plug flow वाक्य
उदाहरण वाक्य
मोबाइल
- So Maxwell Model gives trends that have to be completed in real situation followed by Thurston model in a vessel regarding distribution of cells in sheath and plug flows.
- Continuous vertical plug flow digesters are upright, cylindrical tanks where feedstock is continuously fed into the top of the digester, and flows downward by gravity during digestion.
- In terms of trajectory through the reactor, the ideal flow condition for a continuous reactor is plug flow ( since this delivers uniform residence time within the reactor ).
- An example of the effect of mixing is that a continuous stirred-tank reactor will not have as high pollutant conversion per unit volume of reactor as a plug flow reactor.
- In continuous digestion processes, organic matter is constantly added ( continuous complete mixed ) or added in stages to the reactor ( continuous plug flow; first in first out ).
- The key assumption is that as a plug flows through a PFR, the fluid is residence time ( \ tau ) of the plug is a function of its position in the reactor.
- Vascular resistance depends on blood flow which is divided into 2 adjacent parts : a plug flow, highly concentrated in RBCs, and a sheath flow, more fluid plasma release-cell layering.
- The mixing in COBR is achieved by the combination of fluid oscillation and orifice baffles, allowing plug flow to be achieved under laminar flow conditions with the net flow Reynolds number just about 100.
- For example, vessels not completely mixed ( i . e . plug flow reactors ) are more susceptible to the effects of shock loads which may cause cell lysis and release of soluble microbial products.
- Another characteristic of the circulating fluidized bed is, as it required promoting the small contact time of gas and solid catalyst and plug flow, a significant high gas velocity in the riser is needed.
- The flow would travel as a plug flow, with an essentially non-deforming mass travelling on a thin shear zone and the en masse freezing occurs when the driving stress falls below a certain level.
- With respect to batch and Continuously stirred-tank reactors ( CSTRs ) however have a residence time distribution and cannot mirror batch or plug flow reactors, which can cause a difference in the dispersity of final polymer.
- The Plug Flow Tube Reactor ( PFTR ) is a model of an ideal reactor characterized by the input of a premixed reaction mixture of reactants and solvents on one side and a removal of the product on the other side.
- An ideal plug flow reactor has a fixed residence time : Any fluid ( plug ) that enters the reactor at time t will exit the reactor at time t + \ tau, where \ tau is the residence time of the reactor.
- It is however experimentally observed that the velocity of the gas and liquid phases can be significantly different, depending on the flow pattern ( e . g ., plug flow, annular flow, bubble flow, stratified flow, slug flow, churn flow ).
- Dispersion can be differentiated from diffusion in that it is caused by non-ideal flow patterns ( i . e . deviations from plug flow ) and is a macroscopic phenomenon, whereas diffusion is caused by random molecular motions ( i . e . Brownian motion ) and is a microscopic phenomenon.
- Real plug flow reactors do not satisfy the idealized flow patterns, back mix flow or plug flow deviation form ideal behavior can be due to channeling of fluid through the vessel, recycling of fluid within the vessel or due to the presence of stagnant region or dead zone of fluid in the vessel.
- Real plug flow reactors do not satisfy the idealized flow patterns, back mix flow or plug flow deviation form ideal behavior can be due to channeling of fluid through the vessel, recycling of fluid within the vessel or due to the presence of stagnant region or dead zone of fluid in the vessel.
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