Tracking strategic developments for conferring xylose utilization/fermentation by Saccharomyces cerevisiae
Annals of Microbiology volume 70, Article number: 50 (2020)
Efficient ethanol production through lignocellulosic biomass hydrolysates could solve energy crisis as it is economically sustainable and ecofriendly. Saccharomyces cerevisiae is the work horse for lignocellulosic bioethanol production at industrial level. But its inability to ferment and utilize xylose limits the overall efficacy of the process.
Data for the review was selected using different sources, such as Biofuels digest, Statista, International energy agency (IEA). Google scholar was used as a search engine to search literature for yeast metabolic engineering approaches. Keywords used were metabolic engineering of yeast for bioethanol production from lignocellulosic biomass.
Through these approaches, interconnected pathways can be targeted randomly. Moreover, the improved strains genetic makeup can help us understand the mechanisms involved for this purpose.
This review discusses all possible approaches for metabolic engineering of yeast. These approaches may reveal unknown hidden mechanisms and construct ways for the researchers to produce novel and modified strains.
Energy demand is rapidly growing worldwide due to population explosion and industrial revolution and enhanced dependence and utilization of natural energy resources. Conventional resources of fuels like petroleum oil, coal, and gas are the major contributors of energy. Consequently, greenhouse gas emission has disrupted the natural atmosphere of earth (Robak and Balcerek 2018). Increasing energy demand cannot be met by the depleting fossil fuel reserves. A study conducted in 2013 on peak oil suggested that peak oil, the theorized time point at which petroleum extraction reaches its maximum and then starts declining, would occur probably before 2030, and it also indicated significant chances of occurrence before 2020 (Miller and Sorrell 2014). Urgency to reduce reliance on conventional sources of energy persists, urging utilization of renewable sources of energy for economic benefit. Another major concern is the environmental impact resulting from the consumption of fossil fuels. Therefore, alternate sources like bioethanol and biodiesel are currently trending worldwide.
Currently, major producers of bioethanol are the USA and Brazil. In 2018, USA ranked first in generating 16.1 billion gallons of biofuel, and Brazil was the second largest producer with 8 billion gallon production (Fig. 1). India stood at seventh position after the European Union, China, Canada, and Thailand with 330 million gallons of bioethanol production in 2018. India stands third in the world for the import of petroleum products. Crude oil import has rapidly increased from 99.40 million ton in 2006 fiscal year to 228.6 MT in 2019 fiscal year (Biofuels Digest, Statista 2019). Among the petroleum products imported, 49% counts for transportation. This could be replaced by bioethanol in the coming years to improve energy utilization scenario nationally.
Biofuels are defined as those fuels which are derived from organic matter. These can be broadly categorized as primary and secondary biofuels. Primary biofuels are used in their crude form, such as fuel wood. It is used for cooking, generating heat, and electricity. However, transport fuels are considered as secondary biofuels, and these include bioethanol and biodiesel. Biofuels, specifically bioethanol and biodiesel, have become the primary need in today’s society as for transportation; dependency on fossil fuel reserves is tremendously increasing. Globally, utilization of energy resources is crucial for shaping the growth and economy of budding nations. Consequently, due to depletion of fossil fuels and increasing power demands along with environmental pollution, the focus of research has shifted towards renewable and environment friendly fuel resources. Utilizing renewable resources for biofuel production serves striking solutions in reducing the green-house gas emissions, thereby lowering the impact on environment. This also reduces dependency on foreign oils, resolves energy security issues, empowers economies, and improves the sustainability of transportation system globally (Tabah et al. 2017).
Bioethanol produced from the edible sources is considered as first generation biofuel. However, this raised the issue of food versus fuel. Therefore, as a substitute, focus shifted towards utilization of cellulosic bioethanol. This second generation bioethanol depends on agricultural residues (such as stover, bagasse, deoiled seed residues, stems, straw, and leaves) which serve as sources of lignocellulosic biomass. Lignocellulosic materials are cheap renewable resources, available in large quantities. Lignocellulosic wastes extracted from energy crops and residues constitute the abundant sources of renewable biomass. Energy security concerns seem resolvable through utilization of lignocellulosic biomass, as it resolves food vs fuel debate and is environmental friendly (Millati et al. 2002). Extensive research is being carried out for the fractionation of this biomass into its constituents to make the process cost effective and to make sugars, like glucose and xylose, available for 2G bioethanol production (Selim et al. 2018). Technology has now advanced from 2G ethanol to 3G and 4G as well. Third generation biofuel is derived from algal biomass; fourth generation biofuels utilize genetically modified algae for enhanced biofuel production (Abdullah et al. 2019). However, producing biofuels like bioethanol from lignocellulosic biomass is an entirely different scenario presenting different set of challenges because of its chemical composition and recalcitrance.
There are other approaches to enhance energy recovery from lignocellulosic biomass such as bio-refining, pretreatment, and waste recycling. Primarily, bio-refining is a promising technique to utilize crop residues, reducing the greenhouse gas emission and producing bio-based products. However, biomass cannot be utilized in its native form and requires pretreatment prior to its conversion. There are various procedures for pretreatment of the lignocellulosic biomass, such as biological pretreatment, chemical, and mechanical pretreatments.
Nutrient recycling is another approach to enhance economic and environmental sustainability in bioethanol production. Collection of biomass ash is one way of nutrient recycling in biofuel production (Ai et al. 2019; Elsayed et al. 2018; Elsayed et al. 2019).
This review focuses on the limitations of the second generation bioethanol production and various possible technologies used for ethanol production. In general, it discusses the genetic engineering as well as random approaches used for ethanol production from lignocellulosic biomass.
