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Journal of Research of the National Bureau of Standards. Section A, Physics and Chemistry logoLink to Journal of Research of the National Bureau of Standards. Section A, Physics and Chemistry
. 1970 Nov-Dec;74A(6):747–760. doi: 10.6028/jres.074A.062

PVT Measurements, Virial Coefficients, and Joule-Thomson inversion Curve of Fluorine

Rolf Prydz 1,**, G C Straty 1,**
PMCID: PMC6730985  PMID: 32523225

Abstract

Experimental PVT measurements on gaseous and liquid fluorine from the triple point (53.5 K) to 300 K at pressures to about 21 MN/m2 are presented. The data are represented by a truncated virial equation in the low-density region. Comparisons of the second virial coefficient from this equation are made with published data. The PVT relationship along the Joule-Thomson inversion curve was obtained from the isotherm-isochore representation of the high density region.

Keywords: Isochores, isotherms, Joule-Thomson inversion curve, liquid densities along melting line, PVT data, second virial coefficient, third virial coefficient

1. Introduction

This laboratory is currently engaged in a comprehensive program to determine the thermodynamic and transport properties of compressed liquid and gaseous fluorine. Extensive, precise, PVT data are essential to the calculation of thermodynamic functions required for engineering development of proposed rocket propulsion systems. Since fluorine is not only the most reactive of all elements but also extremely toxic, it is not surprising that physical properties data on this fluid have either been inconsistent or, in many cases, nonexistent. Recently, however, some thermodynamic data have been reported by the authors of this paper [1, 2, 3].1 The equations representing these data are given in the appendix of this paper for the sake of completeness.

It is the purpose of this paper to report new experimental PVT data from the triple point (53.5 K) to 300 K for pressures to a maximum of 21 MN/m2 (1 MN/m2 = 9.86923 atm). Also reported are derived values for the second and third virial coefficients and the Joule-Thomson inversion curve.

2. PVT Measurements

The experimental apparatus and instrumentation used for the PVT measurements on fluorine have been described earlier [4]. To measure single-phase densities, the common gas expansion method was used. After filling and closing off the sample holder, a sequence of pressure-temperature observations were made on the nearly constant density fluid confined in the PVT cell whose volume was accurately calibrated. Temperatures were regulated at integral values (on IPTS 1948 and the NBS 1955 temperature scale) to permit analysis of the data along isotherms. The temperatures of table 1, however, were converted to IPTS 1968 using the temperature scale differences given by references [5, 6]. When either maximum pressure (21 MN/m2) cr maximum temperature (300 K) was reached, the fluorine sample in the PVT cell was expanded into large calibrated volumes maintained near room temperature. The density could then be determined since the volume of the sample holder and the compressibility factor, PV/RT, of fluorine gas at the conditions in the expansion volumes were known. This fluorine compressibility factor was obtained using Burnett [7] gas expansion techniques. The results of all volume calibrations necessary for the density determination and the Burnett expansion experiment may be obtained from reference [8].

Table 1.

