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Dados-Perry Dados encontrados no Perry Líquido saturado Vapor saturado Universidade de Caxias do Sul Temperatura (K) Temperatura (˚C) Pressão (MPa) Pressão (Pa) Volume (dm³/mol) Volume (m³/kg) Volume (dm³/mol) Volume (m³/kg) Centro de Ciências Exatas e da Tecnologia 100 -173.15 0.0000000253 0.02533 0.061397 0.0013923169 32825000 744381.7039707915 Termodinâmica I - ENQ0238A 115 -158.15 0.0000000107 0.010677 0.06273 0.0014225458 895550 20308.6377758124 Docente - Marcelo Godinho 130 -143.15 0.0000176 17.6 0.064117 0.0014539991 61410 1392.6117422954 Alan Zatti, Karine B. Padilha, Morgana Schenatto 145 -128.15 0.00015328 153.28 0.065568 0.0014869039 7863.4 178.3205206703 160 -113.15 0.0008498 849.8 0.067094 0.0015215094 1564 35.4672653468 175 -98.15 0.0033874 3387.4 0.06871 0.0015581559 428.34 9.7135859582 Dados Valor Unidade 190 -83.15 0.010547 10547 0.070434 0.0015972515 148.77 3.3736988911 Propriedades Propano MM 0.044097 kg/mol 205 -68.15 0.027195 27195 0.072288 0.0016392952 61.804 1.4015465905 R 8.314 Pa*m³/mol*K 220 -53.15 0.060583 60583 0.074301 0.0016849446 29.435 0.667505726 Tn 231.1 K 235 -38.15 0.1203 120300 0.076511 0.0017350613 15.57 0.3530852439 Vc 200 cm³/mol 250 -23.15 0.21798 217980 0.078968 0.0017907794 8.9325 0.2025648003 Pc 42.48 bar 265 -8.15 0.36693 366930 0.08174 0.0018536408 5.4561 0.1237295054 Pc 4248000 Pa 280 6.85 0.58173 581730 0.084925 0.001925868 3.4968 0.0792979114 Tc 369.8 K 295 21.85 0.87805 878050 0.088673 0.0020108624 2.3229 0.0526770529 Zc 0.276 - 310 36.85 1.2726 1272600 0.093229 0.0021141801 1.5815 0.0358641177 Vc 0.0002 m³/mol 325 51.85 1.7837 1783700 0.099036 0.0022458671 1.0902 0.0247227703 Tr T/Tc K 340 66.85 2.432 2432000 0.10706 0.0024278296 0.74835 0.0169705422 ω 0.152 - 355 81.85 3.2432 3243200 0.12025 0.0027269429 0.49375 0.0111969068 369.83 96.68 4.2477 4247700 0.2 0.0045354559 0.2 0.0045354559 Van der Waals Equação Cúbica de Van der Waals Equações utilizadas Temp. (K) Pressão (Pa) a b v³ v² v c v líquido (m³/mol) v líquido (m³/kg) v vapor (m³/mol) v vapor (m³/kg) 100 2.53E-02 0.9387568869 0.0000904696 1 -32822.7399246583 3.71E+01 -0.0033528983 9.91E-05 0.0022463059 32822.7387897 744330.4258725083 115 1.07E-02 0.9387568869 0.0000904696 1 -89548.5624207121 8.79E+01 -0.0079543798 1.01E-04 0.0022871461 89548.5614384 2030717.7685194002 130 1.76E+01 0.9387568869 0.0000904696 1 -61.4103177423 5.33E-02 -0.0000048255 1.03E-04 0.0023285728 61.4094497964 1392.5992651745 145 1.53E+02 0.9387568869 0.0000904696 1 -7.8649782566 6.12E-03 -0.0000005541 1.05E-04 0.0023715308 7.8642000558 178.3386637606 160 8.50E+02 0.9387568869 0.0000904696 1 -1.565447024 1.10E-03 -0.0000000999 1.07E-04 0.0024312576 1.5647440745 35.4841389314 175 3.39E+03 0.9387568869 0.0000904696 1 -0.4296086841 2.77E-04 -0.0000000251 1.05E-04 0.0023924105 0.3723208389 8.4432237765 190 1.05E+04 0.9387568869 0.0000904696 1 -0.1498638648 8.90E-05 -0.0000000081 1.11E-04 0.0025245905 0.1492426673 3.3844177001 205 2.72E+04 0.9387568869 