Lignocellulosic biomass for 2G biofuels
Lignocellulosic biomass comprises cellulose, hemicellulose, and lignin. The LCB (lignocellulosic biomass) derived biofuel, known as 2G biofuel, has several advantages.
Composition of LCB
Components of lignocellulose vary inside the cell walls of LCB (Sarkar et al. 2012), and the proportion of cellulose, hemicellulose, and lignin differs with the type of plant and tissue (Table 1). For instance, cellulose content in dried hardwoods is 40–45% by weight with 24–40% hemicellulose and 18–25% lignin. However, these ratios differ for corn stover, which possess these components as 27–48%, 13–17%, and 14–31%, respectively.
Most abundant component, cellulose is a polymer of D-glucose units linked through β-1,4 linkages. Due to massive hydrogen bonding in its structure, its hydrolysis becomes a tedious task. On the contrary, hemicellulose consists of different types of sugars such as xylose, arabinose, and glucose. Majorly, it consists of pentoses which cannot be fermented easily unlike glucose. Lignin, on the other hand, is a phenolic polymer which possesses CO–C ether bonds throughout. This makes its deconstruction a tedious task (Wang et al. 2014).
Lignocellulosic biomass appears promising in energy sector, but its efficient utilization and conversion to ethanol is a difficult task due to non-utilization of xylose by the fermenting micro-organisms such as yeast and bacteria (Chu and Lee 2007). These microorganisms do not possess metabolic machinery for efficient xylose fermentation to produce ethanol. However, for the cost-effective production of ethanol, both sugars need to be fermented.
Xylose metabolism follows two-step oxido-reductive pathway. Xylose is converted to xylitol by the xylose reductase (XR), which is NADPH-dependent (Webb and Lee 1990). Xylitol then produces xylulose by the enzyme xylitol dehydrogenase (XDH) which is NAD-dependent. Xylulose is catalyzed by xylulokinase (XKS) to produce xylulose-5-phosphate. Finally, xylulose-5-phosphate, an intermediate for pentose phosphate pathway (PPP), enters PPP and glycolysis eventually, yielding ethanol after anaerobic process of fermentation.
There is an alternative route for the production of xylulose from xylose. This substitutional pathway exists in some bacteria and fungi, wherein xylose isomerase catalyzes the reaction and produces xylulose directly from xylose (Mishra and Singh 1993). Xylitol accumulation is thereby inhibited. Pichia stipitis has been studied extensively for its xylose metabolizing properties. An illustration of xylose metabolic pathway is presented in Fig. 2.
Influence of pentose phosphate pathway enzymes on xylose metabolism
Pentose phosphate pathway (PPP) starts with the xylulose-5-P entry, and further intrinsic metabolic activities occur through this route (Kobayashi et al. 2018). PPP can be categorized in two phases—oxidative and non-oxidative. Xylose metabolizing enzyme, such as xylose reductase (XR), requires NADPH (reduced nicotinamide adenosine dinucleotide phosphate) as a co-factor for its proper functioning and effective conversion of xylose to xylitol. In oxidative pathway, NADPH is produced which replenishes the co-factor requirements of XR (Hector et al. 2011). This process plays a vital role in xylose metabolism and thereby ethanol production.
Non-oxidative pathway involves four enzymes. Genes for these are as follows:
ribose-5-phosphate ketolisomerase (RPK1)
D-ribulose-5-phosphate 3 epimerase (RPE1)
TAL1 catalyzes the conversion of glyceraldehyde 3-phosphate and sedoheptulose-7-phosphate to produce erythrose-4-phosphate and fructose-6-phosphate. TKL1 catalyzes aldoses (ribose-5-phosphate, erythrose-4-P, and G-3-P) into ketoses (xylulose-5-phosphate, fructose-6-P, and sedoheptulose-7-phosphate) (Lindqvist et al. 1992). RKI1 and RPE1 catalyze conversions of ribulose-5-P (Miosga and Zimmermann 1996). All the four enzymes are able to catalyze these processes reciprocally (Fig. 3).
PPP enzymes are significantly linked with each other, making the whole process complicated for metabolic engineering purposes (Kobayashi et al. 2017). Although ethanol titers are increased by overexpression of these genes in recombinant S. cerevisiae (Karhumaa et al. 2005; Karhumaa et al., 2007a; Li et al. 2014), but the best combination of these genes for expression in S. cerevisiae has not been demonstrated yet and is yet to be studied in detail (Karhumaa et al., 2007b; Matsushika et al. 2012; Li et al. 2014). Besides overexpression of PPP genes, ethanol production was also observed to be improved with the deletion/disruption of a putative phosphatase PHO13 gene (Karhumaa et al. 2005; Li et al. 2014; Kim et al. 2015; Xu et al. 2016). This clearly demonstrates that there are several other factors involved in the xylose metabolism among which PPP enzymes play a major role.
For efficient co-utilization and fermentation of mixed sugars (glucose + xylose) pertaining to LCB hydrolysates, insights into the xylose transport are mandatory apart from the in-depth knowledge of xylose metabolic pathways. For this, native pentose metabolizing yeasts like Pachysolen tannophilus, Scheffersomyces shehatae, and Scheffersomyces stipitis and Kluyveromyces sp. have been studied. All these strains can ferment xylose to ethanol but at lower rates as compared to glucose fermentation rates (Jeffries 1985). This accounts for their low ethanol tolerance (Maleszka and Schneider, 1982a) and xylitol accumulation. Besides, xylose utilization can occur only after its transport into the cell, so transporters play a significant role in xylose metabolism.
