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- W4245145452 abstract "350/sup 0/F, reducing its viscosity to a low value, only small oil flows can be used in the reactor. A revised start-up procedure was incorporated for Run No. 4. Additional catalyst was added to make up for that lost during the previous run. Start-up went smoothly and the run lasted 44 hours. The feed gas for this run was synthesis gas from IGT's steam-methane reformer containing 10 to 13 percent CO. Poor gas distribution within the reactor led to high localized gas velocities and caused a considerable amount of catalyst to be entrained out of the reactor. This catalyst was collected downstream on the process oil filters. The run was terminated due to a small fire which developed at a leaking flange. The fire was quickly extinguished with no damage done. Before starting another run, it was decided to make modifications on the gas feed system in order to improve gas distribution within the reactor. Bench Scale Unit tests were made on other formulations of the INCO catalyst. In addition, a batch of the Calsicat catalyst used in pilot plant Runs Nos. 1 and 2 was tested in the bench scale unit. These results showed that reduction procedures used during those earlier runs should have been adequate for normal catalyst activity. The reason for its lower than expected activity could also be attributed to poor gas distribution within the pilot plant reactor." @default.
- W4245145452 created "2022-05-12" @default.
- W4245145452 date "1978-06-01" @default.
- W4245145452 modified "2023-09-27" @default.
- W4245145452 title "Liquid phase methanation, pilot plant operation and laboratory support work. Monthly report for April 1978" @default.
- W4245145452 doi "https://doi.org/10.2172/6660048" @default.
- W4245145452 hasPublicationYear "1978" @default.
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