1969
DOI: 10.1299/jsme1958.12.1099
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Thrust of Poppet Valve

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Cited by 17 publications
(14 citation statements)
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“…The chamfered popped study took into account the length of the cone seat, deducing that as the length increased for a constant cone valve was found to be less prone to cavitation than the sharp-edged one, which di ered from that found by angle, the Reynolds number also had to increase to achieve turbulent ow. Also, as the cone angle increased, Urata [2] who showed experimentally and analytically that cavitation was more likely to occur when using the Reynolds number had to increase to achieve turbulent ow. The uid used was a chemical mixing between chamfered seats.…”
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confidence: 99%
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“…The chamfered popped study took into account the length of the cone seat, deducing that as the length increased for a constant cone valve was found to be less prone to cavitation than the sharp-edged one, which di ered from that found by angle, the Reynolds number also had to increase to achieve turbulent ow. Also, as the cone angle increased, Urata [2] who showed experimentally and analytically that cavitation was more likely to occur when using the Reynolds number had to increase to achieve turbulent ow. The uid used was a chemical mixing between chamfered seats.…”
mentioning
confidence: 99%
“…This paper gave an introduction to previous work and pointed out that putational uid dynamics (CFD) simulation for a range of conical seat valve geometries, the ow being turbulent until 1992 very few people attempted to describe mathematically the characteristics of disc and popped valves and incompressible. The aim of the work was to study the reattachment and separation of the ow, the vortex with chamfered seats [2,9,10]. In all these studies a set of assumptions had to be considered, and the research created at the outlet and its relation to the ow forces acting on the spool.…”
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“…2 where I 1 and I 2 denotes the momentum flux of the flow entering and leaving the control volume, P 1 and P 2 constitutes the net force due to pressure distribution at the upstream and downstream side of the control volume, while F fluid stands for the force exerted by the fluid on the valve. As [17] pointed out, the pressure forces can be expressed simply by P 1 = A 1 p 1 , and P 2 = A 1 p 2 , while the momentum flux terms can be assumed to be…”
Section: Theoretical Backgroundmentioning
confidence: 99%