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Thin-film continuous-flow discussion

Two approaches based on fast-atom bombardment (FAB) and introduced almost simultaneously were soon after their first description in 1985 and 1986 commercialized, i.e., the frit-FAB [80] and the continuous-flow Cf-FAB [81]. Both systems are used to introduce part of the column effluent (typically 1-10 pl/min) into a FAB somce. In the frit-FAB system, a capillary transfers the effluent to a stainless-steel or PFTE frit used as a FAB target, while in Cf-FAB system the effluent flows in a thin uniform film over the FAB target. A suitable FAB matrix, e.g., glycerol, should be added to the mobile phase. Analyte molecules are directly desorbed and ionized from the hqtrid film by FAB. These approaches are discussed in Ch. 4.6. [Pg.62]

However, the curve of the sphere drag coefficient has some marked differences from the friction factor plot. It does not continue smoothly to higher and higher Reynolds numbers, as does the / curve instead, it takes a sharp drop at an of about 300,000. Also it does not show the upward jump that characterizes the laminar-turbulent transition in pipe flow. Both differences are due to the different shapes of the two systems. In a pipe all the fluid is in a confined area, and the change from laminar to turbulent flow affects all the fluid (except for a very thin film at the wall). Around a sphere the fluid extends in all directions to infinity (actually the fluid is not infinite, but if the distance to the nearest obstruction is 100 sphere diameters, we may consider it so), and no matter how fast the sphere is moving relative to the fluid, the entire fluid cannot be set in turbulent flow by the sphere. Thus, there cannot be the sudden laminar-turbulent transition for the entire flow, which causes the jump in Fig. 6.10. The flow very near the sphere, however, can make the sudden switch, and the switch is the cause of the sudden drop in Q at =300,(300. This sudden drop in drag coefficient is discussed in Sec. 11.6. Leaving until Chaps. 10 and 11 the reasons why the curves in Fig. 6.22 have the shapes they do, for now we simply accept the curves as correct representations of experimental facts and show how to use them to solve various problems. [Pg.225]


See other pages where Thin-film continuous-flow discussion is mentioned: [Pg.343]    [Pg.343]    [Pg.498]    [Pg.343]    [Pg.114]    [Pg.26]    [Pg.477]    [Pg.158]    [Pg.731]    [Pg.168]    [Pg.168]    [Pg.787]    [Pg.205]    [Pg.1278]    [Pg.189]    [Pg.354]    [Pg.298]    [Pg.121]    [Pg.415]    [Pg.818]   
See also in sourсe #XX -- [ Pg.170 ]




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Thin-film continuous-flow

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