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Smith-Peters

Warren L. McCabe, Julian C. Smith, Peter Harriot, Unit Operations of Chemical... [Pg.281]

Ronald E. Wrolstad Terry E. Acree Eric A. Decker Michael H. Penner David S. Reid Steven 3. Schwartz Charles F. Shoemaker Denise Smith Peter Sporns... [Pg.1380]

Clow, Robert Smith, Peter. 2002. Scandals Help Break the Deal-Drought Life Has Come Back to a Moribund Sector. Financial Times, FT Report on Private Equity, December 12 p. 1. [Pg.415]

Smith, Peter. 2003. Looking to Better Times on the Horizon. Financial Times, Special Report European Private Equity, June 11 pp. I—II. [Pg.416]

Sauer. John C., 3 Schaefer. John P 15 Schorc. Neil E.. 40 Schulenberg, J. W., 14 Schweizer, Edward E., 13 Scott. William J.. 50 Scribner. R. M.. 21 Sccbergcr, Peter H., 68 Semmelhack. Martin F 19 Sengupta, Saumitra, 41 Sethna. Suresh. 7 Shapiro. Robert H.. 23 Sharts, Clay M.. 12. 21 Sheehan, John C.. 9 Sheldon. Roger A.. 19 Sheppard. W. A.. 21 Shibasaki. Masakatsu. 70 Shirley, David A.. 8 Shriner, Ralph L.. I Simmons. Howard E 20 Simonoff, Robert. 7 Slowinski. Franck. 68 Smith, Lee Irvin. I Smith. Peter A. S., 3, 11 Smithers. Roger. 37 Snow. Sheri L 66 Spielman. M. A.. 3 Spoeni, Paul E., 5 Stacey, F. W 13 Stadler. Alexander. 63 Stanforth. Stephen P.. 49. 56 Stetter. Hermann. 40 Struve, W. S., 1 Suter. C. M 3 Swamer. Frederic W.. 8 Swem. Daniel. 7... [Pg.569]

W. H. F. Sasse R. SCHMUTZLER R. E. Schuster James E. Scott Helmut Seidl Lowell R. Smith Peter A. S. Smith A. John Speziale Allan R. Stein Edward C. Taylor Leonard R. Worden Howard E. Zimmerman... [Pg.75]

Warren L. McCabe Julian C. Smith Peter Harriott... [Pg.1135]

Stodola Steam and Gas Turbines, Peter Smith Publishers, p. 312 (Steam Quality). [Pg.17]

Peters, D. C. and Smith, J. M. Trans. Inst. Chem. Eng. 45 (1967) 360. Fluid flow in the region of anchor agitator blades. [Pg.312]

The time required to pass through the high shear zone will be proportional to the volume of the vessel divided by the flow from the turbine. This will be porportional to 1/ND. With a turbine in turbulent flow, turnover is relatively rapid and all the fluid will pass through the impeller region in a relatively short period of time. The flow regime in an anchor or helically agitated vessel can be inferred from the flow studies by Smith and Peters (], 13j. These indicated... [Pg.83]

The streamlines of this flow are shown by Peters and Smith (12). In this case, the effective thickness of this layer appears to be about equal to the gap with the wall, indicating a pressure flow about equal to the drag flow. It can be calculated that this would increase the maximum shear rate on the fluid passing under the agitator blade by a factor of seven. [Pg.84]

Peters, D.C. and Smith, J.M., Trans.Instn. Chem.Engrs. (1967)... [Pg.110]

See other pages where Smith-Peters is mentioned: [Pg.327]    [Pg.581]    [Pg.345]    [Pg.72]    [Pg.1155]    [Pg.1]    [Pg.291]    [Pg.1124]    [Pg.1]    [Pg.327]    [Pg.581]    [Pg.345]    [Pg.72]    [Pg.1155]    [Pg.1]    [Pg.291]    [Pg.1124]    [Pg.1]    [Pg.122]    [Pg.286]    [Pg.69]    [Pg.584]    [Pg.538]    [Pg.110]    [Pg.4]    [Pg.6]    [Pg.8]    [Pg.10]    [Pg.12]    [Pg.14]    [Pg.16]    [Pg.18]    [Pg.20]    [Pg.22]    [Pg.26]    [Pg.28]    [Pg.30]    [Pg.32]    [Pg.34]    [Pg.36]    [Pg.38]    [Pg.40]    [Pg.42]   


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