Effects of coolant volatility on simulated HCDA bubble expansions. [LMFBR]

Tobin, R.J.

doi:10.2172/5338773

Search citation statements

Order By: Relevance

Paper Sections

Select...

(3)1

Citation Types

Supporting

Mentioning

Contrasting

Year Published

1983

Publication Types

Select...

Article1

Relationship

Self Cite0

Independent1

Authors

Journals

Cited by 1 publication

(1 citation statement)

References 0 publications

Supporting

Mentioning

Contrasting

Order By: Relevance

“…The relative penetration velocity was correlated by (5) with a large data spread. Cagliostro et al (1978) studied the effects of vessel internal structures on the work potential of hypothetical core disruptive accidents in a 1/30-scale model of a demonstration size liquidmetal fast breeder reactor. Their conclusion was that Taylor instability appears to be the dominant mechanism for coolant en-vb = 0.54~0 332f0 27…”

Section: (3)mentioning

confidence: 99%

Nonlinear taylor instability of a plane interface between two incompressible fluids with interfacial mass transfer

Chang

Bankoff

1983

AIChE Journal

View full text Add to dashboard Cite

Evanston, IL 60201 such as have occurred in the LNG, aluminum, steel and paper industries, is thought to be nonlinear Taylor instability. An analysis, based on a generalized coordinate method developed by Dienes for a fluid with an arbitrary constitutive law, is here extended to a two-fluid model, with or without mass transfer between the fluids. Numerical results indicate that in a steam-water system entrainment starts in times of order 10-4s at 100 G acceleration normal to the interface. For gas-liquid systems the presence of the second fluid changes the instability growth only slightly. Condensation of steam, even when limited only by the kinetic theory interfacial resistance, also has minor effects on the growth rate. However, condensation on the entrained drops will have a major effect on the acceleration, January, 1983

show abstract

Section: (3)mentioning

confidence: 99%