Since S. cerevisiae is the preferred microbe for bioethanol production from LCB, transporters have been extensively studied for this yeast for conferring effective xylose consumption. It lacks dedicated transporters for xylose uptake. However, it possesses 18 transporters for hexose sugars, classified as Hxt1-Hxt17 and one galactose permease (Gal2), Snf3p, and Rgt2p which transport hexoses inside the cell (Anjos et al. 2013). Nevertheless, only seven transporters are involved in glucose transport, Hxt1–Hxt7 and Gal2. These transporters have been classified into three categories on the basis of their glucose affinity as follows:
High-affinity transporters: Hxt6, Hxt7, Gal 2
Mid-affinity transporters: Hxt2, Hxt4, Hxt5
The high-affinity transporters exhibit higher competitive behavior for xylose transport through glucose repression.
There are two ways of xylose transport—facilitated diffusion and active diffusion. The latter mechanism requires metabolic energy, and sugar uptake is carried out against a concentration gradient. This mechanism can further be classified depending upon the type of metabolic energy preference, like direct energization, chemo-osmotic, or group translocation. On the contrary, facilitated diffusion mechanism possesses no such energy requirements. But both the systems require carrier proteins to transport sugars across the cell membranes and hence become specific to the substrate type/sugars.
As these are substrate specific, the transport systems are competitively inhibited by their analogs or other sugars. Other than these, the chemo-osmotic proton symport-based transport systems, a type of active transport mechanism, also exist, but they are pH-dependent and work only under desired pH conditions (McMillan 1993). For xylose uptake, there are two import systems: low-affinity, high capacity facilitated diffusion mechanism for transportation of both sugars (glucose and xylose); and proton symport system specifically for xylose uptake (high affinity) (Lucas and Van Uden 1986; Kilian and Van Uden 1988; Does and Bisson 1989). Former mechanism is adopted by S. cerevisiae, Candida shehatae, and Schizosaccharomyces pombe. Hxt transporters usually implement transport through facilitated diffusion. However, proton symport mechanism is followed by pentose metabolizing yeast like C. intermedia, Kluyveromyces marxianus, S. stipitis, and C. shehatae. It is generally preferred mode of transport during stresses.
Thus, the major concern has been the co-utilization of mixed sugars during LCB fermentation for bioethanol production. Several approaches involving transporters have been investigated for enhancing co-fermentation. These may be categorized as follows:
Mutagenesis of endogenous hexose transporters for xylose transport (Li et al. 2016)
Heterologous expression of xylose transporters (Belisa et al. 2015)
Heterologous expression of xylose metabolizing genes for alleviation of glucose repression (de Figueiredo et al. 2015)
Combination of above two approaches (Li et al. 2016)
Although various efforts have been done to pursue this research, but each study has a diverse approach. Therefore, additional studies for the creation of an improved strain with enhanced ability to uptake both sugars are mandatory.
Micro-organisms for lignocellulosic biomass fermentation
S. cerevisiae: an organism of choice for industrial fermentation
Saccharomyces cerevisiae is broadly used for 1st generation bioethanol production and is considered most suitable for 2G bioethanol production. This is because of its fermentation properties as it is the best hexose fermenter. Moreover, it can withstand harsh conditions, required at the industrial level. It has high ethanol tolerance and osmo-tolerance and can survive fair concentrations of inhibitors present in the hydrolysates. Micro-organisms other than S. cerevisiae, like bacteria like Zymomonas mobilis and recombinant Escherichia coli, are capable of diverse sugar utilization. However, for industrial fermentation processes, S. cerevisiae is favored. This is due to its stress tolerance properties, GRAS (generally regarded as safe) status, and resistance to bacteriophage infection, making it superior to bacterial fermentation (Dien et al. 2003; Moyses et al. 2016; Albergaria and Arneborg 2016).
Several efforts have been exercised to improve S. cerevisiae strains for mixed sugar fermentation. One such effort was successfully undertaken by Nancy Ho and co-workers working at Purdue University (Ho et al. 1998). S. cerevisiae strain 1400 was genetically engineered by cloning XR, XDH, and XKS genes along with their respective glycolytic promoters. Hence, a good hexose fermenting S. cerevisiae was improved to ferment xylose as well during co-fermentation. They also showed that this strain converts most of the sugars into ethanol rather than byproduct accumulation which is the case in other strategies (Tantirungkij et al. 1993; Kötter et al. 1990; Walfridsson et al. 1997). Moreover, the cloned genes were not affected by glucose in the medium and alleviated catabolite repression. This strain could efficiently ferment both sugars (xylose and glucose) without a lag phase.
Xylose metabolism in S. cerevisiae
Xylose metabolism starts with the uptake of this sugar. As discussed earlier, xylose is transported through the cells via two mechanisms, active and facilitated diffusion. S. cerevisiae imports xylose through facilitated diffusion. However, this transport mechanism has higher glucose specificity than towards xylose. Therefore, this yeast becomes inefficient to metabolize xylose. Although there are homologs of xylose metabolizing genes in this yeast, but the functional metabolic pathway does not exist. Examples of such genes are GRE3, YPR1, SOR1, YJR096W (xylose reductase), YDL246C (xylitol dehydrogenase), YLR070C, and YKS1 (xylulokinase). Moreover, metabolism does not begin immediately after its uptake, and a lag phase is generally observed wherein metabolic enzymes are produced to start metabolism (Gong et al. 1981; Lucas and Van Uden 1986; Jeffries 1983; Toivari et al. 2004).
