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1 g the contribution from transient conduction heat transfer.
2 hich significantly enhances the condensation heat transfer.
3 th liquid-infusion for enhanced condensation heat transfer.
4 uding sample preparation, flow reaction, and heat transfer.
5 d methods for controlling small droplets and heat transfer.
6 icant insulating layer that blunts abdominal heat transfer.
7  gradients, thereby, demonstrating effective heat transfer.
8 ieve a high degree of asymmetry in radiative heat transfer.
9 ortant for almost all applications involving heat transfer.
10 chnologies that leverage nanoscale radiative heat transfer.
11 d handling, on self-cleaning surfaces and in heat transfer.
12 unding non-polar octane molecules can hinder heat transfer.
13 gap-size-dependent enhancements of radiative heat transfer.
14 ndings demand modified or even new models of heat transfer across vacuum gaps at nanometre distances.
15 LPT) in quenching are the bottlenecks to the heat transfer advancements.
16 sidence time while preserving the mixing and heat transfer advantages of flow systems.
17         Super-Planckian near-field radiative heat transfer allows effective heat transfer between a h
18 the nozzle-to-laser separation distance, the heat transfer along the printed silver wire is modeled a
19 ns and electrons) in the thermal domain, the heat transfer analogue to the familiar electrical diode.
20 ation involved a systematic investigation of heat transfer, analyte retention, and migration velocity
21 lasma that can ablate tissue with negligible heat transfer and collateral damage to neighboring tissu
22 ning patterns based on numerical modeling of heat transfer and fluid flow in three dimensions.
23                      A well-tested numerical heat transfer and fluid flow model is used to compare su
24 (CO2 photoreduction), anti-fogging surfaces, heat transfer and heat dissipation, anticorrosion, litho
25  the membrane has an insignificant effect on heat transfer and heat recovery, suggesting that membran
26 ch catalytic reaction kinetics interact with heat transfer and mechanical buckling to create oscillat
27 effect driven by subthermal non-local phonon heat transfer and spectral non-uniform temperature.
28             Using Multiphysics simulation of heat transfer and structural mechanics based on finite e
29    We find a considerable enhancement of the heat transfer and study its dependence on the number of
30                                  Here, using heat transfer and thermodynamics principles, we show how
31 rophilic or neutral surface for condensation heat transfer and to use the superhydrophobic surface fo
32 tive analyses of the electronics, mechanics, heat-transfer and drug-diffusion characteristics validat
33 s found that complex coupled fluid dynamics, heat transfer, and electrostatic phenomena within the sa
34 elds in optical, microwave, radio, acoustic, heat transfer, and other applications with flexibility a
35 e, from underwater operation to phase-change heat transfer applications.
36 e range of water-harvesting and phase-change heat-transfer applications.
37         The impact of wickability, effective heat transfer area, and liquid pressure on CHF is precis
38 n site density, wettability, wickability and heat transfer area.
39 ncreases linearly with the effective surface heat transfer area.
40 rays of nanofibres, we demonstrate effective heat transfer at critical contacts in electronic devices
41  (MFPAF) rely on optical techniques to probe heat transfer at length scales on the order of the phono
42 e MHMS has been redesigned to provide better heat transfer away from the sampler and skimmer cones an
43 esigned through the careful consideration of heat transfer, band broadening, and pressure drop.
44                                              Heat-transfer-based analysis of the data indicates that
45  graphene nanostructures in which noncontact heat transfer becomes a dominant channel.
46 eld radiative heat transfer allows effective heat transfer between a hot and a cold body to increase
47              The ability to enhance or limit heat transfer between a surface and impacting drops is i
48 d-dome digesters buried in the soil to study heat transfer between biogas digester and its surroundin
49 experiments have demonstrated that radiative heat transfer between objects separated by nanometre-sca
50           Here, we show near-field radiative heat transfer between parallel SiC nanobeams in the deep
51 Polder and Van Hove predicted that radiative heat transfer between planar surfaces separated by a vac
52 thosphere is largely governed by the rate of heat transfer by conduction.
53 terintuitive mechanism of increasing boiling heat transfer by incorporating low-conductivity material
54                       At large distances the heat transfer can be described by black body radiation,
55 with dopant, is introduced directly into the heated transfer capillary between the atmosphere and the
56  that gas-phase ion generation occurs in the heated transfer capillary of the instrument in a mechani
57                               CPI utilizes a heated transfer capillary with a vacuum ultraviolet tran
58                                 Pool boiling Heat Transfer Coefficient (HTC) enhancements on spherica
59  demonstrated approximately 100% increase in heat transfer coefficient compared to state-of-the-art d
60 ions, we obtain permissible range of maximum heat transfer coefficient possible in nucleate boiling a
61 by the inlet gas temperature and the overall heat-transfer coefficient in the condensation system.
