Nucleotide sequence of the promoter--operator region of the tryptophan operon of Escherichia coli.
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Biomedical subjects
Publications and source records attributed to G N Bennett.
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A new procedure for the synthesis of the pyrophosphate bond has been employed in the preparation of nucleoside dipyrophosphates from nucleoside 3',5'-diphosphates. The method makes use of a powerful phosphorylating agent generated in a mixture of cyanoethyl phosphate, dicyclohexylcarbodiimide, and mesitylenesulfonyl chloride in order to avoid possible intramolecular reactions between the two phosphate groups on the sugar ring. That such reactions can readily occur was shown by the facile cyclization of deoxyguanosine 3',5'-diphosphate to P1,P2-deoxyguanosine 3',5'-cyclic pyrophosphate in the presence of dicyclohexylcarbodiimide alone. The phosphorylation reagent was initially tested in the conversion of deoxyguanosine 3',5'-diphosphate to the corresponding 3',5'-dipyrophosphate and was then used to phosphorylate 2'-O-(alpha-methoxyethyl)guanosine 3',5'-diphosphate, which had been prepared from 2'-O-(alpha-methoxyethyl)guanosine. In the latter case, the addition of the two beta phosphate groups was accomplished in 40% yield. Removal of the methoxyethyl group from the phosphorylated product gave guanosine 3',5'-dipyrophosphate, which was shown to be identical with guanosine tetraphosphate prepared enzymatically from a mixture of GDP and ATP. A modification of published procedures was also necessary to effect the synthesis of guanosine bis(methylenediphosphonate). Guanosine was treated with methylenediphosphonic acid and dicyclohexylcarbodiimide in the absence of added base. The product consisted of a mixture of guanosine 2',5' - and 3',5'-bis(methylenediphosphonate), which was resolved by anion-exchange chromatography. The 2',5' and 3',5' isomers are interconvertible at low pH, with the ultimate formation of an equilibrium mixture having a composition ratio of 2:3. The predominant constituent of this mixture has been unequivocally identified as the 3',5' isomer by synthesis from 2'-O-tetrahydropyranylguanosine.
The nucleotide sequence of the region preceding the transcription initiation site of the tryptophan operon of Escherichia coli was determined. Essentially all of the trp operator precedes the transcribed portion of the operon. The deduced sequence contains the recognition site of endonuclease Hpa I. This site is protected from Hpa I cleavage by RNA polymerase and by trp repressor. Regions of 2-fold symmetry are present in the DNA sequence.
A number of synthetic methods for the preparation of the 2-O-(alpha-methoxyethyl) derivatives of the 5-diphosphates of adenosine, cytidine, guanosine, and uridine have been studied in order to provide nucleotide substrates that can be applied to the synthesis of specific oligoribonucleotides using polynucleotide phosphorylase. The reaction of nucleoside 5-diphosphates with methyl vinyl ether for a limited time produces low yields of the corresponding 2-O-(alpha-methoxyethyl) derivatives because the rate of methoxyethylation of the 3-hydroxyl groups. A study of the rates of acidic hydrolysis of alpha-methoxyethyl groups in the 2 and 3 positions of nucleosides and nucleotides has been made, and the results obtained form the basis of a more efficient method for the synthesis of the blocked nucleoside diphosphates. The method involves the reaction of nucleoside 5-diphosphates with methyl vinyl ether to give the corresponding 2,3-di-O-(alpha-methoxyethyl)nucleoside 5-diphosphates, and exploits the fact that, in the acidic hydrolysis of these derivatives, the rate of removal of the 3-methoxyethyl group is about twice that of the group in the 2 position. Alternative syntheses were based on the phosphorylation of methoxyethylated nucleosides and nucleotides. The derivatives, 2-O- and 2,3-di-O-(alpha-methoxyethyl)uridine, were prepared by the methoxyethylation of 3,5-di-O-acetyluridine and 5-O-acetyluridine followed by removal of the acetyl groups. The corresponding guanosine derivatives were made by the synthetic routes: (i) guanosine leads to O-2,O-3,O-5,N-2-tetrabenzoylguanosine leads to 2-N-benzoylguanosine leads to O3-acetyl-N-2,O5-dibenzoylguanosine leads to 2-O-(alpha-methoxyethyl)guanosine, and (ii) 2,3-O-isopropylideneguanosine leads to N-2,O5-diacetyl-2,3-O-isopropylideneguanosine leads to N-2,O-5-diacetylguanosine leads to 2,3-di-O-(alpha-methoxyethyl)guanosine. These methoxyethylated nucleosides were converted to the corresponding 5-phosphates by reaction with cyanoethyl phosphate and dicyclohexylcarbodiimide, and then to the corresponding 5-diphosphates by subsequent reaction with 1,1-carbonyldiimidazole and inorganic phosphate.