Overexpression of these native genes in S. cerevisiae enhanced the fermentation process. Xylitol was accumulated as a byproduct. This ascertained the presence of xylose metabolic pathway in hexose fermenting Saccharomyces. For instance, when GRE3 and ScXYL2 were overexpressed, yeast strain could grow on xylose under aerobic conditions, even though glucose was also present. But xylitol accumulation was too high. This could be due to the lower activity of XDH and specificity of Gre3p towards NADPH which is a reductase. XRs are unable to supply NAD+, which work as co-factors for XDH. Therefore, anaerobically feasibility of this reaction is impossible due to limiting NAD+ which requires oxygen. This results in non-utilization of xylose anaerobically in the presence of glucose. Hence, redox imbalance occurs due to the affinity of Gre3p towards NADPH.
Earlier, absence of xylose metabolizing genetic machinery was blamed for inefficiency in xylose utilization by S. cerevisiae. Various strategies were employed for conferring this ability in yeast, such as, by producing xylulose directly from xylose through catalysis by glucose isomerase and then its subsequent fermentation to ethanol (Chandel et al. 2011). Later, with the emphasis on xylose transport, it was revealed that xylose is imported with the aid of hexose transporters, and therefore, its uptake rate is slower (Van Vleet and Jeffries 2009). It is also evident that S. cerevisiae has xylose transport system and other genes responsible for xylose metabolism (Gárdonyi et al. 2003). But it cannot ferment it to ethanol efficiently because xylose fermentation is an oxygenic process while glucose fermentation occurs under oxygen limiting conditions. Moreover, under oxygenic conditions, ethanol produced gets oxidized and lowers the overall efficiency of the process.
Numerous efforts are being carried out to alter the strain genetically so that it can utilize xylose and ferment it to ethanol. Apparently, cellobiose hydrolysis pathway was heterologously expressed in S. cerevisiae. It consisted of a cellodextrin transporter gene (cdt-1) and an intracellular β-glucosidase gene (gh1-1), derived from Neurospora crassa. This allowed cellobiose hydrolysis in the yeast, and co-fermentation of xylose and cellobiose was observed (Wei et al. 2015; Chen et al. 2018). This process is more beneficial because co-utilization of these sugars could enhance the ethanol productivity when compared with glucose and xylose co-fermentation.
Moreover, different strategies employed for constructing a modified strain of S. cerevisiae with xylose metabolizing abilities have dealt with several issues. For instance, heterologous expression of XR, XDH genes in this yeast has been a failure in enhancing ethanol production due to co-factor/redox imbalance.
Co-factor requirements of xylose metabolizing enzymes
Since XR and XDH have specificities for NADPH and NAD respectively, and NADH regeneration solicits oxygenic environment. However, glucose fermentation requires anaerobic conditions. Therefore, during the co-fermentation, redox imbalance is created. To address this, strains with altered co-factor affinities have been constructed. Generally, the modifications are carried out in three ways:
By altering XRs affinity for NADH with respect to NADPH,
By enhancing specificity of XDHs towards NADPH with respect to NAD, and
By alteration of affinities of both enzymes.
For instance, there are two yeast species Candida parapsilosis and Spathaspora passalidarum, in which XRs have higher affinity for NADH than NADPH. S. passalidarum is a better xylose fermenter under oxygen limiting systems (Hou 2012). Several such efforts have been carried out. Some are presented in Table 2, wherein mutagenesis was engaged for alteration of specificities of these co-factors.
XRs have IPKS (Ile-Pro-Lys-Ser) motif. 2′-Phosphate of NADPH interacts with the lysine residue of the motif making it more specific for NADPH (Lee et al. 2008). Therefore, mutations are carried out in XRs more frequently to alter its specificity for NADPH. Reduced specificity for NADPH will lower its requirement during the metabolic pathway; thereby, the process could simultaneously workout with glucose fermentation for mixed substrate fermentation during lignocellulosic fermentation for bioethanol production.
In recombinant strains of S. cerevisiae, xylitol is produced as a major byproduct. It is due to the higher production of NADPH as compared to NADH during the initial assimilation steps of xylose. When XYL1 (xylose reductase) is overexpressed in S. cerevisiae, xylitol accumulation is observed (Kim et al., 2013a). Therefore, proportional increase in XYL2 (xylitol dehydrogenase) with respect to XYL1 reduces xylitol accumulation and enhances ethanol production (Jin and Jeffries 2004). However, NADPH is also mandatory for bioethanol production. This was proved by studies carried out by Jeppsson et al. (2003). P. stipitis produces very low levels of xylitol but is not used for commercial bioethanol production purposes because of lower xylose fermentation rates. Overexpression of xylose metabolizing genes from P. stipitis to S. cerevisiae also does not solve the problem of xylitol accumulation indicating the significant role of other intrinsic factors responsible for low xylitol accumulation in P. stipitis (Jeppsson et al. 2003).
To reduce xylitol production during co-fermentation, several approaches can be adopted. These include, addition of extra electron acceptor to the fermentation medium, altering ammonium assimilation pathways, redirecting carbon fluxes through phosphoketolase pathway, relating furaldehyde reduction to xylose metabolic pathway, and changing the affinities of XR and XDH for NADH and NADPH (Roca et al. 2003; Sonderegger et al. 2004; Almeida et al. 2011).These have resulted in lower accumulation of xylitol with enhanced ethanol production.
Other factors affecting xylose metabolism
On commercial level, temperature is considered a major factor for fermentation as cooling system may elevate the cost of infrastructure. Additionally, it can impact gene expression of yeast strains used for industrial fermentations (Ismail et al. 2013). Likewise, higher temperatures affect PPP enzymes during xylose fermentation (Osiro et al. 2019).
