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Thermosyphon circulation natural

In a thermosyphon or natural-circulation reboiler, there is, of course, no source of air. The aerated liquid is a froth or foam, produced by the vaporization of the reboiler feed. Without a source of heat, there can be no vaporization. And without vaporization, there will be no circulation. So we can say that the source of energy that drives the circulation in a thermosyphon reboiler is the heating medium to the reboiler. [Pg.46]

Figure 5.6 shows a once-through forced-circulation reboiler. Such a reboiler differs from a thermosyphon reboiler in that it has a pump to force circulation, rather than rely on natural or thermosyphon circulation. This seems rather wasteful—and it is. [Pg.53]

When considering the steam side of steam heated reboilers, it is best to think about the reboiler as a steam condenser. The steam, at least for a conventional horizontal reboiler, is usually on the tube side of the exchanger, as shown in Fig. 8.1. The steam is on the tube side, because the shell side was selected for the process fluid. If the reboiler is a thermosyphon, or natural-circulation reboiler, then low-process-side pressure drop is important. For a horizontal reboiler, it is easiest to obtain a low pressure drop for the fluid being vaporized by placing it on the shell side. [Pg.88]

During vaporization or condensation, thermal and hydraulic performances depend essentially on the two-phase flow structure. Furthermore, as very often in industrial processes, the heat exchanger operates in thermosyphon or under natural circulation knowledge of the pressure drop and liquid holdup is of major importance. But there is very little information on two-phase flow characteristics in compact geometries. [Pg.154]

Heat removal through thermosyphon driven natural circulation under both normal operation and hot shut down condition ... [Pg.146]

Thermosyphon circulation (or natural circulation) Partially vaporizing a liquid causes it to flow to a higher elevation. The driving force is the density difference between the denser liquid feed and the less dense, partly vaporized effluent. [Pg.20]

I worked as a process design engineer for Amoco Oil in Chicago until 1980. Likely, I designed about 50 distillation columns, 90 percent of which had horizontal, natural thermosyphon circulation reboilers. [Pg.3]


See other pages where Thermosyphon circulation natural is mentioned: [Pg.304]    [Pg.729]    [Pg.45]    [Pg.726]    [Pg.2459]    [Pg.332]    [Pg.304]    [Pg.78]    [Pg.85]    [Pg.138]    [Pg.559]    [Pg.67]    [Pg.150]    [Pg.3]    [Pg.3]    [Pg.3]   


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