ABP LECCION 8-Andrea Oseguera

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Ejercicio 1
		Datos de Equilibrio Obtenidos del ABP1 Benceno/Tolueno a 101.325KPa
		No.	Formula	Sustancia	Peso Molecular	Temperutara de Ebullicion [°C]
		1	C6H6	Benceno	78.114	80.1
		2	C7H8	Tolueno	92.14	110.6
		PT [KPa]	101.33
		T [°C]	x1	y1
		80.1	0.9950	0.9981
		84.6	0.7864	0.9042
		89.1	0.6054	0.7946
		93.6	0.4474	0.6677
		98.1	0.3085	0.5218
		102.6	0.1858	0.3548
		107.1	0.0768	0.1649
		110.6	-0.0000	-0.0000
		Datos de Operación 
		xF	0.44
		PT [Kpa]	101.33
		mF* [kmol/h]	346.78
		xD	0.9748
		xB	0.0235
		α
		2.6043
		2.5618
		2.5212
		2.4824
		2.4452
		2.4097
		2.3756
		2.3500
		Prom: 	2.4688
		Balance Global 
		-0.00034378
		Balance por componentes 
		-0.0001506036
		D [kmol/h]	151.8280379741
		B [kmol/h]	194.9523058059
		PARA CASO I
		Datos
		Z	0.44
		q	1
		xD	0.9748
		xB	0.0235
		D [kmol/h]	151.8280379741
		B [kmol/h]	194.9523058059
		R 	3.5
		Punto pinch 
		xp	0.44
		yp	0.5588
		S
		3.5045811518
		Rectas
		Linea de Alimentación
		Puntos 
		x	y
		0.44	0.4400
		0.44000	0.5588
		Linea de Rectificación 			Linea de Agotamiento
		Puntos 			Puntos 
		x	y		x	y
		0.9748	0.9748		0.0235	0.0235
		0.44000	0.5588		0.44000	0.56
		Linea de Rectificacion											Alimentacion
		Plato 1		Plato 2		Plato 3		Plato 4		Plato 5			Plato 6
		x	y	x	y	x	y	x	y	x	y		x	y
		0.9748	0.9748	0.94332	0.9503136151	0.88894	0.9080189072	0.79501	0.8349643371	0.67212	0.7393818501		0.53664	0.6340085545
		0.94332	0.9748	0.88894	0.9503136151	0.79501	0.9080189072	0.67212	0.8349643371	0.53664	0.7393818501		0.41530	0.6340085545
		0.94332	0.9503136151	0.88894	0.9080189072	0.79501	0.8349643371	0.67212	0.7393818501	0.53664	0.6340085545		0.41530	0.5405043558
		Linea de Agotamiento 
		Plato 7		Plato 8		Plato 9		Plato 10		Plato 11		Plato 12		Plato 13
		x	y	x	y	x	y	x	y	x	y	x	y	x	y
		0.41530	0.5405043558	0.32635	0.4127658724	0.22841	0.2868787047	0.14680	0.1819821872	0.08655	0.1045432368	0.04865	0.0558322986	0.02598	0.026693661
		0.32635	0.5405043558	0.22841	0.4127658724	0.14680	0.2868787047	0.08655	0.1819821872	0.04865	0.1045432368	0.02598	0.0558322986	0.01242	0.026693661
		0.32635	0.4127658724	0.22841	0.2868787047	0.14680	0.1819821872	0.08655	0.1045432368	0.04865	0.0558322986	0.02598	0.026693661	0.01242	0.0092630748
	 
		Datos
		Z	0.44		xp	0.4400
		q	1.37		yp	0.5588
		xD	0.9748
		xB	0.0235
		D [kmol/h]	151.8280379741
		B [kmol/h]	194.9523058059
		R 	3.5
		Eficiencia de murphee
		70%
		xe	ye	y ope	y' e
		0.9950	0.9981	0.9905351293	0.9958208648
		0.7864	0.9042	0.8282973998	0.8814025169
		0.6054	0.7946	0.6875025266	0.762469933
		0.4474	0.6677	0.5645680409	0.6367808049
		0.3085	0.5218	0.3898578479	0.4821995197
		0.1858	0.3548	0.2321553554	0.3180378317
		0.0768	0.1649	0.0919609334	0.1430430254
		-0.0000	-0.0000	-0.0067060861	-0.0020
		Linea de Rectificacion																	Alimentacion
		Plato 1		Plato 2		Plato 3		Plato 4		Plato 5		Plato 6		Plato 7		Plato 8			Plato 9
		x	y	x	y	x	y	x	y	x	y	x	y	x	y	x	y		x	y
		0.9748	0.9748	0.95671	0.9607298807	0.93106	0.9407799424	0.89469	0.9124930436	0.84312	0.8723852181	0.77272	0.817627584	0.68938	0.7528062069	0.59328	0.678059632		0.49928	0.6049533153
		0.95671	0.9748	0.93106	0.9607298807	0.89469	0.9407799424	0.84312	0.9124930436	0.77272	0.8723852181	0.68938	0.817627584	0.59328	0.7528062069	0.49928	0.678059632		0.41879	0.6049533153
		0.95671	0.9607298807	0.93106	0.9407799424	0.89469	0.9124930436	0.84312	0.8723852181	0.77272	0.817627584	0.68938	0.7528062069	0.59328	0.678059632	0.49928	0.6049533153		0.41879	0.5315797574
		Linea de Agotamiento 
		Plato 10		Plato 11		Plato 12		Plato 13		Plato 14		Plato 15		Plato 16		Plato 17		Plato 18
		x	y	x	y	x	y	x	y	x	y	x	y	x	y	x	y	x	y
		0.41879	0.5315797574	0.35289	0.4468726313	0.28213	0.3559269534	0.21416	0.2685569003	0.15499	0.1925152767	0.10760	0.1315937549	0.07070	0.0841708777	0.04561	0.0519143128	0.02854	0.0299737212
		0.35289	0.5315797574	0.28213	0.4468726313	0.21416	0.3559269534	0.15499	0.2685569003	0.10760	0.1925152767	0.07070	0.1315937549	0.04561	0.0841708777	0.02854	0.0519143128	0.01693	0.0299737212
		0.35289	0.4468726313	0.28213	0.3559269534	0.21416	0.2685569003	0.15499	0.1925152767	0.10760	0.1315937549	0.07070	0.0841708777	0.04561	0.0519143128	0.02854	0.0299737212	0.01693	0.0150499511
		PARA CASO 2 
		Datos
		Z	0.44		Punto pinch 			Rectas
		q	1.37		xp	0.48		Linea de Alimentación
		xD	0.9748		yp	0.5904		Puntos 
		xB	0.0235					x	y
		D [kmol/h]	151.8280379741		S			0.44	0.4400
		B [kmol/h]	194.9523058059		4.1627356021			0.48063	0.5904
		R 	3.5
								Linea de Rectificación 
		Eficiencia de murphee						Puntos 
		65%						x	y
								0.9748	0.9748
		xe	ye	y ope	y' e			0.48063	0.5904
		0.9950	0.9981	0.9905351293	0.9954433122
		0.7864	0.9042	0.8282973998	0.8776092943
		0.6054	0.7946	0.6875025266	0.7571151183			Linea de Agotamiento
		0.4474	0.6677	0.5492341017	0.6262558716			Puntos 
		0.3085	0.5218	0.3770429961	0.4711184879			x	y
		0.1858	0.3548	0.2248741397	0.3093549436			0.0235	0.0235
		0.0768	0.1649	0.0895990116	0.1385676319			0.48063	0.5904
		-0.0000	-0.0000	-0.0056058726	-0.0019692885
