Characterization of two peptide epitopes on Mdm2 oncoprotein that affect p53 degradation

Phosphorylation of Mdm2, in response to DNA damage, resulted in prevention of p53 degradation in the cytoplasm as well as reduction of its binding with monoclonal antibody (mAb) 2A10. Using a 15-mer phage-peptide library, we identified two 2A10-epitopes on human Mdm2 (hdm2): at positions 255-266 (LDSEDYSLSEEG) and 389-400 (QESDDYSQPSTS). Synthetic peptides corresponding to the above sites, inhibit the binding of mAb2A10 to Mdm2 with high (4.5 x 10(-9)M) and moderate affinity (1.1 x 10(-7)M), respectively. Phospho-derivatives of these peptides, and of single human Mdm2 mutations S260D or S395D resulted in a considerable reduction in their binding with mAb2A10. These results provide a molecular explanation for the observation that reactivity of Mdm2 with mAb2A10 is inhibited by phosphorylation.     

Continuous ethanol production by immobilized yeast reactor coupled with membrane pervaporation unit

A system comprised of an immobilized yeast reactor producing ethanol, with a membrane pervaporation module for continuously removing and concentrating the produced ethanol, was developed. The combined system consisted of two integrated circulation loops: In one the sugar-containing medium is circulated through the membrane pervaporation module. The two loops were interconnected in a way allowing for separate parameter optimization (e.g., flow rate, temperature, pH) for each loop.The fermentation unit was 2.0 L bioreactor with five equal segments, packed with 5-mm beads of immobilized yeasts. The bead matrix was a crosslinked polyacrylamide hydrazide gel coated with calcium alginate. The fast circulation loop of the bioreactor allowed for efficient liberation of CO(2) at the top of the immobilized yeast reactor. Continuous operation of the uncoupled reactor for over 50 days with inflowing defined medium or dilute molasses at a residence time of 1.25 h yielded ethanol at a rate of about 10 g/L h.The pervaporation unit was constructed from four 60-cm-long tubular membranes of silicone composite on a polysulfone support. The output from the fermentor was circulated through the inside of the tubes of a unit with a total surface area of 800 cm(2), having an average flux of 150 mL/h, and selectivities to ethanol vs. water up to 7. A vacuum of 30 mb was applied to the outside of the tubes, removing 20-30 g of ethanol per hour, which was collected in condensors. The continuous removal of ethanol, avoiding inhibition of the fermentation process, resulted in an improved productivity and allowed the use of high sugar concentrations (40% wt/vol) offering the potential of a compact system with reduced stillage.The combined system of ethanol production and removal enabled an operative steady state at which the liquid volume of the system, and the concentrations of ethanol within the reactor ( 4% wt/vol), as well as within the flux crossing the pervaporation membrane (17%-20% wt/vol) were kept constant. At the steady state, a 40% wt/vol sugar solution could be continuously added to the fermentor when 12%-20% wt/vol clear ethanol solution was continuously removed by the pervaporation unit. Membrane fouling was reversed by short washing steps, and continuous step operation was maintained by working with two different modules that were interchanged. In this manner, long term continuous operation (over 40 days) was achieved with a productivity of 20-30 g/L h, representing over a twofold increase relative to the continuously operated reactor uncoupled from the membrane and a fivefold increase in comparison with the value obtained fro a corresponding batch fermentation.     

Poly(L-histidyl-L-alanyl-α-L-glutamic acid). I. Synthesis

Poly(L -histidyl-L -alanyl-α-L -glutamic acid) has been prepared in order to test the acid–base catalytic ability of a carboxyl-imidazole hydrogen-bonded system. Two different blocked histidyl-alanyl-glutamic acid monomers were used in the polymerization step. The imidazole ring was blocked with either a dinitrophenyl or a t-butyloxycarbonyl group. The γ-carboxyl of glutamic acid was protected as the benzyl ester. Both the coupling reactions and the polymerization step were via the N-hydroxysuccinimide active ester method. Thiolysis removed the dinitrophenyl group, while hydrogen bromide removed the t-butyloxycarbonyl and the benzyl groups. The water-soluble unblocked polymers obtained were fractionated on Sephadex G-50 or Bio-Gel P30. Fractions within a range of average molecular weights of 2,000 to 25,000 were isolated. Enzymatic oxidation of the acid hydrolyzate of the polymers revealed that no detectable racemization had occurred.     