TEMPERATURE-PRESSURE-DENSITY OBSERVATIONS ON FLUORINE

TEMP
K
PRESSURE
MN/M2
DENSITY
MOL/L
IDENT
74.994 0.0231 0.0379 13101
79.991 0.0249 0.0378 13102
84.997 0.0265 0.0378 13103
90.010 0.0280 0.0378 13104
95.013 0.0296 0.0378 13105
100.010 0.0312 0.0378 13106
109.998 0.0343 0.0377 13107
119.989 0.0374 0.0377 13108
129.987 0.0405 0.0377 13109
139.992 0.0436 0.0376 13110
79.991 0.0479 0.0740 13001
84.997 0.0513 0.0739 13002
90.010 0.0544 0.0739 13003
95.013 0.0575 0.0738 13004
100.010 0.0606 0.0738 13005
109.998 0.0667 0.0737 13006
119.989 0.0729 0.0737 13007
129.987 0.0789 0.0776 13008
139.992 0.0850 0.0735 13009
84.997 0.0955 0.1403 12901
90.010 0.1020 0.1403 12902
95.013 0.1080 0.1402 12903
100.010 0.1139 0.1401 12904
105.004 0.1198 0.1401 12905
119.989 0.1373 0.1398 12906
129.987 0.1489 0.1397 12907
139.992 0.1605 0.1396 12908
90.010 0.1516 0.2118 12801
95.013 0.1609 0.2117 12802
100.010 0.1699 0.2116 12803
105.004 0.1789 0.2115 12804
109.998 0.1879 0.2114 12805
119.989 0.2057 0.2111 12806
129.987 0.2234 0.2109 12807
139.992 0.2410 0.2107 12808
95.013 0.2640 0.3576 12301
100.010 0.2803 0.3574 12302
109.998 0.3112 0.3571 12303
119.989 0.3417 0.3567 12304
129.987 0.3721 0.3563 12305
139.992 0.4022 0.3559 12306
102.008 0.4305 0.5538 12701
105.004 0.4454 0.5537 12702
109.998 0.4699 0.5534 12703
114.994 0.4942 0.5531 12704
119.989 0.5183 0.5528 12705
129.987 0.5661 0.5522 12706
139.992 0.6136 0.5516 12707
105.004 0.6031 0.7767 12501
109.998 0.6390 0.7763 12502
114.994 0.6740 0.7759 12503
119.989 0.7086 0.7755 12504
124.987 0.7430 0.7751 12505
129.987 0.7772 0.7746 12506
139.992 0.8451 0.7738 12507
111.996 0.9141 1.1436 12402
114.994 0.9465 1.1432 12403
119.989 0.9997 1.1426 12404
129.987 1.1044 1.1413 12405
139.992 1.2075 1.1400 12406
115.993 1.2050 1.5135 8101
117.991 1.2348 1.5132 8102
119.989 1.2641 1.5128 8103
121.988 1.2932 1.5125 8104
123.987 1.3221 1.5121 8105
125.987 1.3510 1.5118 8106
127.987 1.3794 1.5114 8107
129.987 1.4080 1.5111 8108
131.987 1.4363 1.5107 8109
133.988 1.4645 1.5104 8110
135.989 1.4925 1.5101 8111
137.990 1.5206 1.5097 8112
139.992 1.5486 1.5094 8113
141.993 1.5765 1.5090 8114
143.995 1.6042 1.5087 8115
145.996 1.6319 1.5083 8116
147.998 1.6596 1.5080 8117
150.000 1.6871 1.5077 8118
155.005 1.7556 1.5068 8119
160.010 1.8237 1.5059 8120
165.014 1.8916 1.5051 8121
170.019 1.9592 1.5042 8122
175.024 2.0264 1.5033 8123
180.027 2.0936 1.5025 8124
185.030 2.1603 1.5016 8125
190.032 2.2268 1.5007 8126
195.034 2.2931 1.4998 8127
200.035 2.3592 1.4990 8128
210.033 2.4909 1.4972 8129
220.030 2.6218 1.4954 8130
220.030 2.6214 1.4954 8131
230.025 2.7517 1.4935 8132
240.020 2.8812 1.4917 8133
250.014 3.0103 1.4898 8134
260.008 3.1389 1.4880 8135
270.002 3.2670 1.4861 8136
279.997 3.3946 1.4842 8137
289.994 3.5216 1.4822 8138
299.992 3.6484 1.4803 8139
121.988 1.6805 2.1162 12601
124.987 1.7449 2.1154 12602
129.987 1.8504 2.1141 12603
134.988 1.9543 2.1129 12604
139.992 2.0568 2.1116 12605
144.995 2.1583 2.1104 12606
150.000 2.2589 2.1091 12607
125.987 2.0758 2.6479 7401
127.987 2.1314 2.6472 7402
129.987 2.1865 2.6466 7403
131.987 2.2411 2.6459 7404
133.988 2.2954 2.6453 7405
135.989 2.3491 2.6446 7406
137.990 2.4026 2.6440 7407
139.992 2.4558 2.6433 7408
141.993 2.5088 2.6427 7409
143.995 2.5614 2.6420 7410
145.996 2.6138 2.6414 7411
147.998 2.6659 2.6407 7412
150.000 2.7180 2.6401 7413
155.005 2.8470 2.6384 7414
160.010 2.9751 2.6368 7415
