Page 376 - Analysis, Synthesis and Design of Chemical Processes, Third Edition
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tower, return at 45–52°C (115–125°F); return seawater at 43°C (110°F); return tempered water
                                or steam condensate above 52°C (125°F).
                          10.   Cooling air supply at 29–35°C (85–95°F); temperature approach to process, 22°C (40°F).
                          11.   Compressed air 3.1 (45), 10.3 (150), 20.6 (300), or 30.9 barg (450 psi) levels.
                          12.   Instrument air at 3.1 barg (45 psig), –18°C (0°F) dew point.
                                                              3
                          13.   Fuels: gas of 37,200 kJ/m  (1000 Btu/SCF) at 0.35–0.69 barg (5–10 psig), or up to 1.73 barg
                                                                                               3
                                (25 psig) for some types of burners; liquid at 39.8 GJ/m  (6 million Btu/bbl).
                          14.      Heat  transfer  fluids:  petroleum  oils  less  than  315°C  (600°F),  Dowtherms  less  than  400°C
                                (750°F), fused salts less than 600°C (1100°F), direct fire or electricity above 450°F.
                          15.   Electricity: 0.75–74.7 kW. (1–100 hp), 220–550 V; 149–1864 kW (200–2500 hp), 2300–4000
                                V.



                    (Adapted  from  S.  M.  Walas, Chemical  Process  Equipment:  Selection  and  Design,  Stoneham,  MA:
                    Butterworth, 1988. Copyright © 1988 by Butterworth Publishers, adapted by permission of Butterworth
                    Publishers, Stoneham, MA. All rights reserved)


                    References





                                  1. Koen, B. V.,  Definition of the Engineering Method (Washington, DC: American Society
                                     for Engineering Education, 1985).


                                  2. Sieder, E. N., and G. E. Tate, “Heat Transfer and Pressure Drop of Liquids in Tubes,”
                                     Ind. Eng. Chem. 28 (1936): 1429.


                                  3.  Walas,  S.  M., Chemical  Process  Equipment:  Selection  and  Design  (Stoneham,  MA:
                                     Butterworths, 1988).


                    Problems






                       For the ethylbenzene process shown in Appendix B, check the design specifications for the following
                    1. three pieces of equipment against the appropriate heuristics: P-301, V-302, T-302. Comment on any
                       significant differences that you find.


                       For the styrene process shown in Appendix B, check the design specifications for the following three
                    2. pieces of equipment against the appropriate heuristics: E-401, C-401, T-402. Comment on any
                       significant differences that you find.


                       For the drying oil shown in Appendix B, check the design specifications for the following three pieces

                    3. of equipment against the appropriate heuristics: V-501, P-501, H-501. Comment on any significant
                       differences that you find.
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