Page 264 - Chemical engineering design

PIPING AND INSTRUMENTATION
NEERKIN, R. F. (1974) Chem. Eng., NY 81 (Feb. 18) 104. Pump selection for chemical engineers.
NOLTE, C. B. (1978) Optimum Pipe Size Selection (Trans. Tech. Publications). 239
PARKINS, R. (1959) Chem. Eng. Prog. 55 (July) 60. Continuous distillation plant controls.
PEARSON, G. H. (1978) Valve Design (Mechanical Engineering Publications).
PERRY, R.H.and CHILTON, C. H. (eds) (1973) Chemical Engineers Handbook, 5th edn (McGraw-Hill).
PERRY,R. H., GREEN,D. W. and MALONEY, J. O. (eds) (1997) Perry’s Chemical Engineers’ Handbook,7th
edn. (McGraw-Hill).
PETERS,M. S. and TIMMERHAUS, K. D. (1968) Plant Design and Economics for Chemical Engineers, 2nd edn
(McGraw-Hill).
PETERS,M. S. and TIMMERHAUS, K. D. (1991) Plant Design and Economics, 4th edn (McGraw-Hill).
RASE, H. F. (1953) Petroleum Refiner 32 (Aug.) 14. Take another look at economic pipe sizing.
RASMUSSEN, E. J. (1975) Chem.Eng.,NY 82 (May 12th) 74. Alarm and shut down devices protect process
equipment.
SHERWOOD, D. R. (1991) The Piping Guide, 2nd edn (Spon.).
SHINSKEY, F. G. (1976) Chem. Eng. Prog. 72 (May) 73. Energy-conserving control systems for distillation units.
SHINSKEY, F. G. (1984) Distillation Control, 2nd edn (McGraw-Hill).
SHINSKEY, F. G. (1996) Process Control Systems, 4th edn (McGraw-Hill).
SIMPSON, L. L. (1968) Chem. Eng., NY 75 (June 17th) 1923. Sizing piping for process plants.
SMITH,E. and VIVIAN, B. E. (1995) Valve Selection (Mechanical Engineering Publications).
SMITH,P. and ZAPPE, R. W. (2003) Valve Selection Handbook, 5th edn (Gulf Publishing).
WALAS S. M. (1990) Chemical Process Equipment (Butterworth-Heinemann).
WEBSTER, G. R. (1979) Chem. Engr. London No. 341 (Feb.) 91. The canned pump in the petrochemical
environment.

British Standards
BS 806: 1986 Ferrous pipes and piping for and in connection with land boilers.
BS 1600: 1991 Dimension of steel pipes for the petroleum industry.
BS 1646: 1984 Symbolic representation for process measurement control functions and instrumentation.
Part 1: 1977 Basic requirements.
Part 2: 1983 Specifications for additional requirements.
Part 3: 1984 Specification for detailed symbols for instrument interconnection diagrams.
Part 4: 1984 Specification for basic symbols for process computer, interface and shared display/control
functions.

American Standards

USAS B31.1.0: The ASME standard code for pressure piping.
ASA B31.3.0: The ASME code for petroleum refinery piping.

5.12. NOMENCLATURE

Dimensions
in MLT£
A Plant attainment (hours operated per year)
B Purchased cost factor, pipes £L 1
a Capital charges factor, piping
b Maintenance cost factor, piping
T
Cf Annual pumping cost, piping £L 1 1
Cp Capital cost, piping £L 1
T
Ct Total annual cost, piping £L 1 1
d Pipe diameter L
d i Pipe inside diameter L
E Pump efficiency
e Relative roughness