		Linea de Rectificacion																	Alimentación
		Plato 1		Plato 2		Plato 3		Plato 4		Plato 5		Plato 6		Plato 7		Plato 8			Plato 9
		x	y	x	y	x	y	x	y	x	y	x	y	x	y	x	y		x	y
		0.9748	0.9748	0.95849	0.9621136644	0.93603	0.9446472017	0.90511	0.9205994917	0.86255	0.8874907641	0.80394	0.8419068876	0.73281	0.7865858371	0.64970	0.721946217		0.55260	0.6464183584
		0.95849	0.9748	0.93603	0.9621136644	0.90511	0.9446472017	0.86255	0.9205994917	0.80394	0.8874907641	0.73281	0.8419068876	0.64970	0.7865858371	0.55260	0.721946217		0.47173	0.6464183584
		0.95849	0.9621136644	0.93603	0.9446472017	0.90511	0.9205994917	0.86255	0.8874907641	0.80394	0.8419068876	0.73281	0.7865858371	0.64970	0.721946217	0.55260	0.6464183584		0.47173	0.5794034477
		Linea de Agotamiento 
		Plato 10		Plato 11		Plato 12		Plato 13		Plato 14		Plato 15		Plato 16		Plato 17		Plato 18		Plato 19
		x	y	x	y	x	y	x	y	x	y	x	y	x	y	x	y	x	y	x	y
		0.47173	0.5794034477	0.40544	0.4971968274	0.33187	0.4059515543	0.25910	0.3157028888	0.19065	0.2308053224	0.13567	0.1626158035	0.09212	0.1086039219	0.06039	0.0692567742	0.03890	0.042600995	0.02434	0.0245430008
		0.40544	0.5794034477	0.33187	0.4971968274	0.25910	0.4059515543	0.19065	0.3157028888	0.13567	0.2308053224	0.09212	0.1626158035	0.06039	0.1086039219	0.03890	0.0692567742	0.02434	0.042600995	0.01448	0.0245430008
		0.40544	0.4971968274	0.33187	0.4059515543	0.25910	0.3157028888	0.19065	0.2308053224	0.13567	0.1626158035	0.09212	0.1086039219	0.06039	0.0692567742	0.03890	0.042600995	0.02434	0.0245430008	0.01448	0.012309588
	caso iii)
		Datos
		Z	0.44		Punto pinch 			Rectas
		q	0.3333333333		xp	0.3470		Linea de Alimentación
		xD	0.9748		yp	0.4865		Puntos 
		xB	0.0235					x	y
		D [kmol/h]	151.8280379741		S			0.44	0.4400
		B [kmol/h]	194.9523058059		2.3187172775			0.34699	0.4865
		R 	3.5
								Linea de Rectificación 
		Eficiencia de murphee						Puntos 
		80%						x	y
								0.9748	0.9748
		xe	ye	y ope	y' e			0.34699	0.4865
		0.9950	0.9981	0.9905351293	0.9965759698
		0.7864	0.9042	0.8282973998	0.8889889622
		0.6054	0.7946	0.6875025266	0.7731795625			Linea de Agotamiento
		0.4474	0.6677	0.5645680409	0.647096914			Puntos 
		0.3085	0.5218	0.4314604442	0.5037117064			x	y
		0.1858	0.3548	0.2558475065	0.3350451871			0.0235	0.0235
		0.0768	0.1649	0.09973105	0.1518944905			0.34699	0.4865
		-0.0000	-0.0000	-0.0101416912	-0.0020372405
		Linea de Rectificacion																	Alimentacion
		Plato 1		Plato 2		Plato 3		Plato 4		Plato 5		Plato 6		Plato 7		Plato 8			Plato 9
		x	y	x	y	x	y	x	y	x	y	x	y	x	y	x	y		x	y
		0.9748	0.9748	0.95281	0.9576987194	0.91966	0.9319112778	0.86966	0.8930257606	0.79427	0.834389333	0.70110	0.7619247334	0.59132	0.6765378016	0.48428	0.5932852782		0.39527	0.5240531435
		0.95281	0.9748	0.91966	0.9576987194	0.86966	0.9319112778	0.79427	0.8930257606	0.70110	0.834389333	0.59132	0.7619247334	0.48428	0.6765378016	0.39527	0.5932852782		0.32823	0.5240531435
		0.95281	0.9576987194	0.91966	0.9319112778	0.86966	0.8930257606	0.79427	0.834389333	0.70110	0.7619247334	0.59132	0.6765378016	0.484280.5932852782	0.39527	0.5240531435		0.32823	0.4596519796
		Linea de Agotamiento 
		Plato 10		Plato 11		Plato 12		Plato 13		Plato 14		Plato 15		Plato 16		Plato 17
		x	y	x	y	x	y	x	y	x	y	x	y	x	y	x	y
		0.32823	0.4596519796	0.27648	0.3855861469	0.22260	0.3084699622	0.17001	0.2331949585	0.12518	0.1690310374	0.08697	0.1143381306	0.05803	0.07292423	0.03738	0.0433639908
		0.27648	0.4596519796	0.22260	0.3855861469	0.17001	0.3084699622	0.12518	0.2331949585	0.08697	0.1690310374	0.05803	0.1143381306	0.03738	0.07292423	0.02264	0.0433639908
		0.27648	0.3855861469	0.22260	0.3084699622	0.17001	0.2331949585	0.12518	0.1690310374	0.08697	0.1143381306	0.05803	0.07292423	0.03738	0.0433639908	0.02264	0.022264608
Ejercicio 1
Equilibrio liquido-vapor de Benceno/Tolueno 
a 101.325 KPa al 100%
Curva de Equilibrio	0.99503102256333897	0.78644561556101333	0.60542880768580476	0.44737469903707766	0.30853329795043022	0.18583626808520987	7.6761015625631188E-2	-4.7351692688264262E-6	0.99808617995868043	0.90416185282428474	0.79459882149167782	0.66772913231079478	0.52177452189911866	0.35484460725779099	0.16493535058559944	-1.1127806207993125E-5	x=y	0	0.1	0.2	0.3	0.4	0.5	0.6	0.7	0.8	0.9	1	0	0.1	0.2	0.3	0.4	0.5	0.6	0.7	0.8	0.9	1	x Fraccion mol de Benceno en liquido
y Fracción mol de Benceno en vapor
Equilibrio liquido-vapor de Benceno/Tolueno 
a 101.325 KPa al 65%
