Page 186 - APPLIED PROCESS DESIGN FOR CHEMICAL AND PETROCHEMICAL PLANTS, Volume 1, 3rd Edition

Fluid Flow 159

Simpson, L. L. and Weirick, M. L., "Designing Plant Piping," Yu, F. C., "How to Calculate Optimum Pipe Size for Liquids,"
Chem. Eng. Deskbook, April 3, 1978, p. 33. Hydrocarbon Processing, vol. 72, no. 6,June 1993, p. 67.
Soliman, R. H. and Collier, P. B., "Pressure Drop in Slurry Lipton, S., "Reduce fugitive Emissions Through Improved
Lines," Hydrocarbon Processing, vol. 69, no. 11, 1990, p. 60. Process Equipment," Chemical Engineering Progress, vol. 88, no.
Cheng, X. X. and Turton, R., "How to Calculate Pipe Size With- 10, Oct. 1992, p. 61.
out Iteration," Chem. Eng., vol. 97, no. 11, 1990, p. 187.
Doolin,J., Kawohl, R., McGuire,]. T., Prang, A., and Dodson. ].,
Morrison, G. L., DeOue, R. E., Panak, D. L., and Nail, G. H., "Pumping Difficult Fluids," Chemical Engineering, vol. 98, no .
"The Flow Field Inside an Orifice Flow Meter," Chem. Eng. 12, Dec. 1991, p. 67.
Prog., vol. 86, no. 7, 1990, p. 75.
Tosun. I. and Aksahin, L "Calculate Critical Piping Parameters,"
Hooper, W. B., "The Two-K Method Predicts Head Losses in Chemical Engineering. vol. 100, no. 3, March 1993. p. 165.
Pipe Fittings." Chemical Engineering, Aug. 24, 1981, p. 96.
Hughson, R. V., "Plumb the Power of Piping Programs," Chem.
Landis, R. L., "Solve flashing-fluid critical-flow problems," Chem- Eng. Prag., vol. 88, no. 6,June 1992, p. 95.
ical Engineering, March 8, 1982, p. 79.
Grown, N. P. and Heyood, N. I., "The Right Instrumentation for Mills, D., "Troubleshooting Pneumatic Conveying. Parts I and
Slurries," Chemical Engineering, vol. 99, no. 9, Sept. 1992, p. l 06. 2," Chem. Eng., vol. 97, nos. 6 and 7,June and july 1990.
Beasley, M. E., "Choosing Valves for Slurry Service," Chemical Kroupa, R., "Selecting Valves for Tough Conditions," Chem. Eng.,
Engineering, vol. 99, no. 9, Sept. 1992, p. 112. vol. 100, no. 2, Feb. 1993, p. 74.