As discussed earlier, xylose is not metabolized if glucose is present, and this “glucose repression” creates hindrance in the co-fermentation of both sugars. Glucose repression refers to the inability of the yeast cells to utilize xylose, when glucose is present in the same medium. Once glucose is completely utilized, then xylose uptake starts. This has also been revealed recently that xylose is not sensed extracellularly by this yeast as a fermentative substrate. Presence of xylose initiates the same response in yeast as the low concentrations of glucose which is non-fermentative. Therefore, xylose paradox could be resolved by integrating metabolic engineering with sugar sensing and signalomics of the yeast strains (Osiro et al. 2019).
Non-conventional native pentose fermenting yeasts
There are non-conventional yeast strains capable of xylose fermentation; these have been identified and studied in detail. These yeast species are able to metabolize xylose and produce ethanol as well through fermentation. Examples of such yeast are Pichia, Pachysolen, Brettanomyces, Candida, Clavispora, Kluyveromyces, and Schizosaccharophora, etc. Among these, Pichia stipitis is considered as the best native pentose fermenting yeast with high ethanol titers through xylose fermentation (McMillan 1993; Sharma et al. 2016). Other strains like Candida shehatae and Pachysolen tannophilus are also good fermenters of xylose. These strains have been investigated meticulously, and it has been established that some of these can produce ethanol through xylose fermentation even under anaerobic environments (Skoog et al. 1990; Fonseca et al. 2007).
However, there are certain constraints faced in using these strains for commercial purposes. These include low ethanol tolerance, low osmotic tolerance, low sugar tolerance, and low inhibitor tolerance. Since these yeast species cannot tolerate higher concentrations of ethanol, resultant ethanol productivity is lowered. Moreover, their rate of fermentation of xylose is lower as compared to that of glucose by S. cerevisiae. In addition to this, they possess low tolerance for hydrolysate inhibitors generated during the pretreatment of LCB. Inhibitors have been categorized majorly as phenolics, furans (HMF and furfural), and weak acids (Parajó et al. 1996).
There are certain confinements associated with all the fermenting micro-organism involved in co-fermentation of mixed sugars (glucose and xylose). These hinder the overall process and limit the production of ethanol. Although efforts are being done to reduce these constraints, but still accuracy has not been achieved.
Scope for improvement
Complicated inter-connected metabolic pathways hinder the development of improved strains; therefore, metabolic engineering strategies should be exercised.
Metabolic engineering came into existence in 1991 (Bailey 1991). As the name suggests, it encompasses all those engineering and modification tacts which are linked to the metabolism of organism. It is the study of metabolic pathway involving rewiring of one or more paths so as to yield a desired metabolic product such as bioethanol (Stephanopoulos 2007; Lee 2012). This strategy can be utilized to enhance xylose utilization and fermentation by studying its metabolism. Xylose metabolism has been comprehensively investigated in pentose fermenting yeasts, and the regulatory genes/enzymes have been identified. These xylose metabolizing genes were expressed in S. cerevisiae, exhibiting 0.51 g g−1theoretical yield through xylose metabolism and fermentation. However, maximal productivities were lower (Ostergaard et al. 2000).
Different approaches of metabolic engineering include rational metabolic engineering, inverse metabolic engineering, and evolutionary engineering (Nevoigt 2008). Description and advantages of these strategies have been given in Table 3.
As P. stipitis is widely known for its xylose metabolism, genes from this yeast are transferred to S. cerevisiae for improving its mixed sugar fermentation potential. Initially, through genetic engineering, XYL1, XYL2, and XKS from Pichia, were expressed in Saccharomyces. Other way, XI from bacteria was also heterologously expressed in this yeast. This enhanced ethanol production but with lower fermentation rates unlike glucose. But none of these engineering efforts resulted in a significantly improved strain. These strategies relied on the existing knowledge of metabolism and genes involved in it. However, there are several other factors, genes, enzymes, and pathways associated with xylose metabolism which complicate its fermentation. As a result, such strategies require configuration to construct an improved strain. Later, ratios of the above mentioned genes were optimized for higher ethanol productivities (Eliasson et al. 2001; Matsushika and Sawayama 2008). In addition, dedicated xylose transporters were also transferred to industrial yeasts, and alteration in the specificities of coenzymes required by XR and XDH was also performed through genetic engineering approaches (Matsushika and Sawayama 2008; Matsushika et al. 2008).
To maximize the utilization of xylose by yeast strains, especially S. cerevisiae, various genetic engineering efforts have been carried out. However, the resultant strains are unable to produce ethanol on the industrial levels. This might be due to the complex nature of the yeast metabolic regulations (Selim et al. 2018). S. cerevisiae is considered for genetic manipulation as it has the most studied genome, and various engineering tools are present to manipulate its pathways for the purpose. Moreover, pentose fermenting yeast strains are unable to ferment both hexoses and pentoses simultaneously. Due to this, introduction of new pathways in the genetically modified strains is considered as the best mechanism to overcome this issue.
With the advent of pentose fermenting yeast strains, interest in the biochemical pathways for the metabolism of xylose emerged (Maleszka and Schneider, 1982b; Slininger et al. 1982). Thereby, biocatalyst engineering appeared as a platform to produce bioethanol through yeast sp. To illustrate, enzymes responsible for the eight reactions of xylose metabolism to ethanol were identified in yeast for functional expression in S. cerevisiae. This was followed by a combinatorial expression analysis so as to screen the rate limiting steps (Latimer and Dueber 2017). Through this metabolic evolution, different ways were invented to adjust for the disconnection between the actual biochemical patterns and the expected ones.
