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1 Lista 1 Problema 2) E ciência de um refrigerador de Carnot: k = QF W = QF jQQj �QF = 1 jQQj QF � 1 onde W = jQQj �QF k = QF W = QF jQQj �QF = 1 jQQj QF � 1 Usando a relação válida para o ciclo de Carnot jQQj QF = TQ TF obtemos k = 1 TQ TF � 1 Cálculo do calor: Q = mc�T +mL Q = 10� 2:05� 103 � 20 + 10� 340� 103 Q = 3:82� 106J TQ = 303; 15 K; TF = 253; 15 K E ciência: k = 1 303:15 253:15 � 1 = 5:06 Por de nição k = QF W e W = QF k Obtemos 1 W = 7:549 4� 105 J W = 754:9 4 kJ = 754:9 4 3600 kWh = 0:21kWh Problema 3) P = 1200 W TQ = 313; 15 K; TF = 293; 15 K Então k = 1 313:15 293:15 � 1 k = 14:65 jQQj = QF +W = (k + 1)P�t jQQj = 15:65� 1200� 3600 jQQj = 6:76� 107 J Problema 5) Q = ncp�T ! �T = Q ncp �V = nR p �T = nR p Q ncp = RQ 5 2Rp = 2Q 5p W = p�V = p 2Q 5p W = 2 5 Q!W = 200 J Problema 6) �U = 0!W = Q W = Q = T�S = 400� 50 = 20 kJ Problema 8) (a) 2 pbVb = paVa pb = pa Va Vb ! pb = 0; 5 atm pcV c = paV a pc = pa � Va Vc � ! pc = (0; 5)1;4 = 0; 379 atm (b) Qab = paVa ln Vb Va = 1; 0 ln 2:0 = 0; 693 atm:l Qbc = �U = ncvTc � ncvTb Qbc = cv R (pcVc � pbVb) Qbc = 5 2 (0; 379� 2; 00� 0; 500� 2; 00) = �0:605 atm:l � = 1� jQbcj Qab � = 1:0� 0:605 0:693 = 0:127 (c) W = Qab � jQbcj W = 0:693� 0:605 = 0:088 atm:l W = 0:088� 100 = 8; 8 J Problema 10) (a) QAB = cp R pA (VB � VA) = 5 2 � 5; 0 = 12; 5 atm:l QCD = cp R pC (VD � VC) = 5 2 � 0; 5 (15; 2� 22; 8) = �9; 5 atm:l 3 Rendimento � = 1� jQCDj QAB � = 1; 0� 9; 5 12; 5 = 0; 24 (b) Invertendo o ciclo, a e ciência do refrigerador ca dada por k = QCD W = QCD jQAB j �QCD k = 9; 5 12; 5� 9; 5 ! k = 3; 2 Problema 12) (a) Q12 = �U12 = ncv (T2 � T1) Q12 = 1 2 � 3 2 R (1000� 250) Q12 = 3 4 � 8; 314 (1000� 250) = 4:676; 6 J Q23 = Z S3 S2 T2ds = T2 (S3 � S2) Q23 = 1000 (20� 28) = �8:000 J k = Q12 jQ23j �Q12 k = 4:676; 6 8:000� 4:676; 6 = 1; 4 (b) Veja a gura do problema 8. 2 Lista 2 Problema 2) W1 = Q1 �Q2; W2 = Q2 �Q3 � = W Q1 = W1 +W2 Q1 = Q1 �Q3 Q1 4 � = 1� Q3 Q1 Q1 Q2 = T1 T2 ; Q3 Q2 = T3 T2 Escrevendo Q2 = Q1 T2 T1 obtemos Q3 Q2 = Q3 Q1 T1 T2 = T3 T2 ! Q3 Q1 = T3 T1 Portanto, demonstra-se que � = 1� T3 T1 Problema 3) (a) k = Qf W ; W = jQqj �Qf jQqj = Qf +W = Qf + Qf k jQqj = 42 + 42 5; 7 = 49; 37 kcal (b) W = 42 5; 7 = 7; 37 kcal Problema 4) (a) Q = 500 cal!W = Q = 500 cal (b) Rendimento da máquina: � = 1� jQf j Qq = 1� T2 T1 � = 1� T2 T1 = 1� 300 400 = 0; 25 Logo, jQf j = Qq T2 T1 jQf j = 500� 300 