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Lee R Lynd

Publications and source records attributed to Lee R Lynd.

At least 19 recordsLinked to original sources
PubMed2006

Conversion of paper sludge to ethanol, II: process design and economic analysis.

Process design and economics are considered for conversion of paper sludge to ethanol. A particular site, a bleached kraft mill operated in Gorham, NH by Fraser Papers (15 tons dry sludge processed per day), is considered. In addition, profitability is examined for a larger plant (50 dry tons per day) and sensitivity analysis is carried out with respect to capacity, tipping fee, and ethanol price. Conversion based on simultaneous saccharification and fermentation with intermittent feeding is examined, with ethanol recovery provided by distillation and molecular sieve adsorption. It was found that the Fraser plant achieves positive cash flow with or without xylose conversion and mineral recovery. Sensitivity analysis indicates economics are very sensitive to ethanol selling price and scale; significant but less sensitive to the tipping fee, and rather insensitive to the prices of cellulase and power. Internal rates of return exceeding 15% are projected for larger plants at most combinations of scale, tipping fee, and ethanol price. Our analysis lends support to the proposition that paper sludge is a leading point-of-entry and proving ground for emergent industrial processes featuring enzymatic hydrolysis of cellulosic biomass.

Conservation of Natural Resources↗
PubMed2006

Conversion of paper sludge to ethanol. I: impact of feeding frequency and mixing energy characterization.

In this paper, conversion of paper sludge to ethanol was investigated with the objective of optimization of the overall operation costs. Experimental work was undertaken to optimize cellulase loading, and to determine mixing energy requirements. It was found that decreasing feeding frequency (feed additions per residence time) allows the cellulase loading to be decreased at least two fold with no decrease in cellulose conversion but also entails mixing a slurry of higher solids content and lower conversion at the beginning of the operating cycle. The viscosity of paper sludge slurries was found to increase exponentially with decreasing conversion and increasing solid content. In particular, the viscosity (V) was described well by equation V = e(kX-X )(0)(S-S)(0)+C (V viscosity (cp), X conversion, S solid content (g/L), k, X (0), S (0), C are empirical parameters). Added costs associated with operating at low feeding frequencies (including higher mixing energy and higher capital costs for the motor and for sludge hold tasks) were found to be small compared to the economic benefits resulting from reduced cellulase loading.

Cellulase↗
PubMed2006

Enzyme-microbe synergy during cellulose hydrolysis by Clostridium thermocellum.

Specific cellulose hydrolysis rates (g of cellulose/g of cellulase per h) were shown to be substantially higher (2.7- to 4.7-fold) for growing cultures of Clostridium thermocellum as compared with purified cellulase preparations from this organism in controlled experiments involving both batch and continuous cultures. This "enzyme-microbe synergy" requires the presence of metabolically active cellulolytic microbes, is not explained by removal of hydrolysis products from the bulk fermentation broth, and appears due to surface phenomena involving adherent cellulolytic microorganisms. Results support the desirability of biotechnological processes featuring microbial conversion of cellulosic biomass to ethanol (or other products) in the absence of added saccharolytic enzymes.

Cellulose↗
PubMed2006

Hydrolysis and fermentation of amorphous cellulose by recombinant Saccharomyces cerevisiae.

In this study, we expressed two cellulase encoding genes, an endoglucanase of Trichoderma reesei (EGI) and the beta-glucosidase of Saccharomycopsis fibuligera (BGL1), in combination in Saccharomyces cerevisiae. The resulting strain was able to grow on phosphoric acid swollen cellulose (PASC) through simultaneous production of sufficient extracellular endoglucanase and beta-glucosidase activity. Anaerobic growth (0.03h(-1)) up to 0.27gl(-1) DCW was observed on medium containing 10gl(-1) PASC as sole carbohydrate source with concomitant ethanol production of up to 1.0gl(-1). We have thus demonstrated the construction of a yeast strain capable of growth on and one-step conversion of amorphous cellulose to ethanol, representing significant progress towards realization of one-step processing of cellulosic biomass in a consolidated bioprocessing configuration. To our knowledge, this is the first report of a recombinant strain of S. cerevisiae growing on pure cellulose.

Base Sequence↗
PubMed2006

A functionally based model for hydrolysis of cellulose by fungal cellulase.

