Programação EES

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Programa de fluidos para EES

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s_1[1] = entropy(R1$; x=x[1]; T=T[1])s_1[2] = entropy(R2$; x=x[1]; T=T[1])v_1[1] = volume(R1$; P=P[1]; T=T[1])v_2[1] = volume(R2$; P=P[1]; T=T[1])s_1[3] = entropy(R1$; P=P[3]; x=x[3])s_2[3] = entropy(R2$; P=P[3]; x=x[3])v_1[3] = volume(R1$; P=P[3]; x=x[3])v_2[3] = volume(R2$; P=P[3]; x=x[3])v_1[2] = volume(R1$; P=P[2]; s=s_1[2])v_2[2] = volume(R2$; P=P[2]; s=s_2[2])q_L = h[1]-h[4] "evaporador"q_H = h[2]-h[3] "condensador"W_c = abs( h[2]-h[1]) "compressor"q_dot_L = m_dot * (h[1]-h[4]) "evaporador"q_dot_H = m_dot * (h[2]-h[3]) "condensador"W_dot_c = ABS(m_dot * ( h[2]-h[1])) "compressor"COF = abs(q_L/W_c)h[1] = ((lambda/(lambda+1)) * hp1_1) + ((1/(lambda+1)) * hp1_2)hp1_1 = enthalpy(R1$; x=x[1]; T=T[1])hp1_2 = enthalpy(R2$; x=x[1]; T=T[1])s_1[1] = entropy(R1$; x=x[1]; T=T[1])s_1[2] = entropy(R2$; x=x[1]; T=T[1])v_1[1] = volume(R1$; P=P[1]; T=T[1])v_2[1] = volume(R2$; P=P[1]; T=T[1])s_1[3] = entropy(R1$; P=P[3]; x=x[3])s_2[3] = entropy(R2$; P=P[3]; x=x[3])v_1[3] = volume(R1$; P=P[3]; x=x[3])v_2[3] = volume(R2$; P=P[3]; x=x[3])v_1[2] = volume(R1$; P=P[2]; s=s_1[2])v_2[2] = volume(R2$; P=P[2]; s=s_2[2])q_L = h[1]-h[4] "evaporador"q_H = h[2]-h[3] "condensador"W_c = abs( h[2]-h[1]) "compressor"q_dot_L = m_dot * (h[1]-h[4]) "evaporador"q_dot_H = m_dot * (h[2]-h[3]) "condensador"W_dot_c = ABS(m_dot * ( h[2]-h[1])) "compressor"COF = abs(q_L/W_c)h[1] = ((lambda/(lambda+1)) * hp1_1) + ((1/(lambda+1)) * hp1_2)hp1_1 = enthalpy(R1$; x=x[1]; T=T[1])hp1_2 = enthalpy(R2$; x=x[1]; T=T[1])s_1[1] = entropy(R1$; x=x[1]; T=T[1])s_1[2] = entropy(R2$; x=x[1]; T=T[1])v_1[1] = volume(R1$; P=P[1]; T=T[1])v_2[1] = volume(R2$; P=P[1]; T=T[1])s_1[3] = entropy(R1$; P=P[3]; x=x[3])s_2[3] = entropy(R2$; P=P[3]; x=x[3])v_1[3] = volume(R1$; P=P[3]; x=x[3])v_2[3] = volume(R2$; P=P[3]; x=x[3])v_1[2] = volume(R1$; P=P[2]; s=s_1[2])v_2[2] = volume(R2$; P=P[2]; s=s_2[2])q_L = h[1]-h[4] "evaporador"q_H = h[2]-h[3] "condensador"W_c = abs( h[2]-h[1]) "compressor"q_dot_L = m_dot * (h[1]-h[4]) "evaporador"q_dot_H = m_dot * (h[2]-h[3]) "condensador"W_dot_c = ABS(m_dot * ( h[2]-h[1])) "compressor"COF = abs(q_L/W_c)h[1] = ((lambda/(lambda+1)) * hp1_1) + ((1/(lambda+1)) * hp1_2)hp1_1 = enthalpy(R1$; x=x[1]; T=T[1])hp1_2 = enthalpy(R2$; x=x[1]; T=T[1])s_1[1] = entropy(R1$; x=x[1]; T=T[1])s_1[2] = entropy(R2$; x=x[1]; T=T[1])v_1[1] = volume(R1$; P=P[1]; T=T[1])v_2[1] = volume(R2$; P=P[1]; T=T[1])s_1[3] = entropy(R1$; P=P[3]; x=x[3])s_2[3] = entropy(R2$; P=P[3]; x=x[3])v_1[3] = volume(R1$; P=P[3]; x=x[3])v_2[3] = volume(R2$; P=P[3]; x=x[3])v_1[2] = volume(R1$; P=P[2]; s=s_1[2])v_2[2] = volume(R2$; P=P[2]; s=s_2[2])q_L = h[1]-h[4] "evaporador"q_H = h[2]-h[3] "condensador"W_c = abs( h[2]-h[1]) "compressor"q_dot_L = m_dot * (h[1]-h[4]) "evaporador"q_dot_H = m_dot * (h[2]-h[3]) "condensador"W_dot_c = ABS(m_dot * ( h[2]-h[1])) "compressor"COF = abs(q_L/W_c)h[1] = ((lambda/(lambda+1)) * hp1_1) + ((1/(lambda+1)) * hp1_2)hp1_1 = enthalpy(R1$; x=x[1]; T=T[1])hp1_2 = enthalpy(R2$; x=x[1]; T=T[1])s_1[1] = entropy(R1$; x=x[1]; T=T[1])s_1[2] = entropy(R2$; x=x[1]; T=T[1])v_1[1] = volume(R1$; P=P[1]; T=T[1])v_2[1] = volume(R2$; P=P[1]; T=T[1])s_1[3] = entropy(R1$; P=P[3]; x=x[3])s_2[3] = entropy(R2$; P=P[3]; x=x[3])v_1[3] = volume(R1$; P=P[3]; x=x[3])v_2[3] = volume(R2$; P=P[3]; x=x[3])v_1[2] = volume(R1$; P=P[2]; s=s_1[2])v_2[2] = volume(R2$; P=P[2]; s=s_2[2])q_L = h[1]-h[4] "evaporador"q_H = h[2]-h[3] "condensador"W_c = abs( h[2]-h[1]) "compressor"q_dot_L = m_dot * (h[1]-h[4]) "evaporador"q_dot_H = m_dot * (h[2]-h[3]) "condensador"W_dot_c = ABS(m_dot * ( h[2]-h[1])) "compressor"COF = abs(q_L/W_c)h[1] = ((lambda/(lambda+1)) * hp1_1) + ((1/(lambda+1)) * hp1_2)hp1_1 = enthalpy(R1$; x=x[1]; T=T[1])hp1_2 = enthalpy(R2$; x=x[1]; T=T[1])s_1[1] = entropy(R1$; x=x[1]; T=T[1])s_1[2] = entropy(R2$; x=x[1]; T=T[1])v_1[1] = volume(R1$; P=P[1]; T=T[1])v_2[1] = volume(R2$; P=P[1]; T=T[1])s_1[3] = entropy(R1$; P=P[3]; x=x[3])s_2[3] = entropy(R2$; P=P[3]; x=x[3])v_1[3] = volume(R1$; P=P[3]; x=x[3])v_2[3] = volume(R2$; P=P[3]; x=x[3])v_1[2] = volume(R1$; P=P[2]; s=s_1[2])v_2[2] = volume(R2$; P=P[2]; s=s_2[2])q_L = h[1]-h[4] "evaporador"q_H = h[2]-h[3] "condensador"W_c = abs( h[2]-h[1]) "compressor"q_dot_L = m_dot * (h[1]-h[4]) "evaporador"q_dot_H = m_dot * (h[2]-h[3]) "condensador"W_dot_c = ABS(m_dot * ( h[2]-h[1])) "compressor"COF = abs(q_L/W_c)h[1] = ((lambda/(lambda+1)) * hp1_1) + ((1/(lambda+1)) * hp1_2)hp1_1 = enthalpy(R1$; x=x[1]; T=T[1])hp1_2 = enthalpy(R2$; x=x[1]; T=T[1])s_1[1] = entropy(R1$; x=x[1]; T=T[1])s_1[2] = entropy(R2$; x=x[1]; T=T[1])v_1[1] = volume(R1$; P=P[1]; T=T[1])v_2[1] = volume(R2$; P=P[1]; T=T[1])s_1[3] = entropy(R1$; P=P[3]; x=x[3])s_2[3] = entropy(R2$; P=P[3]; x=x[3])v_1[3] = volume(R1$; P=P[3]; x=x[3])v_2[3] = volume(R2$; P=P[3]; x=x[3])v_1[2] = volume(R1$; P=P[2]; s=s_1[2])v_2[2] = volume(R2$; P=P[2]; s=s_2[2])q_L = h[1]-h[4] "evaporador"q_H = h[2]-h[3] "condensador"W_c = abs( h[2]-h[1]) "compressor"q_dot_L = m_dot * (h[1]-h[4]) "evaporador"q_dot_H = m_dot * (h[2]-h[3]) "condensador"W_dot_c = ABS(m_dot * ( h[2]-h[1])) "compressor"COF = abs(q_L/W_c)h[1] = ((lambda/(lambda+1)) * hp1_1) + ((1/(lambda+1)) * hp1_2)hp1_1 = enthalpy(R1$; x=x[1]; T=T[1])hp1_2 = enthalpy(R2$; x=x[1]; T=T[1])s_1[1] = entropy(R1$; x=x[1]; T=T[1])s_1[2] = entropy(R2$; x=x[1]; T=T[1])v_1[1] = volume(R1$; P=P[1]; T=T[1])v_2[1] = volume(R2$; P=P[1]; T=T[1])s_1[3] = entropy(R1$; P=P[3]; x=x[3])s_2[3] = entropy(R2$; P=P[3]; x=x[3])v_1[3] = volume(R1$; P=P[3]; x=x[3])v_2[3] = volume(R2$; P=P[3]; x=x[3])v_1[2] = volume(R1$; P=P[2]; s=s_1[2])v_2[2] = volume(R2$; P=P[2]; s=s_2[2])q_L = h[1]-h[4] "evaporador"q_H = h[2]-h[3] "condensador"W_c = abs( h[2]-h[1]) "compressor"q_dot_L = m_dot * (h[1]-h[4]) "evaporador"q_dot_H = m_dot * (h[2]-h[3]) "condensador"W_dot_c = ABS(m_dot * ( h[2]-h[1])) "compressor"COF = abs(q_L/W_c)h[1] = ((lambda/(lambda+1)) * hp1_1) + ((1/(lambda+1)) * hp1_2)hp1_1 = enthalpy(R1$; x=x[1]; T=T[1])hp1_2 = enthalpy(R2$; x=x[1]; T=T[1])