processes was evaluated.The color changing from three different evaporations was measured by lightness values(L*),redness values(a*)and yellowness(b*)values,total color difference(TCD)and brown pigment formation index(A420).The result indicated that the change in Hunter parameters,L*and b*,fitted well with the first-order kinetic model while a*,TCD,and Browning index followed the zero-order kinetic model.The observed apparent viscosities(μa)of pineapple concentrate at 55-85℃through the three different evaporation methods were also measured.In relation to temperature and shear rate,the viscosity decreased as these two parameters increased,for all concentrated pineapple juice.On comparing the values ofμa of pineapple concentrate from different concentration methods,pineapple concentrate from MHE has higher values than those from MVE and RVE.The Duncan test,applied to the experimental results,indicates no significant difference in theμa of pineapple juice concentrate by MVE and by RVE.

钢液真空处理过程中Mn挥发动力学研究

Mn作为提高钢材强度的主要元素之一,在钢液真空处理过程中的挥发会对钢材成分及质量控制产生不利影响,因此,明确钢液中Mn的挥发机理,并据此精确调控钢液中Mn含量,对于保证钢材质量显得尤为重要。本研究针对X80管线钢的真空精炼处理过程,分析了气相压强和熔炼温度对钢液中Mn挥发行为的影响。结果表明:随着熔炼温度的升高和气相压强的降低,钢液中Mn挥发速率明显加快;在熔炼温度1903 K、气相压强19 Pa、处理时间40 min条件下,Mn挥发率高达92.26%。在熔炼温度1823~1973 K、气相压强19~670 Pa条件下,Mn挥发遵循一级反应规律,其表观挥发速率常数在(0.41~26.56)×10^(-5)m/s范围内;在气相压强19~670 Pa、熔炼温度1903 K的条件下,Mn挥发主要受气相传质的限制;在气相压强226 Pa、熔炼温度1823~1973 K的条件下,Mn挥发的表观活化能达到120.20 kJ/mol,限制性环节为气-液界面反应;本研究条件下,液相传质对Mn挥发速率的影响较小。

脱硫废液中硫酸钙的结晶机制及动力学研究

脱硫废液中硫酸钙结晶的大小和晶习差异将直接导致其易积垢于热交换面且难以处理,结晶状况对生产工艺、设备配置和过程的经济性均会产生影响,因此硫酸钙的结晶机制及相应的硫酸钙结晶动力学研究可为该脱硫废液的减量化处理和工程设计提供技术支持。通过对脱硫废液的水质特征分析、沉淀和蒸发结晶,采用显微镜、SEM-EDS及XRD等分析手段,解析结晶产物的微观特征,并研究硫酸钙的结晶机制和结晶动力学行为。结果表明,脱硫废液pH值的不同可导致不同金属离子的沉淀,废液中的重金属离子随着碱度的提高先行沉淀析出,然后废液中的镁离子主要以氢氧化镁的形态沉淀。蒸发结晶过程中废液中的氯离子等杂质存在则影响硫酸钙晶体的结晶和规整度,较高浓度的氯离子优先以氯化物结晶体析出。硫酸钙的结晶过程为晶体成核、晶体生长、晶簇团聚及晶粒成长的渐进历程,由于废液中的杂质可能成为晶核,致使硫酸钙结晶的速率更快,但其变化规律与纯硫酸钙的结晶一致。脱硫废液中硫酸钙晶体的成核速率在很大程度上取决于溶液的过饱和度,钙离子过饱和度越大则结晶速度越快。蒸发过程中硫酸钙晶体生长过程可拟合为1.38级反应过程,反应速率常数为34.62,结晶反应速率方程为r=34.62 C 1.38。

稳定性氢氧同位素在水体蒸发中的研究进展

介绍了同位素分馏的基本概念以及利用稳定同位素研究水体蒸发的基本原理。综述了国内外对水体蒸发中稳定同位素分馏机制的研究,分析了温度、湿度等气象因子对蒸发同位素分馏的影响,对动力分馏模型进行了详细推导,概述了利用同位素估算蒸发量的方法。指出了国内这方面研究的不足,并展望了今后的研究趋势。

