A direct fuel cell for the production of electricity from lignin

This report describes the use of an anthraquinone mediated fuel cell for the direct production of electrical energy from sulfonated lignin and Kraft Black Liquor. The cell produces the equivalent of 1 kWh for each 2-3 lb sulfonated lignin and 5-8 lb black liquor combustibles. In the case of the sulfonated lignin, chain session occurs during the oxidation process, reducing the molecular weight from ca. 2 x 10(4) to less than 1000 D.     

Potential applications of bio-ligninolytic systems

Members of various fungal taxa and actinomycetes have been shown to degrade lignin at least partially. The white-rot wood-decomposing basidiomycetes completely metabolize the complex polymer, exhibit the highest reported rates, and are the most studied. Evidence indicates that their degradation of lignin involves oxidative, non-specific reactions, but the nature of the catalysts and the reactive species remain undefined; the catalysts have not been separated from living cells. Culture conditions optimal for lignin metabolism by white-rot fungi have been described, and several potential applications of whole ligninolytic cultures have been explored preliminarily: (a) partial delignification for the production of cellulosic products (bio-mechanical pulping, bio-bleaching); (b) conversion of lignocellulosics (improving ruminant digestibility, cultivating edible mushrooms) into feed and food; and (c) treatment of lignin-derived wastes (decolorizing, removing BOD, COD). The possibility to biomodify by-product lignins to yield valuable polymeric or low molecular weight chemicals has not been approached experimentally, but is another area of potential application. Improved waste treatment processes might well be the first intentional application of bioligninolytic systems.     

Biodegradation of kraft lignin by a newly isolated bacterial strain, <Emphasis Type="Italic">Aneurinibacillus aneurinilyticus</Emphasis> from the sludge of a pulp paper mill

A kraft lignin-degrading bacterium (ITRC S ₇ ) was isolated from sludge of pulp and paper mill and characterized as Aneurinibacillus aneurinilyticus by biochemical tests and 16SrRNA gene sequencing. The bacterium did not utilize kraft lignin (KL) as the sole source of carbon and energy. However, this strain reduced the color (58%) and lignin content (43%) from kraft lignin-mineral salt medium when supplemented with glucose at pH 7.6 and 30°C after 6 days. The degradation on addition of glucose in culture medium is clear evidence of co-metabolism of KL by A. aneurinilyticus. The analysis of lignin degradation products by GC-MS in ethyl acetate extract from an A. aneurinilyticus-inoculated sample revealed the formation of low molecular weight aromatic compounds such as guaiacol, acetoguaiacone, gallic acid and ferulic acid, indicating that the bacterium can oxidize of the sinapylic (G units) and coniferylic (S units) alcohol units which are the basic moieties that build the hardwood lignin structure. The low molecular weight aromatic compounds identified in extracts of the inoculated sample favors the idea of biochemical modification of the KL to a single aromatic unit.     

Oxidation of a tetrameric nonphenolic lignin model compound by lignin peroxidase

The present study maps the active site of lignin peroxidase in respect to substrate size using either fungal or recombinant wild type, as well as mutated, recombinant lignin peroxidases. A nonphenolic tetrameric lignin model was synthesized that contains beta-O-4 linkages. The fungal and recombinant wild type lignin peroxidase both oxidized the tetrameric model forming four products. The four products were identified by mass spectral analyses and compared with synthetic standards. They were identified as tetrameric, trimeric, dimeric, and monomeric carbonyl compounds. All four of these products were also formed from single turnover experiments. This indicates that lignin peroxidase is able to attack any of the C(alpha)-C(beta) linkages in the tetrameric compound and that the substrate-binding site is well exposed. Mutation of the recombinant lignin peroxidase (isozyme H8) in the heme access channel, which is relatively restricted and was previously proposed to be the veratryl alcohol-binding site (E146S), had little effect on the oxidation of the tetramer. In contrast, mutation of a Trp residue (W171S) in the alternate proposed substrate-binding site completely inhibited the oxidation of the tetrameric model. These results are consistent with lignin peroxidase having an exposed active site capable of directly interacting with the lignin polymer without the advent of low molecular weight mediators.     

