Bacillus amyloliquefaciens B10-127 was used to produce 2,3-butanediol (2,3-BD) from residual glycerol obtained from biodiesel synthesis. Important variables for 2,3-BD fermentation, pH and dissolved oxygen, were studied. When pH was maintained constant, the yield of 2,3-BD was inhibited. The highest 2,3-BD yields were achieved by fermentation without any pH control with an optimized initial pH 6.5. Batch fermentative production of 2,3-BD by B. amyloliquefaciens was investigated using various oxygen supply methods by changing agitation speed. Based on the analysis of three kinetic parameters including specific cell growth rate (micro), specific glucose consumption rate (q(s)) and specific 2,3-BD formation rate (q(p)), a three-stage agitation speed control strategy was proposed, aimed at achieving high concentration, high yield and high productivity of 2,3-BD. Maximum concentration of 2,3-BD reached 38.1 g/L, with the productivity of 1.06 g/(L x h), which were 14.8% and 63.1% over the best results from constant agitation speeds. In a pulse fed-batch fermentation, 2,3-BD concentration and productivity were significantly improved to 71.2 g/L and 0.99 g/(L x h), respectively. To our knowledge, these results were the highest for 2,3-BD production from biodiesel-derived glycerol.
Bacillus ; classification ; metabolism ; Biofuels ; analysis ; Bioreactors ; Butylene Glycols ; metabolism ; Fermentation ; Glycerol ; metabolism ; Hydrogen-Ion Concentration ; Industrial Microbiology ; Oxygen ; analysis

A simple, fast flow injection chemiluminescence (CL) method for the determination of methyl-parathion has been developed. It is based on the reaction of methyl parathion with luminol-H2O2 in the alkaline medium (pH：11.5～12.0), sensitized by water-soluble macromolecule Polyethylene glycol 400. Under the optimal conditions, the CL intensity was linear to the concentration in the range of 5.0×10-8～1.0×10-5　g/mL (r=0.9996), with a detection limit (3σ) of 2.0×10-8　g/mL. Relative standard deviation was less than 4% (n=11) and the recovery was between 82%～93%. This method has been successfully applied to the determination of trace residue of methyl-parathion in grain sample.

The article introduce a rapid method for preparation of fungal chromosome DNA In this method the quartz sand is used to break the fungal cell wall and the chromosome DNA is harvested rapidly in 1～2 h The method is applied successfully by the author to four kinds of fungi Neurospora crassa , Aspergillus oryzae , Morchella esculcnta , Saccharomyces cervisae All the chromosome DNA extracted has the fragment size lager than 20 kb and can be used directly for either digestion with restriction endoenzyme or PCR

We constructed plasmid pMTac to overexpress 3-ketosteroid-Δ1-dehydrogenase (KSDD) in Mycobacterium neoaurum JC-12 for improving androst-1,4-diene-3,17-dione (ADD) production. To construct pMTac, pACE promoter on pMF41 was replaced by tac promoter, and then four recombinants were constructed, which were M. neoaurum JC-12/pMF41-gfp, M. neoaurum JC-12/pMTac-gfp, M. neoaurum JC-12/pMF41-ksdd and M. neoaurum JC-12/pMTac-ksdd. Fluorescence detection results show that much more green fluorescent protein (GFP) was expressed in M. neoaurum JC-12/pMTac-ksdd than M. neoaurum JC-12/pMF41-ksdd. The activity of KSDD was 2.41 U/mg in M. neoaurum JC-12/pMTac-ksdd, 6.53-fold as that of M. neoaurum JC-12 and 4.36-fold as that of M. neoaurum JC-12/pMF41-ksdd. In shake flask fermentation, ADD production of M. neoaurum JC-12/pMTac-ksdd was 5.94 g/L, increased about 22.2% compared to the original strain M. neoaurum JC-12 and 12.7% to M. neoaurum JC-12/pMF41-ksdd. AD (4-androstene-3,17-dione) production of JC-12/pMTac-ksdd was 0.17 g/L, decreased 81.5% compared to M. neoaurum JC-12 and 71.2% to M neoaurum JC-12/pMF41-ksdd. In the 5 L fermenter, 20 g/L phytosterols was used as substrate, ADD production of M. neoaurum JC-12/pMTac-ksdd was improved to 10.28 g/L. pMTac is favorable for expressing KSDD in M. neoaurum JC-12, and overexpression of KSDD has beneficial effect on ADD producing, and it is the highest level ever reported using fermentation method in M. neoaurum.
Androstadienes ; metabolism ; Fermentation ; Industrial Microbiology ; Mycobacterium ; Oxidoreductases ; genetics ; metabolism ; Phytosterols ; metabolism ; Plasmids

