Genetic modification of lignin biosynthesis for improved biofuel production

The energy in cellulosic biomass largely resides in plant cell walls. Cellulosic biomass is more difficult than starch to break down into sugars because of the presence of lignin and the complex structure of cell walls. Transgenic down-regulation of major lignin genes led to reduced lignin content, increased dry matter degradability, and improved accessibility of cellulases for cellulose degradation. This review provides background information on lignin biosynthesis and focuses on genetic manipulation of lignin genes in important monocot species as well as the dicot potential biofuel crop alfalfa. Reduction of lignin in biofuel crops by genetic engineering is likely one of the most effective ways of reducing costs associated with pretreatment and hydrolysis of cellulosic feedstocks, although some potential fitness issues should also be addressed.     

Energy requirements and process design considerations in compression-milling pretreatment of cellulosic wastes for enzymatic hydrolysis

The effectiveness of compression-milling pretreatment of lignocellulosics for enzymatic hydrolysis has been demonstrated for a wide variety of substrate sources. Reductions in the degree of crystallinity and the degree of polymerization of cellulose and partial destruction of the structural integrity of lignocellulosics brought about by compression milling significantly increase the susceptibility of cellulose to enzymatic hydrolysis. The enzymatic hydrolysis yield was found to be directly related to the specific energy input to the cellulosic substrate (kWh/1b substrate) by compression milling, and the energy input can be controlled by the milling time. The enzymatic hydrolysis yeilds from cellulosic materials pretreated by compression milling also vary significantly depending on the source and kind, the composition milling also vary significantly depending on the source and kind, the composition (contents of lignin and other components), and the structure. The power requirements for compression milling which renders equivalent hydrolysis yields also depend on the source and kind of lignocellulosics to be pretreated. For newspaper, the specific energy input required for 55% sugar yield is estimated as 0.3 kWh/lb substrate including 15% power loss. The additional sugar yield gained from the enzymatic hydrolysis of compression-milled newspaper (over and above the sugar yield of untreated substrate) is determined as 453 g sugar/kWh energy input.     

Influence of steam pretreatment severity on post‐treatments used to enhance the enzymatic hydrolysis of pretreated softwoods at low enzyme loadings

It is recognized that some form of post‐treatment will usually be required if reasonable hydrolysis yields (>60%) of steam pretreated softwood are to be achieved when using low enzyme loadings (5 FPU/g cellulose). In the work reported here we modified/removed lignin from steam pretreated softwood while investigating the influence that the severity of pretreatment might have on the effectiveness of subsequent post‐treatments. Although treatment at a lower severity could provide better overall hemicellulose recovery, post‐treatment was not as effective on the cellulosic component. Pretreatment at medium severity resulted in the best compromise, providing reasonable recovery of the water soluble hemicellulose sugars and the use of post‐treatment conditions that significantly increased the enzymatic hydrolysis of the water insoluble cellulosic component. Post‐treatment with alkaline hydrogen peroxide or neutral sulfonation resulted in 62% cellulose hydrolysis at an enzyme loading of 5 FPU/g cellulose, which was four times greater than was obtained when the cellulosic fraction was not post‐treated. When the enzyme loading was increased to 15 FPU/g cellulose, the post‐treated cellulosic fraction was almost completely hydrolyzed to glucose. Despite the higher lignin content (44%) of the sulfonated substrate, similar hydrolysis yields to those achieved after alkaline peroxide post‐treatment (14% lignin content) indicated that, in addition to lignin removal, lignin modification also plays an important role in influencing the effectiveness of hydrolysis when low enzyme loadings are used. Biotechnol. Bioeng. 2011;108: 2300–2311. © 2011 Wiley Periodicals, Inc.     

The cellulose/lignin assembly assessed by molecular modeling. Part 1: adsorption of a threo guaiacyl beta-O-4 dimer onto a Ibeta cellulose whisker.

The assembly of the two major cell wall components, cellulose and lignin, were investigated at the atomistic scale using molecular dynamics simulations. To this end, a molecular model of a cellulose crystal corresponding to the allomorph Ibeta and exhibiting different surfaces was considered to mimic the carbohydrate matrix present in native wood cell wall. The lignin model compound considered here is a threo guaiacyl beta-O-4 dimer. The dynamical process of adsorption of the lignin dimer onto the different surfaces of the cellulose crystal was examined. The modes of association between the two constituents were analyzed; energies of adsorption of the dimer are calculated favorable and of the same order of magnitude on all sides of the cellulosic model, suggesting that the deposition of lignin precursors onto cellulose fibers is non-specific from an enthalpic point of view. Interestingly, geometrical characteristics and energetical details of the adsorption are surface-dependent. Computed data have underlined the predominant contribution of van der Waals interactions for adsorption onto the (200) face, as well as the major influence of H-bonding interactions in the dynamical process of adsorption onto (110) and (1-10) faces. A large number of adsorption sites have been identified and a noticeable "flat" geometry of adsorption of the lignin dimer has been observed, as a consequence of the stacking interactions between lignin aromatic rings and C-H groups of cellulose. Importantly, these dispersive interactions lead to a preferential parallel orientation of lignin aromatic rings relative to the cellulose surface, notably on the (200) face. Such a parallel orientation is consistent with previously reported experimental observations.     