0.0000904696 1 -0.0627626519 3.45E-05 -0.0000000031 1.14E-04 0.002589856 6.22E-02 1.4107280707 220 6.06E+04 0.9387568869 0.0000904696 1 -0.0302817773 1.55E-05 -0.0000000014 1.17E-04 0.0026566917 2.98E-02 0.6749341505 235 1.20E+05 0.9387568869 0.0000904696 1 -0.0163314504 7.80E-06 -0.0000000007 1.21E-04 0.0027411157 1.58E-02 0.359251146 250 2.18E+05 0.9387568869 0.0000904696 1 -0.009625748 4.31E-06 -0.0000000004 1.25E-04 0.0028267342 9.16E-03 0.2077207176 265 3.67E+05 0.9387568869 0.0000904696 1 -0.0060949118 2.56E-06 -0.0000000002 1.29E-04 0.0029362561 5.65E-03 0.1281031806 280 5.82E+05 0.9387568869 0.0000904696 1 -0.0040921886 1.61E-06 -0.0000000001 1.36E-04 0.0030926567 3.66E-03 0.083080681 295 8.78E+05 0.9387568869 0.0000904696 1 -0.0028837387 1.07E-06 -0.0000000001 1.42E-04 0.0032252001 2.47E-03 0.055915223 310 1.27E+06 0.9387568869 0.0000904696 1 -0.0021157249 7.38E-07 -0.0000000001 1.52E-04 0.0034373714 1.71E-03 0.0386893221 325 1.78E+06 0.9387568869 0.0000904696 1 -0.0016053263 5.26E-07 -0 1.65E-04 0.0037525273 1.02E-03 0.0231310155 340 2.43E+06 0.9387568869 0.0000904696 1 -0.0012527886 3.86E-07 -0 1.87E-04 0.0042498684 8.45E-04 0.0191580456 355 3.24E+06 0.9387568869 0.0000904696 1 -0.0010005183 2.89E-07 -0 2.10E-04 0.0047657106 5.80E-04 0.0131576053 369.83 4.25E+06 0.9387568869 0.0000904696 1 -0.0008143358 2.21E-07 -0 2.62E-04 0.0059368906 2.91E-04 0.006593144 Peng Robinson Equação Cúbica de Peng Robinson Equações Utilizadas Temp. (K) Pressão (Pa) w ƙ α a b v³ v² v c v líquido (m³/mol) v líquido (m³/kg) v vapor (m³/mol) v vapor (m³/kg) 100 0.02533 0.152 0.6028181683 1.6614205466 1.6821961544 0.0000563156 -0.02533 831.3999985735 -1.588554563 0.0000920972 5.99E-05 0.0013572398 32822.7378682 744330.4049753951 115 0.010677 0.152 0.6028181683 1.6033735844 1.6234233309 0.0000563156 -0.010677 956.1099993987 -1.5157355008 0.0000883918 6.06E-05 0.0013750436 89548.5606887 2030717.7515182437 130 17.6 0.152 0.6028181683 1.5499402827 1.5693218604 0.0000563156 -17.6 1080.8190088453 -1.4475877916 0.0000849495 6.15E-05 0.0013948386 61.4088315946 1392.5852460394 145 153.28 0.152 0.6028181683 1.5003411352 1.5191024892 0.0000563156 -153.28 1205.5213679437 -1.3833221816 0.0000817259 6.25E-05 0.0014169123 7.8636838242 178.326957032 160 849.8 0.152 0.6028181683 1.4539941703 1.4721759683 0.0000563156 -849.8 1330.1921429971 -1.3223494216 0.0000786875 6.36E-05 0.0014416149 1.5643055405 35.4741941749 175 3387.4 0.152 0.6028181683 1.410451254 1.4280885597 0.0000563156 -3387.4 1454.7592365126 -1.2642157729 0.0000758088 6.48E-05 0.0014693884 0.4285912349 9.7192832831 190 10547 0.152 0.6028181683 1.369358594 1.3864820473 0.0000563156 -10547 1579.0660392923 -1.208563018 0.0000730689 6.62E-05 0.0015007625 0.1489480747 3.3777371405 205 27195 0.152 0.6028181683 1.3304310752 1.3470677506 0.0000563156 -27195 1702.8384970659 -1.1551024736 0.0000704508 6.77E-05 0.0015363798 0.0619306933 1.4044196507 220 60583 0.152 0.6028181683 1.2934349289 1.3096089777 0.0000563156 -60583 1825.6682315774 -1.1035974441 