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contributor authorRoman Adinberg
contributor authorJacob Karni
contributor authorMichael Epstein
date accessioned2017-05-09T00:14:17Z
date available2017-05-09T00:14:17Z
date copyrightAugust, 2004
date issued2004
identifier issn0199-6231
identifier otherJSEEDO-28356#850_1.pdf
identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/130762
description abstractA novel solar process and reactor for thermochemical conversion of biomass to synthesis gas is described. The concept is based on dispersion of biomass particles in a molten inorganic salt medium and, simultaneously, absorbing, storing and transferring solar energy needed to perform pyrolysis reactions in the high-temperature liquid phase. A lab-scale reactor filled with carbonates of potassium and sodium was set up to study the kinetics of fast pyrolysis and the characteristics of transient heat transfer for cellulose particles (few millimeters size) introduced into the molten salt medium. The operating conditions were reaction temperatures of 1073–1188 K and a particle peak-heating rate of 100 K/sec. The assessments performed for a commercial-scale solar reactor demonstrate that pyrolysis of biomass particles dispersed in a molten salt phase could be a feasible option for the continuous, round-the-clock production of syngas, using solar energy only.
publisherThe American Society of Mechanical Engineers (ASME)
titleSolar Gasification of Biomass: A Molten Salt Pyrolysis Study
typeJournal Paper
journal volume126
journal issue3
journal titleJournal of Solar Energy Engineering
identifier doi10.1115/1.1753577
journal fristpage850
journal lastpage857
identifier eissn1528-8986
keywordsTemperature
keywordsParticulate matter
keywordsBiomass
keywordsSolar energy
keywordsPyrolysis
keywordsHeating
keywordsFuel gasification AND Modeling
treeJournal of Solar Energy Engineering:;2004:;volume( 126 ):;issue: 003
contenttypeFulltext


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