Environmental pressures caused by population growth and consumerism require the development of resource recovery from waste, hence a circular economy approach. The production of chemicals and fuels from organic waste using mixed microbial cultures (MMC) has become promising. MMC use the synergy of bio-catalytic activities from different microorganisms to transform complex organic feedstock, such as by-products from food production and food waste. In the absence of oxygen, the feedstock can be converted into biogas through the established anaerobic digestion (AD) approach. The potential of MMC has shifted to production of intermediate AD compounds as precursors for renewable chemicals. A particular set of anaerobic pathways in MMC fermentation, known as chain elongation, can occur under specific conditions producing medium chain carboxylic acids (MCCAs) with higher value than biogas and broader applicability. This review introduces the chain elongation pathway and other bio-reactions occurring during MMC fermentation. We present an overview of the complex feedstocks used, and pinpoint the main operational parameters for MCCAs production such as temperature, pH, loading rates, inoculum, head space composition, and reactor design. The review evaluates the key findings of MCCA production using MMC, and concludes by identifying critical research targets to drive forward this promising technology as a valorisation method for complex organic waste.

The facultatively anaerobic, thermophilic bacterium Geobacillus thermoglucosidasius is being developed as an industrial micro-organism for cellulosic bioethanol production. Process improvement would be gained by enhanced secretion of glycosyl hydrolases. Here we report the construction of a modular system for combining promoters, signal peptide encoding regions and glycosyl hydrolase genes to facilitate selection of the optimal combination in G. thermoglucosidasius. Initially, a minimal three-part E. coli–Geobacillus sp. shuttle vector pUCG3.8 was constructed using Gibson isothermal DNA assembly. The three PCR amplicons contained the pMB1 E. coli origin of replication and multiple cloning site (MCS) of pUC18, the Geobacillus sp. origin of replication pBST1 and the thermostable kanamycin nucleotidyltransferase gene (knt), respectively. G. thermoglucosidasius could be transformed with pUCG3.8 at an increased efficiency [2.8×10⁵ c.f.u. (µg DNA)⁻¹] compared to a previously reported shuttle vector, pUCG18. A modular cassette for the inducible expression and secretion of proteins in G. thermoglucosidasius, designed to allow the simple interchange of parts, was demonstrated using the endoglucanase Cel5A from Thermotoga maritima as a secretion target. Expression of cel5A was placed under the control of a cellobiose-inducible promoter (P_βglu) together with a signal peptide encoding sequence from a G. thermoglucosidasius C56-YS93 endo-β-1,4-xylanase. The interchange of parts was demonstrated by exchanging the cel5A gene with the 3′ region of a gene with homology to celA from Caldicellulosiruptor saccharolyticus and substituting P_βglu for the synthetic, constitutive promoter P_Up2n38, which increased Cel5A activity five-fold. Cel5A and CelA activities were detected in culture supernatants indicating successful expression and secretion. N-terminal protein sequencing of Cel5A carrying a C-terminal FLAG epitope confirmed processing of the signal peptide sequence.

Fermentations provide an alternative to fossil fuels for accessing a number of biofuel and chemical products from a variety of renewable and waste substrates. The recovery of these dilute fermentation products from the broth, however, can be incredibly energy intensive as a distillation process is generally involved and creates a barrier to commercialization. Membrane processes can provide a low energy aid/alternative for recovering these dilute fermentation products and reduce production costs. For these types of separations many current polymeric and inorganic membranes suffer from poor selectivity and high cost respectively. This paper reviews work in the production of novel mixed-matrix membranes (MMMs) for fermentative separations and those applicable to these separations. These membranes combine a trade-off of low-cost and processability of polymer membranes with the high selectivity of inorganic membranes. Work within the fields of nanofiltration, reverse osmosis and pervaporation has been discussed. The review shows that MMMs are currently providing some of the most high-performing membranes for these separations, with three areas for improvement identified: Further characterization and optimization of inorganic phase(s), Greater understanding of the compatibility between the polymer and inorganic phase(s), Improved methods for homogeneously dispersing the inorganic phase.

Production of medium chain carboxylic acids (MCCA) as renewable feedstock bio-chemicals, from food waste (FW), requires complicated reactor configurations and supplementation of chemicals to achieve product selectivity. This study evaluated the manipulation of organic loading rate in an un-supplemented, single stage stirred tank reactor to steer an anaerobic digestion (AD) microbiome towards acidogenic fermentation (AF), and thence to chain elongation. Increasing substrate availability by switching to a FW feedstock with a higher COD stimulated chain elongation. The MCCA species n-caproic (10.1 ± 1.7 g L⁻¹) and n-caprylic (2.9 ± 0.8 g L⁻¹) acid were produced at concentrations comparable to more complex reactor set-ups. As a result, of the adjusted operating strategy, a more specialised microbiome developed containing several MCCA-producing bacteria, lactic acid-producing Olsenella spp. and hydrogenotrophic methanogens. By contrast, in an AD reactor that was operated in parallel to produce biogas, the retention times had to be doubled when fed with the high-COD FW to maintain biogas production. The AD microbiome comprised a diverse mixture of hydrolytic and acidogenic bacteria, and acetoclastic methanogens. The results suggest that manipulation of organic loading rate and food-to-microorganism ratio may be used as an operating strategy to direct an AD microbiome towards AF, and to stimulate chain elongation in FW fermentation, using a simple, un-supplemented stirred tank set-up. This outcome provides the opportunity to repurpose existing AD assets operating on food waste for biogas production, to produce potentially higher value MCCA products, via simple manipulation of the feeding strategy.

Clonal variation, wherein a range of specific productivities of secreted proteins are observed from supposedly identical transformants, is an accepted aspect of working with Pichia pastoris. It means that a significant number of transformants need to be tested to obtain a representative sample, and in commercial protein production, companies regularly screen thousands of transformants to select for the highest secretor. Here, we have undertaken a detailed investigation of this phenomenon by characterising clones transformed with the human serum albumin gene. The titers of nine clones, each containing a single copy of the human serum albumin gene (identified by qPCR), were measured and the clones grouped into three categories, namely, high-, mid- and low-level secretors. Transcriptomic analysis, using microarrays, showed that no regulatory patterns consistently correlated with titer, suggesting that the causes of clonal variation are varied. However, a number of physiological changes appeared to underlie the differences in titer, suggesting there is more than one biochemical signature for a high-secreting strain. An anomalous low-secreting strain displaying high transcript levels that appeared to be nutritionally starved further emphasises the complicated nature of clonal variation.