By A. Kayode Coker
The fourth variation of Ludwig’s utilized method layout for Chemical and Petrochemical crops, quantity Three is a middle reference for chemical, plant, and method engineers and offers an unrivalled reference on tools, technique basics, and assisting layout facts. New to this variation are improved chapters on warmth move plus extra chapters thinking about the layout of shell and tube warmth exchangers, double pipe warmth exchangers and air coolers. warmth tracer requisites for pipelines and warmth loss from insulated pipelines are lined during this re-creation, besides batch heating and cooling of technique fluids, strategy integration, and commercial reactors. The ebook additionally seems to be on the troubleshooting of approach apparatus and corrosion and metallurgy.
- Assists engineers in quickly interpreting difficulties and discovering potent layout equipment and mechanical requisites
- Definitive consultant to the choice and layout of varied gear kinds, together with warmth exchanger sizing and compressor sizing, with confirmed layout codes
- Batch heating and cooling of technique fluids supported through Excel programs
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Additional info for Ludwig’s Applied Process Design for Chemical and Petrochemical Plants
Example text
0 TP 310 Stn. Stl. Stl. 43 Continued Heat Transfer Chapter | 15 17-19 Cr (TP 439) 44 W/m C Temp. 6 Ni-Fe-Cr-Mo-Cu (N08825) W/m C Temp. I. 6 Al-6XN (N08367) References ASME Sect. VIII, Div. 2, 1998 Edition Huntington Alloy Inc. Bul. E. Tech. Publication Nos. 291, 360 & 648 Babcock & Wilcox Co. American Brass Co. Teledyne Wah Chang Albany Airco, Inc. Trans. T. Vol. 21 pp. 1061-1078 Cabot-Stellite Carpenter Technology International Nickel Co. , Table D-12, © 1999 and 1991. 9 FIGURE 15-14 Tube-side pass arrangements.
The tube-side fluid enters one end of the exchanger and leaves from the opposite end. Generally, these baffles are not as convenient from a connecting pipe arrangement viewpoint as units with an even number of passes, in which the tube-side fluid enters and leaves at the same end of the exchanger. See Figures 15-1C and 15-1G and Table 15-1. Two-pass tube-side. For these conditions one head end baffle is usually in the center, and no baffle is in the return end, as the fluid will return through the second pass of itself.
The K shell is a special cross-flow shell used for kettle reboilers with an integral vapor disengagement space in the shape of an enlarged shell. A U-tube bundle (AKU) can be used if the heating fluid is steam. However, if the fouling stream is used as the heating medium, a pull-through, TEMA T type floating head bundle would be appropriate. One of the advantages of the kettle type reboiler over the stab-in bundle is that the heat transfer surface area is unlimited; therefore it can be designed for any heat load to the tower.