Catalysts For Upgrading Coal Derived Liquids PDF Download

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Catalysts for Upgrading Coal-derived Liquids

Catalysts for Upgrading Coal-derived Liquids
Author: Oklahoma State University. School of Chemical Engineering
Publisher:
Total Pages:
Release: 1977
Genre: Catalysts
ISBN:

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Catalysts for Upgrading Coal-derived Liquids. Quarterly Report, January 1-March 31, 1980

Catalysts for Upgrading Coal-derived Liquids. Quarterly Report, January 1-March 31, 1980
Author:
Publisher:
Total Pages:
Release: 1980
Genre:
ISBN:

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Construction of the new trickle-bed reactor was completed and one experiment was conducted. The experimental run was made using a Pamco coal-derived liquid containing 0.40% sulfur and 0.95% nitrogen. The catalyst utilized was an American Cyanamide HDN-30, Ni-Mo-Al2O3. Run conditions were at 399C (750F), 1500 psig and space times up to two hours. Sample analyses are not yet available from this experiment. Two runs were completed in the Catalyst Life Test Unit (CLTU) utilizing a liquid containing 50% Synthoil and 50% Raw Anthracene oil. This fluid has a 0.54% sulfur and 1.21% nitrogen. Two Ni-MoAl2O3 catalysts were used - Shell-324, and H-Oil. Both experiments were terminated prematurely because of equipment malfunction. Sample analyses are not yet available from these two experiments.


Catalysts for Upgrading Coal-derived Liquids. Quarterly Report, October 1-December 31, 1979

Catalysts for Upgrading Coal-derived Liquids. Quarterly Report, October 1-December 31, 1979
Author:
Publisher:
Total Pages:
Release: 1980
Genre:
ISBN:

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The design and partial construction of a new trickle-flow, packed bed reactor system was achieved. This reactor will be used to conduct investigations of throwaway type catalysts and zoned or mixed catalyst beds. It will also be used to support studies of catalyst activity decay. Most of these decay studies will be conducted in the Catalyst Life Test Unit (CLTU). The CLTU has been improved by redesign of the H2 flow system and several minor changes. A new H2 supply system has been designed and items ordered for installation. One experimental run was conducted in one of the three reactors of the CLTU. Raw anthracene oil was the feedstock and a vendor catalyst was used (Nalco, NM-502, Ni-Mo-Al2O3). Run conditions were: 700F(371C), 1500 psig and 2.0 hour space time (volume hourly). The objective of this run was to test equipment, familiarize personnel and to obtain a data base for future experiments. The sulfur removal was better than 95% throughout the 162 hours of operation. However, nitrogen removal activity decayed from 70% to about 35% after only 30 to 50 hours.