Skip to main content
U.S. Department of Energy
Office of Scientific and Technical Information

Visit to Gelsenberg hydrogenation plant

Technical Report ·
OSTI ID:7177664
This detailed report covered typical plant operations for hydrogenation of bituminous coal at 700 atm in the liquid phase, and 300 atm in vapor phase operations. Product from the liquid phase was saturated in the vapor phase, then cracked in another vapor phase operation. Apparently, quantity was the driving force behind this plant's operation because there was no aromatization attempt or iso-octane production. The increase in pressure for the liquid phase from 300 to 700 atm reduced asphalt yield, allowing linger operating periods of the carbonizing ovens without decoking. Less unreacted coal meant greater yields of product as well as easier handling of sludge by-product. The increased pressure increased the gasoline yield, as well as the throughput. The annual production capacity was on the order of 340,000 metric tons (tes.) of gasoline and 100,000 tes. propane and butane. Hydrogen production was derived mainly from coke as water gas and amounted to over 100,000 m/sup 3//hr. The process mills for grinding and pasting were typical except for CO/sub 2/ flooding to eliminate explosion hazard. Coal paste consisted of pasting oil, 45% to 46% coal, 1.2% FeSO/sub 4/ and 1.5% Bayermasse as catalysts, and 0.3% NaS to remove HCl. Bayermasse was an impure form of Fe/sub 2/O/sub 3/. Coal content was later decreased to 40%, enabling transfer through a heat exchanger prior to addition of high pressure hydrogen. This reduced preheater overload and failure. Temperature of the converters was controlled to maintain an output of heavy pasting oil equal to the input used in the paste, thus yields of other components were dependent upon recovery of this product. Output of newly-formed heavy oil was kept balanced with losses of heavy oil in sludge processing. 11 tables, 4 figures, 2 flowsheets
Research Organization:
Combined Intelligence Objectives Subcommittee
OSTI ID:
7177664
Report Number(s):
TOM-196-548-595
Country of Publication:
United States
Language:
English

Similar Records

CIOS evaluation report 70: Gelsenberg, A. G. [340,000 tons/yr gasoline at 100,000 tons/yr propane and butane]
Technical Report · Fri Jun 08 00:00:00 EDT 1945 · OSTI ID:7220556

Flow sheet at Lu-Op plant for auto gasoline for 170/sup 0/ E. P. gasoline for DHD from bituminous coal
Technical Report · Mon Nov 02 00:00:00 EDT 1942 · OSTI ID:6728775

Report of conference on exchange of experiences with Gelsenberg
Technical Report · Sun Oct 19 23:00:00 EST 1941 · OSTI ID:6129265