The use of plastic or synthetic polymer is getting accelerated as the global population grows. Most of the plastic has been produced from fossil fuel and it causes considerable concern about climate change and fossil depletion. Lignocellulosic biomass...
The use of plastic or synthetic polymer is getting accelerated as the global population grows. Most of the plastic has been produced from fossil fuel and it causes considerable concern about climate change and fossil depletion. Lignocellulosic biomass is a sustainable carbon source and can produce various fuels and chemicals by replacing conventional fossil fuel. Although many studies have been performed to produce bio-based plastic from lignocellulosic biomass, there is a limitation due to the fact that they mainly focused on the element technologies. However, for commercialization, the development of an integrated process is indispensable by designing a separation process. Therefore, in this Master’s study, we develop the integrated process producing bioplastic and biodegradable plastic monomers and analyze to estimate the feasibility and sustainability of the developed process.
In Application Ⅰ, we propose a process for synthesis of 2,5-furandicarboxylic acid (FDCA), which is a monomer of bioplastic, from biomass-derived cellulose through catalytic conversion. Cellulose is dehydrated to 5-hydroxymethylfurfural and subsequently oxidized to FDCA. To reduce utility consumption, we designed a heat exchanger network for heat integration. The minimum selling price (MSP) of FDCA is determined to be $1,532/ton, which is comparable to the market price of terephthalic acid (TPA). Through the LCA, we quantify the environmental impact and figure out how to enhance the developed process in terms of sustainability viewpoints.
In Application Ⅱ, we propose an integrated process for the production of lactic acid, which is a biodegradable plastic monomer, from lignocellulosic biomass through biochemical conversion. Biomass is produced to lactic acid via dry dilute acid pretreatment, biodetoxification, and simultaneous saccharification and fermentation. We conduct heat integration and reduce utility consumption mainly required in the separation subsystem. Our TEA reveals that the MSP of lactic acid is determined to be $1,498/ton, which is approximate to the market price of lactic acid ($1,526/ton). Further, we evaluate the proposed process via integrative analyses including pioneer plant, and uncertainty analyses to quantify the risk and uncertainty during the construction and fluctuation of market situation. Through the LCA, we found the major contributor to environment and suggest the method for improving the sustainability of the process.