西安交通大学热流科学与工程教育部重点实验室,西安,710049
网络首发:2020-02-10,
纸质出版:2020
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贾秀璨 1, 王建 2, 孙艳军 2, 等. 丙烷与POE润滑油气液相平衡的实验研究[J]. 西安交通大学学报, 2020,54(2):78-85+136.
Experimental Study on Vapor-Liquid Equilibrium of Propane and POE Lubricant Oil[J]. 2020, 54(2): 78-85+136.
贾秀璨 1, 王建 2, 孙艳军 2, 等. 丙烷与POE润滑油气液相平衡的实验研究[J]. 西安交通大学学报, 2020,54(2):78-85+136. DOI: 10.7652/xjtuxb202002010.
Experimental Study on Vapor-Liquid Equilibrium of Propane and POE Lubricant Oil[J]. 2020, 54(2): 78-85+136. DOI: 10.7652/xjtuxb202002010.
为了研究环保制冷剂丙烷(R290)与多元醇酯类(POE)润滑油的相平衡性质
通过气相色谱质谱方法对多元醇酯类润滑油POE22的组分和各组分所占的摩尔分数进行了分析
在此基础上使用等体积饱和法在278.15~348.15 K的温度范围内对R290在POE润滑油中的溶解度进行了测定
并采用活度系数NRTL模型对实验结果进行了关联。结果表明:POE22润滑油中主要含有4种酯类化合物和3种添加剂
这7种成分在润滑油中占比99.49%。由模型计算得到的R290与POE22二元混合物理论平衡压力值和实验平衡压力值的平均绝对偏差为0.565%
最大相对偏差为2.934%。此外
在温度范围278.15~348.15 K内未发现制冷剂R290与润滑油存在化学反应或不互溶的现象。将实验结果与文献中报道的R290在两种矿物油(ISO VG12和NM100P)中的溶解度进行了对比
发现POE油更适合R290。
The gas chromatography mass spectrometry method is used to analy-e the components and the share of each component in POE22 and to study the phase equilibrium properties of the environmental refrigerant propane(R290)and polyol ester(POE)lubricant. Then the isochoric saturation method is used to measure the solubilities of R290 in POE22 at 278.15 - 348.15 K
and the NRTL model is used to correlate the experiment results. The results show that POE22 is mainly composed of four ester compounds and three additives
and the seven components accounts for 99.49% in POE22. The absolute average deviation and the maximum relative deviation between the calculated theoretical pressure value and the experimental pressure value are 0.565% and 2.934%
respectively. Moreover
no chemical reaction or immiscibility phenomenon between R290 and oil are found in the temperature range from 278.15 to 348.15 K. Experimental results are compared with the reported solubility of R290 in two mineral oils(ISO VG12 a
熊爱凌, 韩厚德, 曹红奋. R290及其冷冻油混合物互溶特性研究 [J]. 上海海事大学学报, 2004(3): 66-70.
XIONG Ailing, HAN Houde, CAO Hongfen. Study on intersolubility of R290 and its refrigerated oil mixture [J]. Journal of Shanghai Maritime University, 2004(3): 66-70.
CHOUDHARI C S, SAPALI S N. Performance investigation of natural refrigerant R290 as a substitute to R22 in refrigeration systems [J]. Energy Procedia, 2017, 109: 346-352.
MOISES A, MARCELINO N, BARBOSA J R. Solubility, density and viscosity of mixtures of isobutane(R-600a)and a linear alkylbenzene lubricant oil [J]. Fluid Phase Equilibria, 2010, 292(1/2): 7-12.
LI Keqiao, CAI Dehua, LIU Yue, et al. Thermodynamic analysis of a novel exhaust heat-driven non-adiabatic ejection-absorption refrigeration cycle using R290/oil mixture [J]. Energy Conversion and Management, 2017, 149: 244-253.
GAO Yu, HE Guogeng, CHEN Peidong, et al. Energy and exergy analysis of an air-cooled waste heat-driven absorption refrigeration cycle using R290/oil as working fluid [J]. Energy, 2019, 173: 820-832.