假单胞菌S—42对偶氮染料的脱色和降解代谢

Pseudomonas S-42 was capable of decolorizing azo dyes such as Diamira Brilliant Orange RR(DBO-RR), Direct Brown M (DBM), Eriochrome Brown R(EBR) and so on. The cell suspension, cell-free extract and purified enzyme of Pseud. S-42 could decolorize azo dyes under similar conditions: the optimum pH and temperature laid 7.0 and 37 degrees C respectively. The efficiencies of decolorizing of DBO-RR, DBM, EBR by intact cells stood more than 90%. When the cell concentration was 15 mg(wet)/ml and the reaction time was 5 hours, the decolorizing activity for above three azo dyes by intact cells were 1.75, 2.4, 0.95 micrograms dye/mg cell, respectively. Cell-free extract and purified enzyme could well express the decolorizing activity only under the anaerobic condition and added NADH. Purified enzyme belongs to azoreductase, its molecular weight is about 34,000-2000 daltons, and its Vmax and Km for DBO-RR are 13 mumol.mg protein-1.min-1 and 54 mumol/L. The results of the detection of the biodegrading products of DBO-RR by spectrophotometric and NaNO2 reactional methods showed that the biodegradation of azo dyes was initiated by the reduction cleavage of azo bonds. It was hypothesized that biodegrading metabolism pathway of DBO-RR by Pseudomonas S-42.     

Factors affecting lignin degradation in lignocellulose by Phanerochaete chrysosporium

Cultural conditions affecting lignin degradation by Phanerochaete chrysosporium in various lignocellulosic materials were studied in comparison to an isolated lignin preparation. With shallow mycelial cultures, the degradation of lignin in wood proceeded more slowly in a 100% O₂-atmosphere than in an air atmosphere, indicating that pure oxygen was toxic to the fungus. The organism was able to degrade lignin efficiently even under 30% CO₂ and 10% O₂ concentrations. Evolution of ¹⁴CO₂ from labelled lignocellulosic materials was shown not to be representative of total lignin degradation. Addition of glucose to the culture did not affect lignin degradation measured by ¹⁴CO₂ evolution, whereas lignin degradation measured by Klason lignin method stopped completely (poplar) or slowed considerably (straw). Due to partial depolymerization of lignin to soluble products, measuring only the evolution of ¹⁴CO₂ results in an underestimation of the total amount of lignin bioaltered. The soluble products from all of the tested lignocellulosic materials and from the isolated lignin had an average molecular weight of about 1,000 and the products could be further fractionated by ion exchange chromatography. The relative amount of these products could be varied from 15 to 45% from the original lignin.     

Microbial degradation of lignin

The transformations of lignin that occur during its biodegradation are complex and incompletely understood. Certain fungi of the white-rot group, and possibly other fungi and bacteria, completely decompose lignin to carbon dioxide and water. Other fungi and bacteria apparently degrade lignin incompletely. Differences in lignin-degrading abilities observed for different organisms may result from differences in the completeness of their ligninolytic enzyme systems. Not all lignin components may be attacked by a particular organism. Alternatively, different organisms may differ in their basic mechanisms of attack on lignin. The basic pathways of lignin degradation have been elucidated only for certain representatives of the white-and brown-rot fungi. Although it is known that each of the principal structural components of lignin is attacked by other fungi and bacteria, the biochemistry of that attack has not been elucidated. Work with low molecular weight lignin models has provided only limited information on possible pathways of lignin degradation by microorganisms. There is little evidence to suggest a correlation between abilities to degrade single-ring aromatic or lignin model compounds and the ability to degrade polymeric lignin. More evidence has come from analysis of spent culture media for lignin breakdown products and from comparative chemical analyses of sound lignins versus decayed lignin residues. Accumulated evidence with the most thoroughly studied white-rot fungi suggests that with these fungi lignin degradation proceeds by way of extracellular mixed-function oxygenases and dioxygenases, which catalyse demethylations, hydroxylations and ring-fission reactions within a largely intact polymer, concomitant with some release of low molecular weight lignin fragments. There are also apparent relationships between lignin, carbohydrate and nitrogen metabolism for some organisms, but the relationships may vary from one organism to another. Although research is now mostly at a basic level, industrial applications may result from lignin degradation research. Considerable potential exists for the development of bioconversions which might produce low molecular weight chemicals from waste lignins, and thereby reduce our dependence on petroleum as a source of these chemicals. Alternatively, such bioconversions might produce chemically altered forms of polymeric lignin that may be valuable industrially.     

