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Errata to: M.-D. Staicovici, Coabsorbent and Thermal Recovery Compression Heat Pumping Technologies, DOI 10.1007/978-3-642-54684-6
Corrections to be made to the book “Coabsorbent and Thermal Recovery Compression Heat Pumping Technologies, author Mihail-Dan Staicovici
Page | Present text | Corrections to be made = the text which the “Present text” must be replaced with |
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viii, row 12 from top | The discharge gas superheat recovery is converted… | The recovered discharge gas superheat is converted… |
17, row 14 from bottom | elaborated it 1824. | elaborated it in 1824. |
21, row 10 from bottom | Than, | Then, |
22, row 2 from bottom | in eqn. (1.98) | inequality (1.98) |
22, row 5 from bottom | In in eqn. (1.98) | In inequality (1.98) |
23, 1st row from top | In eqn. (1.100) | inequality (1.100) |
23, row 8 from top | in eqn. (1.101) | inequality (1.101) |
23, row 10 from top | In eqn. (1.102) | Inequality (1.102) |
23, row 2 from bottom | in eqn. (1.108) | inequality (1.108) |
23, row 3 from bottom | ineqn. (1.105) | Inequality (1.105) |
23, row 12 from bottom | In in eqn. (1.105) | In inequality (1.105) |
23, row 15 from bottom | In eqn. (1.103) | Inequality (1.103) |
27, row 3 from top | calculated with the help the arithmetical mean | calculated with the help of the arithmetical mean |
29, row 18 from bottom | where \( - \left( {dE} \right)_{irrev} \) is the exergy dissipation | where \( - \frac{\partial E}{\partial t}dt \) is the exergy dissipation |
36, row 12 from bottom | free energy relationship as \( U = F + TS \), Eq. (1.155), | free energy relationship as \( U = F + TS \), Eq. (1.164), |
45, row 7 from top | Eq. (1.208) partial derivatives are given by Eqs. (1.160) and (1.161) of Table 1.1, … | Eq. (1.208) partial derivatives are given by Eqs. (1.169) and (1.170) of Table 1.1, … |
61, row 6 from top | Introducing Eq. (1.244) in Eq. (1.243), it is obtained: | Introducing Eqs. (1.244) and (1.243) in Eq. (1.242), it is obtained: |
61, Eq. (1.248) | \( \left[ {\frac{{\partial q_{mix} }}{{\partial \left( {1 - y} \right)}}} \right]_{{m_{1} }} \left[ {\frac{{\partial \left( {1 - y} \right)}}{{\partial m_{2} }}} \right]_{{m_{1} }} = - y\left[ {\frac{{\partial q_{mix} }}{\partial y}} \right]_{{m_{2} }} \) | \( \left[ {\frac{{\partial q_{mix} }}{{\partial \left( {1 - y} \right)}}} \right]_{{m_{1} }} \left[ {\frac{{\partial \left( {1 - y} \right)}}{{\partial m_{2} }}} \right]_{{m_{1} }} = - y\left[ {\frac{{\partial q_{mix} }}{\partial y}} \right]_{{m_{1} }} \) |
61, Eq. (1.249) | \( q_{d2} = q_{mix} - y\left[ {\frac{{\partial q_{mix} }}{\partial y}} \right]_{{m_{2} }} \) | \( q_{d2} = q_{mix} - y\left[ {\frac{{\partial q_{mix} }}{\partial y}} \right]_{{m_{1} }} \) |
61, rows 4 and 5 from bottom | Eqs. (1.243) and (1.246) | Eqs. (1.242) and (1.249) |
Fig.1.21 |
|
|
62, Eq. (1.252) | \( \left( {1 - y} \right)\left[ {\frac{{\partial q_{{d_{1} }} }}{\partial y}} \right]_{{m_{2} }} + y\left[ {\frac{{\partial q_{{d_{2} }} }}{\partial y}} \right]_{{m_{1} }} = 0 \) | \( \left( {1 - y} \right)\left[ {\frac{{\partial q_{{d_{1} }} }}{\partial y}} \right]_{{m_{1} }} + y\left[ {\frac{{\partial q_{{d_{2} }} }}{\partial y}} \right]_{{m_{2} }} = 0 \) |
