首页> 外文OA文献 >I. An apparatus for the measurement of liquid diffusion coefficients. II. Supersaturation in hydrocarbon systems. 1. N-pentane in the liquid phase. 2. Statistical procedures for supersaturation data. III. Volumetric and phase behavior of hydrocarbon systems. 1. Hydrogen-n-hexane. 2. n-Heptane
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I. An apparatus for the measurement of liquid diffusion coefficients. II. Supersaturation in hydrocarbon systems. 1. N-pentane in the liquid phase. 2. Statistical procedures for supersaturation data. III. Volumetric and phase behavior of hydrocarbon systems. 1. Hydrogen-n-hexane. 2. n-Heptane

机译:I.一种用于测量液体扩散系数的装置。 II。烃系统中的过饱和。 1.液相中的正戊烷。 2.过饱和数据的统计程序。 III。烃系统的体积和相行为。 1.氢正己烷。 2.正庚烷

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摘要

I. An apparatus was constructed for the measurement of Fick diffusion coefficients in the liquid phase under steady state conditions at pressures up to 10,000 psi. and at temperatures from 40 to 460[degrees]F. The apparatus consists of a device for the feed of a gas at an accurately known rate, a diffusion cell, and a device identical to the feed equipment for the withdrawal of a gas. The details of construction are given and a tentative method of operation is discussed.II. 1. A limited number of measurements were made of the effect of the degree of supersaturation on the rate of bubble formation as shown by the time for the first bubble to form in liquid n-pentane. Data were taken at 160[degrees] and 280[degrees]F. in an isochoric cell and at 160[degrees]F. in an isobaric apparatus which is described. The results show that for a given degree of supersaturation the times of bubble formation are widely distributed and must be considered statistically.II. 2. A procedure for the treatment of supersaturation data is discussed which includes a derivation of a theoretical distribution function for the times of formation of the first bubbles, a regression analysis based on an elementary hypothesis for the dependence of the rate of bubble formation on the degree of supersaturation, and a study of several pertinent confidence intervals.III. 1. The volumetric behavior of four mixtures of different composition in the binary system hydrogen-n-hexane was investigated at pressures up to 10,000 pounds per square inch for eight temperatures in the interval between 40 and 460[degrees]F. The composition of coexisting phases in the heterogeneous region was determined at seven temperatures from 40 to 400[degrees]F. and at pressures up to 10,000 pounds per square inch. The results are presented in tabular and graphical form.III. 2. Prior work on n-heptane by other investigators was extended as a preliminary to the study of the binary system methane-n-heptane. The molal volume of n-heptane is reported in tabular and graphical form as a function of pressure up to 10,000 pounds per square inch at eight temperatures covering the range from 40 to 460[degrees]F.
机译:I.构造用于在高达10,000psi的压力下在稳态条件下测量液相中的菲克扩散系数的设备。温度为40至460°F。该装置包括用于以精确已知的速率供给气体的装置,扩散池以及与用于排出气体的供给装置相同的装置。给出了详细的构造,并讨论了尝试的操作方法。对过饱和度对气泡形成速率的影响进行了有限的测量,如第一个气泡在液态正戊烷中形成的时间所示。数据是在160°F和280°F下获取的。在等渗细胞中,温度为160°F。在所描述的等压设备中。结果表明,对于给定的过饱和度,气泡形成的时间分布广泛,必须进行统计学处理。 2.讨论了处理过饱和数据的程序,其中包括推导形成第一个气泡的时间的理论分布函数,基于基本假设的回归分析,该假设基于气泡的形成速率对气泡的依赖性。过饱和度和几个相关置信区间的研究。 1.研究了八种温度在40至460°F之间的温度下,在最高10,000磅/平方英寸的压力下,二元体系氢-正己烷中四种不同组成的混合物的体积行为。在40到400°F的七个温度下确定了异质区域中共存相的组成。压力高达每平方英寸10,000磅结果以表格和图形形式呈现。 2.其他研究者先前对正庚烷的研究被扩展为对甲烷-正庚烷二元系统的研究的基础。以表格和图表形式报告正庚烷的摩尔体积,它是在40至460°F的八个温度下高达10,000磅/平方英寸的压力的函数。

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    Nichols William Burt;

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  • 年度 1957
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