Major focus is generally paid over the modification of S. cerevisiae yeast. For xylose fermentation, P. stipitis has also been manipulated. Through metabolic engineering PPP, sugar transport, terminal steps of fermentation, glycolysis, and the interconnection between fermentation and respiration could be manipulated. Since S. cerevisiae does not possess metabolic pathway for xylose assimilation, genes from P. stipitis are expressed in it for better xylose metabolism. However, this resulted in very low levels of xylose assimilation. Although xylose metabolism has been studied, deeper insights of non-conventional yeasts fermenting xylose could enhance the engineering strategies (Jeffries 2009). Theoretically, ethanol yields could be enhanced by S. cerevisiae through xylose assimilation by harboring xylose reductase, xylitol dehydrogenase, and xylulokinase. But the precision has still not been achieved so as to determine which approach is responsible to enhance the fermentative properties of the yeast (Karhumaa et al., 2007a). Moreover, deeper knowledge of the interconnected pathways is required to modify yeast strains to effectively utilize lignocellulosic biomass for fermentation (Jin et al. 2004). Therefore, non-conventional xylose fermenting yeast like P. stipitis has attracted much attention to study biochemical, physiological, and genetic regulations for improving fermentation traits of S. cerevisiae.
With the overexpression of xylose reductases and xylitol dehydrogenases (XYL1 and XYL2) from P. stipitis to S. cerevisiae, significant ethanol yields were not enhanced due to xylitol accumulation. This occurred due to the dual cofactor preferences of XYL1 and XYL2 of P. stipitis and an imbalance in the activities of oxidative and non-oxidative PPP (Kötter and Ciracy 1993). Similarly, engineering of PPP enzymes into yeast also led to the improvements in ethanol titers. Such as overexpression of TAL1 and TKL1 in Saccharomyces cerevisiae (S. cerevisiae) at 30 °C and overexpression of all PPP genes at 36 °C resulted in the highest ethanol productivities (Kobayashi et al. 2017).
Transketolase (TKL1) and Transaldolase (TAL1) are PPP enzymes; overexpression of TKL1 from Pichia strain to Saccharomyces strain results in reduced growth rate of the modified strain on xylose containing minimal medium (Metzger and Hollenberg 1994). It was also observed that when TKL1 from Pichia was overexpressed in Saccharomyces along with XYL1 and XYL2, the recombinant strain showed faster growth rate than the strain expressing XYL1 and XYL2 alone (Walfridsson et al. 1995). Nonetheless, the growth rate of the transformant was lower than that of the parent strain due to the plasmid burden carrying three genes (XYL1, XYL2, and TAL1) (Bao et al. 1997; Meinander et al. 1999).
To determine the ability of S. cerevisiae to assimilate and metabolize xylose, xylose reductases were expressed in this yeast system. This led to the xylose assimilation under oxygenic conditions along with the production of xylitol when there was no other sugar substrate in the medium (Kötter et al. 1990; Amore et al. 1991). On the contrary, overexpression of XYL2 leads to the accumulation of xylulose, suggesting XKS activity inhibits the xylose assimilation and utilization (Jin and Jeffries 2003).
As discussed earlier, first successful recombinant strain of S. cerevisiae was constructed by Ho et al. The recombinant strain was efficient in xylose and mixed sugar fermentation. Ho et al. used XR and XDH from P. stipitis. Whereas when endogenous XKS gene was overexpressed, it was unable to grow on xylulose (Rodriguez-Peña et al. 1998). Although when all the endogenous genes were overexpressed, ethanol fermentation was efficiently carried out (Toivari et al. 2001). This infers that regulated expression of XKS is mandatory for efficient ethanol production. Several such efforts have been carried out since then for creating a modified and improved strain (Karhumaa et al. 2007a; Ni et al. 2007; Matsushika and Sawayama 2008; Matsushika et al. 2009; Van Vleet and Jeffries 2009).
Recent advances in genetic engineering tools such as the advent of CRISPR-Cas (Clustered Regularly Interspaced Short Palindromic Repeat) technology has been a milestone for strain development (Cong et al. 2013). CRISPR-associated nucleases, Cas 9, have been used to create sequence specific double strand breaks in vitro. This technique has been used for reverse engineering in S. cerevisiae to confer xylose fermentation (Bao et al. 2014; Jansen et al. 2017). Genetic changes occurring in the strains improved through evolutionary engineering have been studied, and the same genes are targeted in the host organisms to produce single nucleotide mutations through CRISPR-Cas9 molecules.
As discussed earlier, S. cerevisiae does not possess xylose specific transporters; it cannot properly consume xylose present in the lignocellulosic biomass. It exports xylose through glucose specific transporters. Therefore, there is tremendous scope of improvement in ethanol production through heterologous expression of xylose specific transporters in this yeast. A lot of research has diverted towards transporter engineering.
Heterologous transfer of transporter genes has also facilitated xylose metabolism during co-fermentation processes. For instance, cryptic hexose transporter (chimeric Hxt11/2 transporter), engineered into a D-xylose transporter, resulted in the co-fermentation of mixed sugars (Shin et al. 2017). As stated in the earlier section, HXT transporters are responsible for glucose uptake in S. cerevisiae. The two mechanisms of sugar transport have been discussed, facilitated diffusion, and proton symport mechanism. Former mechanism is more promising as it does not require much energy for sugar uptake. A transporter from C. intermedia following the xylose/glucose proton symport mechanism was transported into S. cerevisiae. This enhanced xylose consumption, but the Km was 10 folds lower than for glucose (Leandro et al. 2006). Other two transporters, GSX1 and GXF1, enhance glucose uptake ten times higher than glucose. When gxf1 was engineered in S. cerevisiae, there was not much effect on the growth rate of this yeast at higher xylose concentrations. However, at lower concentrations of xylose, it promoted the growth of the yeast strain (Runquist et al. 2009).
