Valorizing recycled paper sludge by a bioethanol production process with cellulase recycling
Introduction
The economic feasibility of second-generation bioethanol relies on two major cost factors: the substrate and the enzymes. The identification of a cheaper, abundant and easily hydrolysable material has assumed a critical role for a more economic production of fermentable sugars. Recently, an increased utilization of different kinds of residues came as an interesting alternative to the traditional lignocellulosic substrates, enabling a considerable reduction on substrate cost, and also an additional valorization for some of these otherwise useless materials.
Recycled paper sludge (RPS) is a residue originated from the paper recycling process, more specifically, from the treatment of the liquid effluents generated in that process. It is mostly composed of small fibers with approximately 40% of carbohydrates that cannot anymore be incorporated on recycled paper (Marques et al., 2008a). Also, due to the chemical contamination, namely with ink particles, this residue has high environmental impact being usually disposed on landfills, which represents a considerable expenditure for these companies. Considering an approximate production of this waste around 300 kg per ton of recycled paper (Balwaik and Raut, 2011) and taking into account an estimated 47 millions tons of recycled paper produced only in Europe by the year of 2005 (Monte et al., 2009), this corresponds to around 14 million tons of RPS that need to be discarded. In spite of the notable potential of this material, coupled with a high worldwide availability, only few studies have been conducted so far exploring its further valorization (Presetyo and Park, 2013). Some examples refer to Lark et al. (1997) who have studied RPS hydrolysis and subsequent fermentation to ethanol by Kluyveromyces marxianus. Also Marques et al. studied its potential for bio-ethanol production by Pichia stipitis (Marques et al., 2008a) and lactic acid production by Lactobacillus rhamnosus ATCC 7469 (Marques et al., 2008b).
In addition to the substrate cost, the cost of the enzymes required to hydrolyze lignocellulosic materials (cellulases and/or hemicellulases) represents one of the biggest obstacles for their economically viable conversion, due the competition from the less expensive fossil fuels. Great debate has been established concerning the exact cost of cellulases, with distinct values being pointed out by different authors. Klein-Marcusschamer et al. (2012) estimated a cost on ethanol production around $ 0.68 per gallon, close to $ 0.5 per gallon recently suggested by Novozymes (http://novozymes.com/en/news/news-archive/Pages/45713.aspx). However, Aden and Foust (2009) have also already reported a value around $ 0.1 per gallon, close to $ 0.3 reported by Lynd et al. (2008) and $ 0.32 reported by Dutta et al. (2010). Independently of the exact figure, it is consensually recognized that the enzymes cost is a major determinant of the cellulosic ethanol competitiveness, driving in the last years intense efforts to reduce the loading employed in the process. The reduction of the cost associated to enzymes has been commonly pursued following three main strategies: increasing the efficiency of enzymes; reducing enzymes production cost; and reutilizing the enzymes (Pribowo et al., 2012). Over the last years (even decades), most of the attention has been given to the first two strategies, through intense and constant research operated by both industry (e.g. Novozymes; DSM; Genencor) and academia. Through a close collaboration with Novozymes and Genencor, NREL (USA) conducted a joint project that resulted in a reduction of cellulase cost up to 10-fold (http://www.nrel.gov/docs/fy13osti/59013.pdf). Nevertheless, some authors have already admitted that such strategies will not allow pushing down cellulases cost much further. In this context, the recovery (and posterior reutilization) of cellulases has recently emerged as a very promising concept, as using enzymes multiple times will allow a natural reduction on its consumption.
Numerous studies have been conducted for some years now in what concerns the mechanisms of enzyme adsorption/desorption (Lindedam et al., 2013, Pribowo et al., 2012, Rodrigues et al., 2014, Tu et al., 2007), addressing the complexity associated to different enzymes and substrates. In a similar way, possible strategies to facilitate and/or conduct the recovery of these enzymes have already been individually studied. According to Gomes et al. (2015), enzymes remaining in the liquid fraction are usually recovered either by ultrafiltration or by addition to fresh substrate (and posterior separation), while solid-bound enzymes normally require a change of pH or the addition of specific chemical compounds (that interfere with solid-enzyme interaction). Nevertheless, very few studies were conducted so far presenting an integrated approach of such strategies to the hydrolysis of a specific lignocellulosic material over multiple rounds.
Here we conduct an overall study regarding the feasibility of using RPS as substrate for 2G-bioethanol production in a system of multiple rounds of hydrolysis with cellulase recycling. The conservation of enzymatic activity and its final partition between solid and liquid fractions is initially accessed followed by an evaluation regarding the recovery efficiency of solid-bound enzymes. Afterwards, a process with multiple rounds of hydrolysis and enzymes recycling was implemented, monitoring the activity levels and the degree of solids conversion over the entire process.
Section snippets
Enzymes and substrate
Enzymatic hydrolysis were conducted through the combined action of the commercial cocktail Celluclast (Sigma-Aldrich, C2730), complemented with the commercial β-glucosidase preparation Novozyme 188 (Novozymes). The activities of these preparations were determined to be 45 FPU/mL and 611 IU/mL, respectively.
The recycled paper sludge (RPS) was kindly provided by RENOVA (Torres Novas, Portugal). This refers to a solid (with approx. 53% (w/v) water) obtained from the wastewater treatment of paper
RPS composition on the main lignocellulosic components
The feasibility of using nRPS as substrate for 2G-bioethanol must be assessed. This depends on the presence of a meaningful amount of carbohydrates that can be later converted, and on its susceptibility to hydrolysis by cellulases.
As a residue derived from a production process that uses materials with some degree of heterogeneity (different types of paper residues), RPS composition is equally expected to present some variations from different production batches (Chen et al., 2014).
Conclusions
This study demonstrates the feasibility of cellulase recycling following hydrolysis/fermentation of RPS. This system may be highly interesting economically, as it exploits a substrate with significant costs of disposal. A strategy of cellulase recycling was efficiently applied over 4 rounds of hydrolysis. The addition of only 30% of fresh enzymes enabled an efficient conservation of activity levels and high solid conversions through the process. Additional improvements may still be achieved
Acknowledgements
The authors acknowledge the financial support of the Portuguese Foundation for Science and Technology (FCT) under the scope of the strategic funding of UID/BIO/04469/2013 unit, COMPETE 2020 (POCI-01-0145-FEDER-006684) and the Project RECI/BBB-EBI/0179/2012 (FCOMP-01-0124-FEDER-027462). The financial support of FCT through GlycoCBMs Project PTDC/AGR-FOR/3090/2012–FCOMP-01-0124-FEDER-027948 and the PhD grant to DG (SFRH/BD/88623/2012) is equally acknowledged. The authors also thank RENOVA
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2021, Journal of Environmental Chemical EngineeringCitation Excerpt :By reducing the fresh enzyme supplementation to 65% in a recycling setup of three consecutive fed-batch fermentations, a reduction of about 23% of the enzyme loading was achieved. Despite using a much lower enzyme dosage (5 FPU/gds of Cellic® CTec 3), the current study demonstrated a higher total ethanol concentration from multiple rounds of recycling (1.5-fold, Table 6) compared to previous SHF studies on PS reported by Gomes et al. [13,19]. The differences observed between our study and previous recycling studies on PS could be partly attributed to the high concentration of fermentable sugars (70% w/w, Table 1) in the substrate and demonstrates significant applicability for large-scale production.