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The system consists of a 9-layer drift chamber with 24 jet cells and a proportional chamber in a common gas volume.
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A three electrode impinging jet cell was used to improve the mass transfer of the reactant to the electrode surface.
Precipitation of the crystalline solid is performed in a tubular reactor of adjustable length equipped with a free jet cell.
First, in order to negate the effect of the radial velocity jump at the jet boundary, the radial velocity of the external gas is reset not to zero but to its value at the last jet cell.
As a result, the modified Jameson cell was more efficient (higher loaded carrier recoveries) than the conventional jet cell (CJC) in removing heavy metals ions.
Considering all the above, the electrochemical jet cell stands as a rather promising design for the efficient hydrogen peroxide electro-generation.
An impinging jet cell was used to investigate the influence of the convection on the kinetics of scale deposition in a carbonically pure water.
Because this jet cell operates with a high air hold-up, it presented a very good efficiency (capture of oil droplets by bubbles) at low residence time (high-rate separation) and showed to be simple, compact and easy to operate.
In the modified jet cell, the downcomer was sealed at the bottom with a diffuser, and the re-flotation of detached flocs and the probability of bubbles/particles capture was enhanced, which improved the recovery rate.
Results of laboratory studies showed mean separation efficiencies of the order of 80% when used as a conventional jet cell (CJC) with feed emulsions (droplets size of about 20 μm) ranged between 100 and 400 mg/L petroleum concentration.
Stereo mini-jet cells will be indispensable components of a future e+e− linear collider central tracker such as JLC-CDC.
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