首页> 外文期刊>Journal of Molecular Liquids >Experimental study of the one-, two-, and three-phase isochoric heat capacities of n-hexane + water mixtures near the lower critical line. Part I. Experimental results
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Experimental study of the one-, two-, and three-phase isochoric heat capacities of n-hexane + water mixtures near the lower critical line. Part I. Experimental results

机译:下临界线附近正己烷+水混合物的一相,两相和三相等容热容的实验研究。第一部分实验结果

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The one-, two-, and three-phase isochoric heat capacities (C _(VX)) of n-hexane + water mixtures near the lower critical line, including UCEP, have been measured with a high-temperature and high-pressure nearly constant-volume adiabatic calorimeter. The measurements were made in the temperature range from 443 K to 501 K for 8 liquid and vapor isochores from 121.07 kg m ~(- 3) to 377.5 kg m ~(- 3). The isochoric heat capacity jump (quasi-static thermograms supplemented by the sensor of adiabatic control) technique has been used to accurately measure the liquid-liquid-vapor (L-L-V) and liquid-vapor (L-V) phase transition parameters (T _S, ρ _S). The expanded uncertainty of the heat-capacity measurements at 95% confidence level with a coverage factor of k = 2 is estimated to be 0.06% for density (ρ), 15 mK for temperature (T), and 2% to 3% for isochoric heat capacity (C _V). The liquid-gas critical temperatures,T _C(x), and the critical densities,ρ _C(x) (lower critical lines) for binary n-hexane + water mixtures were determined from the measured saturated properties (C _(VS),T _S, ρ _S) near the critical point. The temperature, density, and the pressure at the UCEP (T _(UCEP) = 496.13 ± 0.2 K, P _(UCEP) = 5.220 ± 0.10 MPa, ρ _(UCEP) = 263.92 ± 2 kg m ~(- 3)) were extracted from the measured critical line and three-phase experimental data. For the first time we reported the temperature dependent behavior of C VX near UCEP.
机译:在包括UCEP在内的较低临界线附近,正己烷+水混合物的一相,两相和三相等速热容(C _(VX))已在高温和高压下进行了测量。等体积绝热量热仪。在443 K至501 K的温度范围内对121.07 kg m〜(-3)至377.5 kg m〜(-3)的8个液体和蒸气等压线进行了测量。等容热容量跃迁(通过绝热控制传感器补充准静态热谱图)技术已用于精确测量液-液-汽(LLV)和液-汽(LV)相变参数(T _S,ρ_S )。在覆盖系数k = 2的95%置信水平下,热容量测量的扩展不确定性估计为:密度(ρ)为0.06%,温度(T)为15 mK,等渗为2%至3%热容(C _V)。由测量的饱和特性(C _(VS),)确定二元正己烷+水混合物的液化气临界温度T _C(x)和临界密度ρ_C(x)(下临界线)。 T _S,ρ_S)接近临界点。 UCEP处的温度,密度和压力(T _(UCEP)= 496.13±0.2 K,P _(UCEP)= 5.220±0.10 MPa,ρ_(UCEP)= 263.92±2 kg m〜(-3) )是从实测临界线和三相实验数据中提取的。我们首次报告了UCEP附近C VX的温度依赖性行为。

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