Bolha T Nrtl e Wilson

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nrtl
	Encontre a temperatura e a composição da fase vapor do sistema etanol (1)/tolueno(2) na pressão de 180 kPa e x1=0,7. Dados:
	Utilize o modelo de Wilson	T (ºC)	P sat
	P (kpa)	75	T (K)	Modelo
	x1	0.55000000000000004	x2	0.44999999999999996
	R	1.9870000000000001	Antoine
	Espécie	Ai	Bi	Ci	b12 (cm³/mol)	-253.88	T1 sat	(B/A - lnP)-C
	1	16.5938	3644.3	239.79	b21 (cm³/mol)	845.21	P1 sat
	2	16.262	3799.89	226.35	alfa (cal/mol)	0.2994
	T (Celsius)	T (K)	P1 sat	P2 sat 	Tal 21	Tal 12	G21	G12	Gama 1	Gama 2	Y1	Y2	F(Tk)
	K-1	T1 sat	57.0662572949	330.0662572949	75	17.3665775073	1.2887409572	-0.3871056356	0.6798731498	1.1228829351	1.0913534013	1.2614009369	0.6002443707	0.1314373028	-0.2683183264
	K 	T2 sat	91.7785293295	364.7785293295	271.1598864627	75	1.1661045543	-0.3502687193	0.7053002336	1.1105667322	1.0899487606	1.2393104986	2.1673694694	0.5576897244	1.7250591937
	k+1	61.7386982374	334.7386982374	90.7147436405	21.5850243295	1.2707521019	-0.3817022321	0.6835447321	1.1210678273	1.0912300834	1.258224371	0.7259314867	0.162952822	-0.1111156914
	63.556551552	336.556551552	97.5287971018	23.4461755627	1.2638883493	-0.3796405321	0.684950866	1.1203760359	1.0911756524	1.2570063684	0.7804210246	0.176831952	-0.0427470235
	64.6931514103	337.6931514103	102.0020838495	24.6775718476	1.2596343829	-0.3783627467	0.6858238009	1.1199474968	1.091139862	1.2562498452	0.8161892911	0.1860071749	0.002196466
	64.6376038104	337.6376038104	101.7795648866	24.6161439309	1.2598416159	-0.3784249943	0.6857812499	1.1199683694	1.0911416421	1.2562867284	0.8144100915	0.1855496095	-0.000040299
	64.6386045917	337.6386045917	101.7835703515	24.6172495092	1.2598378817	-0.3784238726	0.6857820166	1.1199679933	1.0911416101	1.2562860638	0.8144421181	0.1855578449	-0.000000037
	64.638605511	337.638605511	101.783574031	24.6172505248	1.2598378782	-0.3784238716	0.6857820173	1.1199679929	1.09114161	1.2562860632	0.8144421475	0.1855578525	0
	64.638605511	337.638605511	101.783574031	24.6172505248	1.2598378782	-0.3784238716	0.6857820173	1.1199679929	1.09114161	1.2562860632	0.8144421475	0.1855578525	0
wilson
	Encontre a temperatura e a composição da fase vapor do sistema etanol (1)/tolueno(2) na pressão de 180 kPa e x1=0,7. Dados:
	Utilize o modelo de Wilson	T (ºC)	P sat
	P (kpa)	180	T (K)	Modelo
	x1	0.7	x2	0.3
	R	1.9870000000000001	Antoine
	Espécie	Ai	Bi	Ci	V1 (cm³/mol)	56.68	T1 sat	(B/A - lnP)-C
	1	14.0098	3103.01	219.78	V2 (cm³/mol)	106.85	P1 sat
	2	16.6758	3674.49	226.45	a12 (cal/mol)	1556.45
	a21 (cal/mol)	210.52
	T (Celsius)	T (K)	P1 sat	P2 sat 	ᴧ21	ᴧ12	gama 1	gama 2	Y1	Y2	F(Tk)
	K-1	T1 sat	132.1611593835	405.1611593835	180	619.7732369711	0.4084024654	0.272711433	1.1521881807	2.1780179227	0.8065317265	2.2497953636	2.0563270901
	K 	T2 sat	93.5482750165	366.5482750165	60.7287192135	180	0.3973058851	0.2224610324	1.1577496191	2.2840671465	0.2734225338	0.685220144	-0.0413573223
	k+1	94.3095551659	367.3095551659	62.2040569144	184.9729969721	0.3975439699	0.2234485264	1.1576364118	2.2818722165	0.2800376493	0.703474571	-0.0164877797
	94.8142616518	367.8142616518	63.1978196751	188.3320439232	0.3977013482	0.2241033563	1.1575614486	2.2804193323	0.2844930655	0.7157933898	0.0002864552
	94.8056427309	367.8056427309	63.1807435318	188.2742616836	0.3976986637	0.2240921727	1.1575627281	2.280444128	0.2844165094	0.7155815575	-0.0000019331
	94.8057005038	367.8057005038	63.1808579816	188.2746489513	0.3976986817	0.2240922477	1.1575627195	2.2804439618	0.2844170225	0.7155829773	-0.0000000002
	94.8057005106	367.8057005106	63.1808579948	188.2746489962	0.3976986817	0.2240922477	1.1575627195	2.2804439618	0.2844170226	0.7155829774	0
Plan3