Curva de Equilibrio	0.99503102256333897	0.78644561556101333	0.60542880768580476	0.44737469903707766	0.30853329795043022	0.18583626808520987	7.6761015625631188E-2	-4.7351692688264262E-6	0.99808617995868043	0.90416185282428474	0.79459882149167782	0.66772913231079478	0.52177452189911866	0.35484460725779099	0.16493535058559944	-1.1127806207993125E-5	x=y	0	0.1	0.2	0.3	0.4	0.5	0.6	0.7	0.8	0.9	1	0	0.1	0.2	0.3	0.4	0.5	0.6	0.7	0.8	0.9	1	Rectificacion	0.9748	0.95848899709203195	0.95848899709203195	0.95848899709203195	0.95848899709203195	0.93603211648398432	0.93603211648398432	0.93603211648398432	0.93603211648398432	0.905113632	22586783	0.90511363222586783	0.90511363222586783	0.90511363222586783	0.86254526819062305	0.86254526819062305	0.86254526819062305	0.86254526819062305	0.80393742695528048	0.80393742695528048	0.80393742695528048	0.80393742695528048	0.73281036199765492	0.73281036199765492	0.73281036199765492	0.73281036199765492	0.64970227903056266	0.64970227903056266	0.64970227903056266	0.64970227903056266	0.55259503218184314	0.55259503218184314	0.55259503218184314	0.55259503218184314	0.47172730653356598	0.47172730653356598	0.47172730653356598	0.9748	0.9748	0.9748	0.96211366440491375	0.96211366440491375	0.96211366440491375	0.96211366440491375	0.94464720170976557	0.94464720170976557	0.94464720170976557	0.94464720170976557	0.92059949173123057	0.92059949173123057	0.92059949173123057	0.92059949173123057	0.88749076414826233	0.88749076414826233	0.88749076414826233	0.88749076414826233	0.84190688763188493	0.84190688763188493	0.84190688763188493	0.84190688763188493	0.78658583710928709	0.78658583710928709	0.78658583710928709	0.78658583710928709	0.72194621702377093	0.72194621702377093	0.72194621702377093	0.72194621702377093	0.6464183583636558	0.6464183583636558	0.6464183583636558	0.6464183583636558	0.57940344774898844	Linea de Rectificacion	
0.9748	0.48063162217659133	0.9748	0.59044681724846004	Linea de Agotamiento	
2.35E-2	0.48063162217659133	2.35E-2	0.59044681724846004	Agotamiento	0.47172730653356598	0.40544376004040739	0.40544376004040739	0.40544376004040739	0.40544376004040739	0.33187230953084135	0.33187230953084135	0.33187230953084135	0.33187230953084135	0.25910442797489258	0.25910442797489258	0.25910442797489258	0.25910442797489258	0.19065116025911427	0.19065116025911427	0.19065116025911427	0.19065116025911427	0.13566966214015286	0.13566966214015286	0.13566966214015286	0.13566966214015286	9.2119653005715035E-2	9.2119653005715035E-2	9.2119653005715035E-2	9.2119653005715035E-2	6.0393880992050938E-2	6.0393880992050938E-2	6.0393880992050938E-2	6.0393880992050938E-2	3.8901213242104278E-2	3.8901213242104278E-2	3.8901213242104278E-2	3.8901213242104278E-2	2.43409760062493E-2	2.43409760062493E-2	2.43409760062493E-2	2.43409760062493E-2	1.4477123327239562E-2	1.4477123327239562E-2	1.4477123327239562E-2	0.57940344774898844	0.57940344774898844	0.57940344774898844	0.49719682738589399	0.49719682738589399	0.49719682738589399	0.49719682738589399	0.40595155428895224	0.40595155428895224	0.40595155428895224	0.40595155428895224	0.31570288881789249	0.31570288881789249	0.31570288881789249	0.31570288881789249	0.23080532238630336	0.23080532238630336	0.23080532238630336	0.23080532238630336	0.16261580353902555	0.16261580353902555	0.16261580353902555	0.16261580353902555	0.10860392190119642	0.10860392190119642	0.10860392190119642	0.10860392190119642	6.9256774175439753E-2	6.9256774175439753E-2	6.9256774175439753E-2	6.9256774175439753E-2	4.2600994999647569E-2	4.2600994999647569E-2	4.2600994999647569E-2	4.2600994999647569E-2	2.4543000849197819E-2	2.4543000849197819E-2	2.4543000849197819E-2	2.4543000849197819E-2	1.2309587952612094E-2	Linea de alimentacion	0.44	0.48063162217659133	0.44	0.59044681724846004	Curva de Equilibrio nueva	0.99503102256333897	0.78644561556101333	0.60542880768580476	0.44737469903707766	0.30853329795043022	0.18583626808520987	7.6761015625631188E-2	-4.7351692688264262E-6	0.99544331224556004	0.87760929425995982	0.75711511828589717	0.62625587161304086	0.47111848787577038	0.30935494360531118	0.13856763193325738	-1.9692884689597148E-3	x Fraccion mol de Benceno en liquido
y Fracción mol de Benceno en vapor
Ejercicio 2
	a	Datos de Equilibrio Obtenidos del ABP1 Hexano/p-xileno a 101.325KPa
		No.	Formula	Sustancia	Peso Molecular
		1	C6H14	Hexano	86.177
		2	C8H10	p-xileno	106.167
		PT [KPa]	101.33
		Datos Experimentales de n-Hexano/p-Xileno
		T [K]	X1	Y1
		411.55	0	0
		409.25	0.0110	0.0690
		403.15	0.0420	0.2250
		391.45	0.1230	0.4870
		385.25	0.1650	0.5870
		382.95	0.1920	0.6250
		369.45	0.3390	0.7850
		364.45	0.4090	0.8310
		359.75	0.4970	0.8670
		356.05	0.5780	0.8980
		351.35	0.7010	0.9410
		347.95	0.7970	0.9660
		345.75	0.8680	0.9780
		343.15	0.9530	0.9930
		342.03	1	1
		α
		6.6635
		6.6221
		6.7687
		7.1927
		7.0139
		7.1192
		7.1052
		6.5975
		6.4278
		6.8028
		7.2366
		6.7604
		6.9961
		Prom: 	6.8697
	d
		Datos			Balance Global 
		F [kmol/h]	100		0
		Z	0.45		Balance por componentes 
		q	0.5		0
		xD	0.95
		xB	0.03		Rectas
		D [kmol/h]	45.652173913		Linea de Alimentación 
		B [kmol/h]	54.347826087		m 	-1
					intercepción 	0.9
		x'	0.228956041		Puntos 
		y'	0.671043959		x	y
					0.45	0.45
		Rmin 	0.6309967537		0.26065	0.64
		R 
		0.8203			Linea de Rectificación 			Linea de Agotamiento
					Puntos 			Puntos 
		Punto pinch 			x	y		x	y
		xp	0.26		0.95	0.95		0.03	0.03
		yp	0.64		0.26065	0.64		0.26065	0.64
		S
		0.609048455
		Linea de Rectificacion							Alimentación 
		Plato 1		Plato 2		Plato 3			Plato 4
		x	y	x	y	x	y		x	y
		0.95	0.95	0.73556	0.8533650306	0.4430337422	0.721541369		0.2806973828	0.6483863181
		0.73556	0.95	0.4430337422	0.8533650306	0.2806973828	0.721541369		0.2134861798	0.6483863181
		0.73556	0.8533650306	0.4430337422	0.721541369	0.2806973828	0.6483863181		0.2134861798	0.514753145
		Plato 5		Plato 6		Plato 7
		x	y	x	y	x	y