A new functionally based kinetic model for enzymatic hydrolysis of pure cellulose by the Trichoderma cellulase system is presented. The model represents the actions of cellobiohydrolases I, cellobiohydrolase II, and endoglucanase I; and incorporates two measurable and physically interpretable substrate parameters: the degree of polymerization (DP) and the fraction of beta-glucosidic bonds accessible to cellulase, F(a) (Zhang and Lynd, 2004). Initial enzyme-limited reaction rates simulated by the model are consistent with several important behaviors reported in the literature, including the effects of substrate characteristics on exoglucanase and endoglucanase activities; the degree of endo/exoglucanase synergy; the endoglucanase partition coefficient on hydrolysis rates; and enzyme loading on relative reaction rates for different substrates. This is the first cellulase kinetic model involving a single set of kinetic parameters that is successfully applied to a variety of cellulosic substrates, and the first that describes more than one behavior associated with enzymatic hydrolysis. The model has potential utility for data accommodation and design of industrial processes, structuring, testing, and extending understanding of cellulase enzyme systems when experimental date are available, and providing guidance for functional design of cellulase systems at a molecular scale. Opportunities to further refine cellulase kinetic models are discussed, including parameters that would benefit from further study.

Cellulase↗
PubMed2005

Theoretical analysis of selection-based strain improvement for microorganisms with growth dependent upon extracytoplasmic enzymes.

This study analyzes selection in continuous culture as a means to improve the growth of microorganisms dependent upon the expression of extracytoplasmic enzymes. A quantitative, theoretical model was developed that considers increases in enzyme activity and/or expression due to mutation in conjunction with reaction and diffusion at the cell surface and in the surrounding boundary layer. This model was applied to a system consisting of a recombinant yeast cell growing on either soluble or insoluble substrates by virtue of extracytoplasmic enzymes either with or without tethering to the cell surface. Our results indicate that selection of faster-growing cells can be effective, arbitrarily defined as a faster-growing mutant representing 1% of the population in < or =3 months, but only under some conditions. For both soluble and insoluble substrates, tethering of enzymes to the cell surface is required for selection to be effective under the conditions examined. Significant increases in heterologous enzyme expression (2.5-fold for mutants as compared to the parent strain) are also required. In the soluble substrate/enzyme tethered case, the value of k(S) must also be low in order for selection to be effective. Cells growing on non-native substrates by virtue of extracytoplasmic enzyme production are expected to experience selective pressure in response to several additional factors, including cell shape, distance of the cell-substrate gap, properties of the gap, and perhaps mutation frequency. However, these factors exert a smaller impact on selection time and it is not clear that favorable values for these factors are required in order for selection to be effective.

Biotechnology↗
PubMed2005

Cellulose utilization by Clostridium thermocellum: bioenergetics and hydrolysis product assimilation.

The bioenergetics of cellulose utilization by Clostridium thermocellum was investigated. Cell yield and maintenance parameters, Y(X/ATP)True = 16.44 g cell/mol ATP and m = 3.27 mmol ATP/g cell per hour, were obtained from cellobiose-grown chemostats, and it was shown that one ATP is required per glucan transported. Experimentally determined values for G(ATP)P-T (ATP from phosphorolytic beta-glucan cleavage minus ATP for substrate transport, mol ATP/mol hexose) from chemostats fed beta-glucans with degree of polymerization (DP) 2-6 agreed well with the predicted value of (n-2)/n [corrected] (n = mean cellodextrin DP assimilated). A mean G(ATP)(P-T) value of 0.52 +/- 0.06 was calculated for cellulose-grown chemostat cultures, corresponding to n = 4.20 +/- 0.46. Determination of intracellular beta-glucan radioactivity resulting from 14C-labeled substrates showed that uptake is different for cellulose and cellobiose (G2). For 14C-cellobiose, radioactivity was greatest for G2; substantially smaller but measurable for G1, G3, and G4; undetectable for G5 and G6; and n was approximately 2. For 14C-cellulose, radioactivity was greatest for G5; lower but substantial for G6, G2, and G1; very low for G3 and G4; and n was approximately 4. These results indicate that: (i) C. thermocellum hydrolyzes cellulose by a different mode of action from the classical mechanism involving solubilization by cellobiohydrolase; (ii) bioenergetic benefits specific to growth on cellulose are realized, resulting from the efficiency of oligosaccharide uptake combined with intracellular phosphorolytic cleavage of beta-glucosidic bonds; and (iii) these benefits exceed the bioenergetic cost of cellulase synthesis, supporting the feasibility of anaerobic biotechnological processing of cellulosic biomass without added saccharolytic enzymes.

