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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
                         1.  Short, B. E., (Ed.),  Air Conditioning Refrigerating Data Book  Refrigeration Institute, Prentice Hall, Inc. (1979)
                                        th
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                         7.  Jordan, R. C. and G. B. Priester, Refrigeration and Air Condi-  31. “Refrigeration Compressors,” Specifying Engineer, p. 111, Sept.
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                         8.  Mehra, Y. R., “How to Estimate Power and Condenser Duty  McGraw-Hill, Inc., V. 102, No. 1, p. 65 (1995). All rights
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                         9.  Mehra, Y. R., “Refrigerant Charts for Propylene Systems,”           Bibliography
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