Production of Bacterial Proteins from Cellulosic Materials

An aerobic mesophilic Pseudomonas sp. isolated from activated sludge degraded different cellulosic materials to varying-degrees. The degradability was mostly influenced by the lignin content and the crystalline nature of the substrate. Filter paper and cotton fibres, containing little lignin, were degraded maximally. Lignin-rich Pinus and Larix needles were digested to a lesser extent. There was a difference between natural substrates and substrates that had undergone industrial treatment. At maximal protein production, the isolate converted 11–40% (w/w) of cellulosic substrates into proteins. Alkali treatment of the substrates had only little effect. Cellulose contained in pig-waste was also degraded by the isolate. At first there was a period of protein production, but after long incubation, the efficiency of conversion of cellulose to protein decreased.     

Biodegradation of cellulosic materials: Substrates,microorganisms, enzymes and products

Cellulosic materials are the only renewable resources available in large quantities which need to be properly utilized to meet our needs of energy, chemicals, food and feed for a long-range solution. A variety of lignocellulosic materials are available and microorganisms capable of degrading either one or more of the three main constituents, viz. cellulose, hemicellulose and lignin have been studied. At least three different enzymes of the multicomponent cellulase system, i.e. cellobiohydrolase endo-glucanase and β-glucosidase are involved in the degradation of crystalline cellulose into glucose. Their mode of action and the manner in which they bring about hydrolysis of crystalline cellulose is discussed in detail. The involvement of parallel enzymes for hemicellulose degradation is also known to some extent but needs to be studied more elaborately, independently and in combination with cellulases. The potential of cellulosic biomass as a source of fuel and petroleum-sparing substances is also reviewed.     

Effect of peracetic acid, sodium hydroxide and phosphoric acid on cellulosic materials as a pretreatment for enzymatic hydrolysis

Crystalline cellulose and cellulosic wastes have been treated with various concentrations of peracetic acid and other reagents at 100°C for various times, washed with water, ethanol and air dried. For each treated cellulose, the degree of enzymatic solubilization was measured with Trichoderma viride cellulase [1,4-(1,3;1,4)-β-d-glucan 4-glucanohydrolase, EC 3.2.1.4]. Cellulosic wastes such as sunflower stalks, wheat straw and sugar-cane bagasse were solubilized effectively by the enzyme. Delignification of wheat straw with 1% sodium hydroxide and treatment of this straw with peracetic acid enhanced the degree of enzymatic solubilization. Infrared spectra of the untreated and treated cellulosic wastes were recorded.     

Sugarcane Internode Composition During Crop Development

Sugarcane sugar and bagasse can be utilized for the production of ethanol or other biofuels. A better understanding of the changes in composition with development along the stalk and with crop development will maximize the usage of sugarcane for this purpose. Two experiments were designed to elucidate internode composition changes during the growing season. In experiment 1, an internode of stalks of 5 modern cultivars were marked at the start of elongation, and then sampled every 1 to 2?weeks from July until October. Sugars were extracted and assayed, and a sequential detergent method was used to estimate hemicellulose, cellulose, and lignin contents. In experiment 2, internodes 1, 3, 5, 7, 9, and 11 down the stalk were sampled in late July (grand growth) and late September (ripening). Internode length, fresh weight, dry weight, water content, and sugar contents were determined as well as cell wall composition. Both experiments were repeated in 2?years. As internodes elongated, total sugar increased, and hemicellulose decreased as a proportion of neutral detergent fiber, while cellulose and lignin increased. After elongation, sucrose and lignin increased, and cellulose content decreased with internode age. The variability in cell wall composition among the five cultivars suggests that selection for desirable composition may be possible. In Experiment 2, hemicellulose contents were lower, and lignin and ash contents were higher at ripening than during grand growth. Delaying sugarcane harvest to maximize sucrose content may decrease bagasse suitability for cellulosic ethanol production because of the increased lignin content.     