FUKUTA M, YANAGISAWA T, IWATA H, et al. Performance of compression/absorption hybrid refrigeration cycle with propane/mineral oil combination [J]. International Journal of Refrigeration, 2002, 25(7): 907-915.
王晓坡, 孙艳军, 龚娜, 等. DME与POE基础油溶解度的实验与理论研究 [J]. 工程热物理学报, 2015, 36(5): 937-940.
WANG Xiaopo, SUN Yanjun, GONG Na, et al. Experimental and theoretical study on solubility of DME and POE basic oil [J]. Journal of Engineering Thermophysics, 2015, 36(5): 937-940.
WANG Xiaopo, SUN Yanjun, KANG Kai. Experimental investigation for the solubility of R1234ze(E)in pentaerythritol tetrahexanoate and pentaerythritol tetraoctanoate [J]. Fluid Phase Equilibria, 2015, 400: 38-42.
FU Yidong, HAN Lizhong, ZHU Mingshan. PVT properties, vapor pressures and critical parameters of HFC-32 [J]. Fluid Phase Equilibria, 1995, 111(2): 273-286.
ROSHANI G H, ROSHANI S, NAZEMI E, et al. Online measuring density of oil products in annular regime of gas-liquid two phase flows [J]. Measurement, 2018, 129: 296-301.
张笑云, 杨异. 3种常用润滑油密度与温度关系的研究 [J]. 物理通报, 2017, 36(12): 88-90.
ZHANG X Y, YANG Y. Study on the relation between density and temperature of three common lubricating oils [J]. Physics Bulletin, 2017, 36(12): 88-90.
HU Jiawen, WANG Rong, MAO Shide. Some useful expressions for deriving component fugacity coefficients from mixture fugacity coefficient [J]. Fluid Phase Equilibria, 2008, 268(1/2): 7-13.
YU Y, LI Y, HOSSAIN N, et al. Nonrandom two-liquid activity coefficient model for aqueous polyelectrolyte solutions [J]. Fluid Phase Equilibria, 2019, 497: 1-9.
FANG Lingyun, GAO Zanjun, WANG Xiaoyu, et al. Solubility and miscibility for the mixture of(ethyl fluoride+alkylbenzene oil)[J]. Journal of Chemical Engineering Data, 2014, 59(5): 1636-1642.
GIOVANNI D N, GIANLUCA C, MARIANO P, et al. A semi-empirical correlation for the estimation of the second virial coefficients of refrigerants [J]. International Journal of Refrigeration, 2016, 68: 242-251.
DONG Li, ZHENG Danxing, WU Xianghong. Working pair selection of compression and absorption hybrid cycles through predicting the activity coefficients of hydrofluorocarbon+ionic liquid systems by the UNIFAC model [J]. Industrial Engineering Chemistry Research, 2012, 51(12): 4741-4747.
RAZZOUK A, MOKBEL I, GARCíA J, et al. Vapor pressure measurements in the range 10-5 Pa to 1 Pa of four pentaerythritol esters: density and vapor-liquid equilibria modeling of ester lubricants [J]. Fluid Phase Equilibria, 2007, 260: 248-261.
SUN Yanjun, WANG Xiaopo, GONG Na, et al. Solubility of trans-1, 3, 3, 3-tetrafluoropropene(R1234ze(E))in pentaerythritol ester heptanoic acid(PEC7)and in pentaerythritol tetranonanoate(PEC9)between 283.15 K [J]. Fluid Phase Equilibria, 2015, 387: 154-159.
FANG Lingyun, GAO Zanjun, WANG, Xiaoyu. Solubility and Miscibility for the Mixture of(ethyl fluoride+alkylbenzene oil)[J]. Journal of Chemical Engineering Data, 2014, 59(5): 1636-1642.
SUN Yanjun, WANG Xiaopo, GONG Na, et al. Solubility of dimethyl ether in pentaerythritol tetrahexanoate(PEC6)and in pentaerythritol tetraoctanoate(PEC8)between(283.15 and 353.15)K [J]. Journal of Chemical Engineering Data, 2014, 59(11): 3791-3797.
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