Diagrama PxV Propano

Esta é uma pré-visualização de arquivo. Entre para ver o arquivo original

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