RI 5841 Pilot Plant Development Of The Hot-Gas-Recycle Process For The Synthesis Of High-B.T.U. Gas ? Summary

- Organization:
- The National Institute for Occupational Safety and Health (NIOSH)
- Pages:
- 32
- File Size:
- 5255 KB
- Publication Date:
- Jan 1, 1961
Abstract
A high-B.t.u, gas can be synthesized by the catalytic methanation of a mixture of 2.5 to 3 parts of hydrogen to 1 part of carbon monoxide, obtained in the gasification of coal, using a steel catalyst followed by Raney nickel in a hot-gas-recycle system. Conversion of 99 percent of the H2+CO yields a fuel gas with a heating value of 983 to 1130 B.t.u. per cubic foot containing 78 to 96 percent methane, no carbon monoxide, and very small amounts of unsaturated hydrocarbons. With the steel catalyst alone, conversions were 85 to 90 percent, giving a fuel gas of 810 to 868 B.t.u, per cubic foot, or 847 to 975 B.t.u. on a C02-free basis. INTRODUCTION In 1948 the U.S, marketed production of natural gas was 5.15 trillion cubic feet; by 1958 it had reached 11.0 trillion cubic feet, a rate of growth of 8 percent annually. 4 5 Although demand is expected to increase less rapidly, by 1966 it may reach 16 trillion cubic feet, based on an estimated 4.7 percent annual increase.6
Citation
APA:
(1961) RI 5841 Pilot Plant Development Of The Hot-Gas-Recycle Process For The Synthesis Of High-B.T.U. Gas ? SummaryMLA: RI 5841 Pilot Plant Development Of The Hot-Gas-Recycle Process For The Synthesis Of High-B.T.U. Gas ? Summary. The National Institute for Occupational Safety and Health (NIOSH), 1961.