0.0000679398 6.94E-05 0.0015748292 2.95E-02 0.6694285383 235 120300 0.152 0.6028181683 1.2581756505 1.2739087916 0.0000563156 -120300 1947.0152324704 -1.0538509873 0.0000655231 7.16E-05 0.0016238305 1.56E-02 0.3543617456 250 217980 0.152 0.6028181683 1.2244893432 1.2398012463 0.0000563156 -217980 2066.2243239726 -1.0056971509 0.0000631894 7.40E-05 0.0016779293 8.97E-03 0.203372327 265 366930 0.152 0.6028181683 1.1922363719 1.2071449604 0.0000563156 -366930 2182.5461143007 -0.9589945466 0.0000609282 7.68E-05 0.0017410533 5.48E-03 0.1241904062 280 581730 0.152 0.6028181683 1.161296614 1.1758183094 0.0000563156 -581730 2295.1595219037 -0.9136215417 0.0000587301 8.01E-05 0.0018154659 3.51E-03 0.0794978309 295 878050 0.152 0.6028181683 1.1315658432 1.1457157635 0.0000563156 -878050 2403.1820812191 -0.8694725983 0.0000565865 8.40E-05 0.0019042937 2.32E-03 0.0526689918 310 1272600 0.152 0.6028181683 1.1029529313 1.116745055 0.0000563156 -1272600 2505.6727584527 -0.8264554397 0.000054489 8.87E-05 0.0020119237 1.57E-03 0.0356829082 325 1783700 0.152 0.6028181683 1.0753776536 1.088824956 0.0000563156 -1783700 2601.5998516832 -0.7844888281 0.0000524299 9.46E-05 0.0021445592 1.07E-03 0.0243730145 340 2432000 0.152 0.6028181683 1.0487689454 1.0618835131 0.0000563156 -2432000 2689.8004436249 -0.7435007992 0.0000504013 1.02E-04 0.0023104077 7.23E-04 0.0163872983 355 3243200 0.152 0.6028181683 1.0230635012 1.0358566295 0.0000563156 -3243200 2768.827223176 -0.7034272422 0.0000483952 1.11E-04 0.0025165255 4.30E-04 0.0097550641 369.83 4247700 0.152 0.6028181683 0.9984818236 1.0109675647 0.0000563156 -4247700 2835.5548158821 -0.6646505912 0.0000464231 1.21E-04 0.0027426702 1.25E-04 0.0028387055 Redlich-Kwonh Equação Cúbica de Redlich-Kwonh Equações Utilizadas Temp. (K) Pressão (Pa) a b v³ v² v c v líquido (m³/mol) v líquido (m³/kg) v vapor (m³/mol) v vapor (m³/kg) 100 0.02533 18.1948278373 0.0000625536 0.02533 -831.4 1.7674756844 -0.0001138153 6.65E-05 0.0015074167 32822.7377083 744330.4013492981 115 0.010677 18.1948278373 0.0000625536 0.010677 -956.11 1.6368682802 -0.0001061333 6.75E-05 0.0015307264 8954.85606182 203071.7749919496 130 17.6 18.1948278373 0.0000625536 17.6 -1080.82 1.5281826686 -0.0000998226 6.87E-05 0.0015569032 61.4088133312 1392.5848318752 145 153.28 18.1948278373 0.0000625536 153.28 -1205.53 1.4355873149 -0.0000945184 6.99E-05 0.0015862341 7.8636967817 178.3272508713 160 849.8 18.1948278373 0.0000625536 849.8 -1330.24 1.355212756 -0.0000899789 7.14E-05 0.0016191171 1.5643371675 35.4749113885 175 3387.4 18.1948278373 0.0000625536 3387.4 -1454.95 1.2843740246 -0.0000860363 7.30E-05 0.0016560572 0.4286337697 9.7202478555 190 10547 18.1948278373 0.0000625536 10547 -1579.66 1.2211367886 -0.0000825703 7.49E-05 0.0016977137 0.1489966804 3.3788393852 205 27195 18.1948278373 0.0000625536 27195 -1704.37 1.1640609325 -0.000079492 7.69E-05 0.0017449466 6.20E-02 1.4055912185 220 60583 18.1948278373 0.0000625536 60583 -1829.08 1.1120423655 -0.0000767342 7.93E-05 0.0017988919 2.96E-02 0.6706135453 