165.014 3.1021 2.6352 7416
170.019 3.2284 2.6336 7417
175.024 3.3538 2.6319 7418
180.027 3.4784 2.6303 7419
185.030 3.6024 2.6287 7420
190.032 3.7260 2.6270 7421
195.034 3.8486 2.6254 7422
195.034 3.8486 2.6254 7422
200.035 3.9711 2.6238 7423
210.033 4.2145 2.6204 7424
220.030 4.4562 2.6171 7425
230.025 4.6964 2.6138 7426
240.020 4.9347 2.6104 7427
230.025 4.6968 2.6140 7428
240.020 4.9356 2.6106 7429
250.014 5.1732 2.6072 7430
260.008 5.4093 2.6038 7431
270.002 5.6446 2.6004 7432
279.997 5.8785 2.5969 7433
289.994 6.1114 2.5933 7434
299.992 6.3432 2.5897 7435
129.987 2.6958 3.6637 7201
131.987 2.7788 3.6627 7202
133.988 2.8604 3.6617 7203
135.989 2.9410 3.6608 7204
137.990 3.0209 3.6598 7205
139.992 3.1001 3.6588 7206
141.993 3.1786 3.6579 7207
143.995 3.2565 3.6569 7208
145.996 3.3341 3.6560 7209
147.998 3.4110 3.6550 7210
150.000 3.4876 3.6540 7211
155.005 3.6773 3.6517 7212
160.010 3.8649 3.6493 7213
165.014 4.0507 3.6470 7214
170.019 4.2350 3.6446 7215
175.024 4.4179 3.6423 7216
180.027 4.5994 3.6399 7217
180.027 4.5995 3.6401 7218
185.030 4.7802 3.6378 7219
190.032 4.9597 3.6354 7220
195.034 5.1383 3.6330 7221
200.035 5.3160 3.6307 7222
210.033 5.6689 3.6259 7223
220.030 6.0188 3.6211 7224
230.025 6.3662 3.6163 7225
240.020 6.7110 3.6114 7226
250.014 7.0537 3.6065 7227
260.008 7.3946 3.6015 7228
270.002 7.7335 3.5966 7229
279.997 8.0706 3.5915 7230
289.994 8.4063 3.5865 7231
299.992 8.7404 3.5813 7232
150.000 3.9137 4.3084 8501
165.014 4.6013 4.2998 8502
180.027 5.2692 4.2913 8503
200.035 6.1393 4.2799 8504
230.025 7.4114 4.2626 8505
133.988 3.2925 4.7443 7001
135.989 3.4060 4.7430 7002
137.990 3.5176 4.7416 7003
139.992 3.6277 4.7403 7004
141.993 3.7366 4.7389 7005
143.995 3.8445 4.7376 7006
145.996 3.9514 4.7363 7007
147.998 4.0575 4.7350 7008
150.000 4.1629 4.7337 7009
155.005 4.4233 4.7304 7010
160.010 4.6804 4.7272 7011
165.014 4.9344 4.7240 7012
170.019 5.1861 4.7208 7013
175.024 5.4345 4.7176 7014
180.027 5.6819 4.7144 7015
185.030 5.9278 4.7113 7016
190.032 6.1719 4.7081 7017
195.034 6.4144 4.7049 7018
200.035 6.6558 4.7018 7019
210.033 7.1347 4.6954 7020
220.030 7.6091 4.6890 7021
210.033 7.1344 4.6952 7022
220.030 7.6091 4.6888 7023
230.025 8.0796 4.6824 7024
240.020 8.5464 4.6759 7025
250.014 9.0103 4.6693 7026
260.008 9.4713 4.6627 7027
270.002 9.9295 4.6560 7028
279.997 10.3848 4.6493 7029
289.994 10.8367 4.6425 7030
299.992 11.2872 4.6357 7031
137.990 3.7717 5.4871 8301
139.992 3.9057 5.4855 8302
141.993 4.0376 5.4839 8303
143.995 4.1679 5.4823 8304
145.996 4.2969 5.4808 8305
147.998 4.4249 5.4792 8306
150.000 4.5515 5.4776 8307
155.005 4.8645 5.4737 8308
160.010 5.1727 5.4699 8309
165.014 5.4770 5.4660 8310
170.019 5.7784 5.4622 8311
175.024 6.0765 5.4585 8312
180.027 6.3724 5.4547 8313
185.030 6.6661 5.4509 8314
190.032 6.9578 5.4471 8315
195.034 7.2477 5.4433 8316
200.035 7.5357 5.4395 8317
210.033 8.1071 5.4319 8318
220.030 8.6730 5.4242 8319
220.030 8.6718 5.4241 8320
230.025 9.2328 5.4165 8321
240.020 9.7891 5.4087 8322
250.014 10.3417 5.4008 8323
260.008 10.8902 5.3929 8324
270.002 11.4359 5.3849 8325
279.997 11.9776 5.3769 8326
289.994 12.5164 5.3687 8327
299.992 13.0526 5.3605 8328
137.990 3.9283 6.0824 6901
139.992 4.0827 6.0805 6902
141.993 4.2341 6.0787 6903
143.995 4.3832 6.0769 6904
145.996 4.5308 6.0751 6905
147.998 4.6767 6.0733 6906
150.000 4.8213 6.0715 6907
155.005 5.1779 6.0671 6908
160.010 5.5288 6.0627 6909
165.014 5.8752 6.0583 6910
