Sergio  Nardini

Sergio Nardini


Research Focus & Metrics

Academic Career Length

37Years (1990-Present)

(Calculated once Scilit publication data is synced: current year − year of first publication + 1)

Representative Publications

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1 September 2009 in Energy
Verified
Journal Article
Closed access
Vincenzo BiancoVincenzo Bianco
Vincenzo Bianco
Oronzio MancaOronzio Manca
Oronzio Manca
Sergio  NardiniSergio Nardini
Sergio Nardini

1 December 2009 in Applied Thermal Engineering
Verified
Journal Article
Closed access
Vincenzo BiancoVincenzo Bianco
Vincenzo Bianco
FCF. Chiacchio
F. Chiacchio
Oronzio MancaOronzio Manca
Oronzio Manca
Sergio  NardiniSergio Nardini
Sergio Nardini

1 May 2012 in Applied Thermal Engineering
Verified
Journal Article
Closed access
Oronzio MancaOronzio Manca
Oronzio Manca
Sergio  NardiniSergio Nardini
Sergio Nardini
DRDaniele Ricci
Daniele Ricci

1 March 2011 in International Journal of Thermal Sciences
Verified
Journal Article
Closed access
Vincenzo BiancoVincenzo Bianco
Vincenzo Bianco
Oronzio MancaOronzio Manca
Oronzio Manca
Sergio  NardiniSergio Nardini
Sergio Nardini

1 November 2010 in Applied Energy
Verified
Journal Article
Closed access
Vincenzo BiancoVincenzo Bianco
Vincenzo Bianco
Oronzio MancaOronzio Manca
Oronzio Manca
Sergio  NardiniSergio Nardini
Sergio Nardini
Alina Adriana MineaAlina Adriana Minea
Alina Adriana Minea

1 February 2003 in Numerical Heat Transfer, Part A: Applications
Verified
Journal Article
Closed access
Oronzio MancaOronzio Manca
Oronzio Manca
Sergio  NardiniSergio Nardini
Sergio Nardini
KKKhalil Khanafer
Khalil Khanafer
KVKambiz Vafai
Kambiz Vafai
Mixed convection in an open cavity with a heated wall bounded by a horizontally insulated plate is studied numerically. Three basic heating modes are considered: (a) the heated wall is on the inflow side (assisting flow); (b) the heated wall is on the outflow side (opposing flow); and (c) the heated wall is the horizontal surface of the cavity (heating from below). Mixed convection fluid flow and heat transfer within the cavity is governed by the buoyancy parameter, Richardson number (Ri), and Reynolds number (Re). The results are reported in terms of streamlines, isotherms, wall temperature, and the velocity profiles in the cavity for Ri=0.1 and 100, Re=100 and 1000, and the ratio between the channel and cavity heights (H/D) is in the range 0.1-1.5. The present results show that the maximum temperature values decrease as the Reynolds and the Richardson numbers increase. The effect of the H/D ratio is found to play a significant role on streamline and isotherm patterns for differentheating configurations. The present investigation shows that the opposing forced flow configuration has the highest thermal performance in terms of both maximum temperature and average Nusselt number.