01982nas a2200241 4500008004100000022001400041245016500055210006900220260009900289300001400388490000800402520103100410653001801441653001201459653001801471653002601489653002501515100001801540700001801558700002101576700001401597856012901611 2010 eng d a0960-852400aBiocatalytic approach for the utilization of hemicellulose for ethanol production from agricultural residue using thermostable xylanase and thermotolerant yeast0 aBiocatalytic approach for the utilization of hemicellulose for e aTHE BOULEVARD, LANGFORD LANE, KIDLINGTON, OXFORD OX5 1GB, OXON, ENGLANDbELSEVIER SCI LTDcJUL a5366-53730 v1013 a

A hydrolysis of 62% and 50% for OSX (Oat spelt xylan) and WBH (Wheat bran hemicellulose) were obtained in 36 h and 48 h using Accellerase(TM) 1000 at 50 degrees C wherein thermostable xylanase from alkalothermophilic Thermomonospora sp. yielded 67% (OSX) in 3 h and 58% (WBH) in 24 h at 60 degrees C, favouring a reduction in process time and enzyme dosage. The rate of hydrolysis with thermostable xylanase was increased by 20% with the addition of nonionic surfactant tween 80 or biosurfactant sophorolipid. The simultaneous saccharification and fermentation (SSF) of OSX and WBH using thermostable xylanase and D. hansenii in batch cultures produced 9.1 g/L and 9.5 g/L of ethanol, respectively and had a shorter overall process time than the separate hydrolysis and fermentation (SHF). The immobilized yeast cells in Ca-alginate matrix produced ethanol with a yield of 0.46 g/g from hemicellulosic hydrolysates and were reused six times with 100% fermentation efficiency. (C) 2010 Elsevier Ltd. All rights reserved.

10aBiosurfactant10aEthanol10aHemicellulose10aThermostable xylanase10aThermotolerant yeast1 aMenon, Vishnu1 aPrakash, Gyan1 aPrabhune, Asmita1 aRao, Mala uhttps://library.ncl.res.in/content/biocatalytic-approach-utilization-hemicellulose-ethanol-production-agricultural-residue-002367nas a2200241 4500008004100000022001400041245016600055210006900221260007300290300001200363490000800375520144300383653001201826653002201838653001501860653002701875653002501902653001801927100001801945700001801963700001401981856013001995 2010 eng d a0168-165600aEnzymatic hydrolysis and ethanol production using xyloglucanase and debaromyces hansenii from tamarind kernel powder: galactoxyloglucan predominant hemicellulose0 aEnzymatic hydrolysis and ethanol production using xyloglucanase  aPO BOX 211, 1000 AE AMSTERDAM, NETHERLANDSbELSEVIER SCIENCE BVcAUG a233-2390 v1483 a

The hydrolysis and ethanol production from tamarind kernel powder (TKP), a rich source of galactoxyloglucan (GXG) was investigated for the first time using xyloglucanase and thermotolerant Debaromyces hansenii. The acid hydrolysis of TKP with 2N H(2)SO(4) at 120 degrees C for 30 min yielded an overall saccharification of 94% based on the total available carbohydrate content and further fermentation at 40 degrees C with thermotolerant D hansenii produced an ethanol yield of 0.35 g/g. A maximum hydrolysis of 55 and 78% for GXG was obtained in 48 h at 50 degrees C using Thermomonospora xyloglucanase (TXy) and accellerase (TM) 1000, respectively. The synergistic effect of beta-galactosidase and xyloglucanase was demonstrated by the exogenous addition of beta-galactosidase to TXy which improved the overall hydrolysis of GXG by 30%. The rate of hydrolysis of GXG with TXy and accellerase was increased by 15-20% in the presence of chemical surfactants (tween 80 and toluene) or protein additive (BSA). The fermentation of enzymatic hydrolysates of GXG by TXy and accellerase with free cells at 40 degrees C produced an ethanol yield of 0.39 and 0.41 g/g whereas with immobilized cells produced 0.45 and 0.43 g/g, respectively, with a theoretical conversion efficiencies of 78-88%. The immobilized yeast cells were reused six times at 40 degrees C with 100% fermentation efficiency. (C) 2010 Elsevier B.V. All rights reserved.