170.019 6.2174 6.0540 6911
175.024 6.5565 6.0496 6912
180.027 6.8924 6.0453 6913
185.030 7.2260 6.0410 6914
190.032 7.5572 6.0366 6915
195.034 7.8860 6.0323 6916
200.035 8.2131 6.0279 6917
210.033 8.8617 6.0192 6918
220.030 9.5038 6.0105 6919
230.025 10.1405 6.0017 6920
240.020 10.7703 5.9929 6921
250.014 11.3966 5.9841 6922
260.008 12.0190 5.9751 6923
270.002 12.6373 5.9662 6924
279.997 13.2518 5.9571 6925
289.994 13.8633 5.9479 6926
299.992 14.4706 5.9387 6927
139.992 4.2052 6.5928 7801
141.993 4.3745 6.5908 7802
143.995 4.5407 6.5888 7803
145.996 4.7050 6.5868 7804
147.998 4.8670 6.5848 7805
150.000 5.0275 6.5828 7806
155.005 5.4232 6.5779 7807
160.010 5.8120 6.5730 7808
165.014 6.1955 6.5681 7809
170.019 6.5732 6.5633 7810
175.024 6.9484 6.5586 7811
180.027 7.3206 6.5538 7812
185.030 7.6898 6.5490 7813
190.032 8.0560 6.5442 7814
195.034 8.4200 6.5395 7815
200.035 8.7819 6.5346 7816
210.033 9.4992 6.5251 7817
220.030 10.2098 6.5154 7818
230.025 10.9136 6.5058 7819
230.025 10.9148 6.5061 7820
240.020 11.6123 6.4962 7821
250.014 12.3046 6.4862 7822
260.008 12.9920 6.4762 7823
270.002 13.6750 6.4661 7824
279.997 14.3536 6.4559 7825
289.994 15.0284 6.4456 7826
299.992 15.6989 6.4353 7827
139.992 4.2620 6.8747 2701
141.993 4.4415 6.8725 2702
143.995 4.6175 6.8704 2703
145.996 4.7909 6.8683 2704
147.998 4.9623 6.8662 2705
150.000 5.1318 6.8642 2706
155.005 5.5490 6.8590 2707
160.010 5.9593 6.8540 2708
165.014 6.3637 6.8489 2709
170.019 6.7637 6.8439 2710
175.024 7.1593 6.8389 2711
180.027 7.5515 6.8339 2712
185.030 7.9406 6.8290 2713
190.032 8.3270 6.8240 2714
195.034 8.7109 6.8190 2715
200.035 9.0924 6.8140 2716
210.033 9.8489 6.8040 2717
220.030 10.5977 6.7940 2718
230.025 11.3398 6.7839 2719
220.030 10.5990 6.7943 2720
230.025 11.3409 6.7842 2721
240.020 12.0771 6.7740 2722
250.014 12.8074 6.7638 2723
260.008 13.5329 6.7535 2724
270.002 14.2532 6.7430 2725
279.997 14.9689 6.7325 2726
289.994 15.6802 6.7219 2727
299.992 16.3876 6.7111 2728
141.993 4.5958 7.6840 7501
143.995 4.8006 7.6815 7502
145.996 5.0015 7.6791 7503
147.998 5.2001 7.6767 7504
150.000 5.3960 7.6743 7505
155.005 5.8780 7.6683 7506
160.010 6.3513 7.6624 7507
165.014 6.8179 7.6565 7508
170.019 7.2790 7.6507 7509
175.024 7.7353 7.6449 7510
180.027 8.1862 7.6392 7511
185.030 8.6352 7.6334 7512
190.032 9.0807 7.6276 7513
190.032 9.0802 7.6275 7514
195.034 9.5228 7.6217 7515
200.035 9.9626 7.6159 7516
210.033 10.8353 7.6043 7517
220.030 11.6987 7.5926 7518
230.025 12.5549 7.5808 7519
240.020 13.4022 7.5689 7520
250.014 14.2444 7.5570 7521
260.008 15.0797 7.5449 7522
270.002 15.9091 7.5327 7523
279.997 16.7342 7.5203 7524
289.994 17.5523 7.5078 7525
299.992 18.3667 7.4953 7526
185.030 8.9694 8.0302 8401
195.034 9.9172 8.0179 8402
210.033 11.3172 7.9994 8403
230.025 13.1530 7.9743 8404
143.995 4.9168 8.3819 11901
145.996 5.1430 8.3791 11902
147.998 5.3652 8.3764 11903
150.000 5.5847 8.3737 11904
155.005 6.1242 8.3671 11905
160.010 6.6540 8.3605 11906
165.014 7.1759 8.3539 11907
170.019 7.6922 8.3474 11908
175.024 8.2027 8.3409 11909
180.027 8.7093 8.3345 11910
185.030 9.2117 8.3280 11911
190.032 9.7107 8.3215 11912
195.034 10.2065 8.3150 11913
200.035 10.6993 8.3085 11914
210.033 11.6772 8.2955 11915
220.030 12.6444 8.2825 11916
210.033 11.6741 8.2952 11917
220.030 12.6416 8.2821 11918
230.025 13.5995 8.2689 11919
240.020 14.5502 8.2556 11920
250.014 15.4923 8.2422 11921
260.008 16.4281 8.2287 11922
