CIESC Journal ›› 2019, Vol. 70 ›› Issue (9): 3248-3255.DOI: 10.11949/0438-1157.20190354
• Thermodynamics • Previous Articles Next Articles
Yubo CHEN(),Zhao YANG(),Rui ZHAI,Biao FENG,Zijian LYU,Wenzhong ZHAO,Yingying GE
Received:
2019-04-04
Revised:
2019-06-24
Online:
2019-09-05
Published:
2019-09-05
Contact:
Zhao YANG
通讯作者:
杨昭
作者简介:
陈裕博(1995—),男,硕士研究生,基金资助:
CLC Number:
Yubo CHEN, Zhao YANG, Rui ZHAI, Biao FENG, Zijian LYU, Wenzhong ZHAO, Yingying GE. Miscibility measurement and evaluation method of R290/R1234yfwith mineral oil[J]. CIESC Journal, 2019, 70(9): 3248-3255.
陈裕博, 杨昭, 翟瑞, 冯彪, 吕子建, 赵文仲, 葛滢滢. R290/R1234yf与矿物油的互溶性测试及评价方法[J]. 化工学报, 2019, 70(9): 3248-3255.
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Refrigerants and oil | Chemical identifier | Half structural formula | Mass fraction purity/% | Boiling point/℃ | Saturated liquid density (15℃)/(kg·m-3) | Viscosity(40℃)/(mm2·s-1) | Global warming potential (GWP) |
---|---|---|---|---|---|---|---|
R1234yf | 2,3,3,3-tetra-fluoropropene | CH2=CFCF3 | ≥99.9 | -29.8 | 1127.2 | 0.125 | <1 |
R290 | propane | CH3CH2CH3 | ≥99.96 | -42.2 | 507.5 | 0.177 | 3.3 |
mineral oil | SUNISO 3GS | — | — | — | 909.0 | 29.5 | — |
Table 1 Properties of refrigerant and lubricant
Refrigerants and oil | Chemical identifier | Half structural formula | Mass fraction purity/% | Boiling point/℃ | Saturated liquid density (15℃)/(kg·m-3) | Viscosity(40℃)/(mm2·s-1) | Global warming potential (GWP) |
---|---|---|---|---|---|---|---|
R1234yf | 2,3,3,3-tetra-fluoropropene | CH2=CFCF3 | ≥99.9 | -29.8 | 1127.2 | 0.125 | <1 |
R290 | propane | CH3CH2CH3 | ≥99.96 | -42.2 | 507.5 | 0.177 | 3.3 |
mineral oil | SUNISO 3GS | — | — | — | 909.0 | 29.5 | — |
R290 mass fraction in R290/R1234yf refrigerant/% | Oil rate/% | Critical miscibility temperature/K |
---|---|---|
24.68 | 9.75 | 305.15 |
25.37 | 9.67 | 294.15 |
25.96 | 9.60 | 285.65 |
26.73 | 9.85 | 276.65 |
27.03 | 10.27 | 273.15 |
28.41 | 10.07 | 259.65 |
29.28 | 9.51 | 250.65 |
30.90 | 10.13 | 243.15 |
33.28 | 9.81 | 233.15 |
34.95 | 10.25 | 226.65 |
Table 2 Miscibility result of R290/R1234yf with
R290 mass fraction in R290/R1234yf refrigerant/% | Oil rate/% | Critical miscibility temperature/K |
---|---|---|
24.68 | 9.75 | 305.15 |
25.37 | 9.67 | 294.15 |
25.96 | 9.60 | 285.65 |
26.73 | 9.85 | 276.65 |
27.03 | 10.27 | 273.15 |
28.41 | 10.07 | 259.65 |
29.28 | 9.51 | 250.65 |
30.90 | 10.13 | 243.15 |
