CIESC Journal ›› 2019, Vol. 70 ›› Issue (1): 24-31.DOI: 10.11949/j.issn.0438-1157.20180970
• Thermodynamics • Previous Articles Next Articles
Chen GENG1(),Yajun GUO1(),Song FENG2,Qincheng BI2
Received:
2018-08-30
Revised:
2018-10-24
Online:
2019-01-05
Published:
2019-01-05
Contact:
Yajun GUO
通讯作者:
郭亚军
作者简介:
耿宸(1994—),女,硕士研究生,<email>Gengchench@163.com</email>|郭亚军(1966—),女,硕士,副教授,<email>879400635@qq.com</email>
基金资助:
CLC Number:
Chen GENG, Yajun GUO, Song FENG, Qincheng BI. Density measurements of endothermic hydrocarbon fuel using random temperature signal cross-correlation[J]. CIESC Journal, 2019, 70(1): 24-31.
耿宸, 郭亚军, 冯松, 毕勤成. 随机温度信号互相关法测量吸热型碳氢燃料密度[J]. 化工学报, 2019, 70(1): 24-31.
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URL: https://hgxb.cip.com.cn/EN/10.11949/j.issn.0438-1157.20180970
L/mm | ρxy(τ) |
---|---|
80 | 0.8967 |
148 | 0.9259 |
180 | 0.8476 |
228 | 0.7933 |
280 | 0.7581 |
Table 1 Dependence of correlation coefficient ρxy(τ) on thermocouples’ spacing L
L/mm | ρxy(τ) |
---|---|
80 | 0.8967 |
148 | 0.9259 |
180 | 0.8476 |
228 | 0.7933 |
280 | 0.7581 |
T/K | ρexp/(kg/m3) | ρlit/(kg/m3) | (Δρ/ρ)/% |
---|---|---|---|
298.8 | 752.0 | 748.8 | 0.43 |
307.6 | 748.1 | 742.5 | 0.76 |
318.0 | 737.1 | 735.0 | 0.29 |
329.3 | 728.5 | 726.9 | 0.22 |
338.7 | 716.9 | 720.2 | -0.46 |
348.1 | 709.4 | 713.5 | -0.58 |
358.6 | 703.6 | 706.0 | -0.34 |
368.0 | 695.8 | 699.2 | -0.49 |
378.4 | 688.9 | 691.7 | -0.41 |
388.1 | 686.7 | 684.7 | 0.30 |
398.2 | 674.8 | 677.3 | -0.36 |
407.2 | 672.4 | 670.6 | 0.26 |
417.6 | 661.7 | 662.9 | -0.18 |
426.9 | 658.2 | 655.9 | 0.35 |
436.4 | 650.8 | 648.7 | 0.33 |
445.1 | 640.7 | 642.0 | -0.2 |
Table 2 Relative error (Δρ/ρ) of experimental density (ρexp) of n-dodecane compared with published data (ρlit) at 5 MPa
T/K | ρexp/(kg/m3) | ρlit/(kg/m3) | (Δρ/ρ)/% |
---|---|---|---|
298.8 | 752.0 | 748.8 | 0.43 |
307.6 | 748.1 | 742.5 | 0.76 |
318.0 | 737.1 | 735.0 | 0.29 |
329.3 | 728.5 | 726.9 | 0.22 |
338.7 | 716.9 | 720.2 | -0.46 |
348.1 | 709.4 | 713.5 | -0.58 |
358.6 | 703.6 | 706.0 | -0.34 |
368.0 | 695.8 | 699.2 | -0.49 |
378.4 | 688.9 | 691.7 | -0.41 |
388.1 | 686.7 | 684.7 | 0.30 |
398.2 | 674.8 | 677.3 | -0.36 |
407.2 | 672.4 | 670.6 | 0.26 |
417.6 | 661.7 | 662.9 | -0.18 |
426.9 | 658.2 | 655.9 | 0.35 |
436.4 | 650.8 | 648.7 | 0.33 |
445.1 | 640.7 | 642.0 | -0.2 |
T/K | ρexp/(kg/m3) | ρlit/(kg/m3) | (Δρ/ρ)/% |
---|---|---|---|
303.1 | 681.8 | 687.3 | -0.80 |
313.3 | 673.1 | 679.2 | -0.90 |
323.0 | 668.5 | 671.4 | -0.43 |
332.7 | 661.3 | 663.6 | -0.35 |
344.1 | 656.9 | 654.2 | 0.41 |
353.2 | 644.4 | 646.8 | -0.37 |