400 = 375 cal (c) W = jQf j = 375 cal 5 Problema 6) Q = mcg�T +mLF +mc�T 0 Qg = 10� 0; 50� 10 + 10� 80 + 10� 1; 0� 15 Qg = 1; 0 kcal �S = Qg Tlago = 1000:0 288: = 3; 47 cal=K Problema 7) (a) QI = nRT ln V 0 V + ncv (T"� T 0) QI = pV ln V 0 V + cv � p"V 0 R � p 0V 0 R � QI = pV ln V 0 V + cv R (p"� p0)V 0 QI = pV ln 2 + cv R � 2p� p 2 � 2V = pV ln 2 + 3cv R V QI = pV ln 2 + 4; 5pV p0 = 2p; V 0 = V=2; p" = 2p; V " = 2V QII = pV ln V 0 V + cp R p0 (V "� V 0) = pV ln V 0 V + 2cp R p � 2V � V 2 � QII = pV ln V 0 V + 3cp R pV = �pV ln 2 + 3cp R pV QII = �pV ln 2 + 7; 5pV (b) WI = pV ln V 0 V = pV ln 2 WII = pV ln V 0 V + 2p (V "� V 0) = �pV ln 2 + 3pV (c) 6 �UI = ncv (T"� T 0) = cv R � 2p� p 2 � V 0 = cv R 3 2 p (2V ) �UI = 3cv R pV = 4; 5pV �UII = 2p�V = 2p 3 2 V = 3pV (d) �SI = nRT ln V 0 V T + Z T" T 0 dQ T = R ln V 0 V + Z T" T 0 ncvdT T �SI = R ln 2 + cv ln T" T 0 �SI = R ln 2 + cv ln p"V " p0V 0 �SI = R ln 2 + cv ln 2p p 2 = R ln 2 + 2cv ln 2 �SI = 4R ln 2 �SII = nRT ln V 0 V T + Z T" T 0 dQ T = R ln V 0 V + Z T" T 0 ncpdT T �SII = �R ln 2 + cp ln T" T 0 �SII = �R ln 2 + cp ln p"V " p0V 0 �SII = �R ln 2 + cp ln 2VV 2 = �R ln 2 + 2cp ln 2 �SII = 4R ln 2 Problema 9) (a) p = 5; 00� 103eVi�Va N m2 7 pf = 5; 00� 103e Vi�Vf a = 5; 00� 103e�1 pf = 1:839; 4 N m2 (b) pfVf = nRTf Tf = pfVf R = 1:839; 4� 2; 00 8; 314 Tf = 442 K (c) W = Z Vf Vi pdV W = 5; 00� 103 Z Vf Vi e Vi�V a dVZ 2 1 e1�xdx = 0; 632 W = 5; 00� 103 � 0; 632 W = 3:160 J (d) Processo isobárico: �S1 = Z Tf Ti dQ T = Z Tf Ti ncpdT T = ncp ln Tf Ti = ncp ln pfVf piVi �S1 = cp ln Vf Vi = 2; 5R ln 2 Processo isovolumétrico: �S2 = Z Tf Ti dQ T = Z Tf Ti ncvdT T = ncv ln Tf Ti = ncv ln pfVf piVi �S2 = cv ln pf pi = 1; 5R ln 1:839; 4 5:000 �S2 = �1; 5R �S = �S1 +�S2 = 2; 5R ln 2� 1; 5R �S = 0; 233R Processo isotérmico: �S1 = Q Ti = nRTi ln Vf Vi Ti = nR ln Vf Vi = R ln 2 8 Processo isovolumétrico: �S2 = Z Tf Ti dQ T = Z Tf Ti ncvdT T = ncv ln Tf Ti = ncv ln pfVf piVi �S2 = cv ln pf pi = 1; 5R ln 1:839; 4 5:000 piVf = nRTi = p0V0 pi = p0V0 Vf = 5:000 2; 0 = 2:500 �S2 = 1; 5R ln 1:839; 4 2:500 �S2 = �0:460 28R �S = R ln 2� 0:460 28R �S = 0; 233R Problema 10) k = Qf W ; d dt jQqj = 1; 8� 106 cal=hora W = jQqj �Qf = jQqj � kW W = jQqj 1 + k dW dt = 1 1 + k d dt jQqj dW dt = 1 1 + k 1; 8� 106 3:600 cal s dW dt = 500 4; 8 cal s = 104; 17 cal s dW dt = 104; 17� 4; 186 cal s dW dt = 436 W 9
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