Wangyun Won
Korea University · 工学
研究室紹介
Professor Wangyun Won's research lab specializes in sustainable chemical processes and renewable resource utilization, focusing on the catalytic conversion of biomass into high-value chemicals and biofuels. The lab develops integrated process systems that combine catalysis, separation technologies, and heat integration to enhance energy efficiency and reduce environmental impact. Key research directions include the production of biobased monomers like 2,5-furandicarboxylic acid (FDCA) and 1,5-pentanediol from lignocellulosic biomass, as well as hydrogen storage and production technologies such as the toluene–methylcyclohexane system and steam methane reforming with carbon capture. The lab emphasizes techno-economic analysis and life-cycle assessment to guide the design of economically viable and environmentally sustainable processes.
Research Overview
Research Output Trend
Figures are computed from collected data and may differ slightly.
Selected Papers
152,5-Furandicarboxylic acid (FDCA), an eco-friendly biobased material, can replace petroleum-based terephthalic acid (TPA), in the polymer industry, for applications such as water bottle production and food packaging. In this study, an integrated process was developed for the coproduction of FDCA as a biobased plastic monomer and 1,5-pentanediol as a high-value product from lignocellulosic biomass using catalytic conversions and designing separation areas. The integrated process has several energ
A new process is developed to produce 2,5-furandicarboxylic acid from cellulose and evaluated <italic>via</italic> techno-economic analysis and life-cycle assessment.
Steam methane reforming (SMR) process is regarded as a viable option to satisfy the growing demand for hydrogen, mainly because of its capability for the mass production of hydrogen and the maturity of the technology. In this study, an economically optimal process configuration of SMR is proposed by investigating six scenarios with different design and operating conditions, including CO2 emission permits and CO2 capture and sale. Of the six scenarios, the process configuration involving CO2 capt
The toluene (TOL)–methylcyclohexane (MCH) system is one of the viable solutions because of its high stability and high hydrogen storage capacity (6.2%). However, the high volatilities of TOL and MCH and the accumulative byproducts make it difficult to transport hydrogen. Considering these limitations, we developed a new strategy introducing an extraction column and pressure swing adsorption with heat integration to reduce the required energy utilities. Furthermore, a comprehensive system-level a