Flow behaviour analysis through a venturi designed for industrial and environmental processes

For instance, when the pressure at the venturi throat is not sufficiently low, the sheet cavity length is not long enough for the cloud cavitation shedding to occur (Keil et al.,

In this paper, by means of well-resolved but computationally demanding numerical simulations extending previous work (Shimizu and Kida 2009), we have investigated the part of

However, considering the high yields of the liquid pre-cheese processes, the From ’ Innov and MMV processes consumed less water (7.42 and 8.41 L of water per kg of cheese

The two species showed slightly lower final cell numbers when shaken for 4 days either during the exponential or the stationary phase, namely between 86.5% and 96.3% of the

To evaluate the performance of the Bayesian procedure with noise estimated from a single photon-count trace using the block-transformation, we apply Approach 2 to TACFs calculated

In the flow modelling and in the correlation, the liquid phase is considered as a unique fluid with its own physical parameters. In order to model the oil/water mixture,

In the first part of the paper, experimental results including mean radial and tangential velocity components, as well as three turbulent correlations, are presented for

Figure 2b reveals that the tangential velocity profile is divided into three distinct zones: the two boundary layers adjacent to the disks wall in which the axial gradients