Adenosine Triphosphate↗
PubMed2005

Consolidated bioprocessing of cellulosic biomass: an update.

Biologically mediated processes seem promising for energy conversion, in particular for the conversion of lignocellulosic biomass into fuels. Although processes featuring a step dedicated to the production of cellulase enzymes have been the focus of most research efforts to date, consolidated bioprocessing (CBP)--featuring cellulase production, cellulose hydrolysis and fermentation in one step--is an alternative approach with outstanding potential. Progress in developing CBP-enabling microorganisms is being made through two strategies: engineering naturally occurring cellulolytic microorganisms to improve product-related properties, such as yield and titer, and engineering non-cellulolytic organisms that exhibit high product yields and titers to express a heterologous cellulase system enabling cellulose utilization. Recent studies of the fundamental principles of microbial cellulose utilization support the feasibility of CBP.

Animals↗
PubMed2005

Role of spontaneous current oscillations during high-efficiency electrotransformation of thermophilic anaerobes.

Current oscillations at about 24 MHz were observed during electrotransformation (ET) of the thermophilic anaerobes Clostridium thermocellum ATCC 27405, C. thermocellum DSM 1313, and Thermoanaerobacterium saccharolyticum YS 485, using a pulse gated by a square signal generated by a custom generator. In experiments in which only the field strength was varied, all three of these strains resulted in a one-to-one correspondence between the appearance of current oscillations and successful ET. Oscillations accompanied ET of both C. thermocellum strains only at field strengths of > or =12 kV/cm, and ET was only observed above the same threshold. Similarly, for T. saccharolyticum, oscillations were only observed at field strengths of > or =10 kV/cm, and ET was only observed above the same threshold. When a passive electrical filter consisting of an inductor and resistor in parallel was added to the system to prevent the development of oscillations, ET efficiencies were reduced dramatically for all three strains at all field strengths tested. The maximum tested field strength, 25 kV/cm, resulted in the maximum measured transformation efficiency for all three strains. At this field strength, the efficiency of ET in the absence of oscillations was decreased compared to that observed in the presence of oscillations by 500-fold for C. thermocellum ATCC 27405, 2,500-fold for C. thermocellum DSM 1313, and 280-fold for T. saccharolyticum. Controls using the same apparatus with Escherichia coli cells or a resistor with a value representative of the direct current resistance of typical cell samples did not develop oscillations, and ET efficiencies obtained with E. coli were the same with or without the electrical filter included in the pulse generator circuit. The results are interpreted to indicate that spontaneously arising oscillations have a large beneficial effect on transformation efficiency in the system employed here and that the development of oscillations in this system is affected by the cell species present.

Bacteria, Anaerobic↗
PubMed2005

Regulation of cellulase synthesis in batch and continuous cultures of Clostridium thermocellum.

Regulation of cell-specific cellulase synthesis (expressed in milligrams of cellulase per gram [dry weight] of cells) by Clostridium thermocellum was investigated using an enzyme-linked immunosorbent assay protocol based on antibody raised against a peptide sequence from the scaffoldin protein of the cellulosome (Zhang and Lynd, Anal. Chem. 75:219-227, 2003). The cellulase synthesis in Avicel-grown batch cultures was ninefold greater than that in cellobiose-grown batch cultures. In substrate-limited continuous cultures, however, the cellulase synthesis with Avicel-grown cultures was 1.3- to 2.4-fold greater than that in cellobiose-grown cultures, depending on the dilution rate. The differences between the cellulase yields observed during carbon-limited growth on cellulose and the cellulase yields observed during carbon-limited growth on cellobiose at the same dilution rate suggest that hydrolysis products other than cellobiose affect cellulase synthesis during growth on cellulose and/or that the presence of insoluble cellulose triggers an increase in cellulase synthesis. Continuous cellobiose-grown cultures maintained either at high dilution rates or with a high feed substrate concentration exhibited decreased cellulase synthesis; there was a large (sevenfold) decrease between 0 and 0.2 g of cellobiose per liter, and there was a much more gradual further decrease for cellobiose concentrations >0.2 g/liter. Several factors suggest that cellulase synthesis in C. thermocellum is regulated by catabolite repression. These factors include: (i) substantially higher cellulase yields observed during batch growth on Avicel than during batch growth on cellobiose, (ii) a strong negative correlation between the cellobiose concentration and the cellulase yield in continuous cultures with varied dilution rates at a constant feed substrate concentration and also with varied feed substrate concentrations at a constant dilution rate, and (iii) the presence of sequences corresponding to key elements of catabolite repression systems in the C. thermocellum genome.