Integrating Separation and Conversion—Conversion of Biorefinery Process Streams to Biobased Chemicals and Fuels

The concept of the integrated biorefinery is critical to developing a robust biorefining industry in the USA. Within this model, the biorefinery will produce fuel as a high-volume output addressing domestic energy needs and biobased chemical products (high-value organics) as an output providing necessary economic support for fuel production. This paper will overview recent developments within two aspects of the integrated biorefinery—the fractionation of biomass into individual process streams and the subsequent conversion of lignin into chemical products. Solvent-based separation of switchgrass, poplar, and mixed feedstocks is being developed as a biorefinery “front end” and will be described as a function of fractionation conditions. Control over the properties and structure of the individual biomass components (carbohydrates and lignin) can be observed by adjusting the fractionation process. Subsequent conversion of the lignin isolated from this fractionation leads to low molecular weight aromatics from selective chemical oxidation. Together, processes such as these provide examples of foundational technology that will contribute to a robust domestic biorefining industry.     

Hydroxymethylation and oxidation of Organosolv lignins and utilization of the products

Organosolv lignins obtained from Eucalyptus grandis, sugarcane bagasse and Picea abies by Acetosolv, Formacell and Organocell processes were characterized, fractionated and converted to hydroxymethylated and oxidized products. The reactivity of lignins with formaldehyde did not improve significantly with the fractionation. Both eucalyptus Acetosolv (EAc) and eucalyptus Formacell (EFo) lignins retained high heterogeneity in relation to the molecular weight distribution but not in relation to structural units. The temperatures of the exothermic peaks and the apparent activation energies for the cross-linking are different for hydroxymethylated lignins and phenol, with similar cure temperatures of the resols. Chemical oxidation using cobalt(II) and manganese(II) salts furnished oxidized lignins with improved chelating properties. These chelating agents can remove up to 14% of Mn present in pulps, decreasing the peroxide consumption in the bleaching process. The products obtained can be also used as oxidized phenols and controlled-release matrices. Oxidation of Acetosolv bagasse lignin with polyphenol oxidase furnishes lignins with chelating capacity 110% higher than that of original lignin.     

Molecular weight distribution of Pinus radiata kraft mill wastewater treated by anaerobic digestion

Kraft mill is responsible for massive discharge of highly polluted effluents. The main characteristics of this effluent are high toxicity and low biodegradability due to tannin, lignin and chlorophenol compounds. The composition may vary dramatically depending, for instance, on the utilised feedstock and process. The purpose of this work was to investigate the molecular weight distribution of Pinus radiata kraft pulping wastewater treated by anaerobic digestion by using two types of anaerobic reactors: fixed bed and sludge blanket. Anaerobic sludge blanket (UASB) and anaerobic filter (AF) were operated. In both reactors, the total alkalinity ranged between 1.0 and 1.5 g CaCO3/l, while the organic load rate (OLR) was increasing during operation from 1.2 to 3.3 gCOD/l d. COD and total phenolic compounds (UV215) removal ranged between 30-50% and 13-20%, respectively, while the BOD5 removal ranged 60-90%. However only a partial biodegradation (10-43%) of tannin and lignin was observed. Results from ultrafiltration analyses indicated that the fraction with a molecular weight (MW) < 1000, COD and colour decreased after anaerobic treatment, but the total phenolic compounds increased. In the 1000 < MW < 10,000 fraction, there was no change in COD, UV215 and colour. In the > 10,000 MW fraction, colour and COD fraction increased by 14% and 5%, respectively, after anaerobic treatment. It can be concluded from this study, that treatment with UASB or AF reactors is not enough, under the conditions tested, for a large COD removal from Pinus radiata wastewater.     

