A definition of gas-liquid plug flow in horizontal pipes

1990 ◽  
Vol 16 (2) ◽  
pp. 233-242 ◽  
Author(s):  
Z Ruder ◽  
T.J Hanratty
2016 ◽  
Vol 754 ◽  
pp. 092001 ◽  
Author(s):  
A V Kovalev ◽  
A A Yagodnitsyna ◽  
A V Bilsky

1998 ◽  
Vol 53 (1) ◽  
pp. 71-74 ◽  
Author(s):  
Claude de Bellefon ◽  
Sylvain Caravieilhes ◽  
Catherine Joly-Vuillemin ◽  
Daniel Schweich ◽  
Alain Berthod

AIChE Journal ◽  
2015 ◽  
Vol 62 (1) ◽  
pp. 315-324 ◽  
Author(s):  
Dimitrios Tsaoulidis ◽  
Panagiota Angeli

2000 ◽  
Vol 41 (10-11) ◽  
pp. 85-91 ◽  
Author(s):  
D. Van Gauwbergen ◽  
J. Baeyens

The modelling of the reverse osmosis process is needed to fully evaluate its potential and facilitate scale up. The definition of the flow regime in the concentrate channel is of paramount importance. The present paper describes our experimental investigations on RTD and relates the RTD response curves to the regime of flow in the concentrate channel. Results demonstrate (i) that dead zones are present; (ii) that both a Plug Flow with Dispersion (PFD) and Probabilistic Time Delay (PTD) model can be used to characterise the flow; and (iii) that PFD- and PTD-model parameters assume nearly constant values for a given geometry which simplifies the prediction of the RTD for any desired flow rate.


Author(s):  
Abderraouf Arabi ◽  
Karim Ragui ◽  
Yacine Salhi ◽  
Abdelkader Filali

Sensors ◽  
2014 ◽  
Vol 14 (11) ◽  
pp. 20235-20244 ◽  
Author(s):  
Yusuke Fuchiwaki ◽  
Hidenori Nagai

2011 ◽  
Vol 27 (3) ◽  
pp. 225-225 ◽  
Author(s):  
Yusuke FUCHIWAKI ◽  
Masato SAITO ◽  
Shin-ichi WAKIDA ◽  
Eiichi TAMIYA ◽  
Hidenori NAGAI

1998 ◽  
Vol 120 (3) ◽  
pp. 495-501 ◽  
Author(s):  
J. H. Tonouchi ◽  
T. J. Held ◽  
H. C. Mongia

A gas turbine combustor is modeled using a two-reactor, finite-rate mixing and chemistry gas particle approach. The first reactor, used to simulate combustion in the primary zone, permits independent definition of the rates of macromixing and micromixing within the reactor, and the amount of premixing of fuel and air entering the reactor. Finite-rate macromixing is simulated by consideration of the fluid particle residence time distribution frequency function and the ages of the particles in the reactor. Finite-rate micromixing is simulated using a modified Coalescence-Dispersion (C-D) model. The second reactor model simulates combustion in the dilution zone of the combustor, and is modeled as a plug flow reactor with cross-flowing jets of dilution air and co-flowing streams of cooling film air. The primary zone reactor model predicts physically reasonable trends in mean temperature, and CO and NOx emissions as the macromixing and micromixing parameters are varied with respect to the perfectly stirred reactor limit. The model also has shown to predict the correct trends in modeling NOx and CO emissions from aircraft engine gas turbine combustors.


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