Big Chemical Encyclopedia

Chemical substances, components, reactions, process design ...

Articles Figures Tables About

The Low-Velocity Burn-Out Regime

The characteristic that has been called the low-velocity regime (M2) would have been observed at a much earlier stage if burn-out data had existed for experiments covering a very wide range of mass velocities with the other system parameters fixed. Even today there is no really good direct example of [Pg.246]

In Fig. 26, the dotted lines correspond to 100% quality at the tube exit and represent the 0/G ratios obtained from the following heat-balance equation for a uniformly heated tube (with k = 1)  [Pg.247]

Because of the closeness of the low-velocity regime to the 100% quality line, it is to be expected that latent heat will be the dominant fluid property controlling burn-out in this regime. In fact, it has been found (M3) that latent heat alone can adequately represent all the low-velocity regime data, which includes pressures ranging from 15 to 2000 psia. For uniformly heated round tubes, for example, the appropriate burn-out equation obtained, based on Eq. (18), is  [Pg.248]

Equation (21) fits the published data belonging to the low-velocity regime (Fig. 27), with an rms error of 5.5 %, and is applicable to any system pressure. [Pg.248]


Fig. 27. Approximate boundary of the low-velocity burn-out regime for water flowing in round tubes. The low-velocity regime lies to the left of any given curve [from Macbeth (M2)]. Fig. 27. Approximate boundary of the low-velocity burn-out regime for water flowing in round tubes. The low-velocity regime lies to the left of any given curve [from Macbeth (M2)].

See other pages where The Low-Velocity Burn-Out Regime is mentioned: [Pg.207]    [Pg.246]   


SEARCH



Velocity, burning

© 2024 chempedia.info