ScholarWorks@Korea University: Hong, Seung kwan

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Hong, Seung kwan (홍승관)

College of Engineering (School of Civil, Environmental and Architectural Engineering)

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Tel 02-3290-3322
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Desalination:24||Forward osmosis:22||Forward osmosis (FO):18||Membrane fouling:12||Seawater desalination:11||Reverse osmosis:11||Draw solution:9||Reverse osmosis (RO):8||Membrane distillation:6||Wastewater reuse:6||Silt density index (SDI):6||Modified fouling index (MFI):6||Fertigation:6||Fouling index:5||RO membrane:5||Fouling reversibility:5||Energy efficiency:5||Bromide:5||Nanofiltration:4||Membrane capacitive deionization:4||Disinfection byproducts:4||Organic fouling:4||Membrane cleaning:4||Wastewater reclamation:4||Fouling:4||Flow fieldflow fractionation (FlFFF):4||Energy consumption:4||Membrane capacitive deionisation:4||Specific energy consumption:3||Wastewater treatment:3||Reverse solute flux:3||Pressure assisted osmosis (PAO):3||Irrigation:3||Biofouling:3||Interfacial polymerization:3||Colloidal fouling:3||Hydrophobicity:3||Cakeenhanced osmotic pressure (CEOP):3||Fouling control:3||Pressure assisted osmosis:3||Membrane surface characterization:3||reverse osmosis:3||Forward osmosis (FO) membrane:3||Geosmin:3||Ultrapure water (UPW):3||Shale gas produced water (SGPW):3||Membrane capacitive deionization (MCDI):3||Hybrid system:2||Sensitivity analysis:2||nanofiltration:2||Separation:2||Polyethylene:2||Specific energy consumption (SEC):2||Electrosorption:2||Multiple membrane array system (MMAS):2||Surface roughness:2||DBPs:2||Prechlorination:2||Pretreatment:2||RO membranes:2||Pressure retarded osmosis:2||Ultrafiltration:2||Triply periodic minimal surfaces:2||Seawater reverse osmosis:2||Fouling mechanism:2||Internal concentration polarization (ICP):2||Seawater reverse osmosis (SWRO) desalination:2||Hybrid systems:2||Polyamide thin film composite membrane:2||organic fouling:2||2MIB:2||FlFFF stabilization:2||Resource recovery:2||Visualization system:2||Industrial application:2||Ion desorption:2||Osmotic dewatering:2||High water recovery:2||Water permeability (A):2||Fouling potential:2||Membrane orientation:2||Rainwater harvesting:2||Modified fouling index:2||Fertilizer drawn forward osmosis:2||Osmotic equilibrium:2||Microfiltration:2||Pressure decay test:2||Lowenergy consumption:2||seawater desalination:2||Structural parameter (S):2||Transparent exopolymer particles:2||membrane:2||Fertiliser draw solution:2||Reverse salt diffusion:2||Nanofiltration (NF):2||PRORO hybrid process:2||forward osmosis:2||biofouling:2||Dynamic hysteresis:2||Seawater:2||Membrane integrity:2||Membrane distillation (MD):2||Highsalinity and hightemperature seawater:1||Arabian gulf:1||Electrochemical deionization (EDI) concentrate reclamation:1||Water treatment:1||Static mixers:1||Kenics mixer:1||Pretreatment for seawater desalination:1||Retardation of wetting:1||Capacitive deionization (CDI):1||Constant voltage (CV):1||Iodide:1||Coldcathode Xray irradiation: reverse osmosis (RO):1||UF membrane fouling:1||Nitrate removal:1||Realtime observation:1||Flowthrough reactor:1||Simulation:1||Ionexchange membrane bioreactor:1||Nitrogen removal:1||Recovery:1||membranes:1||Pressure retarded osmosis (PRO):1||Surface chemical heterogeneity:1||Iron corrosion:1||Blending system:1||Organic convection and diffusion:1||Reverse draw solute flux:1||Brackish groundwater:1||Model:1||Osmotic dilution:1||Antibacterial:1||acylase:1||quorum sensing:1||nanofiltration (NF):1||Polytetrafluoroethylene (PTFE) hollow fiber membrane:1||Granular activated carbon (GAC):1||Organic matters:1||seawater reverse osmosis desalination:1||pH and calcium effects:1||effective diffusivity:1||effective osmotic pressure:1||membrane surface property:1||cake filtration theory:1||monosodium glutamate:1||Draw solute:1||Food