		0.2134861798	0.514753145	0.1346563209	0.3064921084	0.0671941251	0.1282633633
		0.1346563209	0.514753145	0.0671941251	0.3064921084	0.022776694	0.1282633633
		0.1346563209	0.3064921084	0.0671941251	0.1282633633	0.022776694	0.0109167082
		Datos
		Z	0.45		Punto pinch 			Rectas
		q	0.5		xp	0.2606		Linea de Alimentación
		xD	0.95		yp	0.6394		Puntos 
	f)	xB	0.03					x	y
		D [kmol/h]	26.82		S			0.45	0.4500
		B [kmol/h]	12.452		0.609048455			0.26065	0.6394
		R 	0.8203
								Linea de Rectificación 
		Eficiencia de murphee						Puntos 
		75%						x	y
								0.95	0.95
		xe	ye	y ope	y' e			0.26065	0.6394
		0.0000	0.0000	-0.0493	-0.0123
		0.0110	0.0690	-0.0202	0.0467
		0.0420	0.2250	0.0617	0.1842			Linea de Agotamiento
		0.1230	0.4870	0.2757	0.4342			Puntos 
		0.1650	0.5870	0.3867	0.5369			x	y
		0.1920	0.6250	0.4580	0.5832			0.03	0.03
		0.3390	0.7850	0.6747	0.75740.26065	0.6394
		0.4090	0.8310	0.7062	0.7998
		0.4970	0.8670	0.7459	0.8367
		0.5780	0.8980	0.7824	0.8691
		0.7010	0.9410	0.8378	0.9152
		0.7970	0.9660	0.8811	0.9448
		0.8680	0.9780	0.9130	0.9618
		0.9530	0.9930	0.9514	0.9826
		1.0000	1.0000	0.9725	0.9931
		Linea de Rectificacion									Alimentacion
		Plato 1		Plato 2		Plato 3		Plato 4			Plato 5
		x	y	x	y	x	y	x	y		x	y
		0.95	0.95	0.81887	0.8909092691	0.63621	0.8085921166	0.42996	0.7156484904		0.30375	0.6587740641
		0.81887	0.95	0.63621	0.8909092691	0.42996	0.8085921166	0.30375	0.7156484904		0.25575	0.6587740641
		0.81887	0.8909092691	0.63621	0.8085921166	0.42996	0.7156484904	0.30375	0.6587740641		0.25575	0.626398913
		Linea de Agotamiento 
		Plato 6		Plato 7		Plato 8		Plato 9		Plato 10
		x	y	x	y	x	y	x	y	x	y
		0.25575	0.626398913	0.22842	0.5542086465	0.17508	0.4132826207	0.11623	0.2578143021	0.06586	0.1247361857
		0.22842	0.626398913	0.17508	0.5542086465	0.11623	0.4132826207	0.06586	0.2578143021	0.02860	0.1247361857
		0.22842	0.5542086465	0.17508	0.4132826207	0.11623	0.2578143021	0.06586	0.1247361857	0.02860	0.0262924238
Ejercicio 2
Equilibrio liquido-Vapor Hexano/p-Xileno
a 101.33 KPa
x=y	0	0.1	0.2	0.3	0.4	0.5	0.6	0.7	0.8	0.9	1	0	0.1	0.2	0.3	0.4	0.5	0.6	0.7	0.8	0.9	1	0	1.0999999999999999E-2	4.2000000000000003E-2	0.123	0.16500000000000001	0.192	0.33900000000000002	0.40899999999999997	0.497	0.57799999999999996	0.70099999999999996	0.7970000000000000	4	0.86799999999999999	0.95299999999999996	1	0	6.9000000000000006E-2	0.22500000000000001	0.48699999999999999	0.58699999999999997	0.625	0.78500000000000003	0.83099999999999996	0.86699999999999999	0.89800000000000002	0.94099999999999995	0.96599999999999997	0.97799999999999998	0.99299999999999999	1	Linea de Alimentación	0.45	0.26064848966084564	0.45	0.63935151033915438	Linea de Rectificación	
0.95	0.26064848966084564	0.95	0.63935151033915438	Linea de Agotamiento	
0.03	0.26064848966084564	0.03	0.63935151033915438	Rectificacion	0.95	0.73555999999999999	0.73555999999999999	0.73555999999999999	0.73555999999999999	0.44303374218338731	0.44303374218338731	0.44303374218338731	0.44303374218338731	0.28069738280889828	0.28069738280889828	0.28069738280889828	0.95	0.95	0.95	0.85336503057765456	0.85336503057765456	0.85336503057765456	0.85336503057765456	0.72154136904369892	0.72154136904369892	0.72154136904369892	0.72154136904369892	0.64838631810036462	Agotamiento	0.28069738280889828	0.2134861797547099	0.2134861797547099	0.2134861797547099	0.2134861797547099	0.13465632091329138	0.13465632091329138	0.13465632091329138	0.13465632091329138	6.7194125128697976E-2	6.7194125128697976E-2	6.7194125128697976E-2	6.7194125128697976E-2	2.2776693979432078E-2	2.2776693979432078E-2	2.2776693979432078E-2	0.64838631810036462	0.64838631810036462	0.64838631810036462	0.51475314503164604	0.51475314503164604	0.51475314503164604	0.51475314503164604	0.30649210844097369	0.30649210844097369	0.30649210844097369	0.30649210844097369	0.12826336325133564	0.12826336325133564	0.12826336325133564	0.12826336325133564	1.0916708191988804E-2	x fracción mol de Hexano en liquido
y fracción mol de Hexano en vapor 
Ejercicio 3
	A)	Datos de Equilibrio Obtenidos del ABP1 Metanol/agua a 101.325KPa
		No.	Formula	Sustancia	Peso Molecular
		1	CH4O	Metanol	32.042
		2	H2O	Agua	18.015
		PT [KPa]	101.33
		Datos Experimentales de Metanol/Agua
		T [°C]	X1	Y1
		100.00	0.0000	0.0000
		96.40	0.0200	0.1340
		93.50	0.0400	0.2300
		91.20	0.0600	0.3040
		89.30	0.0800	0.3650
		87.70	0.1000	0.4180
		84.40	0.1500	0.5170
		81.70	0.2000	0.5790
		78.00	0.3000	0.6650
		75.30	0.4000	0.7290
		73.10	0.5000	0.7790
		71.20	0.6000	0.8250
		69.30	0.7000	0.8700
		67.50	0.8000	0.9150
		66.00	0.9000	0.9580
		65.00	0.9500	0.9790
		64.50	1.0000	1.0000
	d) 
		Datos
		F [kmol/h]	216.8
		α	4.0351
		Z	0.36
		q	1.08		Balance Global 
		xD	0.914		-0.0001168
		xB	0.00565		Balance por componentes 
		D [kmol/h]	84.5743153615		-0.0000000186
		B [kmol/h]	132.2258014385
		x'	0.3870
		y'	0.7245
		Rmin 	0.5614814815			Rectas
						Linea de Alimentación 
		R 				m 	13.5
		0.8422				intercepción 	-4.5
						Puntos 
		Punto pinch 				x	y
		xp	0.3831			0.36	0.36
		yp	0.6713			0.3831	0.6713
		S
		1.309493582				Linea de Rectificación 			Linea de Agotamiento
						Puntos 			Puntos 
						x	y		x	y
