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Liquefaction of subbituminous coals with a basic nitrogenous model process solvent

โœ Scribed by John W. Hellgeth; Larry T. Taylor


Publisher
Elsevier Science
Year
1984
Tongue
English
Weight
842 KB
Volume
63
Category
Article
ISSN
0016-2361

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โœฆ Synopsis


Liquefaction reactions in a tubing-bomb reactor have been carried out as a function of coal, coal sampling source, reaction time, atmosphere, temperature, coal pre-treatment, SRC post-treatment and process solvent. Pyridine as well as toluene conversions ranging from 70 to > 90 wt% involving both eastern bituminous and western subbituminous coals are obtained. 1,2,3,4-Tetrahydroquinoline (THQ) has been extensively used as a process solvent under optimized liquefaction conditions of 2:l solvent:coal, 7.5 MPa HZ, 691 K and 30 min reaction time. Comparisons of THQ with other model process solvents such as methylnaphthalene and tetralin are described. Liquefaction product yield for conversion of subbituminouscoal is markedly decreased when surface water is removed from the coal by drying in vacua at room temperature prior to liquefaction. The effect of mixing THQ with Wilsonville hydrogenated process solvent in the liquefaction of Wyodak and Indiana V coals is described.


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