Induced expression of sarcotoxin IA enhanced host resistance against both bacterial and fungal pathogens in transgenic tobacco

We demonstrate here that induced expression of sarcotoxin IA, a bactericidal peptide from Sarcophaga peregrina, enhanced the resistance of transgenic tobacco plants to both bacterial and fungal pathogens. The peptide was produced with a modified PR1a promoter, which is further activated by salicylic acid treatment and necrotic lesion formation by pathogen infection. Host resistance to infection of bacteria Erwinia carotovora subsp. carotovora and Pseudomonas syringae pv. tabaci was shown to be dependent on the amounts of sarcotoxin IA expressed. Since we found antifungal activity of the peptide in vitro, transgenic seedlings were also inoculated with fungal pathogens Rhizoctonia solani and Pythium aphanidermatum. Transgenic plants expressing higher levels of sarcotoxin were able to withstand fungal infection and remained healthy even after 4 weeks, while control plants were dead by fungal infection after 2 weeks.     

Glutamate dehydrogenase from the aerobic hyperthermophilic archaeon Aeropyrum pernix K1: enzymatic characterization, identification of the encoding gene, and phylogenetic implications

NADP-dependent glutamate dehydrogenase (l-glutamate: NADP oxidoreductase, deaminating, EC 1.4.1.4) from the aerobic hyperthermophilic archaeon Aeropyrum pernix K1 (JCM 9820) was purified to homogeneity for characterization. The enzyme retained its full activity on heating at 95°C for 30 min, and the maximum activity in l-glutamate deamination was obtained around 100°C. The enzyme showed a strict specificity for l-glutamate and NADP on oxidative deamination and for 2-oxoglutarate and NADPH on reductive amination. The K _m values for NADP, l-glutamate, NADPH, 2-oxoglutarate, and ammonia were 0.039, 3.3, 0.022, 1.7, and 83 mM, respectively. On the basis of the N-terminal amino acid sequence, the encoding gene was identified in the A. pernix K1 genome, cloned, and expressed in Escherichia coli. Analysis of the nucleotide sequence revealed an open reading frame of 1257 bp starting with a minor TTG codon and encoding a protein of 418 amino acids with a molecular weight of 46 170. Phylogenetic analysis revealed that the glutamate dehydrogenase from A. pernix K1 clustered with those from aerobic Sulfolobus solfataricus, Sulfolobus shibatae, and anaerobic Pyrobaculum islandicum in Crenarchaeota, and it separated from another cluster of the enzyme from Thermococcales in Euryarchaeota. The branching pattern of the enzymes from A. pernix K1, S. solfataricus, S. shibatae, and Pb. islandicum in the phylogenetic tree coincided with that of 16S rDNAs obtained from the same organisms. Received: April 24, 2000 / Accepted: August 10, 2000     

Responses of immunocompetent cells in the dental pulp to replantation during the regeneration process in rat molars

Responses of immunocompetent cells to tooth replantation during the regeneration process of the dental pulp in rat molars were investigated by immunocytochemistry using antibodies to class II major histocompatibility complex (MHC) molecules (OX6 antibody), monocyte/macrophage lineage cells (ED1 antibody) and protein gene product 9.5 (PGP 9.5), as well as by histochemical reaction for periodic acid-Schiff (PAS). Tooth replantation caused an increase in both the number of OX6- and ED1-positive cells and their immunointensity in the replanted pulp, but almost all PGP 9.5-immunoreactive nerves diminished in the initial stages. By postoperative day 3, many OX6- and ED -immunopositive cells had accumulated along the pulp-dentin border to extend their cytoplasmic processes into the dentinal tubules in successful cases. Once reparative dentin formation had begun after postoperative day 7, OX6- and ED1-immmunopositive cells became scattered in the odontoblast layer, while reinnervation was found in the coronal pulp. The temporal appearance of these immunocompetent cells at the pulp-dentin border suggests their participation in odontoblast differentiation as well as in initial defense reactions during the pulpal regeneration process. On postoperative day 14, the replanted pulp showed three regeneration patterns: (1) reparative dentin, (2) bone-like tissue formation, and (3) an intermediate form between these. In all cases, PAS-reactive cells such as polymorphonuclear leukocytes (PML) and mesenchymal cells occurred in the pulp space. However, the prolonged stagnation of inflammatory cells was also discernible in the latter two cases. Thus, the findings on PAS reaction suggest that the migration of the dental follicle-derived cells into the pulp space and the subsequent total death of the proper pulpal cells are decisive factors for eliciting bone-like tissue formation in the replanted pulp.     

