Abstract
The catalytic reforming process for producing hydrogen for the vegetable oil and other industries is reviewed. The chemistry of the steam-hydrocarbon process and the present status as practiced in the U.S. are outlined. Results of research and development work are presented and a new process utilizing the Girdler «modular» reformer is compared to standard designs. The advantages of «low-temp» carbon monoxide conversion are also discussed. The importance of considering the safety and reliability of new designs is stressed.
References
Chem. Week.90, 104 (1962).
Chem. Eng.68, 62 (1961).
Wagman, D. D., J. E. Kilpatrick, W. J. Taylor, K. S. Pitzer and F. D. Rossini, J. Res. Nat. Bur. St.34, 143–161, (1945).
Mayland, B. J., and G. E. Hays, Chem. Eng. Progr.45, 452–458 (1949).
Comley, E. A., and R. M. Reed, presented at Sixth World Petroleum Conferences, Frankfort/Main. June 1963.
Girdler Catalyst Data Sheets, Chemical Products Div., Chemetron Corp.
Author information
Authors and Affiliations
About this article
Cite this article
Mayland, B.J., Harvin, R.L. & Trimarke, C.R. Recent trends in hydrogen plant technology. J Am Oil Chem Soc 41, 26–61 (1964). https://doi.org/10.1007/BF02654893
Received:
Accepted:
Issue Date:
DOI: https://doi.org/10.1007/BF02654893