Abstract The effluent slurry product from a coal liquefaction reactor is split into two streams. The first stream is subjected to vacuum distillation to produce a vacuum bottoms. The second stream is mixed with particulate char to form a solids-enriched slurry feedstock to a low temperature carbonization plant. The char made in this plant, plus the vacuum bottoms from the first stream, forms a pelletizable composition which serves as a feedstock to a pelletizing plant. By virtue of the foregoing procedure, a reduction of the order of 30 percent in size of the pelletizing plant is effected, as compared to sending to the pelletizing plant all the vacuum bottoms obtainable from the entire coal liquefaction effluent slurry product; yet about the same total weight of pellets is made.
In a coal liquefaction process which employs a liquefaction solvent, wherein an effluent slurry product is recovered which contains a solution of coal liquefaction products in said liquefaction solvent, and finely divided, undissolved solids suspended in said solution, the improvement which comprises: (a) splitting said effluent slurry product into first and second streams; (b) subjecting the first stream to vacuum distillation to yield an overhead distillate fraction and a solids-laden bottoms fraction; (c) mixing the second stream with particulate char, to form a slurry; (d) subjecting the slurry from step (c) to low temperature carbonization to form char and vaporous products; (e) forming a pelletizable composition out of the solids-laden bottoms fraction from step (b) and the char from step (d); (f) pelletizing said pelletizable composition from step (e); and (g) recovering pellets from step (f).
Claim 2
Dependent Claim
136 words
In a coal liquefaction process which employs a liquefaction solvent, wherein an effluent slurry product is recovered which contains a solution of coal liquefaction products in said liquefaction solvent, and finely divided, undissolved solids suspended in said solution, the improvement which comprises: (a) splitting said effluent slurry product into first and second streams; (b) subjecting the first stream to vacuum distillation to yield an overhead distillate fraction and a solids-laden bottoms fraction; (c) mixing the second stream with particulate char, to form a slurry; (d) subjecting the slurry from step (c) to low temperature carbonization to form char and vaporous products; (e) forming a pelletizable composition out of the solids-laden bottoms fraction from step (b) and the char from step (d); (f) pelletizing said pelletizable composition from step (e); and (g) recovering pellets from step (f).