Gene/Protein
Disease
Symptom
Drug
Enzyme
Compound
Pivot Concepts:
Gene/Protein
Disease
Symptom
Drug
Enzyme
Compound
Target Concepts:
Gene/Protein
Disease
Symptom
Drug
Enzyme
Compound
Query: EC:3.2.1.15 (
pectinase
)
2,440
document(s) hit in 31,850,051 MEDLINE articles (0.00 seconds)
Pectinase production studies were carried out in submerged and solid-state conditions from deseeded sunflower head employing Aspergillus niger. The two potential strains of A. niger, DMF 27 for submerged and DMF 45 for solid-state were isolated by multi-step screening technique based on coefficient of pectolysis and capability of
pectinase
production. Process variables such as size of inoculum, pH, temperature, particle size and moisture content were optimized with an aim to achieve the maximum production of pectinases. The increased level of
pectinase
production was recorded at pH 5.0 and temperature 34 degrees C in submerged and solid-state conditions. The optimum inoculum size was 1x10(5)ml(-1) for submerged and 1x10(7)g(-1) for solid-state conditions. Five hundred micrometer particle size and 65% moisture content of the substrate were optimum for the maximum production of pectinases in solid-state condition. Under optimum conditions, maximum production of exo-
pectinase
was 34.2U/g in SSF and endo-
pectinase
was 12.6U/ml in
SmF
.
...
PMID:Optimization of process for the production of fungal pectinases from deseeded sunflower head in submerged and solid-state conditions. 1633 73
A techno-economic analysis of submerged (
SmF
) and solid state fermentation (SSF) processes for Aspergillus carbonarius
polygalacturonase
production was performed to make an appropriate process selection. The downstream processing involved integrated membrane process (IMP) and alginate affinity precipitation (AAP). For a production scale of 30kL purified
polygalacturonase
concentrate per year, the total upstream cost of
SmF
was 14% lower than the SSF process. Downstream processing cost by IMP was 47% lower than AAP. The
SmF
-IMP process required a total capital investment that was 15-24% lower than the
SmF
-AAP and SSF-AAP processes. The corresponding unitary product cost was also lower by 24-36% in
SmF
-IMP process. Thus the
SmF
-IMP process proved to be very attractive from an economic point of view.
...
PMID:Techno-economic analysis of processes for Aspergillus carbonarius polygalacturonase production. 2228 Sep 67