ScholarWorks@Korea University: Kang, Yong Tae

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Kang, Yong Tae (강용태)

공과대학 (기계공학부)

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Tel 02-3290-5952
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CO2 absorption:8||Plate heat exchanger:7||CO2 hydrate:6||COP:6||nbsp:6||Nanoabsorbents:5||Mass transfer enhancement:5||Mass transfer coefficient:5||Condensation:4||Low GWP refrigerants:4||Heat transfer coefficient:4||Pressure drop:4||Al2O3 nanoparticles:4||Kinetic model:3||Frictional pressure drop:3||Mass transfer:3||CO2 conversion:3||Surfactants:3||Nanofluids:3||CO2 regeneration:3||Nanoemulsion absorbents:3||Absorption:3||CO2:3||#8208:3||Experimental correlation:3||R1233zd(E):3||Thermal conductivity:3||Dissociation enthalpy &:2||Thermodynamic promotor:2||Cooling performance:2||Dodecane:2||Ionic liquid:2||LiBr concentration:2||Cooling application:2||Enhancement mechanism:2||pressure drop:2||TaylorCouette flow:2||Dissociation rate:2||Energy transportation:2||Visualization:2||Hydrodynamic effect:2||Plate type dehumidifier:2||Dissociation enthalpy:2||Multiheat sources:2||H2O/LiBr solution:2||Combined heat and mass transfer:2||Artificial neural networks:2||plate heat exchanger:2||Energy performance parameter:2||Condensation heat transfer:2||Ammoniawater:2||Regeneration:2||Mesoporous materials:2||Thermophysical properties:2||Liquid desiccant:2||Bubble pump:2||Lithium chloride:2||District cooling application:2||Photocatalysts:2||Dispersion stability:2||Accelerated control cooling:2||Trigeneration:2||CO2 capture ratio:2||Diffusion absorption refrigeration (DAR):2||double emulsion CO(2)solvents:1||, R1233zd(E):1||CO2 absorption performance:1||Absorbents:1||Plate rolling process:1||Cold thermal energy harvest:1||Compact generator design:1||Nanostructures:1||Formation rate:1||evaporation:1||Adsorbent:1||Recovery:1||capture:1||Energy conversion:1||Nanopastes:1||VCR (vaporcompression refrigeration):1||Absorber:1||hierarchical nanostructures:1||Annular contactors:1||Physical absorption:1||Penetration depth:1||XRD:1||Heatingdominated areas:1||to&:1||CO2 capture:1||Nonlinear region:1||microgels:1||Port dual injection:1||Nanoemulsion:1||Yield rates:1||Solar assisted heat pump:1||CO2 emission reduction:1||CO2 + THF hydrate:1||Liquid pumping power:1||Economic assessment:1||THF:1||Nanoparticle:1||surfactant:1||MEE (multieffect evaporation):1||Diffusion:1||Phase change materials:1||Finite element:1||interference lithography:1||CO2 absorption performance enhancement:1||R32/DMAC:1||Parallel configuration:1||Artificial neural network:1||Indoor CO2 capture:1||Nanoencapsulated solvent:1||LCC analysis:1||waste&:1||System optimization:1||Operational map:1||Performance analysis:1||absorption visualization:1||coalescence:1||Inlet position control:1||Flow stress prediction:1||Grain size uniformity:1||Critical distance:1||PBM:1||District cooling:1||Spray inclination angle:1||H2O/LiBr:1||Optimization:1||Finish cooling temperature:1||Temperature prediction accuracy:1||Low GWP refrigerant:1||High temperature process water:1||Silicone oil:1||Additives:1||level set:1||Total internal reflection fluorescence microscopy:1||Particle size:1||Compressor arrangement:1||SiO2(silica):1||Induction time:1||Light Emitting Diode:1||Desalination:1||Heat pump application:1||Thermal performance:1||Heat transfer enhancement:1||Graphite:1||Nanoparticles:1||polymer nanowires:1||Formation promotors:1||CO2 capture filter:1||Emission reduction:1||CO2 hydrate