2004
DOI: 10.1016/j.ijheatfluidflow.2003.08.003
|View full text |Cite
|
Sign up to set email alerts
|

Vertically upward two-phase flow with a highly viscous liquid-phase in a nozzle and orifice plate

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
3
1
1

Citation Types

0
5
0
1

Year Published

2007
2007
2022
2022

Publication Types

Select...
7
1

Relationship

0
8

Authors

Journals

citations
Cited by 11 publications
(7 citation statements)
references
References 15 publications
0
5
0
1
Order By: Relevance
“…Evaluation of for the intrinsic permeability values of metal foams (Table 1), and the compressibility and viscosity of mineral oil, k f = 1.5 GPa [11] and η f = 450 mPas [16], respectively, clearly shows that the pore pressure inside the tested titanium samples is built up within a small fraction of 1 s. This holds even for the intrinsic permeability values of bone (Table1) which are lower than the one for metal foams. Hence, during the mechanical experiments, lasting typically 10 min, the pore pressure is always quasi‐identical to the oil pressure built up in the pressure cell.…”
Section: Mechanical Testingmentioning
confidence: 99%
“…Evaluation of for the intrinsic permeability values of metal foams (Table 1), and the compressibility and viscosity of mineral oil, k f = 1.5 GPa [11] and η f = 450 mPas [16], respectively, clearly shows that the pore pressure inside the tested titanium samples is built up within a small fraction of 1 s. This holds even for the intrinsic permeability values of bone (Table1) which are lower than the one for metal foams. Hence, during the mechanical experiments, lasting typically 10 min, the pore pressure is always quasi‐identical to the oil pressure built up in the pressure cell.…”
Section: Mechanical Testingmentioning
confidence: 99%
“…Experiments allowed us to obtain mean film thickness and velocity inside the channel. It is shown that film velocity both for ethanol and dodecane increases from 0.2 m/s for Regas = 3.5⋅10 4 up to 0.8 m/s for Regas = 3.3⋅10 5 , where Reynolds number Regas is calculated by the critical diameter of the nozzle. Measured data for ethanol and dodecane film thickness are shown in Fig.…”
Section: Resultsmentioning
confidence: 99%
“…Currently there are no complete studies with accurate and reliable data on the values of shearing stress on the gas-liquid interface under the condition of high relative velocities of gas flow. Existing experimental studies are focused on the measurement of flow integral characteristics and averaged parameters of waves without taking their non-stationary character into consideration [4,5].…”
Section: Introductionmentioning
confidence: 99%
“…Royne 14 and Brignoni 15 analyzed the nozzle pressure drop caused by water and air through different nozzles, respectively, and found that nozzle diameter, length, and chamfer angle were crucial factors for nozzle pressure drop. McNeil 16 disclosed the influence of air with different viscosities and liquids on the nozzle pressure drop. In the hope of improving the performance of jet pumps, researchers have done extensive work from the perspectives of decreasing the pressure drop, analyzing the structure, and optimizing the evaluation methods such as aeration and mixing.…”
Section: Introductionmentioning
confidence: 99%