Research review paperConversion of inulin-rich raw plant biomass to 2,5-furandicarboxylic acid (FDCA): Progress and challenge towards biorenewable plastics
Introduction
The subject of biorenewable polymers is at the center of a pivotal issue in the current plastic manufacturing industry because of their positive impact on global resource depletion and environmental sustainability. These polymers can be produced through the conversion process of biomaterial sources such as plant biomass and plant-derived materials including agricultural residues and other biowastes (Bhatia et al., 2021; Heo et al., 2019, Heo et al., 2020, Heo et al., 2021). The petroleum-based polymers that have been used as feeding materials for the production of commodity plastics (packaging, food containers, and household products, etc.) can be substituted by these polymers derived from the bio-based feedstocks. For example, petroleum-derived PET (polyethylene terephthalate), which has been used to manufacture plastic bottles, can be replaced by PEF (polyethylene 2,5-furandicarboxylate) that can be produced from the feedstocks originated from bioresources and other waste materials. Several venture companies (e.g., Avantium, Corbion, Synvina) are currently in progress towards the marketable production of PEF using FDCA (2,5-furandicarboxylate) (Hwang et al., 2020; Jiang et al., 2020).
FDCA is a monomeric platform intermediate with a cyclic structure belonging to furan chemical groups. It can be readily converted into various value-added chemical products such as; biochemicals (e.g., isoamyl furandicarboxylate, diphenyl furan-2,5-dicarboxylate, etc.), ingredients (Hexanoic acid, macrocyclic ligands, etc.), and commodity polymers (polyesters, polyamides, etc.) (Fig. 1). Due to its wide spectrum of industrial applications and future enormous market potential, FDCA has been classified as an economically feasible platform chemical by the US Department of Energy (DOE). Currently, several venture companies produce FDCA at a commercial scale and demo/pilot plant levels through the oxidation process of HMF (hydroxymethylfurfural) that can be prepared from bio-based feedstocks by way of the dehydration process of bio-based feedstocks (Heo et al., 2019, Heo et al., 2020, Heo et al., 2021; Yi et al., 2014a, Yi et al., 2015a). For example, Dutch renewable chemistry venture company, Avantium has planned to build a 5000 t/y production facility for FDCA using YXY processing technology, which is based on HMF (hydroxymethylfurfural) oxidation process (Table 1) (Avantium, 2020). Other companies also use HMF-based processing systems for the production of FDCA (Table 1). As such, it is evident that HMF is a pivotal player in the current production process of FDCA. Although numerous achievements on HMF-based FDCA production process have been accumulated, its production technologies are not yet fully market-driven, remain technology-driven due mainly to the limited supply of HMF caused by its high price (Cai et al., 2021; Chen et al., 2021; Hameed et al., 2020; Sajid et al., 2018). Accordingly, today's most critical challenge for the marketable production of FDCA should be pointed to the further reduction of its production cost. Our review affords the paramount platform strategies conducible to this challenge by introducing two strategic approaches. One approach is dependent on the use of raw biomass feedstock rich in inulin polymer, which can be used as a feeding substrate for the production of FDCA. Another is dependent on the utilization of biomodification technology conducive to its cost-effective production.
In industrial chemical manufacturing, the use of raw biomass feedstocks is more favorable from a low-carbon bioeconomic point of view compared with the use of fossil resources. This depiction embraces two key concepts, environmental sustainability and the sustainable development of technology for value-added products, including renewable biopolymers. The former is a significant part of current global climate change and the latter is involved with the development of greener technology for bio-based chemical products (Heo et al., 2019, Heo et al., 2020). In the assessment of environmental sustainability, the emissions of GHGs (greenhouse gases; carbon dioxide, methane, nitrous oxide, and fluorinated gases) function as a key indicator (EPA, 2018). In particular, CO2 gas plays as the main contributor of GHG emissions (because ca. 81% of GHG is CO2) (EPA, 2018). Several studies showed from the assessment of environmental sustainability that the use of raw biomass more favorably contributes to the reduction of GHG emissions (from 40 up to 60%, depending on feedstock type and processing system) compared with that of the reference process (IEA Bioenergy, 2019). As such, the use of raw biomass feedstocks is beneficial to the reduction of GHG emissions. In a case study, raw switchgrass for the production of HMF was used to examine the reduction effect of GHG emissions and as a result, a higher reduction of GHG emissions (up to 60%) was observed in its processing system compared with the use of fossil reference, depending on processing types (Heo et al., 2019). In another GHG balance analyses, two production processes of PEF from corn-based fructose and PET derived from fossil resource, both of which can be used as feeding substrates for the production of commodity plastics, were analyzed to compare the reduction efficiency of GHG emissions between them and as a result, the former showed 40–50% lower GHG/CO2 emissions (Hwang et al., 2020; Jiang et al., 2020). The whole procedure of producing FDCA from raw biomass feedstocks is performed through a cascade processing step such as pretreatment of biomass feedstocks, their depolymerization to feed materials (e.g., fructose, glucose), and their dehydration to HMF, separation of intermediates (e.g., HMF), and HMF oxidation to FDCA (Fig. 2). In the direct conversion process of raw biomass feedstocks to FDCA, several processing steps can be eliminated. This elimination can significantly conduce to the reduction of GHG emissions as illustrated in Fig. 2.
