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Solid State Fermentation: An Overview - pierre

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S. BHARGAV et al., <strong>Solid</strong>-state <strong>Fermentation</strong>: <strong>An</strong> <strong>Overview</strong>, Chem. Biochem. Eng. Q. 22 (1) 49–70 (2008) 61bran (264 0.64 U/gds) but glucoamylase productionin different categories of rice flakes varied.Maximum enzyme was produced in coarse (211.5 1.44 U/gds) and medium wastes (192.1 1.15U/gds). The factors affecting enzyme activity withcombination of wastes were attributed to the increasein agglomeration of particles, which resultedin reduced aeration and penetration by fungalmycelia. 114Nutrient supplementation from organic sourcesincreases enzyme production to a greater extentthan inorganic sources. It has also been found thatmost researchers used wheat bran as substrate for-amylase production because it contains sufficientnutrients, it remains loose even in moist conditions,and has a larger surface area. Due to these factors,aeration and mycelial penetration are easier inwheat bran. 109LigninaseLignin is a biopolymer with complex phenylpropanoidstructure and contributes to environmentalpollution. The most common organisms forlignin degradation are white rot fungi. However, activityof Phanerochaete chrysosporium is found tobe most suitable for efficient lignin degradation.Enzymes secreted by white rot fungi are ligninases.They are Lignin Peroxidase (LiP), ManganesePeroxidase (MnP) and H 2 O 2 generating enzymes.Secondary metabolism of these enzymes is triggeredby C, N, S depletion. 115,116The respiration rate of an organism is indicatorof the organism’s activity. Cordova et al. determinedthe relation between the CO 2 evolution rateand enzymatic activity of fungus when grown onsugarcane bagasse pith. There was an increase inCO 2 evolution rate with increase in metabolism. Activityof manganese peroxidase (MnP) was expressedin the idiophase where the residual glucoselevel was the least in the medium. The MnP activityenhanced and then decreased rapidly due to simultaneousprotease activity. Lignin peroxidase activitywas reported during the exponential phase of theorganism’s growth. However, it decreased after fungalsecondary metabolism. This indicates that LiP isless sensitive to MnP for proteolytic action. 117 CO 2generation took place after uptake of O 2 by fungus.However, LiP and MnP activities cannot be studiedin an anaerobic media.Fujian et al. compared lignolytic enzyme activitiesin submerged and solid-state fermentation usingsteam-exploded wheat straw as substrate. LiP,MnP activities in optimum conditions were 61.67UL –1 and 27.12 U L –1 in submerged fermentation,but in solid-state the activities were 365.12 U L –1and 265 U L –1 , respectively. However, in SSF themaximum enzymatic activities reached 2600 U L –1(LiP) and 1375 U L –1 (MnP). 118 This proves the feasibilityof solid-state over submerged fermentation.Developing semi solid-state conditions withinthe bioreactor also enhances lignin enzymes.Dominguez et al. developed a bioreactor based onrotating drums for producing lignolytic enzymes.The enzyme activities at 1 L L –1 min –1 of air werefound to be 1350 U L –1 (LiP) and 364 U L –1 (MnP)respectively. Semisolid-state conditions were maintainedby using nylon sponges for providing inertsupport, which is rotated by regularly passingthrough the nutrient medium. Nylon sponges wereused due to its hydrophobicity, porous nature, affinityfor fungus and moisture retaining capacity.Higher aeration rate avoided the support cloggingand made nutrient availability to organism easier. 116Similarly, Couto et al. used polypropylene spongesas inert support for lignolytic enzyme production. 115Lignin-degrading enzymes were obtained frommushroom Bjerkandera adusta by immobilizing iton polyurethane foams. 119Degradation by lignin enzymes is a non-specificreaction on the basis of free radicals resultingin destabilization of bonds and finally breaking ofmacromolecule. This characteristic increases thepotential for chemical industries; environmental industries;coal industries and extracting importantmetabolites from natural sources.XylanaseDifferent food processing with products suchas straws and brans of different cereals, corn, hulland cobs, sugarcane and cassava bagasse, varioussaw dusts and different fruit processing and oil processingresidues have been used for producingxylanase. Xylanase production requires substratesin very high concentration, with prominent waterabsorbance capacity. Xylanase are produced mainlyby Aspergillus and Trichoderma spp. 120,121 Xylanaseproduction was achieved successfully by Aspergillusfischeri,Aspergillus niger using wheat branand wheat straw as main substrates. 122,123Addition of nitrogen source as supplement isan important step for xylanase production. 123 Sodiumnitrite played a significant role in productionof alkali stable cellulose free xylanase by Aspergillusfischeri. Xylanase in conjunction withcellulolytic enzymes is used for bioconversion oflignocellulosic material to produce fuels and otherchemicals. 122The Koji process was used for productionof xylanase by Aspergillus sulphureus using drykoji. 124 Ghanem et al. produced xylanase usingAspergillus terreus on wheat straw medium. 55Topakas et al. used the Sporotrichum thermophile

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