Later, researchers found out that P. stipitis being a native pentose fermenting yeast possesses high-affinity xylose transporters and low uptake system for glucose/xylose shared uptake (Hahn-Hägerdal et al. 2001). Moreover, it was found out that S. cerevisiae exploits high-affinity xylose transporters for xylose uptake rather than innate low-affinity transporter specific for glucose uptake. Hence, under glucose limiting conditions, both the sugars are utilized together (Meinander and Hagerdal 1997). Since Sut1-3 are the main glucose transporters in P. stipitis, expressions in S. cerevisiae lead to increment in the utilization of both sugars (Katahira et al. 2008). Sut1 and Sut3 have higher affinity for xylose than the corresponding glucose transporters of S. cerevisiae.
Later, it was also found out that apart from yeast and bacteria, filamentous fungi, Aspergillus nidulans and Trichoderma reesei, also possess xylose transporters. xtrD, a xylose transporter from A. nidulans, was introduced into S. cerevisiae, and it was observed that this strain could grow on a wide range of sugars such as xylose, galactose, glucose, and mannose, with highest affinity towards xylose (Colabardini and Ries 2014).
Advantage of this strategy is the targeted approach and thus its precision and accuracy. It does not pose any undesirable adverse effects on the strains. Genetic engineering is precise in targeting a particular gene of interest involved in the metabolism. However, this approach relies on the limited database of metabolic pathways leaving few targets for improvements.
Evolutionary engineering includes all the experimental methods for strain improvement which involve random mutagenesis rather than targeted approach, eventually followed by selection of cells with desired traits (Sauer 2001). This strategy includes several cycles of random mutations and sequential selection, which create genetic mutations involving the desired ones (Sauer and Schlattner 2004) and can be very effective in strain improvement (Overkamp et al. 2002; Sonderegger and Sauer 2003; Shi et al. 2014). Furthermore, this approach has also enhanced the stress tolerance levels of S. cerevisiae (Martín et al. 2007). Major advantage of this technique is no prior information of the genome is required, and random mutations are produced containing the desired ones.
In a study by Kim et al., 2013b, xylose toxicity was removed through evolutionary engineering of S. cerevisiae. Xylose toxicity was evident after the strain was grown on xylose concentrations above 10 g L−1. Third subculture of the strain showed significant improvement in the growth rate and ethanol production. Attfield and Bell (2006) adapted native strain of S. cerevisiae to grow solely on xylose as the sole carbon source with < 6 h doubling time. Similarly, evolutionary engineering can also be used to investigate stress resistance properties of yeast. Koppram et al. (2012) demonstrated inhibitor tolerance in S. cerevisiae TMB3400. After 97 generations, maximum specific growth rate was enhanced to 0.33 h−1. Improved strains displayed better tolerance to inhibitors upon growth in spruce hydrolysates. In another study, evolutionary engineering was employed to increase resistance to hydroxymethyl furfural and furfural by serially transferring the S. cerevisiae cultures to medium containing increasing concentrations of these inhibitors (Liu et al. 2005).
Evolutionary genetic approach
This approach is engaged for recombinant strains to enhance their ethanol productivities and make them stress tolerant. Recombinant strain is subjected to varying stresses, to which it may adapt with time. Adapted best strain is then screened out through selection techniques. As an example, a diploid recombinant strain was mutagenized, and the strain growing on xylose was selected (Demeke et al. 2013). Further, their genomes were shuffled, and selection was done on D-xylose pre-treated spruce hydrolysate. Best cultures were selected and subjected to evolutionary adaptations. Strain at the last stage of xylose fermentation was considered as the most superior yeast for xylose fermentation.
Mutagenesis is either site directed or random, where site directed mutagenesis is a targeted approach, whereas random mutations are not locus specific. Targeted mutations could be used to alter the specificities of cofactors (Watanabe et al. 2005, Watanabe et al. 2007; Matsushika and Sawayama 2008; Matsushika et al. 2008) while random mutations could be easily introduced through approaches like adaptation and protoplast fusion. Moreover, UV-induced mutations and EMS (ethyl methane sulfonate) induced mutations also create such random mutations. Additionally, recombinant strains can also be mutagenized to increase ethanol titers in comparison to the parent strains (Tantirungkij et al. 1994; Sonderegger and Sauer 2003). An outline of different engineering strategies has been provided in Fig. 4.
Chemical mutagenesis using EMS was used to improve ethanol production abilities of S. cerevisiae. Six mutated colonies grew on 10% ethanol concentration, and one of them produced 17.3% more bioethanol than the parent strain (Mobini-Dehkordi et al. 2008). Acetic acid tolerance in S. cerevisiae was enhanced using UV mutagenesis by Zheng et al. (2011).
Strategies other than targeting direct gene involved in xylose metabolism involve pursuing the effect of PPP genes. As mentioned in the “Influence of pentose phosphate pathway enzymes on xylose metabolism” section, there are four major enzymes involved in PPP. Heterologous overexpression of their genes in S. cerevisiae has augmented xylose fermentation process (Jin et al. 2005). Bio-prospecting such genes linked to xylose metabolism indirectly could further enhance the efficacy of the process.
