TY - JOUR
T1 - Spectroscopic studies of coal maceral depolymerization effected by an iron-based catalyst
AU - Wang, H. Paul
AU - Lo, Robert
AU - Sommerfeld, David A.
AU - Huai, Huaying
AU - Pugmire, Ronald J.
AU - Shabtai, Joseph
AU - Eyring, Edward M.
N1 - Funding Information:
The financial support by the US Department of Energy,F ossil EnergyD ivision, throught heC onsortium for Fossil Fuel Liquefaction Science, Contract no.
PY - 1992/7
Y1 - 1992/7
N2 - Demineralized Hiawatha (Utah) coal was divided into narrow density fractions of resinite and vitrinite macerals using a density gradient centrifugation technique. The distribution of an iron-based catalyst in the coal maceral matrix was studied using an electron probe microanalyser. The data indicate that the iron catalyst is evenly dispersed inside the vitrinite. This uniform dispersion is preserved upon mild (275 °C) hydrotreatment and attendant partial depolymerization of the vitrinite maceral. However, the iron catalyst does not completely penetrate into the resinite maceral matrix due to a lack of microporosity. The small amount of dispersed iron catalyst in the resinite causes some depolymerization of maceral components, e.g. dimers, trimers or higher polymers, into monomers. Due to the insufficient dispersion of the iron catalyst in the resinite a competing thermal breakdown of the maceral occurs. This apparently involves a partial dehydrogenation reaction which may be favoured during the hydrotreatment of resinite.
AB - Demineralized Hiawatha (Utah) coal was divided into narrow density fractions of resinite and vitrinite macerals using a density gradient centrifugation technique. The distribution of an iron-based catalyst in the coal maceral matrix was studied using an electron probe microanalyser. The data indicate that the iron catalyst is evenly dispersed inside the vitrinite. This uniform dispersion is preserved upon mild (275 °C) hydrotreatment and attendant partial depolymerization of the vitrinite maceral. However, the iron catalyst does not completely penetrate into the resinite maceral matrix due to a lack of microporosity. The small amount of dispersed iron catalyst in the resinite causes some depolymerization of maceral components, e.g. dimers, trimers or higher polymers, into monomers. Due to the insufficient dispersion of the iron catalyst in the resinite a competing thermal breakdown of the maceral occurs. This apparently involves a partial dehydrogenation reaction which may be favoured during the hydrotreatment of resinite.
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U2 - 10.1016/0016-2361(92)90120-D
DO - 10.1016/0016-2361(92)90120-D
M3 - Article
AN - SCOPUS:0039520797
SN - 0016-2361
VL - 71
SP - 723
EP - 729
JO - Fuel
JF - Fuel
IS - 7
ER -