slurry:1||Variable wave amplitudes and wavelengths:1||Masstransfer enhancement:1||R600a:1||Efficiency improvement:1||Absorption cycle:1||Shuttle effect model:1||polydimethylsiloxane (PDMS):1||Bubble behavior visualization:1||Drag force:1||Plate water cooling optimization:1||CO2 absorbents:1||Flexible solar collector:1||Absorber heat transfer rate:1||Nanoscale surface coating:1||Reversed liquid vibration flow:1||single emulsion droplet:1||COP (coefficient of performance) improvement:1||separation:1||Nanolayer:1||Diffusion visualization:1||TRNSYS:1||Multiwalled carbon nanotube:1||R124:1||Hard templating:1||Photocatalyst:1||LowGWP refrigerant:1||Economic evaluation:1||Convective motion of liquid:1||Interfacial area:1||formation mechanism:1||Temperature gradient:1||Microstructured surfaces:1||Temperature difference:1||Absorption chiller:1||Precise plate cooling:1||Compound semiconductors:1||Wettability:1||Noninvasive:1||Fluid viscosity:1||Domestic refrigeratorfreezer:1||Biogas:1||Purity:1||Heat transfer:1||Carbon additives:1||Nanocomposites:1||Aggregation:1||Carbon nanotube:1||Gasliquid:1||FIBSEM:1||Organic liquid:1||Specific heat:1||Compound semiconductor:1||Photocatalytic CO2 conversion:1||NaOH aqueous solution:1||energy harvesting:1||Life cycle assessment:1||CO2 hydrate slurry &:1||District cooling application &:1||Energy consumption analysis &:1||Printed circuit heat exchanger:1||droplet size prediction model:1||optimum formation frequency:1||Seasonal energy storage:1||Nickel alloy:1||Mass diffusivity:1||Mass transfer visualization:1||Formation:1||Straight finned surface:1||scattered UV:1||Generator:1||Computational fluid dynamics:1||Internal combustion engine:1||Heat transfer model:1||Steamdriven absorption chiller:1||H2O/LiBr double effect:1||Cold energy application:1||Adsorption equilibrium:1||Binary nanoemulsion:1||Nanoconvection:1||Particle suspension:1||plasma etching:1||Hybrid absorption heat pump:1||Serial configuration:1||Condensation heat transfer coefficient:1||energy:1||high&:1||Energy optimization:1||Supercritical CO2:1||CO2 absorption patterns:1||Minimum temperature:1||Absorption rate:1||Shellandplate heat exchanger:1||Bubble wake:1||Coalescence and breakup:1||optomicrofluidics:1||Power consumption rate:1||Ammoniawater absorption:1||Hybrid compression/absorption cycle:1||Nanobsorbents:1||Nanoparticles (SiO2, Al2O3):1||Methanol:1||Reduction of refrigerant flow rate:1||Pressure swing adsorption:1||Formaticin rate:1||Oil droplets:1||Combined system:1||Thermal storage:1||Solarassisted groundsource heat pump:1||CO2 capture ratio &:1||Energy consumption analysis:1||Cooling and heating modes:1||Energy efficiency:1||Nanomaterials:1||mass transfer coefficient:1||bubble breakup:1||Coupled heat transfer:1||Thermal energy release:1||EulerianEulerian method:1||Dissociation:1||Water temperature effect:1||Fuel film:1||Injection strategy:1||Minimum volume:1||CO2 bubble absorption:1||Methanol/Al2O3, nanoabsorbents:1||Carbon capture and utilization:1||Generator arrangement:1||Contact angle:1||Dehumidification effectiveness:1||low GWP refrigerants:1||mesh adaptivity:1||Hindered Brownian motion:1||Evaporator arrangement:1||Hydrate formation:1||Al2O3:1||SiO2:1||CO2(carbon dioxide):1||New refrigerant:1||Refrigeration:1||Bubble motion:1||Heat transfer rate:1||Nanoemulsions absorbents:1||Dynamic viscosity:1||Integrated correlations:1||Pickering emulsion:1||temperature steam generation:1||Methanol production:1||

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