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Plug continuous

Some time later the conditions shown in Figure 2,E, exist. The ice plugs continue to move upward as before. However, air is permitted to enter the /bottom of the tube, so that as the bottom plug melts, the outside level of the reservoir is maintained within the tube, and purified water overflows. [Pg.80]

When the air space has reached the desired volume as shown in Figure 2,F, the air inlet is closed and the plugs continue to move upward, concentrating the saline water. [Pg.80]

Multiple reactions in parallel producing byproducts. Consider again the system of parallel reactions from Eqs. (2.16) and (2.17). A batch or plug-flow reactor maintains higher average concentrations of feed (Cfeed) than a continuous well-mixed reactor, in which the incoming feed is instantly diluted by the PRODUCT and... [Pg.29]

In general terms, if the reaction to the desired product has a higher order than the byproduct reaction, use a batch or plug-flow reactor. If the reaction to the desired product has a lower order than the byproduct reaction, use a continuous well-mixed reactor. [Pg.30]

But what is the correct choice a byproduct reaction calls for a continuous well-mixed reactor. On the other hand, the byproduct series reaction calls for a plug-flow reactor. It would seem that, given this situation, some level of mixing between a plug-flow and a continuous well-mixed reactor will give the best... [Pg.31]

A series combination of plug-flow and continuous well-mixed reactors (Fig. 2.3c and d)... [Pg.33]

Polymerization reactions. Polymers are characterized by the distribution of molecular w eight about the mean as well as by the mean itself. The breadth of this distribution depends on whether a batch or plug-flow reactor is used on the one hand or a continuous well-mixed reactor on the other. The breadth has an important influence on the mechanical and other properties of the polymer, and this is an important factor in the choice of reactor. [Pg.33]

Solution We wish to avoid as much as possible the production of di- and triethanolamine, which are formed by series reactions with respect to monoethanolamine. In a continuous well-mixed reactor, part of the monoethanolamine formed in the primary reaction could stay for extended periods, thus increasing its chances of being converted to di- and triethanolamine. The ideal batch or plug-flow arrangement is preferred, to carefully control the residence time in the reactor. [Pg.50]

Continuous well-mixed reactors to plug-flow... [Pg.271]

The first distinction to be drawn, as far as heat transfer is concerned, is between the plug-flow and continuous well-mixed reactor. In the plug-flow reactor shown in Fig. 13.1, the heat transfer can take place over a range of temperatures. The shape of the profile depends on... [Pg.326]

If samples are introduced batchwise, then the sample enters the flame as a plug and the elements are measured transiently. If the samples are introduced continuously, then the measurement of isotope ratios can also be continuous as long as sample is flowing into the flame. [Pg.396]


See other pages where Plug continuous is mentioned: [Pg.1720]    [Pg.182]    [Pg.404]    [Pg.2045]    [Pg.532]    [Pg.74]    [Pg.110]    [Pg.2033]    [Pg.1724]    [Pg.1720]    [Pg.182]    [Pg.404]    [Pg.2045]    [Pg.532]    [Pg.74]    [Pg.110]    [Pg.2033]    [Pg.1724]    [Pg.29]    [Pg.29]    [Pg.31]    [Pg.33]    [Pg.33]    [Pg.34]    [Pg.34]    [Pg.52]    [Pg.263]    [Pg.2472]    [Pg.51]    [Pg.471]    [Pg.471]    [Pg.55]    [Pg.167]    [Pg.240]    [Pg.287]    [Pg.312]    [Pg.21]    [Pg.140]    [Pg.195]    [Pg.432]    [Pg.69]    [Pg.331]    [Pg.97]    [Pg.431]   
See also in sourсe #XX -- [ Pg.767 ]




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