						0.914	0.914		0.00565	0.00565
						0.38306	0.67		0.38306	0.67
		Linea de Rectificacion									Alimentación 
		Plato 1		Plato 2		Plato 3		Plato 4			Plato 5
		x	y	x	y	x	y	x	y		x	y
		0.914	0.914	0.7977777778	0.8608658357	0.6797018571	0.8068842024	0.5606178314	0.7524416865		0.446883373	0.7004448714
		0.7977777778	0.914	0.6797018571	0.8608658357	0.5606178314	0.8068842024	0.446883373	0.7524416865		0.3553826115	0.7004448714
		0.7977777778	0.8608658357	0.6797018571	0.8068842024	0.5606178314	0.7524416865	0.446883373	0.7004448714		0.3553826115	0.622457316
		Plato 6		Plato 7		Plato 8		Plato 9		Plato 10
		x	y	x	y	x	y	x	y	x	y
		0.3553826115	0.622457316	0.2505317628	0.4375366983	0.1098670194	0.1894527621	0.0315526588	0.0513333275	0.0076616907	0.0091979263
		0.2505317628	0.622457316	0.1098670194	0.4375366983	0.0315526588	0.1894527621	0.0076616907	0.0513333275	0.0013728248	0.0091979263
		0.2505317628	0.4375366983	0.1098670194	0.1894527621	0.0315526588	0.0513333275	0.0076616907	0.0091979263	0.0013728248	-0.0018934571
	f)
		Datos
		Z	0.36		Punto pinch 			Rectas
		q	1.08		xp	0.3831		Linea de Alimentación
		xD	0.914		yp	0.6713		Puntos 
		xB	0.00565					x	y
		D [kmol/h]	84.5743153615		S			0.36	0.3600
		B [kmol/h]	132.2258014385		1.309493582			0.38306	0.6713
		R 	0.8422
								Linea de Rectificación 
		Eficiencia de murphee						Puntos 
		78%						x	y
								0.914	0.914
		xe	ye	y ope	y' e			0.38306	0.6713
		0.0000	0.0000	-0.004314645	-0.0009492219
		0.0200	0.1340	0.0309584348	0.1113308556
		0.0400	0.2300	0.0662315146	0.1939709332			Linea de Agotamiento
		0.0600	0.3040	0.1015045944	0.2594510108			Puntos 
		0.0800	0.3650	0.1367776742	0.3147910883			x	y
		0.1000	0.4180	0.172050754	0.3638911659			0.00565	0.00565
		0.1500	0.5170	0.2602334536	0.4605113598			0.38306	0.6713
		0.2000	0.5790	0.3484161531	0.5282715537
		0.3000	0.6650	0.5247815522	0.6341519415
		0.4000	0.7290	0.6790108565	0.7180023884
		0.5000	0.7790	0.7247285887	0.7670602895
		0.6000	0.8250	0.7704463209	0.8129981906
		0.7000	0.8700	0.8161640531	0.8581560917
		0.8000	0.9150	0.8618817853	0.9033139928
		0.9000	0.9580	0.9075995175	0.9469118938
		0.9500	0.9790	0.9304583836	0.9683208444
		1.0000	1.0000	0.9533172497	0.9897297949
		Linea de Rectificacion												Alimentacion
		Plato 1		Plato 2		Plato 3		Plato 4		Plato 5		Plato 6		Plato 7
		x	y	x	y	x	y	x	y	x	y	x	y	x	y
		0.914	0.914	0.82451	0.873087371	0.73306	0.8312804383	0.64049	0.7889552171	0.54766	0.7465185793	0.45813	0.7055854867	0.38519	0.6722407961
		0.82451	0.914	0.73306	0.873087371	0.64049	0.8312804383	0.54766	0.7889552171	0.45813	0.7465185793	0.38519	0.7055854867	0.34542	0.6722407961
		0.82451	0.873087371	0.73306	0.8312804383	0.64049	0.7889552171	0.54766	0.7465185793	0.45813	0.7055854867	0.38519	0.6722407961	0.34542	0.6048950911
		Linea de Agotamiento 
		Plato 8		Plato 9		Plato 10		Plato 11		Plato 12		Plato 13
		x	y	x	y	x	y	x	y	x	y	x	y
		0.34542	0.6048950911	0.27237	0.4760482957	0.16146	0.2804531264	0.06759	0.1148910827	0.02086	0.0324780385	0.00595	0.0061866162
		0.27237	0.6048950911	0.16146	0.4760482957	0.06759	0.2804531264	0.02086	0.1148910827	0.00595	0.0324780385	0.00127	0.0061866162
		0.27237	0.4760482957	0.16146	0.2804531264	0.06759	0.1148910827	0.02086	0.0324780385	0.00595	0.0061866162	0.00127	-0.0020729029
Ejercicio 3
Ejercicio 4
	A)	Datos de Equilibrio Obtenidos del ABP1 CCl4/CS2 a 101.325KPa de la lección 7
		No.	Formula	Sustancia	Peso Molecular
		1	CCl4 	Tetracloruro de Carbono	153.822
		2	CS2	Disulfuro de Carbono 	76.143
		PT [KPa]	101.33
		Datos Experimentales de CCl4/CS2
		T [°C]	x1	y1	x2	y2
		46.3	0.0049	0.0017	0.9951	0.9983
		49.8	0.1728	0.0704	0.8272	0.9296
		53.3	0.3223	0.1491	0.6777	0.8509
		56.8	0.4559	0.2385	0.5441	0.7615
		60.3	0.5756	0.3397	0.4244	0.6603
		63.8	0.6833	0.4535	0.3167	0.546567.3	0.7805	0.5809	0.2195	0.4191
		70.8	0.8686	0.7229	0.1314	0.2771
		74.3	0.9486	0.8806	0.0514	0.1194
		76.7	0.9993	0.9983	0.0007	0.0017
		Datos de Operación 
		xF	0.669
		PT [Kpa]	101.33
		mF* [kmol/h]	39.269
		α
		2.8031
		2.7579
		2.7152
		2.6748
		2.6367
		2.6006
		2.5664
		2.5340
		2.5034
		2.4832
		Prom: 	2.6275
	d) 
		Datos
		Z	0.669
		q	0.7
		xD	0.975
		xB	0.01
		D [kmol/h]	26.82
		B [kmol/h]	12.452
		x'	0.6107922957
		y'	0.8048179768
		Rmin 	0.8771108143			Rectas
						Linea de Alimentación 
		R 				m 	-2.3333333333
		1.7542				intercepción 	2.23
						Puntos 
		Punto pinch 				x	y
		xp	0.63			0.669	0.669
		yp	0.76			0.63160	0.76
		S
		4.9853988669				Linea de Rectificación 			Linea de Agotamiento
						Puntos 			Puntos 
						x	y		x	y
						0.975	0.975		0.01	0.01
						0.63160	0.76		0.63160	0.76
		Linea de Rectificacion									Alimentación 
		Plato 1		Plato 2		Plato 3		Plato 4			Plato 5
		x	y	x	y	x	y	x	y		x	y
		0.975	0.975	0.9382563302	0.9515971846	0.8810269079	0.915146563	0.7918902815	0.8583735726		0.691814996	0.7946335205
		0.9382563302	0.975	0.8810269079	0.9515971846	0.7918902815	0.915146563	0.691814996	0.8583735726		0.5936157518	0.7946335205
		0.9382563302	0.9515971846	0.8810269079	0.915146563	0.7918902815	0.8583735726	0.691814996	0.7946335205		0.5936157518	0.7106807585