In order to enhance gamma-aminobutyric acid production from L-glutamate efficiently, we amplified the key enzyme glutamate decarboxylase (GAD) encoding gene lpgad from the strain Lactobacillus plantarum GB 01-21 which was obtained by way of multi-mutagenesis and overexpressed it in E. coli BL21. Then we purified GAD by Ni-NTA affinity chromatography and characterized the enzyme to optimize the conditions of the whole-cell transformation. The results showed that the recombinant E. coli BL21 (pET-28a-lpgad) produced 8.53 U/mg GAD, which was increased by 3.24 fold compared with the GAD activity in L. plantarum. The optimum pH and temperature of the enzyme were pH 4.8 and 37 degrees C, respectively. At the same time, we found that Ca2+ and Mg2+ could increase the activity significantly. Based on this, we investigated gamma-aminobutyric acid transformation in 5 L fermentor under the optimum transformation conditions. Accordingly, the yield of gamma-aminobutyric acid was 204.5 g/L at 24 h when the 600 g L-glutamate was added and the mole conversion rate had reached 97.92%. The production of gamma-aminobutyric acid was improved by 42.5% compared with that under the unoptimized transformation conditions. This paved a way for the gamma-aminobutyric acid construction of the industrial applications.
Cloning, Molecular ; Escherichia coli ; enzymology ; genetics ; metabolism ; Glutamate Decarboxylase ; biosynthesis ; genetics ; Glutamic Acid ; metabolism ; Lactobacillus plantarum ; enzymology ; genetics ; Recombination, Genetic ; gamma-Aminobutyric Acid ; biosynthesis

N-Acetylornithine aminotransferase (EC 2.6.1.11, ACOAT) catalyzes the conversion of N-acetylglutamic semialdehyde to N-acetylornithine, the forth step involved in the L-arginine biosynthetic pathways. We studied the enzyme properties to set up reliable theoretical basis for the arginine fermentation optimization. ACOAT encoding gene argD was cloned from an industrial L-arginine producer Corynebacterium crenatum SYPA 5-5. Analysis of argD sequences revealed that only one ORF existed, which coded a peptide of 390 amino acids with a calculated molecular weight of 41.0 kDa. The argD gene from C. crenatum SYPA 5-5 was expressed both in Escherichia coli BL21 and C. crenatum SYPA. Then ACOAT was purified by Ni-NTA affinity chromatography and its specific enzyme activity was 108.2 U/g. Subsequently, the expression plasmid pJCtac-CcargD was transformed into C. crenatum SYPA and the specific activity of ACOAT was improved evidently in the recombinant C. crenatum CCD. Further fermentative character of CCD1 was also analyzed. The results showed that the L-arginine producing ability of the recombinant strain was 39.7 g/L improved by 14.7%.
Arginine ; biosynthesis ; Cloning, Molecular ; Corynebacterium ; enzymology ; genetics ; Escherichia coli ; enzymology ; genetics ; Fermentation ; Industrial Microbiology ; methods ; Metabolic Engineering ; Transaminases ; biosynthesis ; genetics ; Transformation, Bacterial

