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Abstract The current research was designed to reach extracellular protease production potential in different strains of Sordaria fimicola which were previously obtained from Dr. Lamb (Imperial College, London) from North Facing Slope and South Facing Slope of Evolution Canyon. After initial and secondary screening, two hyper-producers strains S2 and N6 were selected for submerged fermentation and cultural conditions including temperature, pH, incubation period, inoculum size, substrate concentration, and different carbon and nitrogen sources were optimized for enzyme production. S2 strain showed maximum protease production of 3.291 U/mL after 14 days of incubation at 30 °C with 7 pH, 1% substrate concentration and 1 mL inoculum, While N6 strain showed maximum protease production of 1.929 U/mL under fermentation optimized conditions. Another aim of the present research was to underpin the biodiversity of genetics and post-translational modifications (PTMs) of protease DPAP (peptidyl-aminopeptidase) in Sordaria fimicola. Five polymorphic sites were observed in amino acid sequence of S. fimicola strains with reference to Neurospora crassa. PTMs prediction from bioinformatics tools predicted 38 phosphorylation sites on serine residues for protease peptidyl-aminopeptidase in S1 strain of S. fimicola while 45 phosphorylation sites on serine in N7 strain and 47 serine phosphorylation modifications were predicted in N. crassa. Current research gave an insight that change in genetic makeup effected PTMs which ultimately affected the production of protease enzyme in different strains of same organism (S. fimicola). The production and molecular data of the research revealed that environmental stress has strong effects on the specific genes through mutations which may cause genetic diversity. S. fimicola is non- pathogenic fungus and has a short life cycle. This fungus can be chosen to produce protease enzyme on a commercial scale.

Studies were carried out on a paddy soil fungal isolate identified to be a strain of Aspergillus niger from Manipal. The parameters that largely impact enzyme production viz., fermentation time, impeller speed, pH, temperature and nutrient supplements were studied. Optimization of production parameters for production of protease was done by the single-parameter mode. Casein served as substrate and proteolytic activity was estimated using Folin-Ciocalteau method at 660 nm. A maximum yield of 71.3 mg tyrosine/g casein substrate was produced in 96 h on a soluble starch medium at pH 4 in shake flask experiments. Production was carried out on a 3-liter fermenter and 40.7 mg of tyrosine was liberated/g of substrate. The enzyme was extracted with 50% ammonium sulfate and sodium dodecyl sulfate-Polyacrylamide gel electrophoresis showed two bands having mw 45.7 kDa and 38.5 kDa, respectively. The enzyme activity was found to be 147.84 U/ml. [ABSTRACT FROM AUTHOR]

Production of industrial aromatic chemicals from renewable resources could provide a competitive alternative to traditional chemical synthesis routes. This review describes the engineering of microorganisms for the production of p-hydroxycinnamic acid (pHCA) and p-hydroxystyrene (pHS) from glucose. The initial process concept was demonstrated using a tyrosine-producing Escherichia coli strain that overexpressed both fungal phenylalanine/tyrosine ammonia lyase (PAL) and bacterial pHCA decarboxylase (pdc) genes. Further development of this bioprocess resulted in uncoupling the pHCA and pHS production steps to mitigate their toxicity to the production host. The final process consists of a fermentation step to convert glucose to tyrosine using a tyrosine-overproducing E. coli strain~ This step is followed by a single biotransformation reaction to deaminate tyrosine to pHCA through immobilized E. coli cells that overexpress the Rhodotorula glutinis PAL gene. Finally, chemical decarboxylation of pHCA produces pHS. This multifaceted approach, which integrates biology, chemistry, and engineering, has allowed development of an economical process at scales suitable for industrial applications. [ABSTRACT FROM AUTHOR]