10aEthanol10aGalactoxyloglucan10aHydrolysis10aTamarind kernel powder10aThermotolerant yeast10aXyloglucanase1 aMenon, Vishnu1 aPrakash, Gyan1 aRao, Mala uhttps://library.ncl.res.in/content/enzymatic-hydrolysis-and-ethanol-production-using-xyloglucanase-and-debaromyces-hansenii-002048nas a2200241 4500008004100000022001400041245014500055210006900200260007300269300001200342490000700354520117600361653001201537653001501549653001301564653001401577653001401591653002501605100001801630700001901648700001401667856012501681 2011 eng d a0378-382000aBioethanol production from renewable polymer lichenan using lichenase from an alkalothermophilic thermomonospora sp and thermotolerant yeast0 aBioethanol production from renewable polymer lichenan using lich aPO BOX 211, 1000 AE AMSTERDAM, NETHERLANDSbELSEVIER SCIENCE BVcMAR a401-4060 v923 a

Biomass feedstocks available decentrally will be more commodious for localized biorefinery approach than the exhaustive large scale and centralized plants driven by cost intensive technology. Lichen is present in a wide range of habitats in a distributed manner. A maximum hydrolysis of 73%-76% for lichenan from Cetraria islandica, Usnea barbata and Parmelia sp. were obtained in 24 h using lichenase from an alkalothermophilic Thermomonospora sp. wherein the hydrolysis was 100% with commercial enzyme Accellerase (TM) 1000. The synergistic role of beta-glucosidase in lichenan hydrolysis was demonstrated by the exogenous addition of beta-glucosidase to Thermomonospora lichenase which resulted in complete hydrolysis. The hydrolysates of lichenan obtained using Accellerase or a cocktail of Thermomonospora lichenase and beta-glucosidase when fermented with free cells of Saccharomyces at 40 degrees C produced an ethanol yield of 0.45 g/g-0.48 g/g with theoretical conversion efficiencies of 93%-96%. The Ca-alginate immobilized yeast cells were reused eight times at 40 degrees C with 100% fermentation efficiency. (C) 2010 Elsevier B.V. All rights reserved.

10aEthanol10aHydrolysis10aLichenan10aLichenase10aSynergism10aThermotolerant yeast1 aMenon, Vishnu1 aDivate, Rupesh1 aRao, Mala uhttps://library.ncl.res.in/content/bioethanol-production-renewable-polymer-lichenan-using-lichenase-alkalothermophilic-002381nas a2200265 4500008004100000022001400041245014900055210006900204260009900273300001000372490000700382520140800389653000601797653000801803653003301811653002301844653001201867653001501879653001401894653002501908100001901933700001801952700001401970856013101984 2013 eng d a0964-830500aApproach towards biocatalytic valorisation of barley beta-glucan for bioethanol production using 1,3-1,4 beta-glucanase and thermotolerant yeast0 aApproach towards biocatalytic valorisation of barley betaglucan  aTHE BOULEVARD, LANGFORD LANE, KIDLINGTON, OXFORD OX5 1GB, OXON, ENGLANDbELSEVIER SCI LTDcAUG a81-860 v823 a

The exploitation of renewable resource containing polymers other than cellulose and hemicellulose are critically important for the feasibility of biofuel production. The potential of 1,3-1,4 glucan 4-gluconohydrolyase mediated saccharification of barley beta-glucan (BG) was investigated for ethanol production using thermotolerant Saccharomyces sp. A maximum hydrolysis of 71% was obtained in 24 h using in-house produced 1,3-1,4 beta-glucanase from an alkalothermophilic Thermomonospora sp. whereas the hydrolysis was 100% with Accellerase (TM) 1000. The synergistic effect of beta-glucosidase and 1,3-1,4 beta-glucanase was demonstrated by the exogenous addition of beta-glucosidase to Thermomonospora 1,3-1,4 beta-glucanase which resulted in complete hydrolysis of BG. The hydrolysates of BG obtained using Accellerase or a cocktail of Thermomonospora 1,3-1,4 beta-glucanase and beta-glucosidase when fermented with free cells of Saccharomyces at 40 degrees C produced an ethanol yield of 0.44 g g(-1) and 0.46 g g(-1) respectively and when fermented with immobilized cells produced a yield of 0.49 g g(-1). The Ca-alginate immobilized yeast cells were reused nine times at 40 degrees C with 100% fermentation efficiency. The economics of barley-to-fuel ethanol program will ameliorate if in addition to barley starch, beta-glucan is also utilized. (c) 2013 Elsevier Ltd. All rights reserved.

10a110a3-110a4 Glucan 4-gluconohydrolyase10aBarley beta-glucan10aEthanol10aHydrolysis10aSynergism10aThermotolerant yeast1 aDivate, Rupesh1 aMenon, Vishnu1 aRao, Mala uhttps://library.ncl.res.in/content/approach-towards-biocatalytic-valorisation-barley-beta-glucan-bioethanol-production-using-0