62, rows 9 and 10 from bottom | Eqs. (1.245) and (1.249) of \( q_{d1} \) and \( q_{d2} \) are further partially derived with respect to \( y \) for \( m_{2} = const. \) and with respect to \( \left( {1 - y} \right) \) for \( m_{1} = const. \), respectively. | Eqs. (1.245) and (1.249) of \( q_{d1} \) and \( q_{d2} \) are further partially derived with respect to \( y \) for \( m_{1} = const. \) and with respect to \( \left( {1 - y} \right) \) for \( m_{2} = const. \), respectively. |
62, Eq. (1.253) | \( \left[ {\frac{{\partial q_{{d_{1} }} }}{\partial y}} \right]_{{m_{2} }} + \left[ {\frac{{\partial q_{{d_{2} }} }}{\partial y}} \right]_{{m_{1} }} = 0 \) | \( \left[ {\frac{{\partial q_{{d_{1} }} }}{\partial y}} \right]_{{m_{1} }} + \left[ {\frac{{\partial q_{{d_{2} }} }}{\partial y}} \right]_{{m_{2} }} = 0 \) |
62, Eq. (1.254) | \( \left[ {\frac{{\partial q_{{d_{1} }} }}{\partial y}} \right]_{{m_{2} }} - \left[ {\frac{{\partial q_{{d_{2} }} }}{\partial y}} \right]_{{m_{1} }} = - 2\left[ {\left[ {\frac{{\partial q_{mix} }}{\partial y}} \right]_{{m_{1} }} - \left[ {\frac{{\partial q_{mix} }}{\partial y}} \right]_{{m_{2} }} } \right] \) | \( \left[ {\frac{{\partial q_{{d_{1} }} }}{\partial y}} \right]_{{m_{1} }} - \left[ {\frac{{\partial q_{{d_{2} }} }}{\partial y}} \right]_{{m_{2} }} = 2\left[ {\left[ {\frac{{\partial q_{mix} }}{\partial y}} \right]_{{m_{1} }} - \left[ {\frac{{\partial q_{mix} }}{\partial y}} \right]_{{m_{2} }} } \right] \) |
62, row 3 from bottom | Equations (1.252) and (1.253) are solved together for \( \left[ {\frac{{\partial q_{{d_{1} }} }}{\partial y}} \right]_{{m_{2} }} \) and \( \left[ {\frac{{\partial q_{{d_{2} }} }}{\partial y}} \right]_{{m_{1} }} \), obtaining: | Equations (1.252) and (1.253) are solved together for \( \left[ {\frac{{\partial q_{{d_{1} }} }}{\partial y}} \right]_{{m_{1} }} \) and \( \left[ {\frac{{\partial q_{{d_{2} }} }}{\partial y}} \right]_{{m_{2} }} \), obtaining: |
62, Eq. (1.255) | \( \left[ {\frac{{\partial q_{{d_{1} }} }}{\partial y}} \right]_{{m_{2} }} = \left[ {\frac{{\partial q_{{d_{2} }} }}{\partial y}} \right]_{{m_{1} }} = 0 \) | \( \left[ {\frac{{\partial q_{{d_{1} }} }}{\partial y}} \right]_{{m_{1} }} = \left[ {\frac{{\partial q_{{d_{2} }} }}{\partial y}} \right]_{{m_{2} }} = 0 \) |
70, row 7 from bottom | The specific Gibbs free enthalpy is at the same time the chemical potential of the system, \( \varphi = \left( {\frac{\partial \varPhi }{\partial G}} \right)_{T,p} \), according to eqn. (1.163). | The specific Gibbs free enthalpy is at the same time the chemical potential of the system, \( \varphi = \left( {\frac{\partial \varPhi }{\partial G}} \right)_{T,p} \), according to eqn. (1.172). |
70, row 9 from bottom | specific Gibbs free enthalpy assessment, \( \varphi \), \( \varphi = \frac{\varPhi }{G} \), (\( \varPhi \left( {T,\,p} \right) = H - TS \), Table 1.1, eqn. (1.159))… | specific Gibbs free enthalpy assessment, \( \varphi \), \( \varphi = \frac{\varPhi }{G} \), (\( \varPhi \left( {T,\,p} \right) = H - TS \), Table 1.1, eqn. (1.168))… |
73, row 12 from bottom | In eqn. (1.283), the last bracket of the right member can be calculated from eqns. (1.276) and (1.277)… | In eqn. (1.283), the last bracket of the right member can be calculated from gas phase eqns. (1.276) and (1.277)… |
