01580nas a2200205   4500008004100000022001400041245007000055210006900125260006900194300001200263490000800275520085000283653002001133653003001153653002201183653001801205100002101223700002601244856010401270       2010                        eng d  a1385-894700aThermoneutral point analysis of ethanol dry autothermal reforming0 aThermoneutral point analysis of ethanol dry autothermal reformin  aPO BOX 564, 1001 LAUSANNE, SWITZERLANDbELSEVIER SCIENCE SAcDEC  a864-8730 v1653 a<p>{Dry autothermal reforming of ethanol can be used to produce a variety of value added products like hydrogen, syngas and also carbon (possible CNF). A thermodynamic analysis of dry autothermal reforming of ethanol has been carried out to locate the thermoneutral temperatures and product composition at those points at 1, 3, 6 and 9 bar reaction pressures. The variations of thermoneutral temperatures and individual product yields at those temperatures have been discussed to find the optimum operating parameters for desired product output from the process. The process operated at thermoneutral conditions can give useful products like hydrogen, syngas (of low ratio) and carbon (possibly CNFs) and also provide a way for CO2 sequestration using renewable ethanol fuel. A maximum of 2.58 moles of syngas of ratio 2.01 obtained at 1 bar</p>10aCO2 utilization10aDry autothermal reforming10aEthanol reforming10aThermoneutral1 aKale, Ganesh, R.1 aKulkarni, Bhaskar, D.  uhttps://library.ncl.res.in/content/thermoneutral-point-analysis-ethanol-dry-autothermal-reforming-001976nas a2200217   4500008004100000022001400041245005300055210005300108260010600161300001400267490000700281520120600288653002601494653003001520653002401550653002401574653002701598100002101625700002601646856008601672       2011                        eng d  a0360-319900aAlternative process for gasoline fuel processors0 aAlternative process for gasoline fuel processors  aTHE BOULEVARD, LANGFORD LANE, KIDLINGTON, OXFORD OX5 1GB, ENGLANDbPERGAMON-ELSEVIER SCIENCE LTDcFEB  a2118-21270 v363 a<p>The article explores the thermodynamics of an alternate hydrogen generation process dry autothermal reforming and its comparison to autothermal reforming process of isooctane for use in gasoline fuel processors for SOFC. A thermodynamic analysis of isooctane as feed hydrocarbon for autothermal reforming and dry autothermal reforming processes for feed OCIR (oxygen to carbon in isooctane ratio) from 0.5 to 0.7 at 1 bar pressure under analogous thermoneutral operating conditions was done using Gibbs free energy minimization algorithm in HSC Chemistry. The trends in thermoneutral points (TNP), important product gas compositions at TNPs and fuel processor energy requirements were compared and analyzed. Dry autothermal reforming was identified as a less energy consuming alternative to autothermal reforming as the syngas can be produced with lower energy requirements at thermoneutral temperatures, making it a promising candidate for use in gasoline fuel processors to power the solid oxide fuel cells. The dry autothermal reforming process for syngas production can also be used for different fuels. (C) 2010 Professor T. Nejat Veziroglu. Published by Elsevier Ltd. All rights reserved.</p>10aAutothermal reforming10aDry autothermal reforming10ahydrogen production10aIsooctane reforming10aThermodynamic modeling1 aKale, Ganesh, R.1 aKulkarni, Bhaskar, D.  uhttps://library.ncl.res.in/content/alternative-process-gasoline-fuel-processors-0