Y.-H. Percival Zhang

Increasing Cellulose Accessibility Is More Important Than Removing Lignin: A Comparison of Cellulose Solvent-Based Lignocellulose Fractionation and Soaking in Aqueous Ammonia

While many pretreatments attempt to improve the enzymatic digestibility of biomass by removing lignin, this study shows that improving the surface area accessible to cellulase is a more important factor for achieving a high sugar yield. Here we compared the pretreatment of switchgrass by two methods, cellulose solvent‐ and organic solvent‐based lignocellulose fractionation (COSLIF) and soaking in aqueous ammonia (SAA). Following pretreatment, enzymatic hydrolysis was conducted at two cellulase loadings, 15 filter paper units (FPU)/g glucan and 3 FPU/g glucan, with and without BSA blocking of lignin absorption sites. The hydrolysis results showed that the lignin remaining after SAA had a significant negative effect on cellulase performance, despite the high level of delignification achieved with this pretreatment. No negative effect due to lignin was detected for COSLIF‐treated substrate. SEM micrographs, XRD crystallinity measurements, and cellulose accessibility to cellulase (CAC) determinations confirmed that COSLIF fully disrupted the cell wall structure, resulting in a 16‐fold increase in CAC, while SAA caused a 1.4‐fold CAC increase. A surface plot relating the lignin removal, CAC, and digestibility of numerous samples (both pure cellulosic substrates and lignocellulosic materials pretreated by several methods) was also developed to better understand the relative impacts of delignification and CAC on glucan digestibility. Biotechnol. Bioeng. 2011; 108:22–30.

High-yield hydrogen production from starch and water by a synthetic enzymatic pathway.

Background The future hydrogen economy offers a compelling energy vision, but there are four main obstacles: hydrogen production, storage, and distribution, as well as fuel cells. Hydrogen production from inexpensive abundant renewable biomass can produce cheaper hydrogen, decrease reliance on fossil fuels, and achieve zero net greenhouse gas emissions, but current chemical and biological means suffer from low hydrogen yields and/or severe reaction conditions. Methodology/Principal Findings Here we demonstrate a synthetic enzymatic pathway consisting of 13 enzymes for producing hydrogen from starch and water. The stoichiometric reaction is C6H10O5 (l)+7 H2O (l)→12 H2 (g)+6 CO2 (g). The overall process is spontaneous and unidirectional because of a negative Gibbs free energy and separation of the gaseous products with the aqueous reactants. Conclusions Enzymatic hydrogen production from starch and water mediated by 13 enzymes occurred at 30°C as expected, and the hydrogen yields were much higher than the theoretical limit (4 H2/glucose) of anaerobic fermentations. Significance The unique features, such as mild reaction conditions (30°C and atmospheric pressure), high hydrogen yields, likely low production costs (

Comparative study of corn stover pretreated by dilute acid and cellulose solvent‐based lignocellulose fractionation: Enzymatic hydrolysis, supramolecular structure, and substrate accessibility

∼2/kg H2), and a high energy-density carrier starch (14.8 H2-based mass%), provide great potential for mobile applications. With technology improvements and integration with fuel cells, this technology also solves the challenges associated with hydrogen storage, distribution, and infrastructure in the hydrogen economy.

Spontaneous High-Yield Production of Hydrogen from Cellulosic Materials and Water Catalyzed by Enzyme Cocktails

Liberation of fermentable sugars from recalcitrant biomass is among the most costly steps for emerging cellulosic ethanol production. Here we compared two pretreatment methods (dilute acid, DA, and cellulose solvent and organic solvent lignocellulose fractionation, COSLIF) for corn stover. At a high cellulase loading [15 filter paper units (FPUs) or 12.3 mg cellulase per gram of glucan], glucan digestibilities of the corn stover pretreated by DA and COSLIF were 84% at hour 72 and 97% at hour 24, respectively. At a low cellulase loading (5 FPUs per gram of glucan), digestibility remained as high as 93% at hour 24 for the COSLIF‐pretreated corn stover but reached only ∼60% for the DA‐pretreated biomass. Quantitative determinations of total substrate accessibility to cellulase (TSAC), cellulose accessibility to cellulase (CAC), and non‐cellulose accessibility to cellulase (NCAC) based on adsorption of a non‐hydrolytic recombinant protein TGC were measured for the first time. The COSLIF‐pretreated corn stover had a CAC of 11.57 m2/g, nearly twice that of the DA‐pretreated biomass (5.89 m2/g). These results, along with scanning electron microscopy images showing dramatic structural differences between the DA‐ and COSLIF‐pretreated samples, suggest that COSLIF treatment disrupts microfibrillar structures within biomass while DA treatment mainly removes hemicellulose. Under the tested conditions COSLIF treatment breaks down lignocellulose structure more extensively than DA treatment, producing a more enzymatically reactive material with a higher CAC accompanied by faster hydrolysis rates and higher enzymatic digestibility. Biotechnol. Bioeng. 2009;103: 715–724.

