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

Title: Conversion of coal to synthetic gasoline and other distillate fuels. Final report, May 1976-June 1982

Technical Report ·
OSTI ID:5082570

Two novel approaches were identified and developed in an experimental, exploratory study to convert coal to gasoline and other distillate fuels: conversion of coal potential catalytic cracking stock via the combination of hydroliquefaction and hydrogen chloride treatment; and conversion of Solvent Refined Coal-II (SRC-II) coal liquids to distillate motor fuels via a combination of chemical or solvent extraction and hydrogenation. The first approach tested the combination of milk hydroliquefaction of Illinois No. 6 coal followed by HCl treatment to achieve nitrogen reduction. Small scale batch experiments on coal hydroliquefaction were carried out using a range of process severities. Subsequent treatment of the liquid products with HCl produced raffinates containing less than 0.1 wt % nitrogen, with potential as catalytic cracking feedstock. The second approach removes phenolic compounds from coal liquids before hydrotreatment. Removal of phenolics reduces hydrogen requirements and increases the rate of hydrodenitrogenation of the raffinate with the extent depending upon the type of extractant and the degree of extraction. Dimethylformaide, aqueous methanol and aqueous sodium hydroxide are effective extractants. Batch and continuous bench-scale units were employed to determine the effects of temperature, pressure, and space velocity on the hydrodenitrogenation of both the unextracted SRC-II middle distillate and extraction raffinate product. The process is capable of producing raffinates which can be upgraded to conventional refinery feedstocks. The extracts have potential as fuel ingredients or as chemical sources. The extraction of phenolics from a mixture of SRC-II naphtha and middle distillate received special attention. Batch and continuous extractions demonstrated that all of the phenolics can be removed from this heart-cut with an aqueous methanol extraction system. 41 figs., 43 tabs.

Research Organization:
Suntech, Inc., Marcus Hook, PA (USA). Applied Research and Development Dept.
DOE Contract Number:
AC22-76ET10592
OSTI ID:
5082570
Report Number(s):
DOE/ET/10592-T7; FE-2306-63; ON: DE86002175
Resource Relation:
Other Information: Portions of this document are illegible in microfiche products
Country of Publication:
United States
Language:
English