362.9 | 640.8 | 638.6 | 0.34 |
372.3 | 633.3 | 630.7 | 0.41 |
383.2 | 625.2 | 621.3 | 0.63 |
393.0 | 610.2 | 612.7 | -0.41 |
405.1 | 605.3 | 601.8 | 0.58 |
413.8 | 589.5 | 593.8 | -0.72 |
424.2 | 587.4 | 584.1 | 0.56 |
433.2 | 572.5 | 575.4 | -0.50 |
443.0 | 561.6 | 565.6 | -0.71 |
453.7 | 556.4 | 554.7 | 0.30 |
463.1 | 549.1 | 544.8 | 0.80 |
474.4 | 537.9 | 532.3 | 1.06 |
Table 3 Relative error (Δρ/ρ) of experimental density (ρexp) of binary mixture of n-octane and n-heptane compared with published data (ρlit) at 5.1 MPa
T/K | ρexp/(kg/m3) | ρlit/(kg/m3) | (Δρ/ρ)/% |
---|---|---|---|
303.1 | 681.8 | 687.3 | -0.80 |
313.3 | 673.1 | 679.2 | -0.90 |
323.0 | 668.5 | 671.4 | -0.43 |
332.7 | 661.3 | 663.6 | -0.35 |
344.1 | 656.9 | 654.2 | 0.41 |
353.2 | 644.4 | 646.8 | -0.37 |
362.9 | 640.8 | 638.6 | 0.34 |
372.3 | 633.3 | 630.7 | 0.41 |
383.2 | 625.2 | 621.3 | 0.63 |
393.0 | 610.2 | 612.7 | -0.41 |
405.1 | 605.3 | 601.8 | 0.58 |
413.8 | 589.5 | 593.8 | -0.72 |
424.2 | 587.4 | 584.1 | 0.56 |
433.2 | 572.5 | 575.4 | -0.50 |
443.0 | 561.6 | 565.6 | -0.71 |
453.7 | 556.4 | 554.7 | 0.30 |
463.1 | 549.1 | 544.8 | 0.80 |
474.4 | 537.9 | 532.3 | 1.06 |
p=3 MPa | p=4 MPa | p=5 MPa | ||||
---|---|---|---|---|---|---|
T/K | ρexp/ (kg/m3) | T/K | ρexp/ (kg/m3) | T/K | ρexp/ (kg/m3) | |
302.3 | 793.5 | 302.2 | 793.8 | 302.0 | 795.5 | |
328.5 | 777.0 | 329.9 | 781.4 | 327.6 | 781.0 | |
349.8 | 763.7 | 349.3 | 764.8 | 347.5 | 769.4 | |
374.7 | 750.2 | 376.7 | 751.7 | 376.8 | 752.1 | |
400.1 | 739.5 | 399.4 | 738.8 | 399.5 | 739.0 | |
425.0 | 719.1 | 424.8 | 719.5 | 424.4 | 723.1 | |
449.8 | 699.2 | 450.8 | 702.0 | 448.5 | 707.1 | |
474.2 | 682.3 | 475.3 | 683.6 | 475.1 | 687.4 | |
498.6 | 661.7 | 501.3 | 664.0 | 501.6 | 666.5 | |
523.8 | 638.7 | 529.6 | 639.0 | 523.7 | 649.2 |
Table 4 Experimental density (ρexp) of endothermic hydrocarbon fuel under T = 302.0—529.6 K, supercritical pressures
p=3 MPa | p=4 MPa | p=5 MPa | ||||
---|---|---|---|---|---|---|
T/K | ρexp/ (kg/m3) | T/K | ρexp/ (kg/m3) | T/K | ρexp/ (kg/m3) | |
302.3 | 793.5 | 302.2 | 793.8 | 302.0 | 795.5 | |
328.5 | 777.0 | 329.9 | 781.4 | 327.6 | 781.0 | |
349.8 | 763.7 | 349.3 | 764.8 | 347.5 | 769.4 | |
374.7 | 750.2 | 376.7 | 751.7 | 376.8 | 752.1 | |
400.1 | 739.5 | 399.4 | 738.8 | 399.5 | 739.0 | |
425.0 | 719.1 | 424.8 | 719.5 | 424.4 | 723.1 | |
449.8 | 699.2 | 450.8 | 702.0 | 448.5 | 707.1 | |
474.2 | 682.3 | 475.3 | 683.6 | 475.1 | 687.4 | |
498.6 | 661.7 | 501.3 | 664.0 | 501.6 | 666.5 | |
523.8 | 638.7 | 529.6 | 639.0 | 523.7 | 649.2 |
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