Production of biocommodities and bioelectricity by cell-free synthetic enzymatic pathway biotransformations: challenges and opportunities.

Cocktail reception: Biohydrogen is produced in high yield from cellulosic materials and water in a one-pot process catalyzed by up to 14 enzymes and one coenzyme. This assembly of enzymes results in non-natural catabolic pathways. These spontaneous reactions are conducted under modest reaction conditions (32 degrees C and atmospheric pressure).

A high-energy-density sugar biobattery based on a synthetic enzymatic pathway

Cell-free synthetic (enzymatic) pathway biotransformation (SyPaB) is the assembly of a number of purified enzymes (usually more than 10) and coenzymes for the production of desired products through complicated biochemical reaction networks that a single enzyme cannot do. Cell-free SyPaB, as compared to microbial fermentation, has several distinctive advantages, such as high product yield, great engineering flexibility, high product titer, and fast reaction rate. Biocommodities (e.g., ethanol, hydrogen, and butanol) are low-value products where costs of feedstock carbohydrates often account for approximately 30-70% of the prices of the products. Therefore, yield of biocommodities is the most important cost factor, and the lowest yields of profitable biofuels are estimated to be ca. 70% of the theoretical yields of sugar-to-biofuels based on sugar prices of ca. US

Efficient sugar release by the cellulose solvent-based lignocellulose fractionation technology and enzymatic cellulose hydrolysis.

0.18 per kg. The opinion that SyPaB is too costly for producing low-value biocommodities are mainly attributed to the lack of stable standardized building blocks (e.g., enzymes or their complexes), costly labile coenzymes, and replenishment of enzymes and coenzymes. In this perspective, I propose design principles for SyPaB, present several SyPaB examples for generating hydrogen, alcohols, and electricity, and analyze the advantages and limitations of SyPaB. The economical analyses clearly suggest that developments in stable enzymes or their complexes as standardized parts, efficient coenzyme recycling, and use of low-cost and more stable biomimetic coenzyme analogs, would result in much lower production costs than do microbial fermentations because the stabilized enzymes have more than 3 orders of magnitude higher weight-based total turn-over numbers than microbial biocatalysts, although extra costs for enzyme purification and stabilization are spent.

Facilitated Substrate Channeling in a Self‐Assembled Trifunctional Enzyme Complex

High-energy-density, green, safe batteries are highly desirable for meeting the rapidly growing needs of portable electronics. The incomplete oxidation of sugars mediated by one or a few enzymes in enzymatic fuel cells suffers from low energy densities and slow reaction rates. Here we show that nearly 24 electrons per glucose unit of maltodextrin can be produced through a synthetic catabolic pathway that comprises 13 enzymes in an air-breathing enzymatic fuel cell. This enzymatic fuel cell is based on non-immobilized enzymes that exhibit a maximum power output of 0.8 mW cm(-2) and a maximum current density of 6 mA cm(-2), which are far higher than the values for systems based on immobilized enzymes. Enzymatic fuel cells containing a 15% (wt/v) maltodextrin solution have an energy-storage density of 596 Ah kg(-1), which is one order of magnitude higher than that of lithium-ion batteries. Sugar-powered biobatteries could serve as next-generation green power sources, particularly for portable electronics.

High-yield hydrogen production from biomass by in vitro metabolic engineering: Mixed sugars coutilization and kinetic modeling

Efficient liberation of fermentable soluble sugars from lignocellulosic biomass waste not only decreases solid waste handling but also produces value-added biofuels and biobased products. Industrial hemp, a special economic crop, is cultivated for its high-quality fibers and high-value seed oil, but its hollow stalk cords (hurds) are a cellulosic waste. The cellulose-solvent-based lignocellulose fractionation (CSLF) technology has been developed to separate lignocellulose components under modest reaction conditions (Zhang, Y.-H. P.; Ding, S.-Y.; Mielenz, J. R.; Elander, R.; Laser, M.; Himmel, M.; McMillan, J. D.; Lynd, L. R. Biotechnol. Bioeng. 2007, 97 (2), 214- 223). Three pretreatment conditions (acid concentration, reaction temperature, and reaction time) were investigated to treat industrial hemp hurds for a maximal sugar release: a combinatorial result of a maximal retention of solid cellulose and a maximal enzymatic cellulose hydrolysis. At the best treatment condition (84.0% H3PO4 at 50 degrees C for 60 min), the glucan digestibility was 96% at hour 24 at a cellulase loading of 15 filter paper units of cellulase per gram of glucan. The scanning electron microscopic images were presented for the CSLF-pretreated biomass for the first time, suggesting that CSLF can completely destruct the plant cell-wall structure, in a good agreement with the highest enzymatic cellulose digestibility and fastest hydrolysis rate. It was found that phosphoric acid only above a critical concentration (83%) with a sufficient reaction time can efficiently disrupt recalcitrant lignocellulose structures.