33.28 | 9.81 | 233.15 |
34.95 | 10.25 | 226.65 |
w 1 | w 2 | w 3 | Z | T CMT/K | T Cal/K | ((T CMT-T Cal)/T CMT)/% |
---|---|---|---|---|---|---|
0.0975 | 0.2227 | 0.6798 | 0.6457 | 301.15 | 299.14 | 0.67 |
0.0985 | 0.2250 | 0.6765 | 0.6431 | 296.15 | 296.62 | -0.16 |
0.0967 | 0.2292 | 0.6741 | 0.6391 | 294.15 | 291.08 | 1.04 |
0.1472 | 0.2532 | 0.5996 | 0.5984 | 286.65 | 272.43 | 4.96 |
0.0960 | 0.2346 | 0.6693 | 0.6336 | 285.65 | 284.69 | 0.34 |
0.1020 | 0.2329 | 0.6651 | 0.6338 | 285.15 | 288.10 | -1.04 |
0.1059 | 0.2417 | 0.6524 | 0.6234 | 274.15 | 279.26 | -1.87 |
0.1495 | 0.2571 | 0.5934 | 0.5934 | 273.15 | 268.74 | 1.62 |
0.0951 | 0.2419 | 0.6630 | 0.6262 | 272.65 | 276.56 | -1.44 |
0.1400 | 0.2669 | 0.5931 | 0.5858 | 270.15 | 259.15 | 4.07 |
0.1688 | 0.2484 | 0.5828 | 0.5966 | 269.15 | 277.77 | -3.20 |
0.2073 | 0.2674 | 0.5252 | 0.5607 | 264.65 | 258.27 | 2.41 |
0.1107 | 0.2527 | 0.6367 | 0.6104 | 262.65 | 268.99 | -2.42 |
0.1535 | 0.2641 | 0.5824 | 0.5843 | 261.65 | 262.39 | -0.28 |
0.1386 | 0.2740 | 0.5873 | 0.5786 | 256.15 | 252.89 | 1.27 |
0.1581 | 0.2720 | 0.5698 | 0.5740 | 252.65 | 255.51 | -1.13 |
0.2199 | 0.2739 | 0.5062 | 0.5481 | 251.15 | 251.83 | -0.27 |
0.2042 | 0.2784 | 0.5174 | 0.5492 | 250.15 | 249.16 | 0.39 |
0.1638 | 0.2818 | 0.5543 | 0.5610 | 248.15 | 247.47 | 0.27 |
0.1830 | 0.2693 | 0.5477 | 0.5679 | 247.15 | 257.75 | -4.29 |
0.1922 | 0.2864 | 0.5215 | 0.5449 | 247.15 | 243.45 | 1.50 |
0.1192 | 0.2721 | 0.6087 | 0.5871 | 246.15 | 252.55 | -2.60 |
0.2174 | 0.2822 | 0.5004 | 0.5393 | 244.65 | 245.24 | -0.24 |
0.2023 | 0.2852 | 0.5125 | 0.5421 | 242.65 | 243.85 | -0.49 |
0.1895 | 0.2963 | 0.5142 | 0.5347 | 239.65 | 236.13 | 1.47 |
0.1707 | 0.2937 | 0.5356 | 0.5452 | 239.15 | 238.37 | 0.33 |
0.1346 | 0.2952 | 0.5702 | 0.5573 | 237.65 | 236.01 | 0.69 |
0.1997 | 0.2943 | 0.5060 | 0.5328 | 235.15 | 237.16 | -0.85 |
0.1863 | 0.3081 | 0.5056 | 0.5228 | 233.15 | 228.01 | 2.21 |
0.2122 | 0.2994 | 0.4884 | 0.5214 | 231.15 | 232.74 | -0.69 |
0.1988 | 0.2926 | 0.5086 | 0.5351 | 230.65 | 238.46 | -3.38 |
0.1783 | 0.3066 | 0.5152 | 0.5278 | 230.65 | 229.17 | 0.64 |
0.1984 | 0.2989 | 0.5026 | 0.5280 | 230.15 | 233.86 | -1.61 |
0.1840 | 0.3166 | 0.4994 | 0.5142 | 227.15 | 222.52 | 2.04 |
0.1971 | 0.3035 | 0.4993 | 0.5233 | 225.15 | 230.70 | -2.46 |
0.2095 | 0.3083 | 0.4822 | 0.5124 | 224.65 | 226.84 | -0.98 |
