By L S Tong
This can be a first-class publication to have for an engineer who take care of two-phase flows and warmth move, if you layout and function nuclear reactors, thermal strength crops and different thermal administration platforms. It presents a origin, with an intensive number of empirical formulae that can be valuable if effectively utilized. What feels lacking during this ebook, - and is normal function of BOOKS on two-phase flows and boiling - is the heavy empiricism, the inability of a systematic thought, the absence of strong theoretical therapy that one may still own after studying this kind of complete compilation. that's to assert, it really is solid for a few one that understands the subject/field, now not for educating anyone approximately boiling warmth move and two-phase flows.
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Extra resources for Boiling heat transfer and two-phase flow
Assuming the perfect gas law, (2- 1 8) where n� is the number of moles of inert gas in the cavity, T� is the absolute temper ature of the cavity environment, and V' is the volume of the cavity at maximum penetration conditions, Eq. (2- 1 7) can be written as (Dwyer, 1 976) , PL where _ , PG _ f T� _ 2 a' ' (r )3 - r' (2- 1 9) POOL BOILING 19 f = 3n�R(tan �/2 ) 1T[COS( �/2 + a)p The value of f depends on the characteristics of the particular surface liquid sys tem , the amount of inert gas trapped in the cavity, and the maximum penetration conditions.
01 7-in. 0 1 7 in. 085 in. 0 mm). Although all the above experimental results were obtained with cylindrical cavities, conical cavities would probably give the same results, as long as \fI/2 <
PL + YG r (2-1 6) Under the conditions for deepest liquid penetration, Eq. g. = r , (2- 1 7) where the primes represent the conditions of maximum boiling suppression. Dwyer ( 1 969) extended Holtz 's concept and not only related r at incipient boiling to r ' at maximum boiling suppression but also related Pi . g. to P ; g . As a result, he was able to achieve simultaneous solutions of Eqs. (2-3) and (2- 1 7) on a more realistic basis. Assuming the perfect gas law, (2- 1 8) where n� is the number of moles of inert gas in the cavity, T� is the absolute temper ature of the cavity environment, and V' is the volume of the cavity at maximum penetration conditions, Eq.