270.002 17.3573 8.2151 11923
279.997 18.2803 8.2013 11924
289.994 19.1973 8.1874 11925
299.992 20.1092 8.1732 11926
141.993 4.7140 8.7499 3102
143.995 4.9677 8.7468 3103
145.996 5.2069 8.7439 3104
147.998 5.4421 8.7411 3105
150.000 5.6739 8.7382 3106
155.005 6.2440 8.7312 3107
160.010 6.8033 8.7243 3108
165.014 7.3548 8.7174 3109
170.019 7.9002 8.7105 3110
175.024 8.4399 8.7037 3111
180.027 8.9755 8.6969 3112
185.030 9.5067 8.6901 3113
190.032 10.0342 8.6833 3114
195.034 10.5584 8.6765 3115
200.035 11.0798 8.6697 3116
210.033 12.1133 8.6560 3117
220.030 13.1363 8.6423 3118
220.030 13.1341 8.6416 3119
230.025 14.1478 8.6278 3120
240.020 15.1530 8.6140 3121
250.014 16.1502 8.6000 3122
260.008 17.1403 8.5859 3123
270.002 18.1231 8.5717 3124
279.997 19.0990 8.5572 3125
289.994 20.0680 8.5426 3126
299.992 21.0320 8.5278 3127
143.995 4.9995 9.0187 8201
145.996 5.2489 9.0157 8202
147.998 5.4935 9.0127 8203
150.000 5.7349 9.0097 8204
155.005 6.3276 9.0024 8205
160.010 6.9099 8.9953 8206
165.014 7.4838 8.9881 8207
170.019 8.0512 8.9809 8208
175.024 8.6132 8.9738 8209
180.027 9.1705 8.9667 8210
185.030 9.7235 8.9596 8211
190.032 10.2729 8.9524 8212
195.034 10.8190 8.9453 8213
200.035 11.3619 8.9381 8214
143.995 4.9977 9.0186 8215
170.019 8.0504 8.9805 8216
200.035 11.3610 8.9378 8217
210.033 12.4354 8.9234 8218
220.030 13.5009 8.9090 8219
230.025 14.5573 8.8945 8220
240.020 15.6029 8.8798 8221
250.014 16.6415 8.8650 8222
260.008 17.6717 8.8501 8223
270.002 18.6956 8.8349 8224
279.997 19.7114 8.8197 8225
289.994 20.7215 8.8043 8226
143.995 5.0676 9.7709 7601
145.996 5.3447 9.7675 7602
147.998 5.6161 9.7641 7603
150.000 5.8835 9.7608 7604
155.005 6.5404 9.7527 7605
160.010 7.1858 9.7446 7606
165.014 7.8231 9.7366 7607
170.019 8.4535 9.7286 7608
175.024 9.0778 9.7206 7609
180.027 9.6972 9.7127 7610
185.030 10.3125 9.7047 7611
190.032 10.9239 9.6968 7612
195.034 11.5312 9.6888 7613
200.035 12.1356 9.6809 7614
210.033 13.3343 9.6649 7615
220.030 14.5208 9.6488 7616
230.025 15.6937 9.6326 7617
230.025 15.6950 9.6329 7618
240.020 16.8613 9.6166 7619
250.014 18.0166 9.6000 7620
260.008 19.1645 9.5833 7621
270.002 20.3049 9.5663 7622
143.995 5.1231 10.8686 8001
145.996 5.4415 10.8647 8002
147.998 5.7518 10.8608 8003
150.000 6.0578 10.8570 8004
155.005 6.8106 10.8477 8005
160.010 7.5519 10.8384 8006
165.014 8.2847 10.8291 8007
170.019 9.0106 10.8199 8008
175.024 9.7306 10.8108 8009
180.027 10.4459 10.8016 8010
185.030 11.1567 10.7925 8011
190.032 11.8630 10.7834 8012
195.034 12.5659 10.7742 8013
200.035 13.2650 10.7650 8014
210.033 14.6522 10.7466 8015
220.030 16.0262 10.7279 8016
230.025 17.3881 10.7092 8017
240.020 18.7385 10.6903 8018
250.014 20.0784 10.6712 8019
260.008 21.4083 10.6519 8020
145.996 5.5018 11.9244 7902
147.998 5.8491 11.9201 7903
150.000 6.1922 11.9159 7904
155.005 7.0392 11.9053 7905
160.010 7.8758 11.8948 7906
165.014 8.7053 11.8843 7907
170.019 9.5289 11.8739 7908
175.024 10.3471 11.8634 7909
180.027 11.1599 11.8530 7910
185.030 11.9686 11.8425 7911
190.032 12.7733 11.8321 7912
195.034 13.5742 11.8216 7913
200.035 14.3705 11.8111 7914
210.033 15.9527 11.7900 7915
220.030 17.5202 11.7687 7916
230.025 19.0742 11.7472 7917
240.020 20.6152 11.7254 7918
145.996 5.5529 13.4190 7701
147.998 5.9507 13.4141 7702
150.000 6.3460 13.4092 7703
155.005 7.3299 13.3969 7704
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55.107 15.4160 45.1315 12113
56.005 18.4968 45.0966 12114

