Effects of cultivation conditions on the production of natamycin with Streptomyces gilvosporeus LK-196

Natamycin is a very attractive antifungal agent with wide applications in medical and food industries. In order to improve the productivity of natamycin, the effects of cultivation conditions were investigated with Streptomyces gilvosporeus LK-196 in the shake flasks and 30-L fermentors. The results showed that dissolved oxygen and shear force would affluence the biosynthesis of natamycin significantly. The high concentration of natamycin (2.03g/L) was achieved under the suitable culture conditions in the shake flask scale. Further investigations in 30-L fermentors showed that the optimal pH was controlled at 6.0 during the whole bioprocess, and the dissolved oxygen level should be more than 30% by adjusting the aeration and agitation rates for high production of natamycin. Under these optimal conditions the high concentration of natamycin (3.94g/L) was achieved with Str. gilvosporeus LK-196 in the 30-L fermentor. Finally, the high-level fermentation process was successfully scaled up to 1000-L fermentors and 18,000-L fermentors in the pilot plant.     

Domain movement of iron sulfur protein in cytochrome bc1 complex is facilitated by the electron transfer from cytochrome b(L) to b(H)

The key step of the "protonmotive Q-cycle" mechanism for cytochrome bc1 complex is the bifurcated oxidation of ubiquinol at the Qp site. ISP is reduced when its head domain is at the b-position and subsequent move to the c1 position, to reduce cytochrome c1, upon protein conformational changes caused by the electron transfer from cytochrome b(L) to b(H). Results of analyses of the inhibitory efficacy and the binding affinity, determined by isothermal titration calorimetry, of Pm and Pf, on different redox states of cytochrome bc1 complexes, confirm this speculation. Pm inhibitor has a higher affinity and better efficacy with the cytochrome b(H) reduced complex and Pf binds better and has a higher efficacy with the ISP reduced complex.     

Domain conformational switch of the iron-sulfur protein in cytochrome bc1 complex is induced by the electron transfer from cytochrome bL to bH

Intensive biochemical, biophysical and structural studies of the cytochrome (cyt) bc(1) complex in the past have led to the formulation of the "protonmotive Q-cycle" mechanism for electron and proton transfer in this vitally important complex. The key step of this mechanism is the separation of electrons during the oxidation of a substrate quinol at the Q(P) site with both electrons transferred simultaneously to ISP and cyt b(L) when the extrinsic domain of ISP (ISP-ED) is located at the b-position. Pre-steady state fast kinetic analysis of bc(1) demonstrates that the reduced ISP-ED moves to the c(1)-position to reduce cyt c(1) only after the reduced cyt b(L) is oxidized by cyt b(H). However, the question of how the conformational switch of ISP-ED is initiated remains unanswered. The results obtained from analysis of inhibitory efficacy and binding affinity of two types of Q(P) site inhibitors, Pm and Pf, under various redox states of the bc(1) complex, suggest that the electron transfer from heme b(L) to b(H) is the driving force for the releasing of the reduced ISP-ED from the b-position to c(1)-position to reduce cyt c(1).     

Enhancement of 5-aminolevulinate production with recombinant Escherichia coli using batch and fed-batch culture system

5-Aminolevulinate (ALA) production with recombinant Escherichia coli Rosetta (DE3)/pET28a(+)-hemA was studied. In batch fermentation, the addition of glucose and glycine was effective to improve ALA production. Then the fed-batch fermentation was conducted with continuous feeding of precursors. When the concentrations of succinic acid and glycine were 7.0 g/l and 4.0 g/l, respectively, in the feeding, the ALA yield reached 4.1g/l. But the molar yield (ALA/glycine) was decreased in the fed-batch fermentation compared to batch fermentation. And it was found that the pH control during fed-batch cultivation was very important for the cell growth and ALA production. A two-stage pH value controlling strategy was suggested, in which, the pH value in the first 6h was regulated at pH 5.9, after then at pH 6.2, and the ALA yield was as high as 6.6g/l via fed-batch fermentation.     