235 120300 18.1948278373 0.0000625536 120300 -1953.79 1.0642122862 -0.0000742449 8.21E-05 0.0018610703 1.57E-02 0.3555635779 250 217980 18.1948278373 0.0000625536 217980 -2078.5 1.0198712573 -0.0000719831 8.53E-05 0.0019335647 9.02E-03 0.2045642116 265 366930 18.1948278373 0.0000625536 366930 -2203.21 0.9784447944 -0.0000699162 8.90E-05 0.0020193287 5.53E-03 0.1253674932 280 581730 18.1948278373 0.0000625536 581730 -2327.92 0.9394527755 -0.0000680176 9.36E-05 0.002122707 3.56E-03 0.0806616854 295 878050 18.1948278373 0.0000625536 878050 -2452.63 0.902487117 -0.0000662658 9.92E-05 0.0022504785 2.37E-03 0.0538278389 310 1272600 18.1948278373 0.0000625536 1272600 -2577.34 0.8671951408 -0.0000646427 1.06E-04 0.0024140573 1.63E-03 0.0368549207 325 1783700 18.1948278373 0.0000625536 1783700 -2702.05 0.8332648409 -0.0000631334 1.16E-04 0.0026345851 1.13E-03 0.0255975713 340 2432000 18.1948278373 0.0000625536 2432000 -2826.76 0.8004126311 -0.000061725 1.31E-04 0.0029601848 7.84E-04 0.0177717786 355 3243200 18.1948278373 0.0000625536 3243200 -2951.47 0.7683654856 -0.0000604069 1.57E-04 0.003552985 5.28E-04 0.0119823125 369.83 4247700 18.1948278373 0.0000625536 4247700 -3074.76662 0.7371625068 -0.0000591833 2.11E-04 0.0047849362 3.02E-04 0.0068454448 Rackett Equação de Rackett (Líquido Saturado) Equações Utilizadas Temperatura (K) Pressão (Pa) Tr (K) Vc (cm³/mol) Vc(m³/mol) Zc V sat (m³/mol) V sat (m³/kg) 100 0.02533 0.2703945056 200 0.0002 0.276 0.0000616728 0.0013986668 115 0.010677 0.3109536814 200 0.0002 0.276 0.0000628601 0.0014255928 130 17.6 0.3515128573 200 0.0002 0.276 0.0000641227 0.0014542284 145 153.28 0.3920720331 200 0.0002 0.276 0.0000654703 0.001484789 160 849.8 0.4326312089 200 0.0002 0.276 0.0000669141 0.001517533 175 3387.4 0.4731903848 200 0.0002 0.276 0.0000684681 0.0015527748 190 10547 0.5137495606 200 0.0002 0.276 0.0000701492 0.0015909012 205 27195 0.5543087364 200 0.0002 0.276 0.0000719789 0.001632397 220 60583 0.5948679123 200 0.0002 0.276 0.0000739844 0.0016778798 235 120300 0.6354270881 200 0.0002 0.276 0.0000762013 0.0017281552 250 217980 0.675986264 200 0.0002 0.276 0.000078677 0.0017843015 265 366930 0.7165454398 200 0.0002 0.276 0.0000814773 0.0018478102 280 581730 0.7571046156 200 0.0002 0.276 0.0000846971 0.0019208307 295 878050 0.7976637915 200 0.0002 0.276 0.0000884804 0.0020066311 310 1272600 0.8382229673 200 0.0002 0.276 0.0000930628 0.002110555 325 1783700 0.8787821431 200 0.0002 0.276 0.0000988724 0.0022423097 340 2432000 0.919341319 200 0.0002 0.276 0.000106829 0.0024227563 355 3243200 0.9599004948 200 0.0002 0.276 0.000119669 0.0027139511 369.83 4247700 1 200 0.0002 0.276 0.0002 0.0045357645 Virial Coeficiente do Virial (Vapor Saturado) Equações Utilizadas Temperatura (K) Pressão (Pa) Tr (K) Pr (Pa) w B˚ B¹ B*Pc/R*Tc z v (m³/mol) v(m³/kg) 100 0.02533 0.2703945056 0.000000006 0.152 -3.3377069575 -41.6572602231 -9.6696105114 0.9999997867 32822.7328346841 744330.290828948 115 0.010677 0.3109536814 0.0000000025 0.152 -2.6522644839 -23.0994145567 -6.1633754965 0.9999999502 89548.5578687831 2030717.6875702005 130 17.6 0.3515128573 0.0000041434 0.152 -2.1650527999 -13.7469419301 -4.2545879733 0.9999498495 61.4071475201 1392.5470558119 145 153.28 0.3920720331 0.0000360854 0.152 -1.8046743187 -8.6389239732 -3.1177907626 0.9997130457 7.8626309236 178.3030801094 160 849.8 0.4326312089 0.0002000612 0.152 -1.5295897638 -5.6664180284 -2.3908853042 0.9988943853 1.5636258733 35.4587811718 175 3387.4 0.4731903848 0.0007974669 0.152 -1.31418847 -3.8455347609 -1.8987097537 0.996800108 0.4281438027 9.7091367366 190 10547 0.5137495606 0.0024829908 0.152 -1.1419267234 -2.6818000355 -1.5495603288 0.9925108568 0.1486517209 3.3710166422 205 27195 0.5543087364 0.0064022883 0.152 -1.0017001327 -1.9110818844 -1.2921845791 0.9850752159 0.0617368136 1.4000229856 220 60583 0.5948679123 0.0142625421 0.152 -0.885812161 -1.3849199866 -1.096319999 0.9737146519 0.0293977188 0.6666602889 235 120300 0.6354270881 0.0283212091 0.152 -0.7887807827 -1.0161872926 -0.9432412512 0.9579594052 0.0155582004 0.3528176607 250 217980 0.675986264 0.0513171834 0.152 -0.7066085769 -0.751818829 -0.8208850389 0.9376828933 0.0089410675 0.2027590879 265 366930 0.7165454398 0.0863832192 0.152 -0.6363205583 -0.5584366311 -0.7212029262 0.913055297 0.0054823878 0.1243256415 280 581730 0.7571046156 0.1369517621 0.152 -0.5756626253 -0.4144440118 -0.6386581151 0.8844738858 0.003539416 0.0802643255 295 878050 0.7976637915 0.2067118676 0.152 -0.5228995716 -0.3055135022 -0.5693376239 0.8524580847 0.0023811449 0.0539978886 310 1272600 0.8382229673 0.2995974292 0.152 -0.4766766146 -0.2219261179 -0.5104093845 0.817569614 0.0016557873 0.0375487507 325 1783700 0.8787821431 0.4199213692 0.152 -0.4359224901 -0.1569561086 -0.4597798186 0.7802966612 0.0011820377 0.0268053988 340 2432000 0.919341319 0.5725451421 0.152 -0.3997803705 -0.1058645825 -0.4158717871 0.7410043838 0.0008612835 0.0195315675 355 3243200 0.9599004948 0.7635190809 0.152 -0.3675577933 -0.065257655 -0.3774769569 0.6997492337 0.0006368059 0.0144410253 369.83 4247700 1 1 0.152 -0.339 -0.033 -0.344016 0.655984 0.0004748447 0.0107681854 Gás Ideal Equação de Estado dos Gases Reais Equação Utilizada Temperatura (K) Pressão (Pa) v (m³/mol) v (m³/kg) 100 0.02533 32822.7398341887 744330.4495586707 115 0.010677 89548.5623302426 2030717.7887439635 130 17.6 61.4102272727 1392.6168962226 145 153.28 7.8648877871 178.3542596335 160 849.8 1.5653565545 35.4980283122 175 3387.4 0.4295182146 9.7403046593 190 10547 0.1497733953 3.3964531664 205 27195 0.0626721824 1.4212346052 220 60583 0.0301913078 0.6846567293 235 120300 0.0162409809 0.368301265 250 217980 0.0095352785 0.2162341762 265 366930 0.0060044423 0.1361644163 280 581730 0.004001719 0.090748101 295 878050 0.0027932692 0.0633437462 310 1272600 0.0020252554 0.0459272826 325 1783700 0.0015148568 0.0343528303 340 2432000 0.0011623191 0.0263582348 355 3243200 0.0009100487 0.0206374292 369.83 4247700 0.0007238662 0.0164153171 Diagrama
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