Chemical Engineering Progress

J. Y. Oldshiie, Chemical Engineering Progress, Mixing of Slurries Near the Ultimate Settled Solids Concentration, 77(5) 95-98 (1981). 

Measurement Error Uncertainty in the interpretation of unit performance results from statistical errors in the measurements, low levels of process understanding, and differences in unit and modeled performance (Frey, H.C., and E. Rubin, Evaluate Uncertainties in Advanced Process Technologies, Chemical Engineering Progress, May 1992, 63-70). It is difficult to determine which measurements will provide the most insight into unit performance. A necessary first step is the understanding of the measurement errors hkely to be encountered. 

Verneuil et al. (Verneuil, V.S., P. Yan, and F. Madron, Banish Bad Plant Data, Chemical Engineering Progress, October 1992, 45-51) emphasize the importance of proper model development. Systematic errors result not only from the measurements but also from the model used to analyze the measurements. Advanced methods of measurement processing will not substitute for accurate measurements. If highly nonlinear models (e.g., Cropley s kinetic model or typical distillation models) are used to analyze unit measurements and estimate parameters, the Hkelihood for arriving at erroneous models increases. Consequently, resultant models should be treated as approximations. 

Lovelace, B. G. 1979. Safe Sampling of Liquid Process Streams. Chemical Engineering Progress [Nov]. Also published in Vol. 13, C.E.P. Technical Manual. 

Nimmo, I. 1995. Adequately Address Abnormal Operations. Chemical Engineering Progress, 91(9), 36-45. 

Basn, P.K. and others. Consider Cnstom Synthesis dnring Pharmacentical R D Chemical Engineering Progress, New York December 1998. 

Swearingen, J. S., Turboexpanders and Proeesses Tliat Use Tliem, Chemical Engineering Progress, Vol. 68, No. 7, July 1972. 

Lucenbach, E. C., How to Update a Catalytic Cracking Unit, Chemical Engineering Progress, February 1979. 

Lockhart, R. W., and Martinelli, R. C., Proposed Correlation of Data for Isothermal Two-Phase, Two-Component Plow in Pipes, Chemical Engineering Progress, 45 39 8, 1949. 

Walter, Y. L. and V. H. Edwards, Consider Bottom Venting for Reactive Liquids, Chemical Engineering Progress, June 2000, p. 34. 

Underwood, A. J. V., Fractional Distillation of Multicomponent Mixtures, Chemical Engineering Progress, 44, 603 (1948). 

Shinskey, F. G., Energy-Conserving Control Systems for Distillation Units, Chemical Engineering Progress, May 1976. 

Bojnowski, J. J., Groghan, R. M., Jr., and Hoffman, R. M., Direct and Indirect Material Balance Control, Chemical Engineering Progress, September 1976. 

Figure 8, from Design Data for Thermosiphon Reboilers, by D. C. Lee, J. W. Dorsey, G. Z. Moore F. Drew Mayfield, Chemical Engineering Progress, Vol. 52, No. 4, pp. 160-164 (1956). Reproduced by permission of the American Institute of Chemical Engineers. 1956 AIChE. ... 

Sloley, A. W., Properly Design Thermosyphon Reboilers, Chemical Engineering Progress, March 1997. 

McCarthy, A. J. and Smith, B. R., Reboiler System Design—The Tricks of the Trade, Chemical Engineering Progress, May 1995. 

Kister, H. Z., K. F. Larson and T. Yanagi, How Do Trays and Packing Stack Up Chemical Engineering Progress, February 1994. 

Bravo, J. L., Select Structured Packings or Trays Chemical Engineering Progress, July 1997. 

McPherson, Lori, How Good Are Your Values for Total Dissolved. Solids Chemical Engineering Progress, November, 1995. 

Dolle, J., and Gilboume, D., Startup of the Skikda LNG Plant, Chemical Engineering Progress, January 1976, p. 39. 

Kirby. G. N., Avoid Common Corrosion Mistakes for Better Performance, Chemical Engineering Progress, April 1997. 

Shah, G. C., Troubleshooting Reboiler Systems, Chemical Engineering Progress, July 1979, p. 53. 

Hasbrouck, J. F., J. G. Kinesh and V. C. Smith, Successfully Troubleshoot Distillation Tow ers, Chemical Engineering Progress, March 1993. 

Dyess. C. E., Putting a 70,000 bbl/day Crude Still Onstream, Chemical Engineering Progress, August 1973, p. 98. 

Benedict, Manson, Webb, George B., and Rubin, Louis C., An Empirical Equation for Thermodynamic Properties of Light Hydrocarbons and Then Mixtures, Chemical Engineering Progress, Vol. 47, No. 8, August, 195 I pp. 419-422. 

A. Hougen and K. M. Marshall Adsorption from a Fluid Stream Flowing Through a Stationary Granular Bed, Chemical Engineering Progress, 43 197 (1967). 

M. M. Mattia Process for Solvent Pollution Control, Chemical Engineering Progress, 66(12) 74-79 (Dec. 1970). 

Palen, J. W. and Taborek, J., Solution of Shell-Side Flow Pressure Drop and Heat Transfer by Stream Analysis Method (Heat Transfer Research, Inc., Alhambra, CA), AICHE Chemical Engineering Progress Symposium Series No. 92, Vol. 65 (1969), pp. 53-63. 

Agreda, V. H., L. R. Partin, and W. H. Heise (1990). High-Purity Methyl Acetate Via Reactive Distillation. Chemical Engineering Progress (February), 40-46. 

Burch, W. M. (1986). Process Modifications and New Chemicals. Chemical Engineering Progress (April), 5-8. 

The Design of Inherently Safer Plants (1988). Chemical Engineering Progress (September), 21. 

Englund, S. M. (1991a). Design and Operate Plants for Inherent Safety—Part 1. Chemical Engineering Progress (March), 85-91. 

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