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溶液模型
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  solution model
     HIGH ORDER SUB-REGULAR SOLUTION MODEL AND ITS APPLICATIONS IN THE CALCULATION OF COMPONENT ACTIVITIES OF MnO-SiO_2-Al_2O_3-CaO MOLTEN SLAG
     高阶亚正规溶液模型及其在MnO-SiO_2-Al_2O_3-CaO炉渣中组元活度的计算
短句来源
     Based on the regular solution model and the previous reports,an evalution of the Gibbs energy of formation of ζ phase (when the stoichiometric components as Mn 4N) was expressed as follows:ΔG 0 Mn 4N =-110850(±3000)+64.714(±2.2) T(J/mol).
     应用规则溶液模型和有关研究报道计算得到 ζ相 (计量组成为Mn4 N )的生成自由能 :ΔG0 Mn4 N =- 110 85 0 (±30 0 0 ) + 6 4.714 (± 2 .2 )T(J/mol) .
短句来源
     Based on the ideal association solution model, the thermodynamic propertiesfor Ag-Ln(Ln=La,Ce,Gd) systems from 1300 to 1600K have been calculated.
     本文利用理想缔合溶液模型,计算了1300—1600K温度范围内,Ag-Ln(Ln=La,Ce,Gd)三个二元系的热力学数据;
短句来源
     Using the geometric models (Kohler and Toop model), as well as general solution model (Chou model), the surface tensions of the Ni_3S_2FeSCu_2S ternary matte were calculated from those of the Ni_3S_2FeS、 FeSCu_2S、 Cu_2SNi_3S_2 pseudobinary systems.
     运用几何模型 (Kohler及Toop模型 )和通用溶液模型 (Chou模型 ) ,由Ni3S2 FeS、FeS Cu2 S和Cu2 S Ni3S2 三个二元边界体系的表面张力计算了Ni3S2 FeS Cu2 S三元系表面张力。
短句来源
     Associate model and substitute solution model were used to describe liguid and teminal solution phases respectively. As to the intermediate compounds Ni 5Zr and Ni 10 Zr 7, sublattice model (Ni) 1(Ni, Va) 4(Ni, Zr) 1 and (Ni, Zr) 10 Zr 7 were selected.
     液相用缔合物模型、端际固溶体用替换溶液模型描述,Ni5Zr和Ni10Zr7则分别选用了(Ni)1(Ni,Va)4(Ni,Zr)1和(Ni,Zr)10Zr7的亚点阵模型。
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  “溶液模型”译为未确定词的双语例句
     At first, liquidus compositions of In_(0.53) Ga_(0.47) As in the temperature region from650 to 700℃ are calculated using the regular model.
     首先用正规溶液模型,在650~700℃间计算了In_(0.53)Ga_(0.47)As的液相组分。
短句来源
     Based on the association solution theory, a temperature—dependent association model(TDAM) was established to describe the excess enthalpiesfor the alcohol—containing systems.
     在溶液活度系数模型的研究中,针对含醇缔合体系的特征,基于缔合溶液理论,导出了一个形式简单、物理意义明确的溶液模型——TDAM(Temperature-Dependent Association Model)。
短句来源
     2. The model of substitutional solution was used to optimize the phase diagram of the ZnO-Bi_2O_3 system, which proved the existence of the 24Bi_2O_3·ZnO compound and ZnO solid solution .
     2.由替换溶液模型优化和计算了ZnO-Bi_2O_3体系相图;
短句来源
     M s temperature,△ G γ→α ,△ G γ→M and mechanical energy have been calculated by means of Shu Zuyaos Fe-X-C model under the working condition of austenitic manganese steel.
     文章在Fe-X-C系规则溶液模型基础上,结合奥氏体锰钢的工况条件,计算了中锰钢和高锰钢在Ms温度和室温时的△Gγ→α,△Gγ→M及外界机械能。
短句来源
     Calculation of Liquidus Isotherms in the Ternary Ga—As—Ge System by the Use of a Quasi—regular Solution Approximation
     用准规则溶液模型计算Ga—As—Ge系液相等温线
短句来源
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  相似匹配句对
     S. models have been found.
     S.模型
短句来源
     model.
     模型
短句来源
     solution;
     溶液;
短句来源
     THERMODYNAMIC MODELS FOR ELECTROLYTE SOLUTIONS
     电解质溶液热力学性质模型
短句来源
     Molecular Thermodynamic Model for Electrolyte Solutions
     电解质溶液的分子热力学模型
短句来源
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  solution model
Regular solution model as applied to the interaction of halides in melt
      
Binary solid-liquid phase diagrams of halides with a common anion and a known mixing energy of the components in melt are analyzed by the regular solution model.
      
