Refining and upgrading of synfuels from coal and oil shales by advanced catalytic processes

Sullivan, R.F.; Rudy, C.E.; Green, D.C.; Chen, H.C.

doi:10.2172/7081062

Cited by 5 publications

(2 citation statements)

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“…The sample was produced from an Illinois No. 6 coal at the Catlettsburg, KY, H-coal Pilot Plant while operating in the synfuel mode (9). A blend of "light" and "heavy" oil products (1:1.5) was distilled by Chevron into narrow-boiling range samples.…”

Section: Methodsmentioning

confidence: 99%

Temperature dependence of the electron spin resonance spectra of a coal-derived vacuum distillation residue and components

Castellano¹,

Chisholm²,

Sprecher³

et al. 1987

Anal. Chem.

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Reference to brand names is to facilitate understanding and is not. meant to imply endorsement by the U.S. Department of Energy. S.M.C. acknowledges support from the faculty research program administered by Oak Ridge Associated Universities for the U.S. Department of Energy. W.P.C. acknowledges support from the USDOE postgraduate research training program administered by Oak Ridge Associated Universities for the U.S. Department of Energy.

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Section: Methodsmentioning

confidence: 99%

Temperature dependence of the electron spin resonance spectra of a coal-derived vacuum distillation residue and components

Castellano¹,

Chisholm²,

Sprecher³

et al. 1987

Anal. Chem.

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“…The goal for the hot solids separation step is to remove the bulk of the entrained solids so as to keep the solids content of the composite oil product below about 250ppm by weight. This amount of fines would be tolerated by a conventional hydrotreating process for upgrading the coal liqaids to transportation fuels (Sullivan, 1978). However, catalyst _cations will be required in conventional hydrotreating processes because of the chemically unfavorable properties of the primary coal liquids.…”

Section: Introductionmentioning

confidence: 99%

Separation of products from mild coal gasification processes

Wallman¹

1991

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This is an informal report intended primarily for internal or limited external • distribution. The opinions and conclusions stated are those of the author and may or may not be those of the Laboratory. Work performed under the auspices of the U.S. Department of Energy by the Lawrence Livermore National Laboratory under Contract W-7405-Eng-48. #ISrI:III_LEION OF THIS DOC.;d_',AENT _" _. _.4i..., . ;t,41TEO DISCLAIMER This document was prepared as an acccount of work sponsored by an agency of the United States Government. Neither the United States Government nor the University of California nor any of their employees, makes any warranty, express or implied, or assumes any legal liability or responsibility for the accuracy, completeness, or usefuh_es's of any information, apparatus, product, or process disclosed, or represents that its use would not infringe privately own rights. Reference herein to any specific commercial products, pn_'ess, or service by trade name, trademark, manufacturer, or otherwise, does not necessarily constitute or imply its endorsement, recommendation, or favoring by the United States Government or the University of California. The views and opinions of authors expressed herein do _ot necessarily state or reflect those of the United States Government or the University of California, and shall not be used for advertising or product endorsement purposes. IThis report has been reproduced directly from the best available cop),.

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Simultaneous hydrodenitrogenation and hydrodeoxygenation of model compounds in a trickle bed reactor

Satterfield

1983

Journal of Catalysis

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Refining and upgrading of synfuels from coal and oil shales by advanced catalytic processes

Cited by 5 publications

References 0 publications

Temperature dependence of the electron spin resonance spectra of a coal-derived vacuum distillation residue and components

Temperature dependence of the electron spin resonance spectra of a coal-derived vacuum distillation residue and components

Separation of products from mild coal gasification processes

Simultaneous hydrodenitrogenation and hydrodeoxygenation of model compounds in a trickle bed reactor

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