From a techno-economic point of view, the direct conversion process of raw feedstocks to FDCA could conduce to the reduction of its production cost. The reason is, as mentioned above because several processing steps can be eliminated (Fig. 2). For example, the production processes of FDCA currently performed by the commercial venture companies are operated with HMF-based FDCA production technology (Table 1). However, its marketable production is not yet enough to produce it on an industrial scale due to the high production cost of HMF. Accordingly, the direct conversion process of raw biomass to FDCA could be significantly conducive to the cost-effective production of FDCA by skipping the costly processing steps (Fig. 2).
As such, the bio-based production process of FDCA is more favorable than the fossil-based process. Particularly, the direct conversion process of raw biomass feedstocks to FDCA is much more beneficial in both the environmental sustainability and bioeconomic points of view. However, there are concerns to be considered. These concerns include food security, disruption of biodiversity, land use, etc. Avoiding these concerns is a matter of great importance. One solution is to utilize non-food plant resources with no intensive systematic farming but capable of growing well in untapped land. Accordingly, the choice of biomass feedstock could be a significant factor for the sustainable development of FDCA production.
As another possible strategy conducible to reducing the cost of FDCA production from plant biomass feedstocks, the application of biomodification technology could be a useful approach. This technology would contribute to facilitating the production process and improving the content of target carbohydrates. As an example, inulin, which can be used as a useful substrate for FDCA production, can be genetically modified according to its application purpose. It is believed that the biomodification application would be a highly favorable approach for reducing the cost of FDCA production using raw plant biomass feedstocks.
The purpose of this review is to afford significant information on the sustainable technology for cost-efficient production of FDCA using inulin-rich raw plant biomass feedstocks by introducing some breakthrough approaches conducive to bio-based FDCA production. The discussion scopes include; the current technology trends of FDCA production, the importance of inulin polymer in producing FDCA, the discussion on plant sources with high content of inulin, new bioprocessing approaches for the direct oxidation of inulin rich raw plant feedstocks to FDCA, and biomodification strategies for enhancing the bioprocess efficiency and for improving the content of inulin in the targeted plant sources.
Section snippets
General profile of FDCA
2,5-Furandicarboxylic acid is a white furan-based organic solid consisting of two carboxylic acid groups on a central furan ring (Fig. 3). This compound is very stable and insoluble in most of the common solvents except DMSO (dimethylsulfoxide). It has a high melting point (342 °C) and boiling point (420 °C). Due to the presence of two carboxylic acid groups, FDCA undergoes the typical chemical reaction patterns of carboxylic acids (Lewkowski, 2001). Its transformation and polymerization
The nature of inulin and its contribution to FDCA production
Inulin polymer is a kind of nonstructural carbohydrate reserved mainly in the plant storage organs such as tuber, root, and bulb. It was observed from FESEM (field emission scanning electron microscope) analysis that these polymer molecules are clustered in the granule-like formations (inulin granule) on which the peanut shell-like structures with small buds are protruded (Fig. 5) (Yi et al., 2013). In order to more efficiently produce FDCA from inulin-rich raw plant feedstocks, inulin
Valorization on technoeconomic feasibility
Technoeconomic feasibility analysis of bio-based FDCA production has been performed to estimate overall capital costs relevant to the processing system, operating cost, and potential revenues using technical and financial parameters. Most of the studies on the economic feasibility of FDCA production have been focused on three categories of processing boundaries: HMF-to-FDCA, fructose-to-FDCA, and lignocellulosic-to-FDCA. For the practical assessments, various calculative simulation models have
Proposed bioprocessing scenarios
In the bio-based production process of FDCA using inulin-rich raw plant feedstock, three essential reaction paths are generally involved: Feedstock pretreatment (fragmentation of cells and/or depolymerization of sugar polymers to sugar monomers), dehydration of sugar monomers to HMF, and HMF oxidation to FDCA (Fig. 2). In these bioprocessing scenarios proposed, relatively more straightforward production processes of FDCA are suggested. These processes avoid the costly separation process of the
Metabolic background of inulin biomodification
Inulin is a carbohydrate polymer reserved mainly in plant storage organs for their energy metabolism and its biosynthesis pathways are relatively less complicated. The synthesis of inulin polymer occurs in the vacuole organelle (Fig. 6). In the first step, two sucrose molecules are catalyzed by sucrose:sucrose 1-fructosyl transferase (1-SST) into one molecule of 1-kestose, the shortest member of inulin families, and the release of one molecule of glucose (Fig. 6). Inulin families are
Concluding remarks
Today's significant issue of plastics manufacturing is focused on technology development for their sustainable production due mainly to the negative impact of petroleum-derived plastics manufacturing on the environment and human society. As a biorenewable precursor of the building block (e.g., PEF; polyethylene furandicarboxylate) for plastic production, FDCA has a highly promising platform chemical. In current, its commercial production companies are burgeoning out. However, the production
Declaration of competing interest
The authors declare that they have no known competing financial interests or personal relationships that could have appeared to influence the work reported in this paper.
Acknowledgments
This work was financially supported by The Dong-A University Research Fund. The authors deeply acknowledge the financial support.
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These authors contributed equally to this work and should be considered as co-first authors.