By Martin B. B. Hocking
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C For 1993. d Stated as phosphate rock, for lack of phosphoric acid data. e Estimated from sodium hydroxide production. htm by WHO. g For 1999. h From FAO Statistical Database. org/servlet3? and follow the links. extracted minerals, depending on the origin of the sulfur. S. and worldwide. S. ranking. American production of most of the chemicals on this list represents the largest single contribution to the world figure. S. ranking data can often be used to estimate both world rankings and world production levels when these data are not available directly.
Except for the cost of the catalyst inventory (which is platinum), the fabrication cost of the ammonia burner itself is relatively low. Follow-up reactions for the process are much slower than this so that the volume of equipment required to contain these parts of the process are much larger and more costly (Chap. 11). Ammonia oxidation represents a process with which it was realized, early in the design stage, that carrying out this step at 600–7008C instead of at near ambient temperatures speeded up the process sufficiently to allow large conversion volumes to take place in a relatively small reactor.
Brechtelsbauer, N. Lewis, P. , Evaluation of a Spinning Disk Reactor for Continuous Processing, Org. Proc. Res. & Devel. 5, 65–68 (2001). 22. M. Rouhi, Microreactors Eyed for Industrial use, Chem. Eng. News, 82(27), 18–19, July 5 (2004). 23. G. , ‘‘Chemical Engineering; a Special Study,’’ Nuffield Foundation, Penguin, Harmondsworth, England, 1971. 24. Smith. Determining Velocity and Reynolds Number in Gas Pipelines and Wells, Technology, 81, 108–112, Dec. 12 (1983). 25. H. W. , ‘‘Perry’s Chemical Engineer’s Handbook,’’ 6th ed.