additive:1||Heavy metal:1||Supersaturation:1||FORO osmotic Dilution process:1||Meshed tube filtration (MTF):1||Nitrate selectivity:1||Mg addition:1||Flow electrode capacitive deionization (FCDI):1||Flow electrodes:1||Economic analysis:1||Carbon dioxide (CO2) capture:1||Wetting:1||Nitrate and phosphate removal:1||Membrane fouling control:1||Osmoticallyenhanced dewatering:1||Zero liquid discharge (ZLD):1||Wastewater from plating industry:1||Solute permeability (B):1||Activated sludge:1||FDFO simulation:1||Pyrophyllite:1||Multiple MD measurements:1||Membrane wetting and fouling:1||Direct potable reuse (DPR):1||water desalination:1||Hydrophilic substrate:1||Antiscaling:1||Seawater reverse osmosis (SWRO):1||Rainwater tank size:1||Blending:1||Temperature polarization:1||MBR:1||Community composition:1||electrospinning:1||Hardness removal:1||Concentration polarization:1||Color removal:1||Ozonation:1||microbial community:1||Toxicity:1||inorganic scale:1||Seawaterlevel ionic strength:1||Membrane biofouling:1||Seawater TDS:1||Surface charge:1||PMS oxidation process:1||Reactive halogen species:1||Activated carbon:1||Flow electrode capacitive deionization:1||Niche application:1||Twostage configuration:1||Solar absorber:1||Process intensification:1||Ionexchange membrane:1||Energy:1||Fouling reversibility (FR):1||Pretreatment:1||Flue gas desulfurization (FGD) wastewater treatment:1||Phosphate equilibrium system:1||Capacitive deionization:1||Heavy metal removal:1||Optimization:1||UVLED:1||OEDRO hybrid system:1||Printed circuit board (PCB) wastewater treatment:1||Split partial single pass (SSP):1||Water production:1||Pore diffusion:1||Fieldscale study:1||Ultrasound cleaning:1||Ceramic membrane bioreactor:1||Supportfree interfacial polymerization:1||Membrane modification:1||Manganese adsorption:1||Magnetite adsorbent:1||antifouling:1||thin film composites:1||Langelier saturation index (LSI):1||Alginate fouling:1||Modelling:1||Wastewater effluent:1||Solution blowing:1||Draw solute diffusivity:1||Membrane performance parameter:1||나노입자:1||위해성:1||ion transport characteristics:1||nanocolloids:1||FlFFF:1||Quorum sensing:1||External surface:1||pressure decay test:1||Chloride:1||Process optimization:1||Osmoticallydriven reversibility index:1||Dissolved air flotation (DAF):1||Shortcircuit:1||Permselective ion exchange membrane (IEM):1||Constant current (CC):1||modified fouling index (MFI):1||Desalination plants:1||Vacuum distillation:1||Highly saline wastewater treatment:1||Anaerobic membrane bioreactor:1||Radioactive liquid waste:1||Osmotic pressure gradient:1||MicrocystinLR:1||Drinking water treatment plant:1||Palladium concentration:1||Reverse solute permeability (B):1||FORO osmotic dilution process:1||Integration of wastewater reclamation and seawater desalination:1||CSG produced water:1||Molecular layerbylayer:1||Water desalination:1||RO brine:1||Power density:1||Atomic force microscopy:1||Draw and feed solution temperature:1||Membrane scaling:1||Silica fouling:1||countercurrent flow FO operation:1||Crossflow direction:1||Hydrodynamic conditions:1||Silver nanoparticles:1||Reverse draw solute permeation:1||Shale gas(셰일가스):1||Membrane distillation(막증발법):1||Plant(플랜트):1||2Methylisoborneol (2MIB):1||drinking water:1||pathogen:1||pyrosequencing:1||Charge distribution:1||Nanoparticles:1||RD membranes:1||SUVA and FEEM:1||adhesion force:1||중공사막:1||cake layer thickness:1||colloidal fouling:1||reverse solute flux:1||Whey concentration:1||Electrode:1||Heat and mass transfer analysis:1||Backwash:1||Decentralized water supply:1||Algal bloom control:1||Theoretical exergy analysis:1||Osmotic energy:1||Phosphate removal:1||Flue gas desulfurization (FGD) wastewater:1||Forward Osmosis:1||Low energy:1||Dewatering:1||Fertilizerdrawn forward osmosis:1||Life cycle assessment:1||Pyrophyllitealumina composite membrane:1||Manganese removal:1||FORO hybrid process:1||Selectivity for hardness:1||Pilotscale operation:1||Reverse