The reaction of the tetranucleotide, pA-A(2)-A, with 2'(3')-0-(alpha-methoxyethyl)uridine 5'-diphosphate, Mg(2+) ions, and M. luteus polynucleotide phosphorylase followed by mild acid treatment to remove the blocking groups results in a 49% yield of the desired single addition product, pA-A(3)-U, together with smaller amounts of pA-A-U, pA-A-A, pA-A(2)-U, pA-A(2)-A, pA-A(3)-A, pA-A(4)-U, and pA-A(4)-A. The side products are thought to arise from the phosphorolysis of the acceptor molecule by the inorganic phosphate formed in the reaction mixture and from subsequent additions to the various oligonucleotide species by the resulting adenosine 5'-diphosphate. A system developed for the removal of inorganic phosphate as it is formed in the synthesis involves the addition to the reaction mixture of calf spleen nucleoside phosphorylase and nicotinamide riboside and, under these conditions, pA-A(3)-U can be prepared in 90% yield with essentially no side products. Under similar conditions, pA-A(3)-A, pA-A(3)-G, and pA-A(3)-C may be prepared from pA-A(2)-A and the appropriate blocked nucleoside diphosphate in yields of 85-94%. The incubation of pA-A(2)-A alone with polynucleotide phosphorylase exhibits the phenomenon of "transnucleotidation" in that the molecule is partially converted to oligonucleotides of smaller and larger chain lengths. In the presence of the phosphate removal system, however, the tetranucleotide is not attacked by the enzyme, and thus, "transnucleotidation" appears to be simply a combination of phosphorolytic and addition reactions catalyzed by trace amounts of inorganic phosphate contaminating the enzyme and/or the substrate.
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Methyl alpha-glucoside (alpha-MG) is a metabolically inert glucose analog sharing the same phosphotransferase system with glucose. The potential of using this compound, which acts as a nontoxic competitive inhibitor, to modulate glucose uptake and subsequently reduce the acetate accumulation rate was investigated. In a complex medium, no significant effect on the growth rate was observed when the alpha-MG to glucose ratio was low. The effect of alpha-MG supplementation on the production of a model recombinant protein, CadA-beta-galactosidase, under the regulation of a pH-inducible promoter in a batch culture was also examined. It was observed that the amount of acetate accumulation was drastically reduced in the presence of alpha-MG. More importantly, recombinant protein productivity was significantly improved. A very high volumetric productivity of approximately 1.6 g/L recombinant protein in a dense culture with an OD600 of 35 was obtained in a simple batch fermentation. Even at this high cell density, the specific protein productivity was maintained at a high level and was estimated to account for about 40% of the total cellular protein.
Genetic and metabolic engineering provide powerful and effective tools for the systematic manipulation and fine tuning of cellular metabolic activities. In this study, successful application of such techniques to enhance recombinant protein production by reducing acetate accumulation in Escherichia coli is presented. The alsS gene from Bacillus subtilis encoding the enzyme acetolactate synthase was introduced into E. coli cells using a multicopy plasmid. This newly introduced heterologous enzyme modifies the glycolytic fluxes by redirecting excess pyruvate away from acetate to acetolactate. Acetolactate is then converted to a nonacidic and less harmful byproduct acetoin, which appears in the broth. Furthermore, comparative fermentation studies show that the reduction in acetate accumulation leads to a significant improvement of recombinant protein production. The expression of a model recombinant CadA/beta-galactosidase fusion protein, under the control of a strong pH-regulated promoter, was found to increase by about 60% for the specific protein activity (to a level of 30% of total cellular protein) and 50% in terms of the volumetric activity in a batch fermenter. In fed-batch cultivation, the engineered strain achieved a volumetric recombinant protein yield of 1.6 million units/mL (about 1.1 g/L of beta-galactosidase), which represented a 220% enhancement over the control strain. In the meantime, acetate excretion was maintained below 20 mM compared with 80 mM for the control, and the final cell density was improved by 35%.
The feasibility of substituting glucose with fructose as a carbon source in Escherichia coli fermentations was investigated. Glucose, the most commonly used sugar in bacterial cultivations, is well-known to pose a number of drawbacks; the most important of which is the Crabtree effect, which results in acidogenesis. Fructose, a glucose structural isomer, offers a reasonable alternative for glucose, since its uptake and utilization are more tightly regulated. Comparative fermentation studies indicate that lower acetate excretion and higher biomass yields were attained in fructose-supplemented growth media compared with those of glucose media. More specifically, cells grown in defined media supplemented with fructose do not excrete detectable amounts of acetate, while about 40 mM of acetate was detected extracellularly in similar glucose cultures. A reduction in the initial growth rate of about 20% was observed with fructose, but final cell densities were about 70% higher compared with glucose supplements. Growth in complex LB media supplemented with fructose again resulted in higher biomass yields (up to 40%) and lower acetate excretion (30-40%) than the comparable glucose media. In bioreactor studies using LB media, acetate levels were reduced from 90 to less than 6 mM, while achieving a 25% improvement in biomass yield. When using richer media, cell densities of more than 40 g L-1 dry cell weight were attained in batch cultivation using fructose compared with 30 g L-1 for glucose. These results have immense applicability in the area of recombinant protein processes. Recombinant E. coli, overexpressing beta-galactosidase under the control of the strong pH-inducible promoter, achieved a volumetric recombinant protein yield of 2.2 million U mL-1 (corresponding to approximately 1.5 g L-1) in batch fructose cultures. This represents a 65% recombinant protein yield enhancement when compared to similar glucose cultivations.