Effect of Maize Biomass Composition on the Optimization of Dilute-Acid Pretreatments and Enzymatic Saccharification

At the core of cellulosic ethanol research are innovations leading to reductions in the chemical and energetic stringency of thermochemical pretreatments and enzymatic saccharification. In this study, key compositional features of maize cell walls influencing the enzymatic conversion of biomass into fermentable sugars were identified. Stem samples from eight contrasting genotypes were subjected to a series of thermal dilute-acid pretreatments of increasing severity and evaluated for glucose release after enzymatic saccharification. The biochemically diverse set of genotypes displayed significant differences in glucose yields at all processing conditions evaluated. The results revealed that mechanisms controlling biomass conversion efficiency vary in relation to pretreatment severity. At highly severe pretreatments, cellulose conversion efficiency was primarily influenced by the inherent efficacy of the thermochemical process, and maximum glucose yields were obtained from cellulosic feedstocks harboring the highest cellulose contents per dry gram of biomass. When mild dilute-acid pretreatments were applied, however, maximum bioconversion efficiency and glucose yields were observed for genotypes combining high stem cellulose contents, reduced cell wall lignin and highly substituted hemicelluloses. For the best-performing genotype, glucose yields under sub-optimal processing regimes were only 10 % lower than the genotype-set mean at the most stringent processing conditions evaluated, while furfural production was reduced by approximately 95 %. Our results ultimately established that cellulosic feedstocks with tailored cell wall compositions can help reduce the chemical and energetic intensity of pretreatments used in the industry and improve the commercial and environmental performance of biomass-to-ethanol conversion technologies.     

Structure and optical properties of plant cell wall bio-inspired materials: cellulose-lignin multilayer nanocomposites

Interfacial affinity between lignin model compound (dehydrogenation polymer [DHP]) and cellulose nanocristals (CN) was studied before building a nanocomposite cellulose/lignin in multilayer form by spin-coating method. The adsorption isotherm of DHP was measured by ellipsometry at the liquid/CN film interface and showed that the surface concentration of adsorbed DHP increases with the bulk concentration in solution. The DHP appeared as globular structures on cellulosic film, as observed by AFM. Spreading a dense lignin layer on CN film gave rise to the disappearance of the InfraRed resonance bands related to the DHP aromatics. The film obtained from alternate layers of cellulose/DHP was transparent in visible light and had weak absorption in UV wavelengths. Optical properties measured in the visible wavelength range by ellipsometry and spectrophotometry indicated that beyond six bilayers (cellulose/DHP), the composite exhibits antireflexion properties.     

Engineering and economics of cellulose saccharification systems

The design of cellulose saccharification systems will govern the economics of biomass conversion to ethanol and other oxygenated compounds. Solids handling of bulky cellulosic materials, chemical processing of a physically and chemically heterogeneous substrate, cellulose pretreatment and product recovery present formidable engineering challenges. Marketing strategy must also be carefully formulated given the variety of hexoses, pentoses, organic acids, as well as lignin which result from biomass processing. Since the intrinsic cost of the biomass is $0.015 to $0.03/lb, and the processing costs are $0.03 to $0.10/lb, the key is to identify products having a value in excess of $0.10/lb which are uniquely suited for production from biomass-derived sugars. Competitive pressures from other carbohydrate sources such as corn and sugar cane must also be considered in the economic analysis. Process concepts and associated costs are presented in a comparison of corn and biomass saccharification routes.     

Effect ofMyrothecium sp. cellulase on different types of cellulose and cellulosic materials

Three types of cellulase preparations were applied to different types of cellulose and cellulosic materials. The action of these types of cellulase on cellulose powder was increased with the increase of enzyme concentration. Both carboxymethyl cellulose (CMC) and sodium carboxymethyl cellulose (Na-CMC) released high amounts of reducing sugar as affected by cellulase application. Different types of paper pulp were moderately hydrolyzed, while agricultural wastes were slightly hydrolyzed. Vegetable and fruits cellulose were equally hydrolyzed but at low rate. Pretreatment of cellulose or cellulosic materials by grinding or by swelling with phosphoric acid gave rise to increased hydrolysis by the enzyme. Cellobiose was detected chromatographically as an intermediate product of hydrolysis of both cellulose and carboxymethyl cellulose with glucose.     