All experimental single-phase PVT data in both the compressed liquid and vapor regions are given in table 1. The column of this table labeled “IDENT” contains the identification number of each data point. The last two digits represent the point number while the remaining digits are the number of the run or experimental isochore. Entries in runs 120 and 121 which contain no value for the density are pressures measured on the melting curve. Experimental PVT data for densities less than 0.22 mol/1 were obtained indirectly, since gas expansion measurements at these low densities were not possible. Pressures were obtained using an air deadweight gage while the density was obtained by heating the PVT cell to 175 K using an extrapolation of the previously determined pressure-density relationship for that isotherm obtained from higher density measurements.

The estimated accuracy of the density measurements is 0.1 percent. However, the corresponding precision is better, indicated by the fact that the standard deviation of all PVT data from eqs (1) and (5) is approximately 0.02 percent in density.

The purity of the fluorine sample used for these measurements was 99.99 percent as determined from residual gas analysis after reaction of fluorine with mercury.

3. Representation of PVT Data

No single equation of state was found capable of representing the data to within its precision. Therefore, to obtain the best possible representation of all the data for computation of thermodynamic functions, the PVT surface was divided into two regions as pictured in figure 1. The data in each region were correlated separately as discussed below.

Figure 1.

Figure 1.

Density-temperature diagram showing the regions used for representation of the PVT data.

3.1. Low-Density Region

All experimental PVT data at densities less than 6.0 mol/1 were represented by the truncated virial equation

P=RT[ρ+B(T)ρ2+C(T)ρ3] (1)

where R = 8.3143 J/mol — K. The decision to use 6.0 mol/1 as a maximum density value for the virial surface was based on the results obtained by fitting the experimental data to eq (1). By varying the maximum experimental density included in the fit of the virial equation, the data were found to exhibit definite systematic deviations in density as well as temperature for all densities greater than 6.0 mol/1. Equation (1) was based on 329 PVT data points in the virial region. Further, 26 measured specific heat (Cv) data points [9] between 6.5 and 6.8 mol/1 at temperatures from 140 K to 300 K were compared to Cv values calculated from the virial equation and the ideal gas values, Cv [8]. The reason for this was to ascertain that the apparent deviations, being of the order of 1.5 percent, were fairly constant and not a function of temperature.

The second and third virial coefficients were represented by

B(T)=i=15BiT(1i)/4 (1a)

and

C(T)=i=16CiT(1i)/2, (1b)

respectively. An iterative method was used to optimize both the number of coefficients of B(T) and C(T) and their temperature dependence. The coefficients of eqs (1a) and (1b) and their significance level obtained through a weighted least-squares fit of all PVT data in this region are given in table 2. Weight factors, W, used in the fitting of eq (1) were defined as

W=1σp2+(Pρσρ)2+(PTσT)2 (2)

where σp2,σρ2,σT2 are the respective variances in pressure, density, and temperature. PVT data below 100 K were weighted relatively less than above this temperature, as the uncertainty of the measurements in this region increases rapidly with decreasing density. The weighted standard deviation in density between the virial surface and all of the 329 PVT data points is 0.041 percent. For consistency eq (1) was constrained to give the proper saturation temperature (137.327 K) for the 6.0 mol/1 isochore [2].

Table 2. Least squares estimate of the coefficients of eqs (1a) and (1b).

Coefficient Least squares estimate of coefficient Standard deviation of coefficient Significance level in percenta
B1 −4.43719523 1.10 99.9+
B2 6.88646977 × 10 1.61 × 10 99.9+
B3 −4.00652537 × 102 8.85 × 10 99.9+
b4 1.04730534 × 103 2.15 × 102 99.9+
b5 −1.05492603 × 103 1.96 × 102 99.9+
C1 3.97288149 × 10−1 6.38 × 10−2 99.9+
C2 −2.80769183 × 10 4.33 99.9+
C3 7.95698766 × 102 1.18 × 102 99.9+
C4 −1.12867697 × 104 1.59 × 103 99.9+
C5 8.01450388 × 104 1.08 × 104 99.9+
C6 −2.27594177 × 105 2.93 × 104 99.9+
a

These parameters are significant at the level indicated when applying the standard F-test.

