Cen Pei-lin

A pair of two-component regulatory genesecrA1/A2 inS. coelicolor

Two-component genes are kinds of genetic elements involved in regulation of antibiotic production inStreptomyces coelicolor. DNA microarray analysis revealed thatecrA1/A2, which mapped at distant sites fromred lucus and encode respectively the kinase and regulator, expressed coordinately with genes of Red specific biosynthetic pathway.ecrA1 andecrA2 gene-disruptive mutants were constructed using homogenotisation by reciprocal double crossover. Fermentation data showed that the undecylprodigiosin (Red) level of production was lower than that of wild-type strain. However, the change of the actinorhodin (Act) production level was not significant compared with wild type. Thus, these experiment results confirmed that the two-component systemecrA1/A2 was positive regulatory element forred gene cluster.

Heterogeneous UV/Fenton catalytic degradation of wastewater containing phenol with Fe-Cu-Mn-Y catalyst

The heterogeneous UV/Fenton process with the appropriate amount of Fe-Mn-Cu-Y as catalyst was developed and various operation conditions for the degradation of phenol were evaluated. The results indicated that by using the heterogeneous UV/Fenton process, the CODcr removal rate reached almost 100% for wastewater containing phenol. Compared with the homogeneous process, the developed catalyst could be used at wider pH range in the UV/Fenton process. Comparison of various heterogeneous process showed that heterogeneous UV/Fenton process was best. The heterogeneous UV/Fenton process with Fe-Mn-Cu-Y catalyst is highly efficient in degrading various organic pollutants.

Improved production of spiramycin by mutant Streptomyces ambofaciens

Strain improvement and medium optimization to increase the productivity of spiramycin were carried out. Of oil tolerant mutant strains screened, one mutant,Streptomyces ambofaciens XC 2–37, produced 9% more spiramycin than the parent strainS. ambofaciens XC 1–29. The effects of soybean oil and propyl alcohol on spiramycin production withS. ambofaciens XC 2–37 were studied. The potency ofS. ambofaciens XC 2–37 was improved by 61.8% with addition of 2% soybean oil in the fermentation medium and 0.4% propyl alcohol at 24 hours after incubation. The suitable time for feeding propyl alcohol is at 24 hours after incubation in flask fermentation and at 20 hours after incubation in fermentor fermentation. The new process withS. ambofaciens XC 2–37 was scaled up for industrial scale production of spiramycin in a 60 m3 fermentor in Xinchang Pharmaceutical Factory, Zhejiang Medicine Company, Ltd., China, and the potency and productivity of fermentation were improved by 42.9%.

Enhanced production of avermectin B1a by medium optimization and glucose feeding with Streptomyces avermilitis

Abstract Avermectin B1a is an important macrolide antibiotic with potent anthlemintic and insecticidal activity. The objective of this study was to enhance productivity of avermectin B1a by optimizing culture medium and glucose feeding fermentation. Results showed that B1a concentration was increased by 48.6% through optimization of nitrogen, carbon sources as well as supplement of 0.2 mM Co2+. It was found that a maximum B1a concentration of 826 mg/l was attained by glucose-feeding in a laboratory scale fermentor, which was two-fold higher than that in the control fermentation. Meanwhile, the proportion of B1a in the total products was increased by 6% with respect to the control process. These results would be very useful for maximizing productivity of avermectin B1a in an up-scaled fermentation.

Effect of inducers on the production of 5-aminolevulinic acid by recombinant Escherichia coli.

Abstract Aminolevulinic acid (ALA) was produced by recombinant Escherichia coli BL21(DE3) (pET28‐A.R‐hemA) harboring the ALA synthase gene (hemA) from Agrobacterium radiobacter zju‐0121. The effects of inducers on the ALA synthase activity and ALA productivity were evaluated. The results indicated that a low isopropyl‐β‐D‐thiogalactoside (IPTG) concentration (0.05 mmol/L) was favorable for high expression of ALA synthase, which resulted in higher ALA productivity. For metabolic engineering applications, lactose was a better substitute of IPTG for active enzyme expression. When lactose concentration was 5 mmol/L, the specific ALA synthase activity and ALA productivity reached 16.7 nmol/(min · mg of protein) and 1.15 g/L, respectively, which were about 15% and 43% higher than those induced by IPTG.