Regional examination shows potential for native feedstock options for cellulosic biofuel production

Kentucky, as with many regions around the globe, has a relatively long growing season with significant rainfall that could produce sizeable quantities of perennial herbaceous and woody biomass on land that does not compete with food crops. Additionally, there are limited options for renewable power production from low carbon sources such as solar-photovoltaic, wind and hydroelectric. Recent studies have shown that producing renewable energy from perennial cellulosic crops, as opposed to starch-based biofuel crops, will have a carbon-mitigating outcome. Currently, there is a lack of data regarding regionally suitable genotypes. Herein, we establish baseline values for multiple entry selections of three native C4 grass species, switchgrass (SW) ( Panicum virgatum L.), eastern gamagrass (EG) (Trispicum dactyloides L. ) and big bluestem (BB) (Andropogon gerardii Vitman ) . Yield potential examined over 7 years showed that environment, species and entries had a significant impact on yield, but EG had higher total yield over the duration of the study. Cellulosic biofuel potential was examined by measurement of saccharification efficiency, relative lignocellulosic energy density, cellulose content and lignin content during three growing seasons. EG had significantly higher digestibility rate than SW and BB. Underlying this was a negative correlation between lignification and saccharification efficiency. However, higher lignin content and higher cellulose content among SW entries resulted in higher energy density relative to EG and BB. These data reveal that locally bred EG varieties were most suited to cellulosic ethanol production under the growing conditions of central Kentucky, USA, compared with SW and BB and suggest the importance of regional examination.     

植物基因工程改善生物质能利用的研究进展

利用植物木质纤维资源发酵生产乙醇越来越受到人们的重视,但是要实现工业化生产仍然存在很多难题。最近,利用植物基因工程技术,改善植物自身性状,包括减少植物自身细胞壁中木质素含量、细胞中积累表达纤维素酶和木聚糖酶等方法,使自生产生的生物质更利于降解利用。目前,对这种新的能源转基因植物的研究取得了一定进展。     

基因工程改善植物生物质能利用的研究进展

利用植物木质纤维资源发酵产乙醇越来越受到人们的重视,但是要达到工业生产仍然存在很多难题。最近在利用植物基因工程技术改善植物自身性状,以利于能源植物的研究方面取得了一定的进展,这些研究包括减少植物自身细胞壁中的木质素含量、细胞中积累表达纤维素酶和木聚耱酶等的方法,使产生的生物质更利于降解利用。     

Effect of xylan and lignin removal by batch and flowthrough pretreatment on the enzymatic digestibility of corn stover cellulose

Compared with batch systems, flowthrough and countercurrent reactors have important potential advantages for pretreating cellulosic biomass, including higher hemicellulose sugar yields, enhanced cellulose digestibility, and reduced chemical additions. Unfortunately, they suffer from high water and energy use. To better understand these trade-offs, comparative data are reported on xylan and lignin removal and enzymatic digestibility of cellulose for corn stover pretreated in batch and flowthrough reactors over a range of flow rates between 160 degrees and 220 degrees C, with water only and also with 0.1 wt% sulfuric acid. Increasing flow with just water enhanced the xylan dissolution rate, more than doubled total lignin removal, and increased cellulose digestibility. Furthermore, adding dilute sulfuric acid increased the rate of xylan removal for both batch and flowthrough systems. Interestingly, adding acid also increased the lignin removal rate with flow, but less lignin was left in solution when acid was added in batch. Although the enzymatic hydrolysis of pretreated cellulose was related to xylan removal, as others have shown, the digestibility was much better for flowthrough compared with batch systems, for the same degree of xylan removal. Cellulose digestibility for flowthrough reactors was related to lignin removal as well. These results suggest that altering lignin also affects the enzymatic digestibility of corn stover.     

Molecular engineering of the cellulosome complex for affinity and bioenergy applications

The cellulosome complex has evolved to degrade plant cell walls and, as such, combines tenacious binding to cellulose with diverse catalytic activities against amorphous and crystalline cellulose. Cellulolytic microorganisms provide an extensive selection of domains; those with affinity for cellulose, cohesins and their dockerin binding partners that define cellulosome stoichiometry and architecture, and a range of catalytic activities against carbohydrates. These robust domains provide the building blocks for molecular design. This review examines how protein modules derived from the cellulosome have been incorporated into chimaeric proteins to provide biosynthetic tools for research and industry. These applications include affinity tags for protein purification, and non-chemical methods for immobilisation and presentation of recombinant protein domains on cellulosic substrates. Cellulosomal architecture provides a paradigm for design of enzymatic complexes that synergistically combine multiple catalytic subunits to achieve higher specific activity than would be obtained using free enzymes. Multimeric enzymatic complexes may have industrial applications of relevance for an emerging carbon economy. Biocatalysis will lead to more efficient utilisation of renewable carbon-fixing energy sources with the added benefits of reducing chemical waste streams and reliance on petroleum.