TY - JOUR
T1 - Correction to
T2 - Darcy–Brinkman Model for Ternary Dusty Nanofluid Flow across Stretching/Shrinking Surface with Suction/Injection (Fluids, (2024), 9, 4, (94), 10.3390/fluids9040094)
AU - Sachhin, Sudha Mahanthesh
AU - Mahabaleshwar, Ulavathi Shettar
AU - Laroze, David
AU - Drikakis, Dimitris
N1 - Publisher Copyright:
© 2024 by the authors.
PY - 2024/10
Y1 - 2024/10
N2 - Figures: In Section 5, we aligned Figures 14–18 by consistently adding all the modelling parameters inside the labels [1]. We also revised the captions for Figures 14–18 to clearly state what they represent [1]. The correct Figure 14, Figure 15, Figure 16, Figure 17, Figure 18 appears below. Text Correction: In Section 2, the following text was added: “Similar to previous studies [2]”, “b is a parameter that is b > 0 for heated and b < 0 for cooled plate”. The correct text appears below. Similar to previous studies [2], here, (Formula presented.), and (Formula presented.) are the velocity components of a fluid and dusty fluid phase along the x- and y-directions, respectively; the dusty and fluid phase temperatures are Tp and T; (Formula presented.) is the dynamic viscosity; (Formula presented.) is the effective density; (Formula presented.) is the thermal conductivity; b is a parameter that is b > 0 for heated and b < 0 for cooled plate; (Formula presented.) is the electrical conductivity; (Formula presented.) and (Formula presented.) are the specific heat coefficients; (Formula presented.) is the heat equilibrium time; (Formula presented.) is the Stokes drag/resistance term; (Formula presented.) is the kinematic viscosity of nanoparticles N; (Formula presented.) is the flow permeability; and (Formula presented.) is a relaxation time parameter, where m denotes the mass of dusty particles [2]. In Section 2, we corrected the typographical error in the definition of the Prandtl number. The correct one is (Formula presented.). In Section 5, we revised the text to avoid ambiguity regarding the results of Figure 14, Figure 15, Figure 16 [1]. The correct text appears below. Figure 14, Figure 15, Figure 16 show the temperatures for the fluid and dusty phases for different values of S = −2, 0 and 2, respectively. Increasing S value increases the thermal boundary layer thickness of the fluid phase. The dusty phase exhibits an increase in the thermal boundary layer when S increases from −2 to 0, while decreases for S = 2. Equations: In Equations (35)–(39), there are typographical errors. We revised the subscript thnf to tnf. In Equation (38), we also revised the κnf to κf. The correct equations appears below: (Formula presented.) (Formula presented.) (Formula presented.) (Formula presented.) (Formula presented.) Nomenclature: We added the units that were missing in several parameters and corrected the typographical errors in some of the parameters [1]. The correct Nomenclature appears below. The authors state that the scientific conclusions are unaffected. These corrections were approved by the Academic Editor. The original publication has also been updated.
AB - Figures: In Section 5, we aligned Figures 14–18 by consistently adding all the modelling parameters inside the labels [1]. We also revised the captions for Figures 14–18 to clearly state what they represent [1]. The correct Figure 14, Figure 15, Figure 16, Figure 17, Figure 18 appears below. Text Correction: In Section 2, the following text was added: “Similar to previous studies [2]”, “b is a parameter that is b > 0 for heated and b < 0 for cooled plate”. The correct text appears below. Similar to previous studies [2], here, (Formula presented.), and (Formula presented.) are the velocity components of a fluid and dusty fluid phase along the x- and y-directions, respectively; the dusty and fluid phase temperatures are Tp and T; (Formula presented.) is the dynamic viscosity; (Formula presented.) is the effective density; (Formula presented.) is the thermal conductivity; b is a parameter that is b > 0 for heated and b < 0 for cooled plate; (Formula presented.) is the electrical conductivity; (Formula presented.) and (Formula presented.) are the specific heat coefficients; (Formula presented.) is the heat equilibrium time; (Formula presented.) is the Stokes drag/resistance term; (Formula presented.) is the kinematic viscosity of nanoparticles N; (Formula presented.) is the flow permeability; and (Formula presented.) is a relaxation time parameter, where m denotes the mass of dusty particles [2]. In Section 2, we corrected the typographical error in the definition of the Prandtl number. The correct one is (Formula presented.). In Section 5, we revised the text to avoid ambiguity regarding the results of Figure 14, Figure 15, Figure 16 [1]. The correct text appears below. Figure 14, Figure 15, Figure 16 show the temperatures for the fluid and dusty phases for different values of S = −2, 0 and 2, respectively. Increasing S value increases the thermal boundary layer thickness of the fluid phase. The dusty phase exhibits an increase in the thermal boundary layer when S increases from −2 to 0, while decreases for S = 2. Equations: In Equations (35)–(39), there are typographical errors. We revised the subscript thnf to tnf. In Equation (38), we also revised the κnf to κf. The correct equations appears below: (Formula presented.) (Formula presented.) (Formula presented.) (Formula presented.) (Formula presented.) Nomenclature: We added the units that were missing in several parameters and corrected the typographical errors in some of the parameters [1]. The correct Nomenclature appears below. The authors state that the scientific conclusions are unaffected. These corrections were approved by the Academic Editor. The original publication has also been updated.
UR - http://www.scopus.com/inward/record.url?scp=85207844791&partnerID=8YFLogxK
U2 - 10.3390/fluids9100241
DO - 10.3390/fluids9100241
M3 - Comment/debate
AN - SCOPUS:85207844791
SN - 2311-5521
VL - 9
JO - Fluids
JF - Fluids
IS - 10
M1 - 241
ER -