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.     

Decolorization of effluent from the bagasse-based pulp mills by white-rot fungus,Schizophyllum commune

Summary The effluent from bagasse-based pulp and paper mills can be decolorized with the white-rot fungus Schizophyllum commune. The influence of pH, nutrients and aeration on the decolorizing efficiency of this fungus has been determined. It was found that it could not degrade lignin unless a more easily metabolized carbon source was made available simultaneously. The addition of carbon and nitrogen not only improved the decolorizing efficiency of the fungus, but also resulted in reduction of the biological oxygen demand (BOD) and chemical oxygen demand (COD) of effluent. A 2-day incubation period was sufficient for lignin breakdown by S. commune. The efficiency of treatment of effluent with this fungus was highest at pH 4–5 and was further improved by intermittent aeration.     

Modification of lignin for the production of new compounded materials

The cell walls of woody plants are compounded materials made by in situ polymerization of a polyphenolic matrix (lignin) into a web of fibers (cellulose), a process that is catalysed by polyphenoloxidases (laccases) or peroxidases. The first attempt to transform the basic strategy of this natural process for use in human craftsmanship was the ancient lacquer method. The sap of the lacquer tree (Rhus verniciflua) contains large amounts of a phenol (urushiol), a polysaccharide and the enzyme laccase. This oil-in-water emulsion solidifies in the presence of oxygen. The Chinese began using this phenomenon for the production of highly creative artwork more than 6,000 years ago. It was the first example of an isolated enzyme being used as a catalyst to create an artificial plastic compound. In order to apply this process to the production of products on an industrial scale, an inexpensive phenol must be used, which is transferred by an enzyme to active radicals that react with different components to form a compounded material. At present, the following approaches have been studied: (1) In situ polymerization of lignin for the production of particle boards. Adhesive cure is based on the oxidative polymerization of lignin using phenoloxidases (laccase) as radical donors. This lignin-based bio-adhesive can be applied under conventional pressing conditions. The resulting particle boards meet German performance standards. By this process, 80% of the petrochemical binders in the wood-composite industry can be replaced by materials from renewable resources. (2) Enzymatic copolymerization of lignin and alkenes. In the presence of organic hydroperoxides, laccase catalyses the reaction between lignin and olefins. Detailed studies on the reaction between lignin and acrylate monomers showed that chemo-enzymatic copolymerization offers the possibility to produce defined lignin-acrylate copolymers. The system allows control of the molecular weights of the products in a way that has not been possible with chemical catalysts. This is a novel attempt to enzymatically induce grafting of polymeric side chains onto the lignin backbone, and it enables the utilization of lignin as part of new engineering materials. (3) Enzymatic activation of the middle-lamella lignin of wood fibers for the production of wood composites. The incubation of wood fibers with a phenol oxidizing enzyme results in oxidative activation of the lignin crust on the fiber surface. When such fibers are pressed together, boards are obtained which meet the German standards for medium-density fiber boards (MDF). The fibers are bound together in a way that comes close to that by which wood fibers are bound together in naturally grown wood. This process will, for the first time, yield wood composites that are produced solely from naturally grown products without any addition of resins.     