A thermodynamically complete equation of two-phase (γ, α) state of cerium was derived in terms of a pseudobinary solid-solution model developed by Aptekar' and Ponyatovskii.
      
The liquid phase, cubic (fluorite-type) zirconia solid solution and tetragonal zirconia solid solution are described by a regular solution model.
      
A thermodynamic analysis of the wetting phenomena in the two-component system, based on Becker's regular solution model for the surface tension of the interphase boundary, explains the minimum in the pw(T) dependence.
      
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In this paper,the activity coefficient of MnO in liquid blast-furnace-type slagshas been evaluated as a function of the basicity ratio,calculated according to a newformula previously proposed by the author,with reference to pure solid MnO as thestandard state.The data of Stukel and Cocubinsky,and Filer and Darken havebeen used as the basis of this calculation.The results of this paper together withthe α_(CaO) values evaluated in a previous paper are discussed from the standpoint ofionic nature of slags.

本文根据已有的热力学及分配数据算出了液态高炉型熔渣内MnO的活度系数与碱度间的关系如图3所示。计算结果显示碱度愈高,温度愈低,则MnO的活度系数亦愈大。如Темкин模型可以适用于液态CaO—MnO—SiO_2系统,则CaO与MnO的活度系数在一定碱度与温度的条件下应该相等(分别以液态CaO与MnO为标准状态),但作者的计算结果显示后者约为前者的4—5倍。这个差异表明Темкин的理想溶液模型不能適用于CaO—MnO—SiO_2系统,一个可能的解释是Ca~(++)与SiO_4~(4-)间组成了稳定的离子偶。

Two associated solution models, ASMA and ASMB were Presented in this paper. Both models can be applied not only to those solutions with both components exhibiting self-association, but also to partially miscible systems and alcohol aqueous solutions. Their applicability can be also extended to multicomponent systems. 13 binary isobaric VLE data (including partially miscible systems) were fitted by these two models. Their fitting accuracies were compared with those obtained by applying three local composition...

Two associated solution models, ASMA and ASMB were Presented in this paper. Both models can be applied not only to those solutions with both components exhibiting self-association, but also to partially miscible systems and alcohol aqueous solutions. Their applicability can be also extended to multicomponent systems. 13 binary isobaric VLE data (including partially miscible systems) were fitted by these two models. Their fitting accuracies were compared with those obtained by applying three local composition equations (wilson,FHW and UNIQUAC). It has been proved that ASMA model shows the highest fitting accuracy.

本文提出两种缔合溶液模型(Associated Solution Model).简称ASMA与ASMB,两者不但适用于各组分均有自我缔合的溶液(包括部分互溶系统及各种醇类水洁液),而且可推广应用于多元系统。 应用新模型来拟合十三套醇类溶液的恒压平衡数据(包括部分互溶系统),并与三种局部组成方程式(Wilson.FHW与UNIQUAC),的关联效果作了对比,证实ASMA的拟合精度最高.

The isobar ic vapor-liquid equilibrium data of thr ee binary systems (sec. Butanol-iso. Butanol, tert. Butanol-iso. Butanol and iso. Butanol-n. Butanol) were determined using the same equilibrium still as shown in our previous paper 16. Our experimental data (including those of three alcohol-alcohol systems and three alcohol aqueous solutions as reported in the previous paper) were fitted by applying the two associated solution models ASMA and ASMB. Then their accuracies were compared with those obtained by...

The isobar ic vapor-liquid equilibrium data of thr ee binary systems (sec. Butanol-iso. Butanol, tert. Butanol-iso. Butanol and iso. Butanol-n. Butanol) were determined using the same equilibrium still as shown in our previous paper 16. Our experimental data (including those of three alcohol-alcohol systems and three alcohol aqueous solutions as reported in the previous paper) were fitted by applying the two associated solution models ASMA and ASMB. Then their accuracies were compared with those obtained by using Wilson, FHW and UNIQUAC equation. It has been proved that for alcohol-alcohol systems the fitting accuracies of ASMA and ASMB models are generally higher than those of the local com position equations. For alcohol aqueous solutions, howerver, UNIQUAC equation shows the highest accuracy except the system of water-isopentanol.

本文采用前文(16)的汽淮平衡器测定仲丁醇-异丁醇,叔丁醇-异丁醇及异丁醇-正丁醇三组二元系统的恒压汽液平衡数据。 实验数据(包括前文侧定的三组醇类-醇类系统和三组醇类水溶液)应用两种缔含溶液模型ASMA和ASMB来关联。同时也与Wilson,FHW及UNIQUAC方程式的关联结果作了对比,证实:对醇类-醇类系统,ASMA与ASMB模型的拟合精度一般比局部组成方程稍高,对于醇类水溶液.除了水-异戊醇系统外,UNIQUAC的拟合精度最高。

 
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