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The dynamic equilibrium data of methyl acetate on Calgon AC could be correlated by Freundlich equation. 由动态吸附数据计算得到的醋酸甲酯的平衡数据，用Freundlich方程进行了关联。
Possibilities of MAZ are analyzed and the equilibrium data and heat data are given. 对甲烷芳烃化(MAZ)的可能性进行分析,并给出了该反应的平衡数据和热数据。
The Liquid Liquid equilibrium data of octane water and octane phosphoric acid water system were measured. 实验测定了不同温度下辛烷水二元体系和辛烷磷酸水三元体系的液液相平衡数据。
And the ideal solution model and a empirical equation were applied to correlate the solid-liquid equilibrium data. 氯化钠溶液中的溶解度,并对实验数据分别采用理想溶液模型和经验方程进行了关联。
J. Gmehling et al., Vapor-Liquid Equilibrium Data Collection, DECHEMA, Frankfurt/Main, 1993. 不知道谁手头有或见过这份资料？可否上传？谢谢！
Next, the physical properties and vapour liquid equilibrium data must be collected, and finally the type of absorber is chosen and designed. 其次，必须收集物理性质和汽一液平衡数据，最后才是选择和设计吸收器。
The phase equilibrium data for CO_2-C_2H_5OH-H_2O-entrainer (ethylene glycol and glycerol) systems at 313. 2K and 10. 1MPa were measured. 测定了313.;2K、10MPa下，CO_2－C_2H_5OH－H_2O－夹带剂（乙二醇或丙三醇）体系的相平衡数据。
The solid-liquid equilibrium data were fitted by Ott's equation and the temperature square deviations were not greater than 0.8 K. 采用Ott方程对固液平衡数据进行关联;温度标准偏差不大于 0.;8K;
The adsorption equilibrium data were fitted with Langmuir equation well.(According) to the adsorption equilibrium data,the model parameters were ob... 这些结果为吸附过程处理含锌废水的设计提供一定的参考。
Isothermal vapor liquid equilibrium data of two binary systems carbon dioxide etanol and carbon dioxide iso propanol at 303. 应用汽液双循环高压相平衡装置，测定了二氧化碳-乙醇和二氧化碳-异丙醇二元混合物分别在303。
In addition, the ternary vapor liquid equilibrium data for the above three components were also determined at 308.65K under the pressures 3.04, 4.02, and 5.00 MPa respectively. 同时还测定了以上3个组分在308.;65K、压力在3
The necessary parameters for simulation calculation were estimated and regressed on the basis of equilibrium data of monocomponent n-paraffins on 5A molecular sieve. 模拟计算所需参数采用估算和回归的方法,通过经验公式估算传质系数,利用单组分正构烷烃在5A分子筛上的吸附平衡数据,直接得到竞争吸附平衡模型参数。
The isobaric vapor-liquid equilibrium data of ethyl 3-hydroxybutyrate-ethyl crotonate-ethanol system and of the related three binary systems were determined at 101. 在汽液双循环玻璃平衡釜中测定3-羟基丁酸乙酯、巴豆酸乙酯、乙醇的二元及三元体系的等压汽液平衡数据,用积分法对其进行了热力学一致性检验。
The solid-liquid equilibrium data for the ternary mixture of o-dibromobenzene + m-dibromobenzene + p-dibromobenzene were determined by differential scanning calorimetry (DSC). 采用差示扫描量热法,通过对一系列“拟二元”物系固液平衡数据的测定,得到了邻二溴苯、间二溴苯和对二溴苯三元物系的固液平衡数据。
Little standard error proved that PR and R-K-S EOS were suitable to regress gas-liquid phase equilibrium data of methyl chloride-n-hexane binary system.PR is superior to R-K-S. 其次，利用Peng-Robinson和Redlich-Kwong-Soave状态方程对一氯甲烷-正己烷气液相平衡数据进行了模拟，计算出了标准误差，证明了Peng-Robinson和Redlich-Kwong-Soave状态方程在拟合一氯甲烷-正己烷二元体系气液相平衡方面是可靠的，且Peng-Robinson状态方程要优于Redlich-Kwong-Soave状态方程。
Vapor-liquid equilibrium data of ethyl acetate-isopropyl ether and ethyl acetate-tetrahydrofuran binary systems were measured at atmospheric pressure(101. 下,用汽液平衡釜测定了乙酸乙酯-异丙醚和乙酸乙酯-四氢呋喃二组分物系的汽液平衡数据。
The atmospheric vapor-liquid equilibrium data of the binary systems cyclohexanol-cyclohexanone,cyclohexanone-diglycol and cyclohexanol-diglycol were measured with a ROSE cell. 用ROSE平衡釜测定了环己醇(1)-环己酮(2)、环己酮(1)-二甘醇(2)、环己醇(1)-二甘醇(2)3对二元系常压下的汽液相平衡数据,并对其进行了热力学一致性检验。
A supereritical fluid extraction process is being investigated for this purpose, A flow apparatus is described for measuring phase equilibrium data for mixtures of solvent and pitch at temperatures up to 675K and pressures to 350 bar. 为此目的,我们正在研究超临界流体萃取工艺。本文所描述的测定溶剂和沥青混合物的相平衡数据的流体装置,能在沥青和溶剂混合后,加热直到675K和350巴的压力条件下测得相平衡数据。
This paper correlates the Vapor-liguid equilibrium data for the systems of i-propyl alcohol(1)-Cyclohexane (2). Methcanol (1)-water(2) and Ethand (1)-water (2) on the base of experiment with the Wilson equation. The results are veny good. 本文在实验的基础上，用威尔逊方程对异丙醇（1）一环已烷（2）、甲醇（1）一水（2）和乙醇（1）一水（2）体系的气液平衡数据进行关联和预测，计算结果和实验数据符合良好。
This pair of scales is not in equilibrium. 这个天平不平衡。