The second and third virial coefficients, calculated from eqs (1a) and (1b), are given in table 3. Also given in this table are the quantities δB and δC, which are the respective estimated uncertainties of the coefficients based on experience gained when fitting the virial surface. A comparison of the second virial coefficient with values obtained by White, Hu, and Johnston [10] is given in figure 2. In the calculation of their data these authors neglected the contribution of the third and higher order virial coefficients, which is the probable reason for their larger negative values, especially at lower temperatures. Temperature scale differences could also account for part of the deviations. Since the data from reference [10] do not represent just the second virial coefficient, further comparisons with eq (1a) were made by converting values from oxygen [11] and argon [12] using corresponding states approach based on critical parameters as follows:

B converted =B(X)ρc(X)ρc(F2) (3)

and

T converted =T(X)Tc(F2)Tc(X) (4)

where X represents either oxygen or argon. The agreement is good as may be seen from figure 2. In fact, the correspondence between values calculated from the second virial coefficient of oxygen and eq (1a) is better than one may justifiably expect from the principle of corresponding states.

Table 3. Second and third virial coefficients of fluorine.

B and δC are estimated uncertainties)

T B δB × 103 C δC × 103
K l/mol l/mol l/mol2 (l/mol)2
80 −0.2396 40 −0.022557 20
85 −.2132 −.013548
90 −.1910 −.007748
95 −.1722 −.004016
100 −.1561 10 −.001624 3
105 −.1422 −.000106
110 −.1301 .000838
115 −.1194 .001409
120 −.1100 .001736
125 −.1017 2 .001905 0.5
130 −.0942 .001973
135 −.0875 .001979
140 −.0815 .001947
145 −.0759 .001893
150 −.0709 0.3 .001828 .03
155 −.0663 .001758
160 −.0621 .001689
165 −.0582 .001621
170 −.0546 .001557
175 −.0512 .001498
180 −.0481 .001442
185 −.0452 .001391
190 −.0425 .001344
195 −.0400 .001301
200 −.0376 .3 .001261 .03
205 −.0354 .001224
210 −.0332 .001190
215 −.0313 .001159
220 −.0294 .001130
225 −.0276 .001104
230 −.0259 .001080
235 −.0243 .001057
240 −.0228 .001037
245 −.0214 .001019
250 −.0200 .3 .001003 .03
255 −.0187 .000988
260 −.0175 .000976
265 −.0163 .000966
270 −.0152 .000957
275 −.0141 .000951
280 −.0131 .000947
285 −.0122 .000946
290 −.0112 .000946
295 −.0104 .000949
300 −.0095 .3 .000955 .04

Figure 2.

Figure 2.

Comparisons of second virial coefficients of fluorine.

3.2. High-Density Region

a. Isotherm Representation

The isotherms in the high-density region (see fig. 1) were represented by polynomials of the form

P=RTρ+i=1nAiρi1, (5)

where A1 = A2 = 0 for T > Tc or p < pc. No more than 3 coefficients were used for the isotherms below 60 K since these consisted of only 4 P — p data points each. As many as 9 coefficients were necessary for the 146 K and 148 K isotherms (slightly above the critical temperature) to adequately represent the data. From 4 to 7 coefficients were needed to represent all of the remaining isotherms. The isotherms in the compressed liquid and vapor phases below the critical temperature were constrained to the corresponding saturation density from reference [2] (see also Appendix). Above 138 K the isotherms were also fitted to the low density data in the virial region to provide a better match of the surfaces around the 6.0 mol/1 isochore.

The standard deviation of the 381 experimental data points in the compressed liquid was only 0.005 percent while the 540 compressed vapor data points exhibit a larger deviation of 0.018 percent. The latter value is higher due mainly to the contribution from the isotherms just above the critical temperature where the deviations are much larger than over the rest of the surface.

b. Isochore Representation

Many calculations of thermodynamic properties require knowledge of the derivatives (∂P/∂T)p and (∂2P/∂T2)p. In the low-density region these derivatives may be calculated directly from eq (1). For densities above 6.0 mol/1 it was first necessary to derive true isochores by calculating pressures at even density increments using the isotherm representations. Density increments of 0.5 mol/1 were used for the 80 isochores between 5.5 and 45.0 mol/1. The true isochores were then represented using functions of the form

P=i=1nAiT(32i). (6)

The number of terms2 of eq (6) varied from 7 at the lowest density to 3 at the 45.0 mol/1 isochore. The good fit of the isotherms was directly carried over in the correlation of these isochores.