osmosis (RU) membrane:1||Apparent solute permeability coefficient:1||Draw organic solution:1||Pipe distribution system:1||Alternative water resources:1||fouling reversibility:1||Pressure:1||PS nanofibers:1||Chemical and physical factors:1||Titania:1||Soy protein:1||Water treatment(수처리):1||Pseudomonas putida:1||Boron solute flux:1||Temperature difference:1||Membrane bioreactor:1||Fertilizer:1||Reverse osmosis (RO) membrane:1||Extracellular polymeric substances (EPS):1||DOC:1||surface tension:1||organics fractionation:1||Flowelectrode capacitive deionization:1||Thinfilm composite membrane:1||Vacuum membrane distillation:1||Enhanced light absorption:1||Computational fluid dynamics:1||Chemical softening:1||Water recovery:1||Quantitative analysis:1||Data analysis:1||HAB:1||Ionselective carbon electrode:1||Ion selectivity:1||Thin film composite membrane:1||Polydopamine:1||Selectivity:1||Internally staged design:1||Industrial wastewater treatment:1||Ultraviolet:1||Microbial aggregation:1||Aluminabased ceramic membrane:1||PVDF polymeric membrane:1||Mineral recovery:1||PVDF membrane:1||Cake fouling index (CFI):1||superoleophilic:1||Natural organic matters (NOM):1||Total dissolved solids (TDS):1||Electrospinning:1||Osmotic backwashing:1||Solute permeability:1||처리:1||Treatment:1||Pseudomonas aeruginosa biofilm:1||외부 표면:1||Hollowfiber membrane:1||Zeta potential:1||bubble point theory:1||membrane integrity test:1||nonbiodegradable (NBD) organics:1||organic accumulation:1||anaerobic toxicity assay:1||UV:1||Polyvinyl alcohol:1||Longterm pilotscale study:1||Staged voltage (SV):1||Design ratios:1||Irreversible fouling:1||pretreatment process:1||Reverse electrodialysis (RED):1||Nitrogen recovery:1||Osmoticallydriven reversibility index (ORI):1||Ultraviolet (UV):1||Disinfection:1||Anaerobic ceramic membrane bioreactor:1||Modulescale modeling:1||Shale gas produced water (SGPW) treatment:1||Membrane distillation crystallization (MDC):1||Cyanobacterial bloom:1||Xylose concentration:1||FO membrane performance parameters:1||Modified fouling index (MD):1||Seawater RO desalination:1||Interfacial adhesion:1||MEMBRANE distillation crystallization (MDC):1||Electrochemical process:1||Electronic industry:1||layerbylayer assembly:1||Sulphonated polymer:1||Draw pressure:1||Feed solute flux:1||Colloidal deposition:1||Inorganic fouling:1||Combined organic and colloidal fouling:1||membrane module length:1||Biofilm:1||superhydrophobic:1||Deposition and transport:1||Surface analysis:1||reverse osmosis (RO):1||saline water:1||Temperature:1||Solute resistivity for diffusion:1||Surface heterogeneity:1||CaCO(3) scale:1||Modified Fouling Index (MFI):1||Silt Density Index (SDI):1||Fouling propensity:1||TDS effect:1||sewage thickening:1||Selective:1||Biochar:1||Inorganic scaling:1||Feed spacers:1||Low energy consumption:1||Modeling:1||Staged configurations:1||UVLED/PMS oxidation:1||Mineral resource recovery:1||Physical cleaning:1||Radioactive iodine:1||Pure permeate:1||Mesoporous carbon:1||Ceramic membrane:1||Scaling control:1||Antiscalant:1||Radiation grafting:1||Monovalent cation permselective exchange membrane:1||Water purification and reclamation:1||nanoscale patterns:1||Spongelike structure:1||Bacterial deposition:1||RO membrane fouling:1||Solute permeability coefficient (B):1||Water flux:1||Cake resistance simulatormodified fouling index nanofiltration:1||Nanocolloidal fouling mechanism:1||oilwater separation:1||reverse osmosis (RO) membrane:1||assimilable organic carbon (AOC):1||Pseudomonas fluorescens strain P17:1||Chemical heterogeneity:1||Particle fouling:1||Water permeability:1||나노기술:1||Nanotechnology:1||membrane surface characteristics:1||Atomic Force Microscopy:1||Accumulation of NBD COD:1||Diffuse source:1||NOM:1||Source water standard:1||흐름전위:1||제타전위:1||Streaming potential:1||natural organic matter (NOM):1||Monosodium glutamate (MSG):1||

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