62 ea is also strongly dependent on the overall heat-transfer coefficient, particularly at higher inlet
63 ergy savings when proper membranes with high heat-transfer coefficients are used.
64  a dramatic increase in near-field radiative heat transfer, comparable to that obtained between bulk
65 ints a way toward solving the volumetric and heat-transfer constraints that limit some other hydrogen
66                    Using accurate, empirical heat-transfer correlations, we estimated the length of t
67 tream stability behind ships, aeroplanes and heat-transfer devices.
68 temperature modulation, to measure radiative heat transfer down to gaps as small as two nanometres.
69                            At the same time, heat transfer efficiency is reduced.
70                                              Heat transfer, electrical potential and light energy are
71 able nanoparticles to absorb light, generate heat, transfer energy, and re-radiate incident photons.
72 bic surfaces for self-cleaning, condensation heat transfer enhancement and anti-icing applications, m
73         We also reveal that the mechanism of heat transfer enhancement is essentially due to the time
74                        The physics governing heat transfer enhancement on textured surfaces is explai
75 d mechanisms including adsorption of DNA and heat-transfer enhancement.
76                                        These heat transfer enhancements imply that the power density
77 uses a mixture of mined nitrate salts as the heat transfer fluid and storage medium, a two-tank therm
78 s, usually by modelling the coupling between heat transfer, fluid dynamics and surface reaction kinet
79 perfluorinated alkanes (PFCs) and poly-ether heat transfer fluids, which are persistent greenhouse ga
80                    Here we measure radiative heat transfer for large temperature differences ( approx
81  Classical molecular dynamics simulations of heat transfer from a carbon nanotube to a model hydrocar
82 ing is an extremely effective way to promote heat transfer from a hot surface to a liquid due to nume
83 ns (<0.5 mm i.d.), essentially instantaneous heat transfer from the assembly to the mobile phase was
84 mmunities and is responsible for significant heat transfer from the lithosphere to the ocean.
85 ees C, suggesting the initiation of stronger heat transfer from the North Atlantic to the deep Pacifi
86 s coupling with absorbed water, and that the heat transfer from the water to the mineral phase is ine
87 ks that are key elements in technologies for heat transfer, fuel cells and portable chemical systems.
88 face density produced a strong impediment to heat transfer, giving rise to a thermal conductivity of
89                            Flowing two-phase heat transfer has been implemented within microvascular
90 expected that this short contact time limits heat transfer; however, the amount of heat exchanged and
91         Moreover, modified combustion (MCE), heat transfer (HTE) and overall thermal efficiencies (OT
92                                    Radiative heat transfer in Angstrom- and nanometre-sized gaps is o
93 ating that conductive models for metamorphic heat transfer in Barrovian terrains are incorrect and mu
94          Here we report studies of radiative heat transfer in few A to 5 nm gap sizes, performed unde
95  enabled elucidation of near-field radiative heat transfer in gaps as small as 20-30 nanometres, quan
96 idity of this theory for modelling radiative heat transfer in gaps as small as a few nanometres.
97 ect has implications for passively enhancing heat transfer in heat exchangers and heat pipes.
98 ions are being developed for ODMPs, mass and heat transfer in osmotic process are becoming better und
99 rived from a realistic mathematical model of heat transfer in subduction zones.
100 eoretical thermodynamic analysis of mass and heat transfer in the membrane condensation system shows
101                                          Its heat transfer into both the midlatitude South Indian Oce
102 , we demonstrate that Er(3+) acts to enhance heat transfer into the Er-PVDF film due to its excellent
103                       Enhancing condensation heat transfer is important for broad applications from p
104         Our observations show that lava-snow heat transfer is slow, and that styles of lava propagati
105 iven spreading factor, the small fraction of heat transferred is controlled by two dimensionless grou
106                                When mass and heat transfer kinetics are limited, conditions that more
107 ated for both limited and unlimited mass and heat transfer kinetics in the thermal separation stage.
108            In the case of unlimited mass and heat transfer kinetics, the energy efficiency of the sys
109         The Scholander-Irving (S-I) model of heat transfer lays the foundation for explaining how end
110            The column is connected through a heated transfer line to a microfabricated differential m
111                        A novel Nichrome wire-heated transfer line was developed to ensure that the ca
112 e generator to an exposure chamber through a heated transfer line.
113 able memory effects were associated with the heated transfer line.
114 tem behavior, particularly the timescales of heat transfer linked to the ocean.