Enzyme diffusion and action on soluble and insoluble substrate biopolymers

The action of enzymes on soluble and insoluble substrate biopolymers is discussed, taking into account enzyme diffusion along the biopolymer “surface” and interaction with interspersed ligand groups that may be modified by the action of the enzyme. It is shown that movement of the enzyme under trhe combined effect of these two processes can be described as a diffusion process characterized by an apparent diffusion coefficient that generally depends on both time and position. Equations describing the system are formulated and some specific examples analyzed in terms of analytical or numerical solutions. The concentration distributions of both the enzyme and the substrate (or product ) were obtained for different systems for which the apparent diffusion coefficient is a function of time only, as well as of both time and position. The relevance of the formulation, as developed, to systems in which reduction in dimensionality leads to enhanced enzyme efficiency is discussed, and possible uses of the theory in studies of biopolymer structure and enzyme-biopolymer interactions are suggested.     

Partition of free and monoclonal-antibody-bound horseradish peroxidase in a two-phase aqueous polymer system--novel procedure for the determination of the apparent binding constant of monoclonal antibody to horseradish peroxidase.

The principle that the antigen and the antibody prefer different phases in an aqueous two-phase system is the analytical basis of the work presented here. The antigen horseradish peroxidase, which is bound to a monoclonal antibody (mAb), is separated from free Ag in an aqueous phase system (polyethylene glycol (PEG)/dextran) as a function of the concentration of mAb. The plot of the partition coefficient kappa of horseradish peroxidase versus the concentration of mAb yields a sigmoidal curve similar to the curve obtained by enzyme-linked immunosorbent assay (ELISA). Comparing the plots normally used for ELISA in order to determine the apparent binding constant of mAb and the number of epitopes on the Ag we derived a relationship between the difference in partitioning of the free Ag and the bound Ag (delta kappa) and the concentration of mAb. The new linear plot of reciprocal delta kappa versus reciprocal concentration of mAb gives the apparent binding constant of mAb, which is evaluated from the slope. From the intercept at the ordinate the maximum difference of the partition coefficient of the free and bound antigen is derived and the apparent partition coefficient of the free monoclonal antibody can be calculated.     

Purification and characterization of Aspergillus niger exo-1,4-glucosidase.

A specific exo-1,4-glucosidase (1,4-alpha-D-glucan glucohydrooase, EC 3.2.1.3) from Aspergillus niger has been partially purified and subsequently characterized by biochemical, physico-chemical and optical methods. Molecular sieve chromatography yields an enzyme with maximal activity at pH 4.2-4.5 close to its isoelectric point. Reduction and carboxymethylation leads to complete loss of activity and O-acetylation of 3 of the 13 tyrosine residues results in loss of 20 % of the activity. Sodium dodecylsulfate-polyacrylamide gel electrophoresis indicates that the native enzyme consists of two major components of molecular weights 63 000 and 57 500, respectively. Small amounts of dissociated material of molecular weight 28 000 and 16 000 as well as aggregates of the order of 100 000 are also present to the extent of 2-5% of the total potein. Following reduction and carboxymethylation under forcing conditions, the bands around 60 000 diminish and the 28 000-30 000, 16 000 and aggregate bands are dominant...     

Geometric Recognition as a Tool for Predicting Structures of Molecular Complexes

Summary The structures of two binary complexes (the TEM-1/BLIP complex and the trypsin/amiloride complex) were predicted prior to their experimental determination and compared to the corresponding experimental structures when these became available. In both predictions the rigid-body geometric docking algorithm ranked the correct solution among the top ones. Additional information concerning the structure and chemical character of the binding site of one of the molecules in the complex was used to single out the correct solution. The results indicate that the combination of geometric surface matching with biochemical information produces a useful tool for structure prediction.