𝔖 Bobbio Scriptorium
✦   LIBER   ✦

Effects of molecule number on nucleate boiling in a system

✍ Scribed by Yong Tian; Xiao-Dong Wang; Xiao-Feng Peng


Publisher
John Wiley and Sons
Year
2005
Tongue
English
Weight
86 KB
Volume
34
Category
Article
ISSN
1099-2871

No coin nor oath required. For personal study only.

✦ Synopsis


Canonical molecular distribution was introduced to analyze characteristics of nucleate boiling when the liquid molecular number is very small. The minimum bulk phase volume in which phase change was able to occur was determined from the thermodynamic theory of bubble formation in a superheated liquid and from the energy distribution of the molecules in the bulk phase at a given temperature and pressure. The energy level of active molecules nearly independently distributing in systems was determined from conservation of mass. The maximum superheat temperature necessary for boiling nucleation was found to relate to the bulk phase volume with the temperature increasing as the volume decreased.


πŸ“œ SIMILAR VOLUMES


On the Number of Blocks in a Generalized
✍ J.H van Lint πŸ“‚ Article πŸ“… 1997 πŸ› Elsevier Science 🌐 English βš– 208 KB

We consider t-designs with \*=1 (generalized Steiner systems) for which the block size is not necessarily constant. An inequality for the number of blocks is derived. For t=2, this inequality is the well known De Bruijn Erdo s inequality. For t>2 it has the same order of magnitude as the Wilson Petr

Effect of a second ethylene molecule on
✍ A. MuΓ±oz-Escalona; J. Ramos; V. Cruz; J. MartΓ­nez-Salazar πŸ“‚ Article πŸ“… 2000 πŸ› John Wiley and Sons 🌐 English βš– 310 KB πŸ‘ 2 views

The PM3(tm) semiempirical method was used to show the effect of a second ethylene molecule in the backside position on the frontside ethylene insertion in the Cp 2 ZrO n Pr Ο© β₯-agostic resting state. The same calculations without a companion second ethylene molecule were performed to compare geometr

Reynolds number and impeller diameter ef
✍ C. Galletti; A. Paglianti; K. C. Lee; M. Yianneskis πŸ“‚ Article πŸ“… 2004 πŸ› American Institute of Chemical Engineers 🌐 English βš– 597 KB

## Abstract Flow instability phenomena in stirred vessels were studied with laser anemometry and flow visualization. The effects of fluid density and viscosity, impeller Reynolds number (__Re__), impeller design, diameter, and off‐bottom clearance were investigated in order to quantify the frequenc