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Miller Plant Cost Estimation

Other multiple-factor methods that have been published in the past are those by C. E. Chilton, Cost Estimation in the Process Industries, McGraw-Hill, New York, I960 M. S. Peters, K. D. Timmerhaus, and R. E. West, Plant Design and Economics for Chemical Engineers, 5th ed., McGraw-Hill, New York, 2003 C. A. Miller, Chemical Engineering, Sept. 13,1965, pp. 226-236 and P. A. Holland, P. A. Watson, and V. K. Wilkinson, Chem. Eng., Apr. 1,1974, pp. 71-76. These methods produced preliminary quality estimates. Most companies have developed their own in-house multiple-factor methods for preliminary cost estimation. [Pg.15]

Miller claims that if the basic equipment estimate has an accuracy of 10%, the most likely plant estimate should have an accuracy of 14%. This is much better than the ratio or Lang estimates, and considerably more accurate than Nichols said was possible with this type of data. 12 He claimed that there is a direct correlation between the cost of an estimate and its probable accuracy. Ever since he stated this in 1951, cost engineers have been trying to prove him wrong. [Pg.254]

The major economic issue in whether succinic acid can compete is the low starting cost of petrochemical raw materials. The target cost for succinic acid from a bioprocess is estimated to be around 0.25/lb for a large-scale plant (Zeikus et al. 1999 Varadarajan and Miller 1999). This target cost is necessary to compete with low-cost petrochemical raw materials. [Pg.50]


See other pages where Miller Plant Cost Estimation is mentioned: [Pg.184]    [Pg.184]    [Pg.252]    [Pg.191]    [Pg.191]    [Pg.252]    [Pg.22]   
See also in sourсe #XX -- [ Pg.249 ]

See also in sourсe #XX -- [ Pg.249 ]




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