Fractionation of wheat straw by atmospheric acetic acid process

Fractionation of wheat straw was investigated using an atmospheric acetic acid process. Under the typical conditions of 90% (v/v) aqueous AcOH, 4% H(2)SO(4) (w/w, on straw), ratio of liquor to straw (L/S) 10 (v/w), pulping temperature 105 degrees C, and pulping time 3h, wheat straw was fractionated to pulp (cellulose), lignin and monosaccharides mainly from hemicellulose with yields of approximately 50%, 15% and 35%, respectively. Acetic acid pulp from the straw had an acceptable strength for paper and could be bleached to a high brightness over 85% with a short bleaching sequence. Acetic acid pulp was also a potential feedstock for fuels and chemicals. The acetic acid process separated pentose and hexose in wheat straw to a large extent. Most of the pentose (xylan) was dissolved, whereas the hexose (glucan) remained in the pulp. Approximately 30% of carbohydrates in wheat straw were hydrolyzed to monosaccharides during acetic acid pulping, of which xylose accounted for 70% and glucose for 12%. The acetic acid lignin from wheat straw showed relatively lower molecular weight and fusibility, which made the lignin a promising raw material for many products, such as adhesive and molded products.     

黄孢原毛平革菌木素过氧化物酶类在天然木素降解中作用的研究

通过诱变得到十一株木素过氧化物酶酶活降低的黄孢原毛平革菌（Ｐｈａｎｅｒｏｃｈａｅｔｅｃｈｒｙｓｏｓｐｏｒｉｕｍ）突变株,用灰色理论分析了其木素过氧化物酶类的产生与木素降解能力间的相关性,并从中筛选到一株木素过氧化物酶缺陷、锰过氧化物酶酶活明显降低的突变株,其木素降解能力为原始菌株的８０％左右。该菌粗酶液作用于纤维素酶酶解杉木木素和天然褐腐木素,可产生小分子的木素降解产物,此反应不需Ｈ２Ｏ２参与。红外光谱分析表明粗酶液对木素的作用主要为氧化作用,因此推测此突变株粗酶液中含有不同于木素过氧化物酶和锰过氧化物酶的与木素氧化降解有关的酶类     

Polymerization of guaiacol and a phenolic beta-O-4-substructure by Trametes hirsuta laccase in the presence of ABTS

The reaction of the monomeric lignin model compound guaiacol and the beta-O-4-type dimer erol (1-(4-hydroxy-3-methoxyphenyl)-2(2-methoxyphenoxy)-propane-1,3-diol with laccase from Trametes hirsuta was studied in the presence of the mediator ABTS (2,2'-azino-di[3ethylbenzothiazoline-6-sulfonic acid]). The product mixtures were analyzed by means of aqueous-phase size exclusion chromatography (SEC) with 50 mM NaOH as eluent. Interestingly, in the laccase-catalyzed reaction with both substrates, the mediator not only functioned as an electron carrier but underwent coupling reactions with the substrate to give polymeric coupling products. The molecular weight of these copolymeric products was significantly higher than the molecular weight of products obtained without ABTS. After ultrafiltration, 33% and 21% of the initially applied ABTS could be found in the polymeric product fraction for the substrates guaiacol and erol, respectively, on the basis of nitrogen analysis. When ABTS was added to substrates after full laccase-catalyzed polymerization, the reaction proceeded toward higher molecular weights.     

Biorefining of softwoods using ethanol organosolv pulping: preliminary evaluation of process streams for manufacture of fuel-grade ethanol and co-products

