Liquefaction of subbituminous coals with a basic nitrogenous model process solvent
โ 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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โฆ 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.
๐ SIMILAR VOLUMES
Coal liquefaction experiments have been carried out to determine the tendency for adduction of several hydrocarbon-and nitrogen-containing structures typical of coal. Principal conclusions are: that even good hydrogen donors such as tetralin and octahydrophenanthrene are adducted readily; that benzy
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The effects of the gas flow rate in the reactors and the boiling point range of the feed solvent on conversion in brown coal liquefaction were investigated in the presence of iron-sulfur catalyst, using a continuous reactor system. An increase in the gas flow rate (GFR) markedly increased the distil