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366 Applied Process Design for Chemical and Petrochemical Plants
T = temperature absolute, ºR = 460 ºF. 15. Starling, K. D., Fluid Thermodynamic Properties for Light Petro-
TR = ton of refrigeration. leum Systems, Gulf Publishing Co. (1973).
t = temperature, ºF. 16. “Technical Bulletin Freon” No. RT-11, E. I. DuPont de
t e = saturation temperature of economizer vapor. Nemours and Co., Inc., Wilmington 98, Del. (1957).
t = temperature difference, ºF. 17. Wert, O. B. and J. E. Garlach, “Ammonia Reciprocating Com-
2
U = overall heat transfer coefficient, Btu/hr(ft ) (ºF). pressors,” Air Conditioning, Heating and Ventilating, p. 89, May
3
v = specific volume, ft /lb. (1959).
W = system flow rate, lb/hr. 18. York Ammonia Absorption Systems, Bul. 40454-2, York Corp.,
w = vapor flow, lb/min. York, PA (1940).
w e = vapor from economizer, lb/min. 19. Zulinke, A., “Economizer Improves Refrigeration Cycle,”
X c1 = composition of liquid being condensed at the top. Refrigeration Engineering, p. 37, Dec. (1958).
X c2 = composition of liquid being condensed. 20. ASHRAE Handbook, Fundamentals, American Society of Heat-
X e = mol fraction of the same component in the liquid in ing, Refrigerating and Air Conditioning Engineers, Inc.
evaporator. (1977–1978)
Y e = mol fraction of one component in the evaporator 21. Scheel, L. F., Gas Machinery, Gulf Publishing Co. (1972)
vapor. 22. Timmerhaus, K. C. and T. M. Flynn, “Cryogenics” chapter, Ency-
clopedia of Chemical Processing and Design, Marcel Dekker, Inc.,
Subscripts V. 13 (1981)
23. Bogart, M., Ammonia Absorption Refrigeration in Industrial
M = mixture.
Processes, Gulf Publishing Co., Houston, Texas, (1981), all
e = economizer.
rights reserved; also see J. Swearingen, Chem. Eng. Prog., Amer-
1,2,3, etc. = reference points to specific conditions of a system.
ican Institute of Chemical Engineers, V. 68, No. 7 (1972). All
rights reserved.
References
24. Refrigeration and Air Conditioning, Air Conditioning and
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