skip to main content
OSTI.GOV title logo U.S. Department of Energy
Office of Scientific and Technical Information

Title: Rate of oxydesulfurization of coal-derived pyrite in hot alkaline solution. [MS Thesis; 50 references]

Technical Report ·
DOI:https://doi.org/10.2172/5206324· OSTI ID:5206324

The rate of oxydesulfurization of coal-derived pyrite with hot dilute sodium carbonate solutions in a fixed bed tubular reactor was investigated. Pyrite used in this study was obtained in the form of nodules from the refuse produced in cleaning coal. The major areas studied included the difference in leaching characteristics of acid cleaned pyrite and uncleaned pyrite, the degree of sulfur removal from pyrite at different locations in the tubular reactor, the effect on sulfur conversion of the gas to liquid volume ratio in the reactor, and the effect of various operating conditions including temperature (100 to 175/sup 0/C), oxygen partial pressure (3.13 to 13.33 atm.), average particle size (114 to 332 ..mu..m.), and reaction time. With the fixed bed tubular reactor, acid cleaned pyrites gave more consistent results than uncleaned pyrites. The degree of sulfur extraction decreased from the point where the leaching solution entered the reactor to where it left and this change appeared to be related to the drop in oxygen partial pressure across the bed. Also, the gas to liquid volume ratio in the reactor affected the sulfur conversion, and at 125/sup 0/C and 13.33 atm. oxygen pressure the optimum ratio was found to be about 0.17. Furthermore, the rate of sulfur extraction increased significantly with increasing temperature, increasing oxygen partial pressure, and decreasing particle size. The shrinking unreacted core model was used to analyze the leaching process. The results showed that diffusion through a hematite shell which forms around a shrinking core of unreacted pyrite controls the overall rate of extraction of sulfur from the pyrite particles.

Research Organization:
Ames Lab., Ames, IA (United States)
DOE Contract Number:
W-7405-ENG-82
OSTI ID:
5206324
Report Number(s):
IS-T-905
Resource Relation:
Other Information: Thesis
Country of Publication:
United States
Language:
English