On the use of enzyme adsorption and specific hydrolysis rate to characterize thermal-chemical pretreatment

Applied Biochemistry and Biotechnology - The pseudo enzyme adsorption isotherm of the pretreated substrate is used to estimate the pretreatment’s effectiveness in generating accessible...     

Kinetics of thermochemical pretreatment of lignocellulosic materials

The results of an experimental study of the acid hydrolysis of hardwood are presented in the form of values for the three parameters, activation energy, power on the acid concentration, and pre-exponen-tial factor, of the first order kinetic constants for each of the following reaction participants: xylan remaining, glucan remaining, xylose formed, and xylose decomposed. These are used as a base for a quantitative theory to predict the temperature, time, and acid concentrations needed for effective pretreatment of the substrate for subsequent enzymatic hydrolysis of the glucan. This theory is based on the assumption that successful pretreatment requires >90% removal of the xylan, <10% removal of the glucan, and >80% xylose yield. This theory is compared with selected published data.     

Renewable energy in the United States

A review of studies of biomass potential in the United States finds a wide variation in the estimates. A number of specific policy-relevant questions about the potential of biofuels in the United States are answered. A recently published global analysis of the potential conflict between land needed for bioenergy and land needed for food is extended to the situation in the United States. A renewable energy supply scenario, capable of meeting the 2001 US energy demand, indicates that there is enough land to support a renewable energy system but that the utilization of biomass would be limited by its land requirement.     

Surface area of pretreated lignocellulosics as a function of the extent of enzymatic hydrolysis

Partially purified S1 nuclease was bound through its carbohydrate moiety to Con A-Sepharose containing increasing amounts of lectin. The retention of activity was high, varying essentially from 75% on the "low lectin" matrix (1 mg Con A/mL of Sepharose), to no detectable activity on the "high lectin" matrix (8 mg Con A/mL of Sepharose). However, approximately 50% activity could be restored in "high lectin" matrix when the coupling was carried out in the presence of glucose, suggesting that the loss of activity on the "high lectin" matrix is caused by conformational changes brought about by the multiple attachment of the enzyme to the matrix. Interaction of Con A with S1 nuclease was used to predict the nature of carbohydrate moiety and its location with respect to the active site of the enzyme. Immobilization resulted in an increase in the optimum temperature, pH, and temperature stabilities, but it did not affect the pH optimum. A marginal increase in the apparent Km was observed. The bound enzyme also showed enhanced stability toward 8 M urea. On repeated use, the bound enzyme retained more than 80% of its initial activity after 6 cycles. These results are discussed taking into consideration the factors affecting immobilized enzymes. In addition, the potential use of immobilized S1 nuclease as an analytical tool is discussed.     

An extension of the Harano-Ooshima rate expression for enzymatic hydrolysis of cellulose to account for changes in the amount of adsorbed cellulase

Three empirical rate expressions, Kinetics I, II, and III, for the enzymatic hydrolysis of cellulose were evaluated in an effort to develop a easy-to-use rate expression. They are based on the following equation:-dV/dX = kV, where V and X are the hydrolysis rate and the fractional conversion. In Kinetic I,k is constant. In Kinetic II, a linear relatinship betweenk and t is assumed. In Kinetic III, an exponential relationship is assumed. The three expressions were applied to enzymatic hydrolysis carried out under seven different conditions in which the kinds of substrates, enzymes, and initial concentrations were varied. All of the examined rate expressions were applied to the hydrolysis with success, but the better accuracies were obtained by Kinetic III, Kinetic II, and Kinetic I in this order. The variations ofk with time found in this study, especially the exponential relationship, were consistent with the effect of the measured changes in the concentration of adsorbed enzyme as predicted by theory developed previously by Ooshima et al. (1).     

Assessing environmental chemical uptake in fetal brain in utero: A preliminary PET/CT study

Summary Exposure to several environmental chemicals in utero is associated with subtle deleterious effects in cognitive, motor and behavioral functions. In order to assess in utero exposure to possible neurotoxins, fetal brain uptake of an exogenous compound given to a pregnant rhesus macaque was investigated using PET/CT imaging. CT clearly delineated the fetus which allowed the time course of the PET tracer in the fetal brain and other organs to be monitored. This study demonstrates the feasibility of quantifying the absolute fetal uptake of chemicals given systemically to the mother.     

Symmetric matrices with given row sums

We identify the extreme points of the set of matrices (a_ij) with a_ij ? 0, a_ij = a_ji and ∑_ja_ij = r_i under the condition that ∑r_i is finite. We also give an example to show that the condition that ∑r_i is finite is essential.     

The effect of enzyme and substrate levels on the specific hydrolysis rate of pretreated poplar wood

Applied Biochemistry and Biotechnology - The hydrolysis of pretreated poplar wood was carried out with initial concentrations of 1.26, 2.52, 5.04 mg proteinJmL of GC123Trichoderma reesei. cellulase...     

Kinetics of enzymatic hydrolysis of lignocellulosic materials based on surface area of cellulose accessible to enzyme and enzyme adsorption on lignin and cellulose

Comparison of the model with experimental data is currently in progress. It appears that more detailed studies of the adsorption dynamics, not just adsorption equilibrium, are needed.     

Introduction to Session 1

Applied Biochemistry and Biotechnology -