含砷铜烟尘砷的选择性分离实验

在氮气气氛下,采用低温焙烧的方法对含砷铜烟尘中的砷进行选择性分离,研究了温度、氮气流量和焙烧时间的变化对砷挥发率的影响,用X射线衍射分析、差热-差重分析等方法研究了含砷铜烟尘中砷的挥发规律,并分析了砷挥发过程的动力学。结果表明,含砷铜烟尘中砷的选择性分离应在低温下进行,避免高温下Zn、Pb挥发损失和As_2O_3生成难挥发的砷酸盐。在250℃,氮气流量300mL/min、焙烧120min的条件下,砷的挥发率为95.68%,渣中砷的含量为0.79%,其他有价金属基本不挥发,实现了砷与其他有价金属的选择性分离,砷以初级As_2O_3产品回收,纯度为96.85%。动力学研究表明,在一定范围内,砷的低温选择性挥发过程符合收缩核模型,其表观活化能为19.71kJ/mol,该过程受内扩散控制。

食品液体(南瓜汁)蒸发浓缩过程动力学研究

本文对蒸发浓缩过程营养损失动力学进行了研究,建立了汽一液一固三相循环流化床蒸发器蒸发浓缩南瓜汁时胡萝卜素损失的动力学模型。实验结果表明:模型预测值与实验值吻合良好,该模型对工业生产有一定的应用价值。

苄青霉素盐结晶过程

本文研究了β-内酰胺类抗菌素药物真空闪蒸结晶过程．以苄青霉素钾盐为例，测定了该物系的结晶热力学相图与介稳区曲线，应用间歇动态法确定了该物系的结晶动力学参数，进而求取了最佳操作时间表.

熔融锰铁高温挥发的实验研究

应用高温密闭电阻,在还原气氛中,通过高温熔融试验,对液态锰铁的高温挥发进行了初步研究。熔融锰铁的温度愈高,平衡蒸气压愈大,挥发速度愈快。熔体中锰的扩散速度是挥发过程的限制性环节。金属锰在锰铁熔体中的扩散动力学方程可近似表达为:C=Cb+（Ci-1-Cb）erf[x/],式中,1733K时,D=2.0×10-5;1793K时,D=3.5×10-5。

蒸发过程中水体稳定同位素富集与空气湿度的关系

通过同位素分馏模型的物理意义分析及实验模拟分析,探讨空气湿度对蒸发过程水体稳定同位素富集过程的影响机理,研究认为:1空气相对湿度决定了扩散系数和自由空气同位素组成对分馏系数的影响比例,空气相对湿度越小,分馏系数受扩散分馏系数影响越大,分馏系数受自由空气水汽同位素组成影响则越小,反之亦然;2空气相对湿度与蒸发残余水体氢氧稳定同位素富集程度具有负相关性,即空气湿度越大越不利于残余水体重同位素富集;3模拟残余水体同位素丰度对空气相对湿度的敏感性呈负指数关系。在无外界气态水介入的蒸发实验中,残余系数为0.194条件下,当相对湿度小于80%时,H、O稳定同位素模拟结果对湿度的敏感性均小于0.0002,即相对湿度变化对模拟残余水体同位素丰度影响很小;当湿度大于80%时,湿度变化对模拟结果的影响呈指数关系急剧增加,湿度大于80%的蒸发实验需要准确观测相对湿度值。

活性炭吸附汽油蒸气动力学性能测定

在蒸发油气吸附回收处理技术中,将活性炭作为首选吸附剂,重点考察研究其吸附汽油蒸气动力学性能。试验结果表明,活性炭的饱和吸附率随吸附操作温度增大而降低,新鲜活性炭在20C时的饱和吸附率高达34％,30C时为30％,活性炭吸附存在劣化度,再生难彻底,影响其使用寿命。活性炭吸附油气速度较快,不同活性炭的吸附饱利和时间略有差别,一般在40min内已经达到或基本接近饱和活性炭吸附塔压降很小,总平均为0.142Pa