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Changes in the inlet streams which affected chemistry did not appear to cause significant changes in the overall mixing layer structure shown in the OH/LII images.
Operationally, displacement chromatography is performed in a manner similar to step-gradient chromatography in which the column is subjected to sequential step changes in the inlet conditions.
Dynamic output voltage, fuel-cell-tube temperature and efficiency responses to step changes in the inlet fuel flow pressure with different values of design parameters are discussed.
Since the changes in the inlet temperatures of external fluid in the condenser and the evaporator contribute significant changes in system's overall irreversibility, due consideration is required in condenser and evaporator temperatures to improve the system performance.
Results show that the presence of an intense thermal gradient at the air inlet of the foam brings about density changes in the inlet region, causing air flow acceleration up to 1.7 times the inlet velocity.
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In particular, the change in the inlet orientation imposes a Rayleigh–Taylor instability at the inlet.
A transient regime invoked by a gradual change in the inlet air humidity is discussed.
The sensitivity evaluated in terms of the relative standard deviation (RSD) showed that for 10% change in the core inlet flow, the response in thermal power change is 0.58%, and for 2.5% change in the inlet lead temperature is 1.87%.
The time to reach the steady state is independent of the amplitude of step change in the inlet temperature of fluids.
For a step-change in the inlet temperature of the any fluid, the outlet temperature of other two fluids reach steady state faster than the fluid whose inlet temperature is changed.
The produced oil and water and pressure change in the inlet were monitored.
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