Biohydrogenation from Biomass Sugar Mediated by In Vitro Synthetic Enzymatic Pathways

Most cascade enzymes in metabolic pathways are spatially held together by noncovalent protein–protein interactions. The formation of a cascade enzyme complex often allows the product of one enzyme to be transferred to an adjacent enzyme where it acts as the substrate, thereby resulting in an enhanced reaction rate, because reaching equilibrium in the cytoplasm is not required; this mechanism is called substrate channeling. In nature, most intracellular enzyme complexes are dynamic so that they may be dissociated or associated, thereby resulting in forestallment of substrate competition among different pathways, regulation of metabolic fluxes, mitigation of metabolite inhibition, and circumvention of unfavorable equilibrium and kinetics. The simplest way to facilitate substrate channeling between cascade enzymes is the construction of fusion proteins, but substrate channeling in fusion proteins might not take place. The assembly of numerous enzymes and/or co-enzymes in vitro is called cascade enzyme biocatalysis and has been proposed for the implementation of complicated bioconversion that microbes and chemical catalysts cannot do, such as hydrogen production from cellulosic materials and water with high yield. Inspired by natural enzyme complexes (e.g., metabolons, which are complexes of sequential enzymes of a metabolic pathway), the construction of static rather than dynamic enzyme complexes could be an important approach to accelerating reaction rates among cascade enzymes and to avoiding the regulation of enzyme–enzyme interactions. For example, Wilner et al. linked glucose oxidase and horseradish peroxidase by DNA scaffolds of different lengths, resulting in reaction rates that were enhanced by 20–30-fold. However, DNA scaffolds may be too costly for scale-up as compared to protein scaffolds. Minteer and co-workers demonstrated that chemical cross-linking of proteins within the mitochondria of Saccharomyces cerevisiae resulted in significant increases of the power output in enzymatic fuel cells. But chemical covalent linking often impairs enzyme activity so that it may not be applied to most intracellular enzymes. Herein we demonstrate a general approach for constructing a static self-assembled enzyme complex by using the highaffinity interaction between cohesin and dockerin modules, which occur in natural extracellular complexed cellulase systems, called cellulosomes. Cohesin domains are part of the natural scaffoldin protein of the cellulosome, which is crucial to the construction of the cellulase complex by binding to enzymes carrying dockerin domains. Bayer et al. proposed to construct designed enzyme complexes by utilizing speciesspecific dockerins and cohesins, which can bind tightly in these complexes at a molar ratio of 1:1. Later, several synthetic mini-cellulosomes containing various extracellular glycoside hydrolases were constructed. However, no one attempted to construct an enzyme complex containing cascade enzymes from a metabolic pathway by using dockerins and cohesins and investigated its potential applications in cascade enzyme biocatalysis. Triosephosphate isomerase (TIM, EC 5.3.1.1), aldolase (ALD, EC 4.1.2.13), and fructose 1,6-bisphosphatase (FBP, EC3.1.3.11) are cascade enzymes in the glycolysis and gluconeogenesis pathways. TIM catalyzes the reversible conversion of glycer-aldehyde-3-phosphate (G3P) to dihydroxy-acetone phosphate (DHAP). ALD catalyzes the reversible aldol condensation of G3P and DHAP to fructose-1,6bisphosphate (F16P). FBP catalyzes the irreversible conversion of F16P to fructose-6-phosphate (F6P; Scheme 1). Previous studies reported that substrate channeling existed in dynamic metabolons of enzymes such as TIM, ALD, or FBP. Three dockerin-free proteins: Thermus thermophilus HB27 TIM (TTC0581) as well as the Thermotoga maritima ALD (TM0273) and FBP (TM1415) were expressed in E. coli and purified to homogeneity by using nickel–nitrilotriacetate (Ni–NTA) resin or a self-cleaving intein. However, a mixture of these three enzymes did not form a putative enzyme complex, as examined by affinity electrophoresis (data not shown). The synthetic static three-enzyme complex was assembled in vitro through a synthetic trifunctional scaffoldin containing a family 3 cellulose-binding module (CBM3) at the N terminus followed by three different types of cohesins from the Clostridium thermocellum ATCC 27405 CipA, Clostridium cellulovorans ATCC 35296 CbpA, and Ruminococcus flavefaciens ScaB (cohesins CTCoh, CCCoh, and RFCoh, [*] Dr. C. You, S. Myung, Y.-H. P. Zhang Biological Systems Engineering Department Virginia Tech, 304 Seitz Hall Blacksburg, VA 24061 (USA) E-mail: ypzhang@vt.edu Homepage: http://www.sugarcar.com