		Plato 6		Plato 7		Plato 8		Plato 9		Plato 10		Plato 11		Plato 12		Plato 13
		x	y	x	y	x	y	x	y	x	y	x	y	x	y	x	y
		0.5936157518	0.7106807585	0.4839927173	0.5790689047	0.3474792212	0.4151727458	0.2169999152	0.2585211496	0.121965501	0.1444241857	0.0640761782	0.0749230893	0.0322237912	0.0366815671	0.0157529156	0.0209185836
		0.4839927173	0.7106807585	0.3474792212	0.5790689047	0.2169999152	0.4151727458	0.121965501	0.2585211496	0.0640761782	0.1444241857	0.0322237912	0.0749230893	0.0157529156	0.0366815671	0.0089636947	0.0209185836
		0.4839927173	0.5790689047	0.3474792212	0.4151727458	0.2169999152	0.2585211496	0.121965501	0.1444241857	0.0640761782	0.0749230893	0.0322237912	0.0366815671	0.0157529156	0.0209185836	0.0089636947	0.0127675417
	f)
		Datos
		Z	0.669		Punto pinch 			Rectas
		q	0.7		xp	0.6316		Linea de Alimentación
		xD	0.975		yp	0.7563		Puntos 
		xB	0.01					x	y
		D [kmol/h]	26.82		S			0.67	0.6690
		B [kmol/h]	12.452		4.9853988669			0.63160	0.7563
		R 	1.7542
								Linea de Rectificación 
		Eficiencia de murphee						Puntos 
		68%						x	y
								0.975	0.975
		xe	ye	y ope	y' e			0.63160	0.7563
		0.9951	0.9983	0.9878189611	0.9949160709
		0.8272	0.9296	0.8808460216	0.9139815978
		0.6777	0.8509	0.7856306936	0.8300398741			Linea de Agotamiento
		0.5441	0.7615	0.6512704539	0.7262195595			Puntos 
		0.4244	0.6603	0.5075236355	0.6114344256			x	y
		0.3167	0.5465	0.3782021915	0.4926694839			0.01	0.01
		0.2195	0.4191	0.2614648733	0.3686753251			0.63160	0.7563
		0.1314	0.2771	0.1557405987	0.2382641883
		0.0514	0.1194	0.0596847732	0.1002966333
		0.0007	0.0017	-0.0011980875	0.0007515968
		Linea de Rectificacion															Alimentacion
		Plato 1		Plato 2		Plato 3		Plato 4		Plato 5		Plato 6		Plato 7			Plato 8
		x	y	x	y	x	y	x	y	x	y	x	y	x	y		x	y
		0.975	0.975	0.95380	0.9614954358	0.92577	0.9436461452	0.88873	0.9200543307	0.83978	0.8888724912	0.78246	0.8523646929	0.71744	0.810953797		0.65313	0.7699934658
		0.95380	0.975	0.92577	0.9614954358	0.88873	0.9436461452	0.83978	0.9200543307	0.78246	0.8888724912	0.71744	0.8523646929	0.65313	0.810953797		0.60044	0.7699934658
		0.95380	0.9614954358	0.92577	0.9436461452	0.88873	0.9200543307	0.83978	0.8888724912	0.78246	0.8523646929	0.71744	0.810953797	0.65313	0.7699934658		0.60044	0.7188734589
		Linea de Agotamiento 
		Plato 9		Plato 10		Plato 11		Plato 12		Plato 13		Plato 14		Plato 15		Plato 16		Plato 17		Plato 18
		x	y	x	y	x	y	x	y	x	y	x	y	x	y	x	y	x	y	x	y
		0.60044	0.7188734589	0.53647	0.6420708428	0.45636	0.5458899932	0.36495	0.4361532418	0.27237	0.3249936002	0.18996	0.2260521103	0.12431	0.147238301	0.07861	0.0923665196	0.04734	0.0548346267	0.02822	0.0318797001
		0.53647	0.7188734589	0.45636	0.6420708428	0.36495	0.5458899932	0.27237	0.4361532418	0.18996	0.3249936002	0.12431	0.2260521103	0.07861	0.147238301	0.04734	0.0923665196	0.02822	0.0548346267	0.01653	0.0318797001
		0.53647	0.6420708428	0.45636	0.5458899932	0.36495	0.4361532418	0.27237	0.3249936002	0.18996	0.2260521103	0.12431	0.147238301	0.07861	0.0923665196	0.04734	0.0548346267	0.02822	0.0318797001	0.01653	0.0178402096
Ejercicio 4
Ejercicio 6
		P Total [atm]	1.2
		Sustancia	x_F
		n-hexano	0.33
		n-heptano	0.37
		n-octano	0.30
		Punto de burbuja
		T [°C]	T [°F]	K_1 	K_2 	K_3	y_1	y_2	y_3	xi=1 	yi=xiki=1
		95	203	1.7	0.76	0.38	0.561	0.2812	0.114	1.00	0.9562
		100	212	1.9	0.85	0.44	0.627	0.3145	0.132	1.00	1.0735
		99.9	211.82	1.8	0.85	0.41	0.594	0.3145	0.123	1.00	1.0315
		99.5	211.1	1.8	0.8	0.4	0.594	0.296	0.12	1.00	1.01
		98	208.4	1.79	0.79	0.39	0.5907	0.2923	0.117	1.00	1
		Punto de Rocio 
		T [°C]	T [°F]	K_1 	K_2 	K_3	x_1	x_2	x_3	yi=1	xi=yi/ki=1
		115	239	2.7	1.3	0.67	0.1222222222	0.2846153846	0.447761194	1.00	0.8545988009
		113.5	236.3	2.6	1.2	0.6	0.1269230769	0.3083333333	0.5000	1.00	0.9352564103
		112	233.6	2.49	1.18	0.59	0.1325301205	0.313559322	0.5084745763	1.00	0.9545640188
		110	230	2.4	1.13	0.56	0.1375	0.3274336283	0.5357142857	1.00	1.000647914
		f	0.6
		Temperatura de operación 
		T [°C]	T [°F]	K_1 	K_2 	K_3	x_1	x_2	x_3	 xi=1	Rachford-Rise
		105	221	2.1	0.99	0.5	0.1987951807	0.3722334004	0.4285714286	0.9996	0.0007
		Capacidad calorifica [Tabla 2-196 Perry 7ma edición] 								Energía de vaporización [ Tabla 2-193Perry 7ma Edición ]
		Sustancia	C1	C2	C3	C4	C5			Sustancia	C1	C2	C3	C4	Tc[K]
		n-hexano	172120.00	-183.78	0.89	0.00	0.00			n-hexano	4.45E+07	0.390020	0.000000	0.000000	507.6
		n-heptano	61.26	314410.00	1824.60	-2547.90	0.00			n-heptano	5.00E+07	0.387950	0.000000	0.000000	540.2
		n-octano	224830.00	-186.63	-0.96	0.00	0.00			n-octano	5.52E+07	0.384670	0.000000	0.000000	568.7
					Fracciones
		Datos			XF	xi	yi
		T ope [K]	378.15		33%	0.1987951807	0.4174698795
		T ref [K]	273.15		37%	0.3722334004	0.3685110664
		f	0.6		30%	0.4285714286	0.2142857143
		TF [K]	T prom Hx [K]	t n-heptano	CpL [J/kmol*K]	Tr Etano	Tr Propano 	Tr i-Butano	ΔH [J/kmol]	t n-heptano	T prom HF [K]	CpL_F [J/kmol*K]	error
		480.935	325.65	0.3584515366	1.7723E+05	0.7449763593	0.7000185117	0.6649375769	3.02E+07	0.3020317164	377.04	1.7686E+05	-0.000
Ejercicio 6
*Asumiendo que Ki no depende de la composición por ser compuestos parecidos, utilizar la ecuación de rachford-rise.