Carbon↗
PubMed2004

Toward an aggregated understanding of enzymatic hydrolysis of cellulose: noncomplexed cellulase systems.

Information pertaining to enzymatic hydrolysis of cellulose by noncomplexed cellulase enzyme systems is reviewed with a particular emphasis on development of aggregated understanding incorporating substrate features in addition to concentration and multiple cellulase components. Topics considered include properties of cellulose, adsorption, cellulose hydrolysis, and quantitative models. A classification scheme is proposed for quantitative models for enzymatic hydrolysis of cellulose based on the number of solubilizing activities and substrate state variables included. We suggest that it is timely to revisit and reinvigorate functional modeling of cellulose hydrolysis, and that this would be highly beneficial if not necessary in order to bring to bear the large volume of information available on cellulase components on the primary applications that motivate interest in the subject.

Cellulase↗
PubMed2004

Electrotransformation of Clostridium thermocellum.

Electrotransformation of several strains of Clostridium thermocellum was achieved using plasmid pIKm1 with selection based on resistance to erythromycin and lincomycin. A custom-built pulse generator was used to apply a square 10-ms pulse to an electrotransformation cuvette consisting of a modified centrifuge tube. Transformation was verified by recovery of the shuttle plasmid pIKm1 from presumptive transformants of C. thermocellum with subsequent PCR specific to the mls gene on the plasmid, as well as by retransformation of Escherichia coli. Optimization carried out with strain DSM 1313 increased transformation efficiencies from <1 to (2.2 +/- 0.5) x 10(5) transformants per micro g of plasmid DNA. Factors conducive to achieving high transformation efficiencies included optimized periods of incubation both before and after electric pulse application, chilling during cell collection and washing, subculture in the presence of isoniacin prior to electric pulse application, a custom-built cuvette embedded in an ice block during pulse application, use of a high (25-kV/cm) field strength, and induction of the mls gene before plating the cells on selective medium. The protocol and preferred conditions developed for strain DSM 1313 resulted in transformation efficiencies of (5.0 +/- 1.8) x 10(4) transformants per micro g of plasmid DNA for strain ATCC 27405 and approximately 1 x 10(3) transformants per micro g of plasmid DNA for strains DSM 4150 and 7072. Cell viability under optimal conditions was approximately 50% of that of controls not exposed to an electrical pulse. Dam methylation had a beneficial but modest (7-fold for strain ATCC 27405; 40-fold for strain DSM 1313) effect on transformation efficiency. The effect of isoniacin was also strain specific. The results reported here provide for the first time a gene transfer method functional in C. thermocellum that is suitable for molecular manipulations involving either the introduction of genes associated with foreign gene products or knockout of native genes.

Anti-Bacterial Agents↗
PubMed2004

Kinetics and relative importance of phosphorolytic and hydrolytic cleavage of cellodextrins and cellobiose in cell extracts of Clostridium thermocellum.

Rates of phosphorolytic cleavage of beta-glucan substrates were determined for cell extracts from Clostridium thermocellum ATCC 27405 and were compared to rates of hydrolytic cleavage. Reactions with cellopentaose and cellobiose were evaluated for both cellulose (Avicel)- and cellobiose-grown cultures, with more limited data also obtained for cellotetraose. To measure the reaction rate in the chain-shortening direction at elevated temperatures, an assay protocol was developed featuring discrete sampling at 60 degrees C followed by subsequent analysis of reaction products (glucose and glucose-1-phosphate) at 35 degrees C. Calculated rates of phosphorolytic cleavage for cell extract from Avicel-grown cells exceeded rates of hydrolytic cleavage by > or = 20-fold for both cellobiose and cellopentaose over a 10-fold range of beta-glucan concentrations (0.5 to 5 mM) and for cellotetraose at a single concentration (2 mM). Rates of phosphorolytic cleavage of beta-glucosidic bonds measured in cell extracts were similar to rates observed in growing cultures. Comparisons of V(max) values indicated that cellobiose- and cellodextrin-phosphorylating activities are synthesized during growth on both cellobiose and Avicel but are subject to some degree of metabolic control. The apparent K(m) for phosphorolytic cleavage was lower for cellopentaose (mean value for Avicel- and cellobiose-grown cells, 0.61 mM) than for cellobiose (mean value, 3.3 mM).

Cellobiose↗
PubMed2004

Cloning and expression of the Clostridium thermocellum L-lactate dehydrogenase gene in Escherichia coli and enzyme characterization.

