Carbon recovery from wastewater through bioconversion into biodegradable polymers
Introduction
Polyhydroxyalkanoates (PHA) are completely biodegradable polyesters that can be biologically produced from renewable resources in contrast to most oil-based production of biologically recalcitrant thermoplastics. The most common PHA are poly(3-hydroxybutyrate), and poly(3-hydroxybutyrate-co-3-hydroxyvalerate), (P(3HB) and P(3HB-co-3HV), respectively). These materials are thermoplastic polyesters with comparable mechanical properties to those of conventional oil based polymers such as polypropylene and polyethylene [1]. The current PHA price depends on monomer composition and it is usually higher for the copolymers; overall, it ranges from 2.2-5.0 €/Kg [2], [3], [4], which is less than typical range of 10–12 €/Kg reported from the beginning of the last decade [2]. Notwithstanding the burden of costs and environmental impacts of plastic trash, the current PHA prices are not deemed to be commercially competitive with respect to conventional petroleum-based polymers, which typically cost less than 1.0 €/Kg [2].
In order to provide a commercial entry of PHA based bioplastics in substitution to the established classical plastics, it is often expressed that the production methods of PHA must become cheaper. Strategies to improve the production economy have included the development of open mixed- instead of pure-culture methods, and the utilization of perceived low or negative cost, waste or residual feedstock that do not compete with primary food crops [5]. Downstream processing costs for PHA recovery from biomass plays a pivotal role in the PHA manufacturing process with respect to material quality, application opportunity, and, in following, its market value [6]. Different types of PHAs offer distinctly different material properties and this also factors into a range in scope of engineering applications and within that spectrum, different regional and niche business models.
PHA are part of the key carbon transformation products occurring during biological wastewater treatment by activated sludge. Dynamic conditions, such as those caused by discontinuous feeding regimes and/or alternate redox conditions (anaerobic/anoxic/aerobic), applied in a variety of process configurations can be used to promote for the enriched presence PHA-storing microorganisms in activated sludge biomass [7]. Given the wide spread utilization of activated sludge in water quality management services and the fact that PHA storing organisms are naturally present in such bioprocesses, much of the MMC PHA research and development has gravitated around biological wastewater treatment with the use of process residuals, wastes and wastewaters. This synergy of service and by-product generation is anticipated to be a logical means to decrease both CAPEX and OPEX costs. For example, in comparison to pure culture PHA production, MMC PHA methods are simpler and less costly since sterile conditions and infrastructure for an axenic bioprocess are not required. Also, PHA are recognised as key platform chemical raw materials within bio-refinery frameworks of bio-based schemes [6], [8]. In particular, in wastewater and solid waste management, PHA production via MMC represents an opportunity for recovering raw wastewater organic carbon by means of biological treatment [9], converting traditional end-of pipe waste treatment into an opportunity for residuals bio-refineries [10].
Over the past 15 years fundamental insights on MMC PHA production have come from laboratory scale research, and this research has been typically focused on three different biological process elements of a so-called three-step process [11], [12], [13] (Fig. 1). More recently, efforts have been devoted to the implementation of such a 3-step process at pilot scale, by the integration of MMC PHA production to wastewater treatment in different process configurations, and with the potential concurrent benefits of sludge minimization [14], and/or process water quality management [15], [16]. The results of this process integration are a benefit of joining essential regional services of waste management with outcomes of bio-based resource generation [17].
This review aims to a) outline strengths and weaknesses of the three-step MMC process, and b) examine methods and opportunities for integrating PHA production with municipal and industrial wastewater treatment infrastructures. A section dedicated in focus of review to the fourth process element of PHA recovery techniques from MMC is also provided. The properties of PHAs and their potential applications are beyond the scope of the present work, but the interested reader may refer to recent publications [1], [18]. Downstream processing and PHA recovery are principal factors influencing polymer properties (physical-chemical, thermal, rheological and mechanical). These properties can strongly affect processing and application challenges and opportunities, wherein production costs versus material value are ultimately judged in commercial business models. The specific nature of the application of the PHA as platform chemicals or bioplastic ingredients will influence the business case to justify the needed capital investments for the material commercial supply. A range of specialized niche and/or high-end product applications may well support a higher cost for these bio-based polymers within specific, and hoped for, regionally driven circular economies supporting renewable resource value chains.
Section snippets
The typical three-step process for MMC PHA production: strengths and weaknesses
The MMC three-step process presented in Fig. 1 could be achieved through a variety of different bioprocess configurations. Flexibility exists to achieve the same principles of bioprocess selection pressure with adaptations depending on the type of wastewaters, flows and concentrations, effluent water quality demands, and the already existing infrastructure. However, the key feature of the three-step bioprocess is the step of PHA accumulation (process element 3) and this process element requires
Conclusions
PHA production using MMC processes represents a paradigm shift to the current practices for wastewater and regional organic residuals management. The fundamentals in state-of-the-art of the polymer production bioprocess in three steps as process elements are well established in the laboratory and they are becoming established also at pilot scale. Most of the principal operational factors have been explored, and preliminary technical-economic analysis and LCA outcomes continue to motivate
Acknowledgements
This work was partially funded by the EU ROUTES project (Contract No 265156, FP7 2007–2013, THEME [ENV.2010.3.1.1-2] Innovative system solutions for municipal sludge treatment and management).
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