Process for coal liquefaction employing selective coal feed
AssigneeInternational Coal Refining Company
InventorsDavid S. Hoover, Edwin N. Givens
Life of this patent
Estimating the term…
Loading patent…
AssigneeInternational Coal Refining Company
InventorsDavid S. Hoover, Edwin N. Givens
Estimating the term…
An improved coal liquefaction process is provided whereby coal conversion is improved and yields of pentane soluble liquefaction products are increased. In this process, selected feed coal is pulverized and slurried with a process derived solvent, passed through a preheater and one or more dissolvers in the presence of hydrogen-rich gases at elevated temperatures and pressures, following which solids, including mineral ash and unconverted coal macerals, are separated from the condensed reactor effluent. The selected feed coals comprise washed coals having a substantial amount of mineral matter, preferably from about 25-75%, by weight, based upon run-of-mine coal, removed with at least 1.0% by weight of pyritic sulfur remaining and exhibiting vitrinite reflectance of less than about 0.70%.
A method for selection of feed coal for processing by direct liquefaction utilizing catalytic materials derived solely from said feed coal to produce low-ash, low-sulfur hydrocarbon products including solvent refined coal, and coal derived pentane soluble oil, which consists essentially of:
An improved coal liquefaction process wherein coal is pulverized and slurried with a pasting oil, heated to at least about 700.degree. to 900.degree. F. and pressurized to about 500 to 5,000 psig, passed with a hydrogen-rich gas and catalytic material derived solely from the feed coal to at least one dissolver, wherein said slurry is retained for sufficient time to convert at least a portion of said feed coal into liquefied reaction product, following which time the reacted liquefaction product is passed to a separator from which vapor and condensate product streams are removed, including a residual bottoms product which is subsequently de-ashed and from which is obtained recycled process solvent, which can be recycled for use as said pasting oil, solvent refined coal distillates and solid refined coal, wherein the coal conversion in said reactor is improved by:
In a direct coal liquefaction process wherein feed coal is slurried with a process derived solvent, heated to at least about 700.degree. to 900.degree. F. and pressurized to about 500 to 5,000 psig, passed with a hydrogen-rich gas and catalytic material derived solely from said feed coal to at least one dissolver, wherein said slurry is retained for sufficient time to react and dissolve at least a portion of said feed coal, following which a reacted product is passed to a separator from which separated vapor and condensed product streams are removed, including a residual bottoms product which is subsequently subjected to a solid separation from which is obtained a solid, substantially ash residue, process solvent which may be recycled and utilized as pasting oil, and solvent refined coal distillates and solids, the improvement which comprises utilizing as said feed coal only washed coal having a substantial amount of mineral matter removed, said washed coal having at least 1.0%, by weight, of pyritic sulfur content and a vitrinite reflectance of less than about 0.70%.
Dependencies are inferred from the claim text.