Para realizar el ejercicio se tomo la información del ejemplo 22.2 que es una continuación del ejemplo 1 y detallan el porcentaje de vaporización 
*Para cada Ki se utilizara el diagrama de DePriester para obtener su valor 
diagrama 6
DIAGRAMA EJERCICIO 6 
Ejercicio 7
		P Total [lbf/in^2]	270
		Sustancia	x_F
		etano	10%
		propano	45%
		i-butano	30%
		n-butano	15%
		Punto de burbuja
		T [°C]	T [°F]	K_1 	K_2 	K_3	K_4	y_1	y_2	y_3	y_4	xi=1 	yi=xiki=1
		60	140	3	1.2	0.57	0.42	0.3	0.54	0.171	0.063	1.00	1.074
		50	122	2.7	0.98	0.48	0.349	0.27	0.441	0.144	0.05235	1.00	0.90735
		55	131	2.8	1.1	0.52	0.38	0.28	0.495	0.156	0.057	1.00	0.988
		58	136.4	2.9	1.15	0.55	0.41	0.29	0.5175	0.165	0.0615	1.00	1.034
		56	132.8	2.88	1.1	0.53	0.39	0.288	0.495	0.159	0.0585	1.00	1.0005
		f	0.9824026475
		Temperatura de operación 
		T [°C]	T [°F]	K_1 	K_2 	K_3	K_4	x_1	x_2	x_3	x_4	 xi=1	Rachford-Rise
		76	168.8	3.44	1.49	0.74	0.56	0.0294371979	0.3037713625	0.4029142456	0.2642041268	1.0003	-0.0003
		Capacidad calorifica [Tabla 2-196 Perry 7ma edición] 								Energía de vaporización [ Tabla 2-193Perry 7ma Edición ]
		Sustancia	C1	C2	C3	C4	C5			Sustancia	C1	C2	C3	C4	Tc[K]
		etano	44.09	89,718.00	918.77	-1,886.00	0.00			etano	2.11E+07	0.606460	-0.554920	0.327990	305.32
		propano	62.98	113,630.00	633.21	-873.46	0.00			propano	2.92E+07	0.782370	-0.773190	0.392460	369.83
		i-butano	172,370.00	-1,783.90	14.76	-0.05	0.00			i-butano	3.76E+07	0.391730	0.000000	0.000000	460.4
		n-butano	191,030.00	-1,675.00	12.50	-0.04	0.00			n-butano	3.62E+07	0.833700	-0.822740	0.396130	425.12
					Fracciones
		DatosXF	xi	yi
		T ope [K]	349.15		10%	0.0294371979	0.1012639609
		T ref [K]	273.15		45%	0.3037713625	0.4526193302
		f	0.65		30%	0.4029142456	0.2981565418
					15%	0.2642041268	0.147954311
		TF [K]	T prom Hx [K]	t etano	t propano	CpL [J/kmol*K]	Tr Etano	Tr Propano 	Tr i-Butano	Tr n-butano	ΔH [J/kmol]	t etano	t propano	T prom HF [K]	CpL_F [J/kmol*K]	error
		402.279	311.15	-0.0190947203	0.1586674959	1.0563E+05	1.1435543037	0.9440824162	0.7583622937	0.821297516	1.31E+07	-0.1060999208	0.0868387426	337.71	1.2836E+05	-0.001
Ejercicio 7
*Asumiendo que Ki no depende de la composición ya que son compuestos muy parecidos, utilazamos la ecuación de rachford-rise.
Para realizar el ejercicio se tomo la información del ejemplo 22.2 que es una continuación del ejemplo 1 y detallan el porcentaje de vaporización 
*Para cada Ki se utilizara el diagrama de DePriester para obtener su valor 
Diagrama 7
DIAGRAMA EJERCICIO 7
Ejercicio 8
		P Total [lbf/in^2]	22.04
		Sustancia	x_F
		n-pentano	0.25
		n-hexano	0.4
		n-heptano	0.35
		Punto de burbuja
		T [°C]	T [°F]	K_1 	K_2 	K_3	y_1	y_2	y_3	xi=1 	yi=xiki=1
		75	167	2	0.8	0.35	0.5	0.32	0.1225	1.00	0.9425
		76	168.8	2.05	0.85	0.36	0.5125	0.34	0.126	1.00	0.9785
		77	170.6	2.09	0.86	0.37	0.5225	0.344	0.1295	1.00	0.996
		77.5	171.5	2.11	0.87	0.38	0.5275	0.348	0.133	1.00	1.0085
		Punto de Rocio 
		T [°C]	T [°F]	K_1 	K_2 	K_3	x_1	x_2	x_3	yi=1	xi=yi/ki=1
		95	203	3	1.35	0.6	0.0833333333	0.2962962963	0.5833333333	1.00	0.962962963
		94	201.2	2.9	1.3	0.59	0.0862068966	0.3076923077	0.5932	1.00	0.9871195432
		93.5	200.3	2.86	1.29	0.58	0.0874125874	0.3100775194	0.6034482759	1.00	1.0009383827
Ejercicio 8
*Para cada Ki se utilizara el diagrama de DePriester para obtener su valor 
Diagrama 8
DIAGRAMA EJERCICIO 8
Ejercicio 9
		P Total [atm]	1
					Presión de vapor. Tabla 2.8 del Perry 7ma Ed.
