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The proposed methodology is demonstrated for a synthetic example for the modelling of a measured reactor frequency response and for the rational fitting of the frequency-dependent parameters corresponding to a single-phase transmission line.
A liquid whistle ultrasonic reactor (frequency 5 30 kHz and intensity, 1.5 2.5 W cm−2) which causes hydrodynamic cavitation has been widely used for industrial wastewater treatment [ 107], oil emulsification [ 108], liquid solid mixture homogenization [ 19] and fat hydrolysis [ 109].
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As the inlet function was only slightly modified in the reactors, frequencies of up to 1 Hz could be imposed for periodic operation.
The average purge intervals obtained were 29 h and 2 min with reactor rotation frequency of 15 min.
This observation allows systematic measurement of ultrasonic stirring throughout electrochemical determination of "equivalent" flow velocity versus various operating parameters (powers, electrode-horn distances, reactor geometry, frequencies, etc).
In order to demonstrate the reserves existing in the design of the CANDU 700 reactor building, frequency-domain calculations were additionally prepared.
A method for obtaining static and dynamic bifurcation points as well as some Hopf degeneracies in chemical reactors using frequency domain analysis is proposed.
While Methanosaeta was detected in high amounts in all the SS reactors, the frequency of other genera differed among SS digesters.
Reduction of electrostatic charge accumulation in fluidized bed polymerization reactors can reduce the frequency of reactor wall sheeting incidents and decrease the cost of operating fluidized bed polymerization reactors.
The model is used to optimize the reactor diameter, ultrasound frequency and power dissipated to the ultrasound transducers.
The samples were then loaded into an RF-PECVD reactor with radio frequency of 13.56 MHz and left for 4 h.
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