ScholarWorks@Dongguk University: Park, Jung hoon

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Park, Jung hoon (박정훈)

College of Engineering (Department of Chemical and Biochemical Engineering)

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Tel 02-2260-8598
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Hollow fiber membrane:6||Perovskite:6||Membrane contactor:5||TiO2:5||CO2 separation:4||Surface modification:4||Oxygen removal:4||hydrogen separation:4||Ceramic membrane:4||BSCF:4||electroless plating:4||Al2O3 hollow fiber:3||Ceramic hollow fiber membrane:3||Oxygen separation:3||Adsorption:3||Perovskite oxides:3||Biogas:3||Coke formation:3||Alumina:2||Oxygen permeation properties:2||photocatalytic membrane reactor:2||Scaleup:2||Hollow Fiber Membrane:2||Module design:2||titanium dioxide:2||Strontium content:2||air purification:2||Greenhouse gas:2||Pd composite membrane:2||Membrane:2||Membrane Contactor:2||ceramic substrate:2||Alumina hollow fiber membrane:2||Pdbased membranes:2||Membrane contactor module:2||gaseous ammonia (NH3) degradation:2||LSCF:2||Al2O3:2||Catalyst:2||Decomposition:2||hydrogen purification:2||CO2:2||Total oxidation:2||Landfill gas:2||Methylcyclohexane:2||Powders: chemical preparation:2||membrane contactor:2||Oxygen adsorption:2||CO2 absorption:2||CO2 capture:2||Combustion technology:1||Comparative method:1||Compatibility:1||Composition:1||Contactor process:1||Cr impurity:1||Cr2O3:1||Crystal structure:1||Deactivation:1||Decomposition reaction:1||Decompression stripping:1||Deoxygen reaction:1||Desorption:1||Dip coating:1||Dipcoating:1||Dispersibility:1||Dualphase ceramic membrane:1||ETS10:1||Electrochemical reaction:1||Electroless plating:1||Electroless plating process:1||Emission:1||Emission factors:1||Emissions:1||Endothermic catalytic cracking:1||Endothermic catalytic pyrolysis:1||Endothermic nonoxidative processes:1||Environment:1||Facilitated transport:1||Flue gas:1||Fuel conversion project:1||Gas separation:1||GasLiquid membrane:1||Gasliquid membrane contactor:1||Grain size:1||Greenhouse Gas:1||H2 recovery:1||HZSM5:1||HZSM5 Zeolite:1||HZSM5 zeolite:1||H2S:1||HZSM5 catalyst:1||Heat Sink:1||Heterogeneous catalysis:1||Heterogeneous photocatalysts:1||Hexadecyl cetyltrimethylammonium bromide (CTAB):1||High phenol removal:1||High process stability:1||Highperformance Pd–Ag–CuBased membranes:1||Hollow Fiber:1||Hollow fiber:1||Hollow fiber catalyst:1||Hollow fiber membrane contactor:1||Hollow fiber membranes:1||Hydrogen (H 2 ) permeability:1||Hydrogen separation:1||Hydrogen separation performance:1||Hydrogen separation properties:1||Hydrogen sulphide:1||Hydrophobic Ceramic Membrane:1||Hydrophobic modification:1||Hydrophobic modified ceramic hollow fiber:1||Hydrothermal synthesis coating:1||Hydrothermal synthesis variables:1||Immobilization strategies:1||Indoor wood stove:1||Industrial wastewater treatment:1||Inorganic membranes:1||Ion Removal Process:1||Ion exchange:1||Iron hydroxide:1||Iron hydroxidebased adsorbents:1||KPHI zeolite:1||Kyoto Protocol:1||LSTF:1||La0.6Sr0.4Co0.2Fe0.8O3delta:1||La0.6Sr0.4Ti0.3Fe0.7O3d protective film:1||La0.6Sr0.4Ti0.3Fe0.7O3delta:1||La1xSrxCo0.2Fe0.8O3d:1||La1xSrxCo1yFeyO3d:1||Landfill gas purification:1||Lightoff temperature:1||Lignin Valorization:1||Lignin recovery:1||Lignin wastewater:1||Liquid absorbent:1||Liquidliquid ceramic hollow fiber membrane contactor:1||Longterm test:1||MCH conversion:1||MIEC:1||Macroporous supports:1||Maximum oxygen uptake:1||Membrane mass transfer resistance:1||Membrane module design:1||Membrane process:1||Mesoporosity:1||Mesoporous adsorbents:1||Metal adsorption:1||Metalbased membrane:1||Metals and alloys:1||Methane oxidation:1||Microporous:1||Microporous ZSM5 zeolite catalyst:1||Mitigation Technology:1||Mixed matrix hollow fiber membranes:1||Mixed matrix membranes:1||Modeling:1||Modification:1||Module fabrication:1||Moisture content:1||Molecular dynamics:1||Monoethanolamine:1||Monoethanolamine (MEA):1||Multivariate ZIF8:1||Ndoped TiO2:1||NH3:1||Namodification:1||Nanofiltration Membrane:1||Nanofiltration membrane:1||Nbdoping membrane:1||NiCrAl Metal