115 s and could supplement conventional metallic heat-transfer materials, which are used in applications
116                                We study this heat transfer mechanism using distinct control knobs to
117 study to directly model a metropolitan scale heat transfer mechanism, we find both enhanced tree cano
118 nflated uncertainties when investigating bio-heat transfer mechanisms and/or performing sophisticated
119 lts highlight the relevant role of different heat transfer mechanisms between MI and IM interfaces: a
120 anced electronic systems depend on efficient heat transfer mechanisms for achieving high power densit
121 nometre-scale distances while avoiding other heat transfer mechanisms, namely conduction.
122  also discuss the advantages of using liquid heat-transfer media as compared to air as the heat-trans
123 eat-transfer media as compared to air as the heat-transfer media.
124 lumn linear velocity for both air and liquid heat-transfer media.
125 ge thresholds were compared to a theoretical heat transfer model of pulsed laser-irradiated nanoparti
126 oiting the time lags and the one-dimensional heat transfer model of soils, we estimate the ALTs.
127 ynthetic Aperture Radar) observation and the heat transfer model of soils.
128 lag was corroborated using a one-dimensional heat-transfer model, which provided insight into the cha
129 d with salt penetration, water migration and heat transfer models, can be used to dynamically simulat
130 ynamics to describe the convergence of these heat transfer modes and the transition from one to the o
131 he boundary between the two most fundamental heat transfer modes, heat conduction by phonons and radi
132 ns the current finding by revealing that the heat transfer modification and enhancement are mainly at
133 ics simulations coupling electromagnetic and heat transfer modules demonstrate that during pulsed las
134 presents negligible resistance to conduction heat transfer normal to it and very large resistance alo
135 y diagnostic is the efficiency of convective heat transfer (Nu).
136                 We achieve an enhancement of heat transfer of almost two orders of magnitude with res
137 e for understanding shear-flow and anomalous heat transfer of NS associated non-equilibrium aggregati
138 ated using screen printing of electrodes and heat transfer of patterned wax paper onto filter paper.
139  also show a 30-40% increase in condensation heat transfer on copper, as a result of the ability of t
140 ngles and high nucleation densities for high heat transfer performance have been typically neglected.
141  result, we can rapidly and reversibly alter heat transfer performance up to an order of magnitude.
142 ing phenomena and enhancing nucleate boiling heat transfer performance.
143 r state-of-the-art calculations of radiative heat transfer, performed within the theoretical framewor
144                    A description of mass and heat transfer phenomena is provided and fundamental prin
145 urier theory for analysing three-dimensional heat transfer problems in systems with an interface.
146        The applicability of Fourier's law to heat transfer problems relies on the assumption that hea
147 ce enhancement of the two-phase flow boiling heat transfer process in microchannels through implement
148  of experiments and theory, we show that the heat transfer process on superhydrophobic surfaces is in
149 cement in boiling and quenching phase-change heat transfer processes by nanoscale surface texturing c
150  dielectric materials typically exhibit poor heat transfer properties due to the dynamics of phonon t
151 ives could provide by enhancing the mass and heat transfer properties, acting as co-catalysts, or imp
152 oxy results in a greater than 5x increase in heat transfer rate at a given superheat temperature.
153              Order of magnitude variation in heat transfer rates and cellulose particle lifetimes was
154 s the nucleation potential of the surface to heat transfer rates has been developed and it successful
155 tunable design parameter to control particle heat transfer rates in industrial biomass reactors.
156 ls for potential applications in sensing and heat transfer, respectively.
157           Flow reactors enhance the mass and heat transfer, resulting in rapid reaction mixing, and e
158                                      A micro-heat transfer sensor was deployed to acquire the ISS pro
159 mal energy conversion calculations including heat transfer suggest that amorphization is a solid-stat
160 t the vapor phase lateral expansion over the heat transfer surface and actively control the surface w
161 currents predicted from near-field radiative heat transfer theory.
162 asitic power consumption and allow efficient heat transfer through good thermal contacts with the hea
163                                   Convective heat transfer through jugular venous return and the circ
164  mammals, generally by estimating conductive heat transfer through their blubber layer.
165 M minimizes thermal resistance by convective heat transfer to a constantly moving droplet in direct c
166                     There was no increase in heat transfer to a tooth analogue when the high volume e
167  a Leidenfrost phenomenon, which impedes the heat transfer to cool the liquid, when the liquid drople
168                             The condition of heat transfer to lignocellulosic biomass particles durin
169 ed within the individual nanostructures when heat transfer to neighbouring nanostructures and the env
170 igh optical absorption of the CNTs and rapid heat transfer to the polymer upon excitation by pulsed l
171 ced within the test system without increased heat transfer to the tooth.
172                 Our set-up enables effective heat transfer using a liquid at previously unattainable
173 important in industrial applications such as heat transfer, water collection, and particle separation
174 ve pressures (-1.0 MPa or lower), continuous heat transfer with the evaporation of liquid water at ne
175 ance detector, multiphysical modeling of the heat transfer within the conductivity cell was performed

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