Nitric oxide nitrates tyrosine residues of tumor-suppressor p53 protein in MCF-7 cells

It has been reported that mammalian cells incubated with excess nitric oxide (NO) accumulate p53 protein but concomitantly this p53 loses its capacity for binding to its DNA consensus sequence. As nitration of tyrosine residues in various proteins has been shown to inhibit their functions, we examined whether NO nitrates tyrosine residues in p53 protein. MCF-7 cells expressing wild-type p53 were incubated with S-nitrosoglutathione for 4 h and cellular extracts were immunoprecipitated with an anti-p53 antibody. Western blot analyses of immunoprecipitates for p53 or for nitrotyrosine revealed low levels of nitrotyrosine in p53 from untreated cells. Incubation with 2 mM S-nitrosoglutathione induced a significant increase in the nitrotyrosine level in p53 protein compared to nontreated cells. These results suggest that excess NO produced in inflamed tissues could nitrate p53 protein, playing a role in carcinogenesis by impairing functions of this tumor-suppressor protein.     

Characteristics and Efficiency of Glutamine Production by Coupling of a Bacterial Glutamine Synthetase Reaction with the Alcoholic Fermentation System of Baker’s Yeast

Glutamine production with bacterial glutamine synthetase (GS) and the sugar-fermenting system of baker’s yeast for ATP regeneration was investigated by determining the product yield obtained with the energy source for ATP regeneration (i.e., glucose) for yeast fermentation. Fructose 1,6-bisphosphate was accumulated temporarily prior to the formation of glutamine in mixtures which consisted of dried yeast cells, GS, their substrate (glucose and glutamate and ammonia), inorganic phosphate, and cofactors. By an increase in the amounts of GS and inorganic phosphate, the amounts of glutamine formed increased to 19 to 54 g/liter, with a yield increase of 69 to 72% based on the energy source (glucose) for ATP regeneration. The analyses of sugar fermentation of the yeast in the glutamine-producing mixtures suggested that the apparent hydrolysis of ATP by a futile cycle(s) at the early stage of glycolysis in the yeast cells reduces the efficiency of ATP utilization. Inorganic phosphate inhibits phosphatase(s) and thus improves glutamine yield. However, the analyses of GS activity in the glutamine-producing mixtures suggested that the higher concentration of inorganic phosphate as well as the limited amount of ATP-ADP caused the low reactivity of GS in the glutamine-producing mixtures. A result suggestive of improved glutamine yield under the conditions with lower concentrations of inorganic phosphate was obtained by using a yeast mutant strain that had low assimilating ability for glycerol and ethanol. In the mutant, the activity of the enzymes involved in gluconeogenesis, especially fructose 1,6-bisphosphatase, was lower than that in the wild-type strain.     

Purification and Characterization of Exo-beta-d-Glucosaminidase from a Cellulolytic Fungus, Trichoderma reesei PC-3-7

Chitosan-degrading activities induced by glucosamine (GlcN) or N-acetylglucosamine (GlcNAc) were found in a culture filtrate of Trichoderma reesei PC-3-7. One of the chitosan-degrading enzymes was purified to homogeneity by precipitation with ammonium sulfate followed by anion-exchange and hydrophobic-interaction chromatographies. The enzyme was monomeric, and its molecular mass was 93 kDa. The optimum pH and temperature of the enzyme were 4.0 and 50 degrees C, respectively. The activity was stable in the pH range 6.0 to 9.0 and at a temperature below 50 degrees C. Reaction product analysis from the viscosimetric assay and thin-layer chromatography and H nuclear magnetic resonance spectroscopy clearly indicated that the enzyme was an exo-type chitosanase, exo-beta-d-glucosaminidase, that releases GlcN from the nonreducing end of the chitosan chain. H nuclear magnetic resonance spectroscopy also showed that the exo-beta-d-glucosaminidase produced a beta-form of GlcN, demonstrating that the enzyme is a retaining glycanase. Time-dependent liberation of the reducing sugar from partially acetylated chitosan with exo-beta-d-glucosaminidase and the partially purified exo-beta-d-N-acetylglucosaminidase from T. reesei PC-3-7 suggested that the exo-beta-d-glucosaminidase cleaves the glycosidic link of either GlcN-beta(1-->4)-GlcN or GlcN-beta(1-->4)-GlcNAc.     

