Contributors: Jadran Vrabec, René Spencer Chatwell, Matthias Heinen
... The files named "Density_profiles_part0x.mp4" demonstrate the time evolution of both the liquid and vapour phase densities. The color coding is according to the main manuscript. The video starts from the initial vapor-liquid equilibrium and transitions into the evaporative dynamics. The file named "Evaporation_atomistic.mp4" gives an exemplary overview of the object under study. The liquid film is centered in the middle and surrounded by vapor on each site.
Contributors: Garrett Mann, Steven Eckels
... This is a Pareto archive from 10 generations of an NSGA-II algorithm seeking to minimize friction factor and maximize heat transfer for a micro-fin tube. The design parameters are fin height, helix angle, and number of starts. The flow rate and Reynolds number is held constant. The archive consists of 80 non-dominated individuals with geometry and corresponding friction factor and heat transfer.
Data for: Influence of substrate temperature on Marangoni convection instabilities in a sessile droplet evaporating at constant contact line mode
Contributors: Wan-Yuan Shi, Tian-Shi Wang
... Two videos are corrsponding to the Marangoni instabilities in a sessile evaporating droplet for Fig.3 and Fig.11 in the paper. The video for Fig.3 is mainly aimed at the state of steady Bénard-Marangoni convection and irregular oscillatory Bénard-Marangoni convection. The video for Fig.11 is mainly aimed at the phenomenon of hydrothermal waves and coexistence of the hydrothermal waves and the irregular oscillatory Bénard-Marangoni convection.
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Data for: DropletSMOKE: a comprehensive multiphase CFD framework for the evaporation of multidimensional fuel droplets
Contributors: Alberto Cuoci, Alessio Frassoldati, Abd Essamade Saufi, Tiziano Faravelli
... OpenFOAM code of the DropletSMOKE solver, written in C++
Data for: Enhanced Thin Film Evaporation via Impinging Electrospray Liquid Jets with Passively Entrained Air
Contributors: Andrei Federov, Peter Kottke, Joel Chapman
... 22DEC17 Post-Calibration corresponds to RTD calibration data as given in supplementary information. "12-22-2017 experiments" is the analyzed data for the confined-film experiments, while "Data INSTR 1 12_22_2017" is the raw DAQ-captured data from those experiments. Experiment Data Fig 9 is further parsed out of the analyzed data. "21DEC2017 Experiments" is the analyzed data for the non-confined film experiments, while "Data INSTR 1 12_21_2017" is the raw DAQ-captured data from those experiments.
Data for: Estimating the transient thermal boundary conditions with an improved space marching technique
Contributors: Zhongwei Huang, Ran Li
... The dataset contains the MATLAB code for the space marching method proposed in the article and the temperature data from the cryogenic quenching experiment.
Data for: Condensation heat transfer and pressure drop characteristics of R134a, R1234ze(E), R245fa and R1233zd in a plate heat exchanger
Contributors: Ji Zhang, Martin Ryhl Kærn, Torben Ommen, Fredrik Haglind, Brian Elmegaard
... Experimental data points of heat transfer coefficient and pressure drop in Figures 6 and 7.
Contributors: Qiang Wang
Supplemental High-Speed Videos for: Experimental comparison and visualization of in-tube continuous and pulsating flow boiling
Contributors: Martin Ryhl Kærn
... These videos show pulsating flow boiling performed by a pulse width modulated expansion valve and continuous flow boiling performed by a stepper motor expansion valve. The cycle time for the pulsating flow are 1 s and 5 s, respectively. The refrigerant is R134a with upstream saturation temperature of 30 C and subcooling of 2 K and 20 K, respectively. Downsteam evaporation temperature is 5 C. The time-averaged mass flux is 100 kg/m2s. More information is available in recent submitted paper.
Data for: Flow Boiling Heat Transfer and Pressure Drop of Refrigerants HFO-1234yf and HFC-134a in Small Circular Tube
Contributors: Chien-Yuh Yang, Hamid Nalbandian, Fu-Chen Lin
... flow boiling heat transfer test results