4. Derived Properties

4.1. Densities of the Liquid at Freezing

Density calculations of the PVT surface below 56 K were obtained by extrapolating isobars computed from the isotherms between 56 K and 64 K. The density of the liquid in equilibrium with the solid derived from the intersections of these isobars with the melting curve, reference [3], was expressed as a function of either temperature or pressure by

ρ melt L=ρt+0.208(TTt), mol /1 (7)

or

ρ melt L=ρt+0.020P(MN/m2). (8)

A value of 44.862 mol/1 was used for the liquid density, pt, at the triple point.

4.2. The Joule-Thomson Inversion Curve

Calculated points on the Joule-Thomson inversion curve are given in table 4. This curve is defined as the locus of points where the Joule-Thomson coefficient is equal to zero. This condition may be described in classical thermodynamics by the relationship

Tρ2(ρT)p=1ρ (9)

or more conveniently

T(PT)ρ=ρ(Pρ)T (10)

Table 4. The Joule-Thomson inversion curve.

T P Density APa
K MN/m2 Mol/l MN/m2
118 2.732 32.615 0.19
120 4.340 32.411 0.21
122 6.092 32.250 0.22
124 7.649 32.058 0.23
126 9.288 31.895 0.23
128 10.861 31.727 0.25
130 12.373 31.556 0.25
132 13.824 31.381 0.26
134 15.278 31.214 0.26
136 16.583 31.024 0.28
138 17.980 30.864 0.27
140 19.155 30.664 0.26
142 20.811 30.573 0.31
144 21.668 30.322 0.31
a

These estimated pressure errors are due to a 1 percent assumed uncertainty in either the isotherm or the isochore derivative.

Equation (10) was solved by an iterative technique using the isotherm derivatives, (∂P/∂p)T, and the isochore derivatives, (∂P/∂T)p, obtained from eqs (5) and (6), respectively. The computed pressure errors in table 4 are based on an assumed uncertainty of 1 percent in these derivatives. No published Joule-Thomson data for fluorine are available for comparison to values tabulated in table 4. However, a comparison with oxygen [11] and argon [12] using the theory of corresponding states based on critical parameters, is given in figure 3.

Figure 3.

Figure 3.

Comparisons of reduced Joule-Thomson inversion curves of fluorine, oxygen, and argon.

Acknowledgments

This work was carried out at the National Bureau of Standards under the sponsorship of the United States Air Force (MIPR No. FO 4611–70-X-0001).

The authors acknowledge the support of the Air Force Rocket Propulsion Laboratory, Edwards, California. Also, thanks are due to G. K. Johnson of Argonne National Laboratory for supplying the purified fluorine used in these experiments.

5. Appendix

Given below are correlations for different properties of fluorine as reported earlier. The number of significant figures given for the coefficients is not justified on the basis of the uncertainty of the data, but are presented to enable duplication of the calculated values.

Vapor Pressure

The following vapor pressure equation was presented in reference [2]:

ln(PPt)=A1X+A2X2+A3X3+A4X(1X)A5 (11)

where X=(1Tt/T)/(1Tt/Tc) and

  • A1= 7.89592346

  • A2= 3.38765063

  • A3= −1.34590196

  • A4= 2.73138936

  • A5= 1.4327

  • Pt= 2.52 × 10−4 MN/m2

  • Tt= 53.4811 K

  • Tc= 144.31 K.

Saturated Liquid Densities

The saturated liquid densities, pl, were described in [2] with the argument Z = 1 — T/Tc, as

(ρlρcρc)=B1Z0.35+i=26BiZi1 (12)

where

  • B1= 1.81881076

  • B2= 8.75236491 × 10−1

  • B3= −8.50458910 × 10−1

  • B4= 1.37284761

  • B5= −1.01331503

  • B6= 2.73840128 × 10−1

  • pc= 15.10 mol/1

  • Tc= 144.31 K

Saturated Vapor Density

The saturated vapor densities, py, were reported by reference [2] as

ln(ρgρc)=C1(ZZ1)+C2Z0.35+i=37CiZi2 (13)

with the argument, Z, as given above. The coefficients are

  • C1 = 4.85547085

  • C2 = −1.96015519

  • C3 = −1.88066900 ×10−1

  • C4 = 6.21165939

  • C5 = −2.29600897 × 101

  • C6 = 4.69524623 × 101

  • C7 = −4.30650270 × 101

The Melting Curve

Straty and Prydz [3] represented the pressures along the solid-liquid melting curve as

P=Pt+P0[(TTc)C1] (14)

where

P0=249.975 MN/m2
c=2.1845,

and the other variables as defined above.

Footnotes

1

Figures in brackets indicate the literature references at the end of this paper.

2

The coefficients of the 70 isotherms and the 80 isochores discussed above, may be obtained from the Cryogenic Data Center, National Bureau of Standards, Boulder, Colorado 80302.

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