CAU Scholar's Space: Lee, Chul-Jin

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Lee, Chul-Jin (이철진)

대학원 (지능형에너지산업융합학과)

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Tel 02-820-5941
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Optimization:6||Dynamic simulation:5||Process design:5||LNG:4||Carbon capture and utilization:3||Economic analysis:3||Computational fluid dynamics:3||FischerTropsch:3||Reactor design:3||Torrefaction:3||1,3Butadiene:3||Process intensification:2||Methyl ethyl ketone:2||Supply chain:2||CO2 capture:2||Process simulation:2||3Hydroxypropionic acid:2||IGCC:2||Quantitative risk assessment:2||Quencher:2||Liquefied natural gas:2||Distributed parameter model:2||CFD:2||Multiobjective genetic algorithm:2||2,3Butanediol:2||Multistream heat exchanger:2||Plate fin heat exchanger:2||Lithiumion battery:2||Biomass gasification:2||LNG Receiving Terminal:2||Power generation:2||Dynamic Simulation:2||LNG terminal:2||Layer patterning:2||Simulation:2||Acrylic acid:2||Methanol synthesis:2||Hydrogen refueling station:2||Catalytic CO<sub>2</sub> hydrogenation:1||Catalytic activity:1||Catalytic methane combustion:1||Catalytic methane reforming:1||Cathode thickness:1||Central production:1||Central storage:1||Chemical absorption:1||Coalfired power plant:1||Coalfiredpower plant:1||Coating thickness:1||Cold box:1||Compression system:1||Compressor:1||Compressor surge:1||Computational fluid dynamic:1||Conceptual design:1||Conversion:1||CuFe2O4 NPs:1||Decision making:1||Decomposition approach:1||Deep learning:1||Dehydration:1||Desalination:1||Design optimization:1||Diffusionabsorption refrigeration:1||Distillation:1||Domino effect:1||Dry reforming:1||Dual fluidized bed:1||Dynamic Modeling:1||Dynamic simulation of compressor systems:1||Economic feasibility:1||Edge defect:1||Electrolyzer:1||Emergency shutdown (ESD):1||Emissionfactor:1||Energy efficiency:1||Energy minimization multiscale drag:1||Engineering Diagram:1||Environmental analysis:1||Evacuation:1||Exergy and economic analyses:1||Exhaust gas cleaning:1||Extraction:1||Extractive distillation:1||FLNG:1||Fault magnitude:1||Fischer–Tropsch:1||Fixedspeed compressor:1||Fluidizedbed reactor:1||Formic acid:1||Gas–solid fluidized bed:1||GastoLiquid process:1||Gastoliquid:1||Gastoliquid process:1||Gaseous hydrogen refueling station:1||Gasification:1||Genetic Algorithm:1||Genetic aggregation:1||Graph Pattern Mining:1||HYSYS Dynamics:1||High energy density:1||High power density:1||Hydrogen:1||Hydrogen Liquefaction:1||Hydrogen generation:1||Hydrogen liquefaction:1||Hydrogen liquefaction cycle:1||Hydrogen production:1||Hydrogen production optimization:1||Hydrogen seaborne transport:1||Hydrogen supply chain:1||Hydrogen supply chain management:1||Hypersaline brine:1||Insitu Joule heater:1||Industrial scale plant:1||Integrated cooling system:1||Interfacial heating:1||Jet type reactor:1||Joule heating:1||Kinetic model:1||LNG liquefaction:1||LNG receiving terminal:1||Levelized cost of hydrogen:1||Li+ ion diffusion:1||LiNi0.6Co0.2Mn0.2O2 (NCM622):1||Lifecycle assessment:1||Ligand:1||Liquefaction:1||Liquefaction process:1||Liquefied hydrogen:1||Liquefied hydrogen refueling station:1||Liquid–liquid extraction:1||Liquid hydrogen carrier:1||Liquid hydrogen storage tank:1||Liquid organic hydrogen carrier:1||Lithiumion battery module:1||Loadsharing control:1||Lowcarbon hydrogen:1||Lowgrade heat recovery:1||MATLAB:1||Machine learning:1||Market dynamics:1||Mass transfer:1||Methanolysis:1||Methyl Ethyl Ketone:1||Methylcyclohexanebased onsite hydrogen refueling station:1||Micro channel reactor:1||Microchannel cooling plate:1||Microchannel reactor:1||Mineral carbonation:1||Mitigation:1||Mixed integer linear programming (MILP):1||Mixed refrigeration process:1||Multiobjective Optimization:1||Multiperiod:1||Multistage