The structural gene for L-lactate dehydrogenase (LDH) (EC.1.1.1.27) from Clostridium thermocellum 27405 was cloned in Escherichia coli by screening the Lambda Zap II phage library of C. thermocellum genomic DNA. In one positive clone, an open reading frame of 948 base pairs corresponded to C. thermocellum ldh gene encoding for the predicted 315-residue protein. The ldh gene was successfully expressed in E. coli FMJ39 (ldh mutant) under the lac promoter. The recombinant enzyme was partially purified from E. coli cell extracts and its kinetic properties were determined. Clostridium thermocellum LDH was shown to catalyze a highly reversible reaction and to be an allosteric enzyme that is activated by fructose-1,6-diphosphate (FDP). For pyruvate, partially purified LDH had Km and Vmax values of 7.3 mmol/L and 87 micromol/min, respectively, and in the presence of FDP, a 24-fold decrease in Km and a 5.7-fold increase in Vmax were recorded. The enzyme exhibited no marked catalytic activity for lactate in the absence of FDP, whereas Km and Vmax values were 59.5 mmol/L and 52 micromol/min, respectively, in its presence. The enzyme did not lose activity when incubated at 65 degrees C for 5 min.

Amino Acid Sequence↗
PubMed2003

Cellodextrin preparation by mixed-acid hydrolysis and chromatographic separation.

A procedure for preparation of purified cellodextrins in gram quantities was developed for use in biochemical and microbiological studies. Cellodextrins were prepared by hydrolyzing microcrystalline cellulose (Avicel) over a period of 4 to 5.5h in the presence of a mixture of 80% (v/v) concentrated hydrochloric acid ( approximately 37 wt.%) and 20% (v/v) concentrated sulfuric acid ( approximately 98 wt.%) at room temperature (22 degrees C). Acetone precipitation, washing ion exchange, and neutralization with barium hydroxide were used to generate a solution of mixed cellodextrins substantially free of acids and salts. Yields following hydrolysis and precipitation were approximately 0.05, approximately 0.07, approximately 0.06, and approximately 0.02 g/g cellulose for cellotriose (G(3)), cellotetraose (G(4)), cellopentose (G(5)), and cellohexose (G(6)), respectively. Cellodextrins with degrees of polymerization from 3 to 11 were separated chromatographically using a 29 x 5-cm I.D. Bio-Rad AG50W-X4 column arranged in series with a 91 x 5-cm I.D. Bio-Gel P4 column. This two-column system was used to obtain cellodextrin preparations at 240 mg/day for G(3), 330 mg/day for G(4), 260 mg/day for G(5), and 130 mg/day for G(6), with purity >99% for G(3), G(4), and G(5) and >95% for G(6). The overall procedure achieves yields comparable to the highest previously reported, employs a separation system that can readily be reused for multiple runs, and avoids use of fuming HCl.

Acetone↗
PubMed2003

Conversion of paper sludge to ethanol in a semicontinuous solids-fed reactor.

Conversion of paper sludge to ethanol was investigated with the objective of operating under conditions approaching those expected of an industrial process. Major components of the bleached Kraft sludge studied were glucan (62 wt.%, dry basis), xylan (11.5%), and minerals (17%). Complete recovery of glucose during compositional analysis required two acid hydrolysis treatments rather than one. To avoid the difficulty of mixing unreacted paper sludge, a semicontinuous solids-fed laboratory bioreactor system was developed. The system featured feeding at 12-h intervals, a residence time of 4 days, and cellulase loading of 15 to 20 FPU/g cellulose. Sludge was converted to ethanol using simultaneous saccharification and fermentation (SSF) featuring a beta-glucosidase-supplemented commercial cellulase preparation and glucose fermentation by Saccharomyces cerevisiea. SSF was carried out for a period of 4 months in a first-generation system, resulting in an average ethanol concentration of 35 g/L. However, steady state was not achieved and operational difficulties were encountered. These difficulties were avoided in a retrofitted design that was operated for two 1-month runs, achieving steady state with good material balance closure. Run 1 with the retrofitted reactor produced 50 g/L ethanol at a cellulose conversion of 74%. Run 2 produced 42 g/L ethanol at a conversion of 92%. For run 2, the ethanol yield was 0.466 g ethanol/g glucose equivalent fermented and >94% of the xylan fed to the reactor was solubilized to a mixture of xylan oligomers and xylose.

Bioreactors↗