Table 3 Miscibility result of R290/R1234yf with mineral oil of various oil ratios
w 1 | w 2 | w 3 | Z | T CMT/K | T Cal/K | ((T CMT-T Cal)/T CMT)/% |
---|---|---|---|---|---|---|
0.0975 | 0.2227 | 0.6798 | 0.6457 | 301.15 | 299.14 | 0.67 |
0.0985 | 0.2250 | 0.6765 | 0.6431 | 296.15 | 296.62 | -0.16 |
0.0967 | 0.2292 | 0.6741 | 0.6391 | 294.15 | 291.08 | 1.04 |
0.1472 | 0.2532 | 0.5996 | 0.5984 | 286.65 | 272.43 | 4.96 |
0.0960 | 0.2346 | 0.6693 | 0.6336 | 285.65 | 284.69 | 0.34 |
0.1020 | 0.2329 | 0.6651 | 0.6338 | 285.15 | 288.10 | -1.04 |
0.1059 | 0.2417 | 0.6524 | 0.6234 | 274.15 | 279.26 | -1.87 |
0.1495 | 0.2571 | 0.5934 | 0.5934 | 273.15 | 268.74 | 1.62 |
0.0951 | 0.2419 | 0.6630 | 0.6262 | 272.65 | 276.56 | -1.44 |
0.1400 | 0.2669 | 0.5931 | 0.5858 | 270.15 | 259.15 | 4.07 |
0.1688 | 0.2484 | 0.5828 | 0.5966 | 269.15 | 277.77 | -3.20 |
0.2073 | 0.2674 | 0.5252 | 0.5607 | 264.65 | 258.27 | 2.41 |
0.1107 | 0.2527 | 0.6367 | 0.6104 | 262.65 | 268.99 | -2.42 |
0.1535 | 0.2641 | 0.5824 | 0.5843 | 261.65 | 262.39 | -0.28 |
0.1386 | 0.2740 | 0.5873 | 0.5786 | 256.15 | 252.89 | 1.27 |
0.1581 | 0.2720 | 0.5698 | 0.5740 | 252.65 | 255.51 | -1.13 |
0.2199 | 0.2739 | 0.5062 | 0.5481 | 251.15 | 251.83 | -0.27 |
0.2042 | 0.2784 | 0.5174 | 0.5492 | 250.15 | 249.16 | 0.39 |
0.1638 | 0.2818 | 0.5543 | 0.5610 | 248.15 | 247.47 | 0.27 |
0.1830 | 0.2693 | 0.5477 | 0.5679 | 247.15 | 257.75 | -4.29 |
0.1922 | 0.2864 | 0.5215 | 0.5449 | 247.15 | 243.45 | 1.50 |
0.1192 | 0.2721 | 0.6087 | 0.5871 | 246.15 | 252.55 | -2.60 |
0.2174 | 0.2822 | 0.5004 | 0.5393 | 244.65 | 245.24 | -0.24 |
0.2023 | 0.2852 | 0.5125 | 0.5421 | 242.65 | 243.85 | -0.49 |
0.1895 | 0.2963 | 0.5142 | 0.5347 | 239.65 | 236.13 | 1.47 |
0.1707 | 0.2937 | 0.5356 | 0.5452 | 239.15 | 238.37 | 0.33 |
0.1346 | 0.2952 | 0.5702 | 0.5573 | 237.65 | 236.01 | 0.69 |
0.1997 | 0.2943 | 0.5060 | 0.5328 | 235.15 | 237.16 | -0.85 |
0.1863 | 0.3081 | 0.5056 | 0.5228 | 233.15 | 228.01 | 2.21 |
0.2122 | 0.2994 | 0.4884 | 0.5214 | 231.15 | 232.74 | -0.69 |
0.1988 | 0.2926 | 0.5086 | 0.5351 | 230.65 | 238.46 | -3.38 |
0.1783 | 0.3066 | 0.5152 | 0.5278 | 230.65 | 229.17 | 0.64 |
0.1984 | 0.2989 | 0.5026 | 0.5280 | 230.15 | 233.86 | -1.61 |
0.1840 | 0.3166 | 0.4994 | 0.5142 | 227.15 | 222.52 | 2.04 |
0.1971 | 0.3035 | 0.4993 | 0.5233 | 225.15 | 230.70 | -2.46 |
0.2095 | 0.3083 | 0.4822 | 0.5124 | 224.65 | 226.84 | -0.98 |
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