75, row 3 from bottom | Gas phase: \(c_{p}^{l}\left( T,{{p}_{0}} \right)={{b}_{1}}+{{b}_{2}}T+{{b}_{3}}{{T}^{2}}\) (1.294) \({{v}^{g}}\left( T,p \right)=\frac{RT}{p}+{{c}_{1}}+\frac{{{c}_{2}}}{{{T}^{3}}}+\frac{{{c}_{3}}}{{{T}^{11}}}+\frac{{{c}_{4}}{{p}^{2}}}{{{T}^{11}}}\) (1.295) | \(c_{p}^{l}\left( T,{{p}_{0}} \right)={{b}_{1}}+{{b}_{2}}T+{{b}_{3}}{{T}^{2}}\) (1.294) Gas phase: \({{v}^{g}}\left( T,p \right)=\frac{RT}{p}+{{c}_{1}}+\frac{{{c}_{2}}}{{{T}^{3}}}+\frac{{{c}_{3}}}{{{T}^{11}}}+\frac{{{c}_{4}}{{p}^{2}}}{{{T}^{11}}}\) (1.295) |
75, row 5 from top | \( \left( {y = 0;Y = 0} \right) \) | \( \left( {y = 0;Y = 1} \right) \) |
78, 1st row from top | Introducing eqns. (1.295), (1.296) and (1.306) in eqn. (1.304), the analytical expression of the gas phase free enthalpy results: | Introducing eqns. (1.295), (1.296) and (1.306) in eqn. (1.307), the analytical expression of the gas phase free enthalpy results: |
128, row 8 from the bottom | This time, temperature is the internal heating temperature…. | This time, \( T_{M} \) temperature is the internal heating temperature…. |
186, row 6 from top | for seen | foreseen |
208, Caption of Fig. 417 | Fig. 4.44 | Fig. 4.45 |
208, row 2 from top | (see Fig. 4.44 of Sect. 4.3.2) | (see Fig. 4.45 of Sect. 4.3.1) |
209, row 2 from the top | Fig. 4.44 | Fig. 4.43 |
210, row 5 from bottom | y GO,1 | ΔT gax,R |
211, row 6 from top | \(\Delta {{T}_{R,i,gax\left( \Delta {{T}_{gax,R,\max }} \right)}}\) | \({{y}_{R,i,gax}}={{y}_{R,i,gax}}\left( \Delta {{T}_{gax,R,\max }} \right)\) |
212, row 3 from the bottom | \( \Delta T_{gax,R,\hbox{max} } \le \Delta T_{gax,R} \le \Delta T_{gax,R,\hbox{max} } \) | \( \Delta T_{gax,R,\hbox{min} } \le \Delta T_{gax,R} \le \Delta T_{gax,R,\hbox{max} } \) |
214, 4th row down from Eq. (4.122) | \(y_{{G,j,gax}^{e}} \) | \( y_{G,j,gax}^{e} \) |
215, 7th row down from Eq. (4.129) | Fig. 4.37a of Sect. 4.2.3 | Fig. 4.38a of Sect. 4.2.3 |
215, | GHE-Gax problem study cases | GHE-Gax problem study cases |
215, row 3 from the bottom | Resorber Heat Excess (RHE) Gax Operation Model | Generator Heat Excess (GHE) Gax Operation Model |
215, row 12 from the bottom | Results of the RHE-Gax Model Run with \( \varDelta T_{gax,R,\hbox{min} } \)- Infinite Equivalent Solutions to A GHE-Gax Problem | Results of the GHE-Gax Model Run with an intermediate \( \varDelta T_{gax,G} \)- Infinite Equivalent Solutions to a GHE-Gax Problem |
216, row 12 down from the top | \( q_{{G,1,gax}^{e}} = 574.6 \) | \( q_{G,1,gax}^{e} = 574.6 \) |
218, row 5 from the bottom | According to the 6th study case, running the 4.2.1.3.2. sub-sub-paragraph model for the configuration… | According to the 6th study case, running the Sect. Generator Heat Excess (GHE) Gax Operation Model for the configuration… |
250, row 13 from top | Equations (5.6) and (1.214)… | Equations (5.6) and (1.223)… |
251, row 2 from bottom | Eq. (1.217)… | Eq. (1.226)… |
265, row 3 from top | Important properties of the cascades at hand is emphasized next | Important properties of the cascades at hand are emphasized next |
266, row 2 from top | Eq. (1.81)… | Eq. (1.65)… |
266, row 6 from top | Eqs. (5.81) (5.82), (5.76) and (5.77) | Eqs. (5.81) and (5.82), Eqs. (5.76) and (5.77) |
267, row 7 from top | Eqs. (1.208) and (1.209)… | Eqs. (1.217) and (1.218)… |
267, row 6 from bottom | Eqs. (1.208) and (1.209)… | Eqs. (1.217) and (1.218)… |
268, 1st row from bottom | (last column, the CO2-NH3 known cascade). Table 5.3. | (last column, the CO2-NH3 known cascade). |