OBJECTIVE: To explore the microsurgical techniques for insular glioma without damaging its surrounding normal structures. METHODS: We retrospectively analyzed 54 patients with insular gliomas who underwent microsurgical operation by trans-syvian fissure approach between May, 2003 and August, 2008 in Xiangya Hospital. We discussed the techniques in the operation and summarized how to protect the key blood vessels, distinguish and protect the surrounding normal structures. RESULTS: There were 36 complete removals,14 secondary complete removals, and 4 partial removals.Six patients had complications after the craniotomy who had temporal speech disorder (aphasia mostly began to recover about 10 days after the craniotomy),4 patients had opposite side paralysis worsening (3 recovered normally and 1 improved after 6 months),4 had light paralysis, and another 3 had paralysis and speech disorder. CONCLUSION The microsurgery by means of trans-syvian fissure approach can well expose the anatomical relation between tumor and its surrounding structures,so that we can remove the tumor and protect the surrounding normal tissues as much as we can.
Adolescent ; Adult ; Brain Neoplasms ; pathology ; surgery ; Cerebral Cortex ; pathology ; surgery ; Female ; Glioma ; pathology ; surgery ; Humans ; Male ; Microsurgery ; methods ; Middle Aged ; Neurosurgical Procedures ; methods ; Retrospective Studies ; Young Adult

Candida glycerinogenes WL2002-5 (C.g) is an important industrial strain for glycerol production. To further improve glycerol production, we reconstructed a binary vector pCAM3300-zeocin-CgGPD1, introduced it to Agrobacterium tumefaciens LBA4404 by electroporation, and then transformed the T-DNA harboring the CgGPD1 to Candida glycerinogenes by Agrobacterium tumefaciens-mediated transformation (ATMT). After 96 h fermentation with glucose as the substrate, we screened a transformant named C.g-G8 with high glycerol production. Compared with the wild strain, the glucose consumption rate of C.g-G8 and the glycerol production were 12.97% and 18.06% higher, respectively. During the fermentation, the activity of glycerol-3-phosphate dehydrogenase of C.g-G8 was 27.55% higher than that of the wild strain. The recombinant Candida glycerinogenes with high glycerol production was successful constructed by ATMT method.
Agrobacterium tumefaciens ; enzymology ; genetics ; Candida ; genetics ; metabolism ; Electroporation ; Fermentation ; Glycerol ; analysis ; metabolism ; Glycerolphosphate Dehydrogenase ; genetics ; Recombination, Genetic ; Transformation, Genetic

A whole-cell catalyst using Escherichia coli BL21(DE3) as a host, expressing L- threonine dehydratase from Escherichia coli, and co-expressing leucine dehydrogenase from Bacillus cereus and glucose dehydrogenase from Bacillus subtilis for cofactor regeneration, was constructed and used for one-pot production of L-2-aminobutyric acid (L-ABA) and D- gluconic acid from L-threonine and D-glucose. We used shake-flask culture to study the whole-cell catalytic condition including temperature, pH, proper permeabilization of cells and optimal wet cells amount. Moreover, the whole-cell catalyst was cultured in 5-L fermentor by fed-batch fermentation, and 164 g/L L-threonine and 248 g/L D-glucose were converted to 141.6 g/L L-ABA and 269.4 g/L D-gluconic acid. The whole-cell catalyst is promising to fulfill industrial requirements for L-ABA and D-gluconic acid.

Glutamic acid is an important amino acid with wide range of applications and huge market demand. Therefore, by performing transcriptome sequencing and re-sequencing analysis on Corynebacterium glutamicum E01 and high glutamate-producing strain C. glutamicum G01, we identified and selected genes with significant differences in transcription and gene levels in the central metabolic pathway that may have greatly influenced glutamate synthesis and further increased glutamic acid yield. The oxaloacetate node and α-ketoglutarate node play an important role in glutamate synthesis. The oxaloacetate node and α-ketoglutarate node were studied to explore effect on glutamate production. Based on the integrated strain constructed from the above experimental results, the growth rate in a 5-L fermenter was slightly lower than that of the original strain, but the glutamic acid yield after 48 h reached (136.1±5.53) g/L, higher than the original strain (93.53±4.52) g/L, an increase by 45.5%; sugar-acid conversion rate reached 58.9%, an increase of 13.7% compared to 45.2% of the original strain. The application of the above experimental strategy improved the glutamic acid yield and the sugar-acid conversion rate, and provided a theoretical basis for the metabolic engineering of Corynebacterium glutamicum.
Citric Acid Cycle ; Corynebacterium glutamicum/metabolism* ; Glutamic Acid/metabolism* ; Metabolic Engineering ; Metabolic Networks and Pathways/genetics*