compressor:1||Multilayer insulation:1||Multimodeoperation:1||Multivariate Granger causality (MVGC):1||NARX:1||NG liquefaction:1||NG pipelines:1||NN:1||Nail penetration:1||Natural gas chain:1||Natural gas hydrate (NGH):1||Numerical CFD simulation:1||Numerical analysis:1||Objective Detection:1||Operating Cost:1||Operating cost:1||Operating cost reduction:1||Operational scenario:1||Optimal membrane distribution:1||Organic Rankine cycle:1||Organic ranking cycle (ORC):1||Palladium membrane:1||Parallel compressor system:1||Parametric analysis:1||Phase change material:1||Phosphoric acid fuelcell (PAFC):1||Piperazine:1||Piping and Instrumentation Diagram:1||Platefin heat exchanger:1||Polydisperity:1||Postcombustion CO2 capture:1||Practical cell:1||Pressure swing adsorption (PSA):1||Price of 2,3Butanediol:1||Principal component analysis:1||Principal component analysis (PCA):1||Probabilistic uncertainty analysis:1||Process control:1||Process integration:1||Process modeling:1||Process optimization:1||Process safety and risk management:1||Process systems engineering:1||Product gas:1||Pseudotwodimensional model:1||Quantitative risk analysis:1||Quantitative risk assessment (QRA):1||Real time optimization:1||Recirculation flow:1||Regasification:1||Regeneration heat duty:1||Removal of water:1||Risk consideration:1||Risk mitigation:1||Root causality:1||SMR:1||Safety:1||Safety management:1||Seawater scrubbing:1||Seismic effect:1||Selectivity:1||Sendout controlling:1||Sensitivityanalysis:1||Sequential leastsquares programming:1||Sizing method:1||Slag:1||Slotdie:1||Stability:1||Steam methane reforming:1||Stochastic programing:1||SulfinolM:1||Support Vector Machine:1||Surge protection:1||Surrogate model:1||Sustainability:1||Syngas:1||Technoeconomic Evaluation:1||Technoeconomic analysis:1||Tecnoeconomic assessment:1||Thermal runaway:1||Thermoeconomic analysis:1||Toluene:1||Toluene diisocyanate production:1||Toxic gas leak:1||Urban:1||Vaporcooling shield:1||Variational autoencoder:1||Waste heat recovery:1||Waterenergy Nexus:1||Wet SOx scrubber:1||ammoniaderived hydrogen refueling station:1||carbon capture and storage:1||carbon capture and utilization:1||catalytic reaction:1||climate:1||coal gasification:1||computational fluid dynamics (CFD):1||convolutional neural network:1||dike:1||economic analysis:1||evolutionary computation:1||fault detection:1||genetic algorithm:1||hydrogen:1||hydrogen carrier:1||hydrogen production:1||kmeans clustering:1||knearest neighbor:1||knearest neighbors:1||liquefied natural gas (LNG):1||membrane macrosegmentation:1||methanol:1||multi mode monitoring:1||object detection:1||optimization design:1||palladium membrane:1||piping and instrument diagram:1||porous media:1||principal component analysis (PCA):1||probit model:1||process simulation:1||quantitative risk assessment:1||refueling station:1||risk assessment:1||risk mitigation:1||steam methane reforming:1||unsupervised learning:1||.:1||urban:1||1,3butadiene:1||1butene:1||2,3Butanediol Dehydration:1||2,3butanediol dehydration:1||Acid gas absorption:1||Acid gas removal:1||Ammonia cracking:1||Antisurge control:1||Antisurge valves:1||Aspen Plus:1||Azeotropic distillation column:1||Azeotropicdistillation column:1||BOG Recondenser:1||BOG numerical model:1||Bayesian optimization:1||Biomass:1||Biomass fuels:1||Biomass to biofuel:1||Byproduct H2:1||CCS (carbon capture and storage):1||CFD modeling and simulation:1||CFD simulation:1||CO<sub>2</sub> utilization:1||CO2 catalytic conversion:1||CO2 catalytic hydrogenation:1||CO2 hydrogenation:1||CO2 reduction:1||CO2 sequestration:1||CO2 storage:1||COE:1||CaMg source separation:1||Calcined dolomite:1||Calcium formate:1||Calcium formate synthesis:1||Carbon intensity:1||Catalyst insertion type:1||Catalyst segmentation:1||

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