300, row 18 from bottom | Appendix 1 | Appendix 7 |
309, row 12 from bottom | , it results that in Eq. … | , it results that inequality … |
309, row 13 from bottom | Indeed, from the obvious in equations | Indeed, from the obvious inequalities |
315, 1st row from bottom | Appendix 2 | Appendix 7 |
324, row 7 from top | Appendix 1 | Appendix 7 |
324, row 8 from top | Equation (7.34) … | i)Equation (7.34) … |
324, row 11 from top | Considering in Eqs. (A7.1, 7.20, 7.28) … | Considering in Eq. (A7.1), Eqs. (7.19, 7.28) … |
324, row 13 from top | Appendix 2 | |
324, row 14 from top | A simple, yet not simplistic, explanation … | ii)A simple, yet not simplistic, explanation … |
331, row 12 from top | Appendix 1 | Appendix 8 |
334, row 2 from top | (see Appendix 1 of this chapter) | (see Appendix 8 of this chapter) |
338, row 13 from bottom | Appendix 1 | Appendix 8 |
338, row 16 from bottom | Appendix 1 | Appendix 8 |
369, 1st row from bottom | Appendix 1 | Appendix 8 |
369, row 7 from bottom | \( 1 > \frac{n\,+\,1}{n\,+\,2}x < 1 \) | \( \frac{n\,+\,1}{n\,+\,2}x < 1 \) |
373, row 4 from bottom | Appendix 1 | Appendix 8 |
375, 1st row | \( \begin{gathered} \eta_{C} \left( \xi \right) = 1 - \frac{{\ln \frac{{T_{2a} }}{{T_{1} }}}}{{\frac{{T_{2a} }}{{T_{1} }} - 1}} \equiv \eta_{C,TFC} = \hfill \\ = 1 - \frac{{2T_{1} }}{{T_{2a} - T_{1} }}\frac{{T_{2a} - T_{1} }}{{T_{2a} + T_{1} }} \hfill \\ \end{gathered} \)(A8.4) | |
378, row 4 from top | \({{T}_{ax}}-{{T}_{{{T}_{2a}}}}\) | \({{T}_{ax}}-{{T}_{2a}}\) |
391, row 6 from top | (see Appendix of this chapter) | (see Appendix 9 of this chapter) |
403, row 2 from top | Eqs. (9.57) and (9.70) | Eqs. (9.56) and (9.70) |
430, row 2 from bottom | (see Appendix) | (see Appendix 9) |
431, row 10 from top | (see Appendix) | (see Appendix 9) |
449, Eq. (9.180) | \( \begin{gathered} \frac{{h_{1} - h_{2} }}{{T_{{f,w}} }} +\frac{{h_{3} - h_{4} }}{{T_{{f,s}} }} + \left( {h_{{ep,w,2}} -h_{{ep,w,1}} } \right)\left( {\frac{1}{{T_{{f,w}} }} -\frac{1}{{T_{{ep,w}} }}} \right) \hfill \\ + \left( {h_{{f,s,4}}- h_{{f,s,3}} } \right)\left( {\frac{1}{{T_{{f,s}} }} -\frac{1}{{T_{{ep,s}} }}} \right) \hfill \\ \end{gathered}\) | \( \begin{gathered} \frac{{h_{1} - h_{2} }}{{T_{{f,w}} }} +\frac{{h_{3} - h_{4} }}{{T_{{f,s}} }} + \left( {h_{{ep,w,2}} -h_{{ep,w,1}} } \right)\left( {\frac{1}{{T_{{f,w}} }} -\frac{1}{{T_{{ep,w}} }}} \right) \hfill \\ + \left( {h_{{f,s,4}}- h_{{f,s,3}} } \right)\left( {\frac{1}{{T_{{f,s}} }} -\frac{1}{{T_{{ep,s}} }}} \right) = 0 \hfill \\ \end{gathered} \) |
451, row 12 from top | Appendix 1 | Appendix 9 |
451, row 13 from top | The natural … | i)The natural … |
452, row 3 from top | Appendix 1 | |
452, row 3 from top | Using the vector … | ii)Using the vector … |
463, row 2 from top | Appendix | Appendix 10 |
465, row 14 from top | Appendix | Appendix 10 |
495, row 3 from bottom | The Heat/sink sources… | The heat/sink sources… |
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Staicovici, MD. (2014). Errata to: Coabsorbent and Thermal Recovery Compression Heat Pumping Technologies. In: Coabsorbent and Thermal Recovery Compression Heat Pumping Technologies. Heat and Mass Transfer. Springer, Berlin, Heidelberg. https://doi.org/10.1007/978-3-642-54684-6_12
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DOI: https://doi.org/10.1007/978-3-642-54684-6_12
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