Protoplast fusion and genome shuffling
Another significant improvement strategy is protoplast fusion. It involves genome shuffling between micro-organisms. This is generally carried out for such strains which do not possess any genetic information (Heluane et al. 1993). It works on the basis of creation of random mutations through genome transfer. To add to its advantages, larger segments of DNA can also be transferred unlike classical genetic engineering approaches which rely on vectors for gene transfer. It also generates a number of fusants which possess desired metabolic traits. For fusion of two strains, a fusogenic reagent is required to bring them in close proximity with each other. It can done via PEG (polyethylene glycol) or though electroporation as well. Fusion can be applied to develop a strain with mixed sugar fermentation potential by shuffling genomes of hexose and xylose fermenting yeasts (Heluane et al. 1993; Lin et al. 2005; Pasha et al. 2007). Also, xylose fermenting strains can be obtained as a result of DNA transfer (Lin et al. 2005).
A fusant strain constructed by Pasha et al. (2007), F11, showed 0.459 g L−1 ethanol yield with 90% fermentation efficiency. In a separate study (Krishnamoorthy et al. 2010), fused S. cerevisiae and K. marxianus and the resultant fusants produced more ethanol than the parent strain (12.5% from 18.09 g L−1 of biomass). Earlier in 1996, Sakanaka et al. (1996) also fused S. cerevisiae and K. marxianus. Among the 40 fusants obtained fusant F1 showed better traits than its parental strains in terms of its growth at high temperature and fermentation abilities.
Genome shuffling, on the other hand, is improvised version of protoplast fusion. It involves several rounds of genetic material transfer leading to an improved strain by the end of process with higher xylose utilization and ethanol yields (Bajwa et al. 2010).
A fusant developed by this technique (Zhang and Geng 2012), ScF2, could utilize up to 250 g L−1 of xylose and produced ethanol as well. When compared with P. stipitis, this fusant was found to be more tolerant towards xylose and showed high ethanol titers. Another fusant CP11 was produced by intergeneric fusion of S. cerevisiae and Candida shehatae (Pasha et al. 2007). It was thermostable at 42 °C and could ferment wood hydrolysates with ethanol yield of 0.459 ± 0.012 g g−1 and 90% fermentation efficiency. Ability to ferment wood hydrolysates signifies its industrial relevance to ferment lignocellulosic biomass. In another experiment, S. cerevisiae HAU1, an industrial strain possessing all the desired traits for fermentation but lacking killer properties, was fused with the killer strain of S. cerevisiae. The resultant strain retained killer properties of S. cerevisiae and could sustain toxic conditions of fermentation on molasses and nutrient recycling (Bajaj and Sharma 2010).
Exposing strains to various stresses for a long time results in a stress tolerant strain. This is called adaptation of the strain. It is advantageous to follow this strategy when the genes responsible for a stress are unknown. Such as, in case of inhibitor tolerance, the genetics behind this is unclear. Therefore, adaptation under stress conditions is studied, and the tolerant strains are monitored for genetic changes potentially led to adaptability to stress. It involves repeated passaging of the cultures to increasing concentration of inhibitors in lignocellulosic hydrolysates. Selection is done on the basis of growth and fermentation traits. Generally, this is applied to recombinant strains (Harner et al. 2015).
However, there are reports of strain improvement in native strains as well. Through adaptation of strains on hydrolysates, cost requirements are reduced as detoxification is not required. Most of the adaptive techniques are employed to generate inhibitor tolerant strains (Zhu et al. 2009; Liu et al. 2004). Another significant application is growth of native strains on xylose to enhance biomass yields (Attfield and Bell, 2006). Table 4 presents different strategies followed to improve strains for co-fermentation potential of strains.
Limitations associated with this strategy are (i) it is time consuming and tedious; (ii) the adapted strains need to be screened out, and this requires high throughput screening technology; and (iii) there are very less criteria for the selection of adapted strains.
Suitability of S. cerevisiaeon commercial scale is broadly known because of its fermentative properties and robustness. Other native pentose fermenting strains have been studied in detail, and their genes have been transferred to Saccharomyces for improvement in xylose fermentation. These involve engineering efforts that have been partially successful in enhancing ethanol yields. But there are constraints associated with these efforts like xylitol accumulation, low xylose fermentation rate, and low ethanol tolerance. Metabolic engineering strategies provide a solution to these limitations. These involve direct or indirect approaches to target single or multiple genes of the metabolic pathways. Among all the metabolic engineering strategies, genetic engineering being the most accurate and appropriate technique results in desired metabolic product within limited time. Besides, for screening the desired clones, simpler methods are also suitable, whereas for other techniques high throughput screening methods are required. But alone this approach cannot generate an improved strain; hence, a combinatorial strategy is required, wherein combination of genetic engineering along with other approaches like adaptation/evolutionary engineering is involved. Furthermore, some uncovered hidden traits of xylose metabolism still need to be revealed to improve the efficacy of co-fermentation processes. This could be done by involving random metabolic approaches as there are several metabolic pathways connected with xylose metabolism, and targeting each pathway is a tedious task. On the other hand, random approaches can alter the flow of the pathways which can later be studied to understand the genetics involved in the improvement strategies.
Availability of data and materials
Data sharing is not applicable to this article as no datasets were generated or analyzed during the current study.
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Authors are also grateful to the Director, ICAR-Indian Agricultural Research Institute, New Delhi, for giving us this platform to conduct research activities. We also acknowledge ICAR-AMAAS (12-124) for providing funds.
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Sharma, S., Arora, A. Tracking strategic developments for conferring xylose utilization/fermentation by Saccharomyces cerevisiae. Ann Microbiol 70, 50 (2020). https://doi.org/10.1186/s13213-020-01590-9
- Saccharomyces cerevisiae
- Metabolic engineering
- Random approaches
- Protoplast fusion