		Sustancia	x_F		Sustancia	C1	C2	C3	C4	C5
		Benceno	20%		Benceno	83.11	-6,486.20	-9.21940	6.98E-06	2.00
		Tolueno	10%		Tolueno	76.95	-6,729.80	-8.17900	5.30E-06	2.00
		O-Xylene	20%		O-Xylene	90.41	-7,955.20	-10.08600	5.96E-06	2.00
		M-Xylene	30%		M-Xylene	85.01	-7,615.90	-9.30720	5.56E-06	2.00
		P-Xylene	20%		P-Xylene	88.72	-7,741.20	-9.86930	6.08E-06	2.00
		f	0.65
		Temperatura de operación 
		T [°C]	T [K]
		129.6850345096	402.8350345096
		Sustancia	P [atm]	Ki	 xi=1	Rachford-Rise
		Benceno	3.71	3.7065864316	0.0724826456	0.1961805452
		Tolueno	1.67	1.6672957671	0.0697475436	0.0465422406
		O-Xylene	0.67	0.6681789497	0.2549991573	-0.0846140882
		M-Xylene	0.71	0.7051241957	0.3711352172	-0.1094387957
		P-Xylene	0.79	0.7882027463	0.2319292916	-0.049121987
				Suma	1.0002938553	-0.0004520851
		Capacidad calorifica [Tabla 2-196 Perry 7ma edición] 								Energía de vaporización [ Tabla 2-193Perry 7ma Edición ]
		Sustancia	C1	C2	C3	C4	C5			Sustancia	C1	C2	C3	C4	Tc[K]
		Benceno	1.2944E+05	-1.6950E+02	6.4781E-01	0	0			Benceno	4.7500E+07	0.45238	0.0534	-0.1181	562.16
		Tolueno	1.4014E+05	-1.5230E+02	6.9500E-01	0	0			Tolueno	5.0144E+07	0.3859	0	0	591.8
		O-Xylene	3.65E+04	1.02E+03	-2.63E+00	3.02E-03	0			O-Xylene	5.53E+07	0.377	0	0	630
		M-Xylene	1.76E+05	-3.00E+02	1.09E+00	0	0			M-Xylene	5.46E+07	0.3726	0	0	617.05
		P-Xylene	-3.5500E+04	1.2872E+03	-2.5990E+00	2.4260E-03	0			P-Xylene	5.3740E+07	0.3656	0	0	616.23
					Fracciones
		Datos			XF	xi	yi
		T ope [K]	402.8350345096		20%	0.0724826456	0.2686631908
		T ref [K]	273.15		10%	0.0697475436	0.1162897842
		f	0.65		20%	0.2549991573	0.1703850691
					30%	0.3711352172	0.2616964215
					20%	0.2319292916	0.1828073045
		TF [K]	T prom Hx [K]	CpL [J/kmol*K]	Tr Benceno	Tr tolueno	Tr O-Xyl	Tr m-xyl	Tr p-xyl	ΔH [J/kmol]	T prom HF [K]	CpL_F [J/kmol*K]	error
		500.021	337.9925172548	1.8420E+05	0.7165843079	0.6806945497	0.6394206897	0.6528401823	0.6537088985	3.39E+07	386.59	2.0240E+05	0.000000
*Asumiendo que Ki no depende de la composición ya que son compuestos muy parecidos, utilazamos la ecuación de rachford-rise.
Para realizar el ejercicio se tomo la información del ejemplo 22.2 que es una continuación del ejemplo 1 y detallan el porcentaje de vaporización 
Ejercicio 9
Ejercicio 10
		P Total [atm]	2
					Presión de vapor. Tabla 2.8 del Perry 7ma Ed.
		Sustancia	x_F		Sustancia	C1	C2	C3	C4	C5
		Benceno	20%		Benceno	83.11	-6,486.20	-9.21940	6.98E-06	2.00
		Tolueno	10%		Tolueno	76.95	-6,729.80	-8.17900	5.30E-06	2.00
		O-Xylene	20%		O-Xylene	90.41	-7,955.20	-10.08600	5.96E-06	2.00
		M-Xylene	30%		M-Xylene	85.01	-7,615.90	-9.30720	5.56E-06	2.00
		P-Xylene	20%		P-Xylene	88.72	-7,741.20	-9.86930	6.08E-06	2.00
		f	0.65
		Temperatura de operación 
		T [°C]	T [K]
		156.8824620057	430.0324620057
		Sustancia	P [atm]	Ki	 xi=1	Rachford-Rise
		Benceno	6.58	3.2909300421	0.0803501813	0.1840766442
		Tolueno	3.17	1.5846503946	0.0724625732	0.042365272
		O-Xylene	1.38	0.6898067662	0.250509035	-0.0777062076
		M-Xylene	1.44	0.7197409847	0.3668236655	-0.1028056393
		P-Xylene	1.60	0.800178235	0.2298544491	-0.0459299217
				Suma	1.000000	0.000000
		Capacidad calorifica [Tabla 2-196 Perry 7ma edición] 								Energía de vaporización [ Tabla 2-193Perry 7ma Edición ]
		Sustancia	C1	C2	C3	C4	C5			Sustancia	C1	C2	C3	C4	Tc[K]
		Benceno	1.2944E+05	-1.6950E+02	6.4781E-01	0	0			Benceno	4.7500E+07	0.45238	0.0534	-0.1181	562.16
		Tolueno	1.4014E+05	-1.5230E+02	6.9500E-01	0	0			Tolueno	5.0144E+07	0.3859	0	0	591.8
		O-Xylene	3.65E+04	1.02E+03	-2.63E+00	3.02E-03	0			O-Xylene	5.53E+07	0.377	0	0	630
		M-Xylene	1.76E+05	-3.00E+02	1.09E+00	0	0			M-Xylene	5.46E+07	0.3726	0	0	617.05
		P-Xylene	-3.5500E+04	1.2872E+03	-2.5990E+00	2.4260E-03	0			P-Xylene	5.3740E+07	0.3656	0	0	616.23
					Fracciones
		Datos			XF	xi	yi
		T ope [K]	430.0324620057		20%	0.0803501813	0.2644268255
		T ref [K]	273.15		10%	0.0724625732	0.1148278452
		f	0.65		20%	0.250509035	0.1728028273
					30%	0.3668236655	0.2640180263
					20%	0.2298544491	0.1839245274
		TF [K]	T prom Hx [K]	CpL [J/kmol*K]	Tr Benceno	Tr tolueno	Tr O-Xyl	Tr m-xyl	Tr p-xyl	ΔH [J/kmol]	T prom HF [K]	CpL_F [J/kmol*K]	error
		518.197	351.5912310029	1.8898E+05	0.7649645332	0.7266516763	0.6825912095	0.6969167199	0.6978440874	3.21E+07	395.67	2.0617E+05	-0.000
*Asumiendo que Ki no depende de la composición ya que son compuestos muy parecidos, utilIzamos la ecuación de rachford-rise.
Para realizar el ejercicio se tomo la información del ejemplo 22.2 que es una continuación del ejemplo 1 y detallan el porcentaje de vaporización 
Ejercicio 10