Production of pipeline gas by hydrogasification of coal

E.J. Pyrcioch, H.L. Feldkirchner

OSTI OAI (U.S. Department of Energy Office of Scientific and Technical Information) · 1972 · 14 citations · 0 references

Concepts

Abstract

Batch reactor and pilot plant studies by the Institute of Gas Technology studied destructive hydrogenation of coal at up to 3800 psi and 2100/sup 0/F to produce high Btu pipeline gas. The two-stage process first converts coal to methane by pyrolysis and hydrogenolysis, and then a slower reaction with steam and hydrogen converts the char residue to methane. In countercurrent downflow tests it was possible to produce an 800 to 900 Btu/cu ft gas from bituminous coal char and hydrogen; however, 900 to 1000 Btu/cu ft gas could not be produced in this manner because the product gas was diluted with hydrogen and carbon oxides. Plant capacity was 82 to 90 billion Btu/day.