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Title: Brown coal ash removal by the sink method (in German)

Technical Report ·
OSTI ID:6888276

Steps were outlined for a flow sheet describing the ash removal process for the production of 1.4 tons of low-temperature carbonization coke per hour. The washing and suspension was accomplished by 400 kg of 30% HCl added to 6.2 tons/hr of crushed, wet, Rhine brown coal. This suspension was mixed, then stirred for 20 minutes, while heavier sand particles sank to a conical collector in the bottom of the apparatus, where sand could be drawn off periodically. The slurry then emptied into a settling clarifier tank where the paste was thickened and the decant was removed. Next, 207 kg of oil and 310 kg more acid were added and mixed thoroughly for 20 minutes in another mixer. This provided intimate mixing for the coal and binding oil, which was sometimes replaced by tar. This coal-oil-HCl emulsion was settled in a clarifier where the decant was recycled. The thickened sludge was filtered in a disc-shaped vacuum filter, and the filtrate was allowed to separate into aqueous and oil layers and the aqueous layer combined with the clarifier recycle. The water was removed from the filter cake in a tubular drier, then reduced to 1 to 3 mm particles by a sieve and roll crusher. Then a mixer insured uniform binding oil distribution before the briquettes were pressed. The final briquette yield was 3.5 tons/hr. The briquettes were then carbonized at low temperature in batches with the capacity of 3.5 tons/hr. This ash removal procedure gave no estimates of effectiveness such as before-and-after compositions, but suggested that a general conversion from a high to a moderate ash level took place. 1 flowsheet

Research Organization:
I.G. Farbenindustrie, A.G., Hoechstadt (Germany)
OSTI ID:
6888276
Report Number(s):
TOM-286-40-42
Country of Publication:
United States
Language:
German