Page 64 - APPLIED PROCESS DESIGN FOR CHEMICAL AND PETROCHEMICAL PLANTS, Volume 1, 3rd Edition

Process Planning, Scheduling and Flowsheet Design 49
s

Plant Black Limit Lines
..---P- la-nl-B- lo- ck_ 9 _ ___,.___, New Steam Line � .....c..-P_l_ on_f_B_ lo_c_k_l6---
----
to Storaqe Tanks
Water Account No.6001
Distribu1ion
Account No.6013 New 50% Caustic
Caustic Transfer Line
Pion!
Bldg.No.96
Additional Evoporotion
Capacity Pl us In-Pion I Dock 3
Storage. Also All Intra-
Block Service Lines, Figure 1-41. Account diagram for accumulation of
Account No. 6014
project costs. Cost estimates must be made to con-
form to same scope basis.

the process engineer present proper breakdown details, 18. Warren, C. W., "How to Read Instrument Flow Sheets, Part I
and these then serve to coordinate the cost breakdowns. and II," Hydrocarbon Processing 54, No. 7, 1975, p. 163 and No.
Figure 1-41 is an example of such an accounting diagram. 9, 1975, p. 191.
19. Ludwig, E. E., Applied Project Engi:neering and Management, 2nd
Ed., Gulf Publishing Co., Houston, Texas, 1988.
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