Mycobacterium avium Subspecies Paratuberculosis in the Inflamed Gut Tissues of Patients with Crohn’s Disease in China and its Potential Relationship to the Consumption of Cow’s Milk: A Preliminary Study

Summary Mycobacterium avium subspecies paratuberculosis infection in domestic livestock is widespread in many countries throughout the world. Studies in Europe and the USA show that M. avium subspecies paratuberculosis can be cultured from retail pasteurized cow’s milk and that these organisms are being transmitted to humans by this route. Most people with chronic inflammation of the intestine of the Crohn’s disease type are infected with these chronic enteric pathogens. The production and consumption of cow’s milk has increased in China and so also has the incidence of Crohn’s disease. The present preliminary investigation was carried out to determine whether M. avium subspecies paratuberculosis is present in the intestinal tissues of Chinese patients with Crohn’s disease who have never left China. Archival paraffin-embedded surgical pathology blocks from patients having surgery for Crohn’s disease (CD) or for cancer (nIBD) in China were studied. M. avium subspecies paratuberculosis was detected by nested IS900 PCR with Southern blotting and amplicon sequencing. The intestinal tissues of 9 of 13 (69.2%) CD patients and 2 of 14 (14.3%) nIBD patients were IS900 PCR positive (P = 0.0063; odds ratio = 13.5). These initial studies suggest that people in China are exposed to M. avium subspecies paratuberculosis and that as in other countries, the infection is significantly associated with Crohn’s disease. M. avium subspecies paratuberculosis in dairy herds and retail milk in China needs to be investigated.     

Bioassay of Mildiomycin and a Rapid, Cost-Effective Agar Plug Method for Screening High-yielding Mutants of Mildiomycin

Summary A simple, reliable and low-cost agar diffusion bioassay for quantitative determination of mildiomycin was developed using a strain of Rhodotorula rubra AS 2.166 as the indicator organism and potato dextrose agar at pH 7.0 as the test medium. With equivalent precision and accuracy to HPLC analysis, this method was applied to analyse mildiomycin in complex culture broth during the fermentation process. A modified agar plug method based on the bioassay was constructed for rapid and efficient screening of high-yielding mutants of mildiomycin. Within four weeks, a high production strain, the mildiomycin productivity of which was 75.5% higher than the parent strain, was obtained from 15,000 mutants.     

Co-production of S-adenosyl-l-methionine and glutathione from spent brewer’s yeast cells

Both S-adenosyl-l-methionine (AdoMet) and glutathione (GSH) are important small molecules with pharmaceutical importance. The co-production of AdoMet and GSH using abundant spent brewer’s yeast cells from the beer industry and with l-methionine supplement was successfully realized. Experimental data showed that improvement of GSH productivity was accompanied by AdoMet accumulation. AdoMet productivity of 40–45 mg g⁻¹ (DCW) was successfully achieved and an additional 13–18 mg g⁻¹ (DCW) GSH was synthesized in spent brewer’s yeast cells.     

High-level expression of soluble human β-defensin-2 in Escherichia coli

Human β-defensin-2 (hBD2) is a short cationic peptide with a broad antimicrobial spectrum. The coding sequence of hBD2 was cloned into pET-32a (+) to construct a fusion expression plasmid, pET32–hBD2, which was transformed into E. coli BL21 (DE3) for expression. The cultivation parameters of the expression vector harboring strain were optimized to produce the fusion protein in soluble form efficiently and to avoid the formation of insoluble inclusion bodies. The optimal conditions were determined as following: cultivation at 28 °C in MBL medium, induction at middle stage of exponential growth with 0.8 mM IPTG, and post-induction expression for 8 h. Under the above conditions, a high percentage of the target fusion protein (≥92.3%) was expressed in soluble form and the volumetric productivity of soluble fusion protein reached 1.3 g/l. The culture process was successfully scaled up in a 10 l bench-top fermentor.