Characteristics and Efficiency of Glutamine Production by Coupling of a Bacterial Glutamine Synthetase Reaction with the Alcoholic Fermentation System of Baker’s Yeast

Glutamine production with bacterial glutamine synthetase (GS) and the sugar-fermenting system of baker’s yeast for ATP regeneration was investigated by determining the product yield obtained with the energy source for ATP regeneration (i.e., glucose) for yeast fermentation. Fructose 1,6-bisphosphate was accumulated temporarily prior to the formation of glutamine in mixtures which consisted of dried yeast cells, GS, their substrate (glucose and glutamate and ammonia), inorganic phosphate, and cofactors. By an increase in the amounts of GS and inorganic phosphate, the amounts of glutamine formed increased to 19 to 54 g/liter, with a yield increase of 69 to 72% based on the energy source (glucose) for ATP regeneration. The analyses of sugar fermentation of the yeast in the glutamine-producing mixtures suggested that the apparent hydrolysis of ATP by a futile cycle(s) at the early stage of glycolysis in the yeast cells reduces the efficiency of ATP utilization. Inorganic phosphate inhibits phosphatase(s) and thus improves glutamine yield. However, the analyses of GS activity in the glutamine-producing mixtures suggested that the higher concentration of inorganic phosphate as well as the limited amount of ATP-ADP caused the low reactivity of GS in the glutamine-producing mixtures. A result suggestive of improved glutamine yield under the conditions with lower concentrations of inorganic phosphate was obtained by using a yeast mutant strain that had low assimilating ability for glycerol and ethanol. In the mutant, the activity of the enzymes involved in gluconeogenesis, especially fructose 1,6-bisphosphatase, was lower than that in the wild-type strain.Glutamine is one of the most important compounds in nitrogen metabolism; it is not only a constituent of proteins but is also a donor of the amino (amido) moiety in the biosynthesis of other amino acids, purines, pyrimidines, pyridine coenzymes, and complex carbohydrates. Glutamine is also used in the treatment of gastric ulcers and has been produced commercially by direct fermentation with certain bacteria (6–10).In recent years, enzymatic synthesis has come to rival direct fermentation as a means of producing amino acids. In the case of glutamine, however, the need for a stoichiometric supply of ATP for the endoergonic reaction of glutamine synthetase (GS) precludes the development of an economically valuable method, unless ATP can be regenerated and recycled.Processes for the production of various substances using dried yeast cells as an enzyme source were established by Tochikura and colleagues (2, 4, 16, 18–20). The processes are driven by the chemical energy of ATP released by the alcoholic fermentation by the yeast, which has been wasted in alcoholic brewing (17). Tochikura and colleagues also designed a process in which the yeast fermentation of sugar is combined with an endoergonic reaction catalyzed by an enzyme from a different microorganism (3). The results suggest that the process offers the possibility of producing many compounds at a high yield by using various biosynthetic reactions and high concentrations of substrates. Tochikura et al. introduced the general idea of coupled fermentation with energy transfer for the process; its principle is indicated in Fig. ​Fig.1,1, with glutamine production as an example. Open in a separate windowFIG. 1Scheme of glutamine production by the coupled fermentation with energy transfer method. ∗1, glycolytic pathway is abridged. ∗2, inorganic phosphate (P_i) is recycled.In the process of coupled fermentation with energy transfer, a catalytic amount of ATP is regenerated with the energy of sugar fermented by yeast, in the form of baker’s yeast (4, 16, 18, 19, 23). The energy-utilizing system for the synthesis can involve the enzyme(s) of yeast itself or those of other organisms. It should be noted that, from another point of view, the use of the energy-utilizing system results in ADP regeneration to complete the fermentation of glucose, and that, if there is no ADP regeneration, the yeast fermentation of sugar can proceed only as follows, in the presence of inorganic phosphate (the Harden-Young effect of inorganic phosphate [1]), 2 · glucose + 2 · inorganic phosphate → fructose 1,6-bisphosphate (FBP) + 2 · C₂H₅OH + 2 · CO₂ (Harden-Young equation), where ADP regeneration for the fermentation of 1 mol of glucose is carried out by the phosphorylation of another mole of glucose to FBP.We previously reported glutamine production, obtained by employing a combination of baker’s yeast cells and GS from Gluconobacter suboxydans, as the first application of the coupled fermentation with energy transfer method for the production of a nonphosphorylated compound (12, 13). In addition, we achieved high-yield glutamine production by using the Corynebacterium glutamicum (Micrococcus glutamicus) enzyme and larger amounts of the substrates (15). The maximum amounts of glutamine formed (23 to 25 g/liter) and the yield based on glutamate (50 to 100%) were to some extent satisfactory, but the yield based on the energy source (glucose) for ATP regeneration was not satisfactory (about 40% of the theoretical value; 2 mol of glutamine can be formed when 1 mol of glucose is consumed).In the present study, we examined the characteristics of glutamine production regarding product yield based on the energy source for ATP regeneration and regarding the reactivity of GS during glutamine production, which is closely related to the product yield. The results of preliminary attempts to improve glutamine production are also described. In these experiments, a yeast mutant which has a low assimilating ability for glycerol and/or ethanol was used.