foam:1||NonPdbased alloy membrane:1||Oil:1||Oxidation:1||Oxidebased membrane:1||Oxygen Adsorption:1||Oxygen Separation:1||Oxygen desorption:1||Oxygen flux:1||Oxygen membrane:1||Oxygen nonstoichiometry:1||Oxygen permeation Temperaturepressure dependence:1||Oxygen production:1||Oxygen sorption/desorption:1||Oxygen uptake capacities:1||Palladium coatings:1||Paris Agreement:1||Pd alloy:1||Pd alloy membrane:1||Pd sputtering:1||PdAg alloy:1||PdCu alloy:1||Pdbased alloy membrane:1||Pddecorated La(0.8)Sr(0.2)Co(0.2)Fe(0.8)O(3delta )catalysts:1||Performance stability test:1||Phenol:1||Photocatalysis:1||Photocatalyst:1||Photocatalytic Decomposition of Ammonia:1||Photocatalytic properly:1||Polydopamine Layer:1||Polyvinyl pyrrolidone (PVP):1||Pore structure:1||Porous electrode:1||Process analysis:1||Production:1||Reaction mechanism:1||Rutile:1||S:1||SDC:1||SSDC:1||Sacrificial graphene oxide interlayer:1||Separation techniques:1||Siloxanes:1||Siloxanes removal:1||Simple membrane screening:1||Single aminebased absorbents:1||Solidstate reaction:1||Structural stability:1||Structureperformance relationships:1||Supercritical catalytic cracking:1||Supercritical jet conditions:1||Surface:1||Surface coating:1||Surface roughness reduction:1||Surfacemodified CeO2 nanoparticles:1||Synthesis methods:1||Tetraethyl Orthosilicate:1||Tetraethyl orthosilicate (TEOS):1||Thin films:1||Tibased membrane:1||TiO2 photocatalyst:1||Titanium:1||Titanium dioxide:1||Titanosilicate:1||Total carbon:1||Triple phase boundary:1||Tripleligands:1||UNFCCC:1||Ultrathin supported membranes:1||VCrY:1||VEC:1||Vacuumassisted dipcoating process:1||Valence electron concentration (VEC):1||Vanadium:1||WGS:1||Wastewater Resources:1||Water purification:1||Water treatment:1||Wavy Form Microchannel Reactor:1||Wavy microchannel:1||Wetted wall column:1||Wood:1||ZSM5 zeolite catalysts:1||Zeolite:1||Zeolite Y:1||Zeolitic imidazolate frameworks:1||alloy membrane:1||alumina:1||alumina hollow fiber support:1||aprotic solvent:1||ceramic membrane:1||chemical absorption:1||chill block melt spinning:1||environmental protection:1||exoTHDCPD:1||gas permeation:1||gasliquid membrane contactors:1||graphene oxide (GO):1||hemodialyzer:1||hollow fiber:1||hollow fiber membrane:1||hydrogen membrane:1||hydrogen permeation:1||indoor air pollution:1||inorganic membrane:1||intermediate layer:1||lignin extract:1||lignin recycling:1||liquidphase temperature:1||membrane applications:1||metal ion separation:1||microstructure:1||nanofiltration:1||oxygen permeability:1||perovskite:1||phase stability:1||phaseinversion process:1||physical absorption:1||polymer hollow fiber membrane:1||polymeric hollow fiber membranes:1||pore structure:1||separation:1||separation process:1||sodium ion removal:1||solidliquid separation:1||uremic toxin removal:1||αalumina membrane:1||교토의정서:1||금속흡착:1||당사국총회:1||메조세공:1||알루미나 중공사막:1||유엔기후변화협약:1||제올라이트 Y:1||405 nm LED Light:1||파리 기후협정:1||Activated charcoal:1||Advanced separation processes:1||Air pollution:1||Al2O3 hollow fiber membranes:1||Al2O3 hollow fiber substrate:1||Al2O3 hollow fibre supports:1||Ammonia adsorption:1||Ammonia cracking processes:1||Anatase:1||Antifouling properties:1||Arrhenius extrapolation:1||Ba0.5Sr0.5Co0.8Fe0.2O3d:1||Ba0.5Sr0.5Co0.8Fe0.2O3delta:1||Ba0.5Sr0.5Co0.8Fe0.2O3δ:1||BaTiO3 and titanates:1||Bariumchromium oxide:1||Batch reactor:1||Binary blended aminebased absorbents:1||Binder Coating:1||Biogas Purification:1||Biomass technologies:1||Black TiO 2:1||Bond parameter:1||CO2 chemical absorption:1||CO(2)absorption:1||CO2 Absorption:1||CO2 Separation:1||CO2 chemical absorption:1||CO2 removal efficiency:1||CO2 tolerance:1||COP:1||Carbon capture:1||Catalytic Deactivation:1||Catalytic deoxidation:1||Catalytic reaction:1||CeO2 nanoparticles:1||CeO2:1||Ceramic Membrane:1||Ceramic hollow fiber membrane contactor:1||Ceria:1||Ceria nanoparticles:1||Ceria slurry:1||Certificated emissions reduction:1||Charcoal:1||Chemical engineering:1||Chemical initiators:1||Chemical machine polishing:1||Chromium poisoning:1||Cobalt tetraphenyl porphyrin:1||

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