Pulps with residual lignin ranging from 6.4-27.4% (w/w) were prepared from mixed softwoods using a proprietary biorefining technology (the Lignol process) based on aqueous ethanol organosolv extraction. The pulps were evaluated for bioconversion using enzymatic hydrolysis of the cellulose fraction to glucose and subsequent fermentation to ethanol. All pulps were readily hydrolyzed without further delignification. More than 90% of the cellulose in low lignin pulps (< or =18.4% residual lignin) was hydrolyzed to glucose in 48 h using an enzyme loading of 20 filter paper units/g cellulose. Cellulose in a high lignin pulp (27.4% residual lignin) was hydrolyzed to >90% conversion within 48 h using 40 filter paper units/g. The pulps performed well in both sequential and simultaneous saccharification and fermentation trials indicating an absence of metabolic inhibitors. Chemical and physical analyses showed that lignin extracted during organosolv pulping of softwood is a suitable feedstock for production of lignin-based adhesives and other products due to its high purity, low molecular weight, and abundance of reactive groups. Additional co-products may be derived from the hemicellulose sugars and furfural recovered from the water-soluble stream.     

Biodegradation of radiolabelled synthetic lignin (14C-DHP) and mechanical pulp in a compost environment

Mineralization of radioactive synthetic lignin (14C-DHP) was studied in a compost environment at 35, 50 and 58 degrees C. Compost samples were successively extracted with water, dioxane and alkali, and the molecular weight distribution of some extracts was determined by gel permeation chromatography (GPC). Biodegradation of lignin-containing spruce groundwood (SGW) and pine sawdust was concurrently determined in controlled composting tests by measuring evolved CO2. The temperatures were the same as in the 14C-DHP mineralization experiment and bleached kraft paper, with a lignin content of 0.2%, was used as a reference. The mineralization of 14C-DHP was relatively high (23-24%) at 35 degrees C and 50 degrees C, although the mixed population of compost obviously lacks the most effective lignin degraders. At 58 degrees C the mineralization of 14C-DHP, as well as the biodegradation of SGW and sawdust, was very low, indicating that the lignin-degrading organisms of compost were inactivated at this temperature. SGW was poorly biodegradable (<40%) in controlled composting tests compared with kraft paper (77-86%) at all temperatures, which means that lignin inhibits the degradation of carbohydrates. During the incubation, water-soluble degradation products, mainly monomers and dimers, and the original 14C-DHP were either mineralized or bound to humic substances. A substantial fraction of 14C-DHP was incorporated into humin or other insolubles.     

Biocatalysis in ionic liquids for lignin valorization: Opportunities and recent developments

Lignin holds tremendous potential as a renewable feedstock for upgrading to a number of high-value chemicals and products that are derived from the petroleum industry at present. Since lignin makes up a significant fraction of lignocellulosic biomass, co-utilization of lignin in addition to cellulose and hemicelluloses is vital to the economic viability of cellulosic biorefineries. The recalcitrant nature of lignin, originated from the molecule's compositional and structural heterogeneity, however, poses great challenges toward effective and selective lignin depolymerization and valorization. Ionic liquid (IL) is a powerful solvent that has demonstrated high efficiency in fractionating lignocellulosic biomass into sugar streams and a lignin stream of reduced molecular weight. Compared to thermochemical methods, biological lignin deconstruction takes place at mild temperature and pressure while product selectivity can be potentially improved via the specificity of biocatalysts (lignin degrading enzymes, LDEs). This review focuses on a lignin valorization strategy by harnessing the biomass fractionating capabilities of ILs and the substrate and product selectivity of LDEs. Recent advances in elucidating enzyme-IL interactions as well as strategies for improving enzyme activity in IL are discussed, with specific emphases on biocompatible ILs, thermostable and IL-tolerant enzymes, enzyme immobilization, and surface charge engineering. Also reviewed is the protein engineering toolsets (directed evolution and rational design) to improve the biocatalysts' activity, stability and product selectivity in IL systems. The alliance between IL and LDEs offers a great opportunity for developing a biocatalytic route for lignin valorization.     

Reactivity of different oxidases with lignins and lignin model compounds

Oxidase activities toward lignins and lignin model compounds failed to produce low molecular weight products. Peroxidase and laccase react similarly, and can be distinguished when both enzymes are present on the basis of pH activity differences with syringaldazine as substrate.