Electrolysis of brine causes caustic formation but also causes Cl2 which must be removed from brine that is coming out of the cell (looks somewhat yellow because of residual Cl2)
We have dechlorination system in which steam ejector is used to create
vacuum which strips chlorine that is dissolved in brine that is coming
out of our electrolysis membrane cell. Of coarse there is condenser in between stripper & ejector (to reduce ejector load)
Cl2 is removed in brine via partial vacuum while its oxides mainly chlorates are decomposed at elevated temperatures... thus outlet of steam ejector (operates at ~12bar @-500mmHg) which carries with it high temperature condensate steam plus residual noncondensable Cl2 from stripper. This chlorinated condensate is directed to a reactor & the heat is used from chlorate decomposition

Now the main part... the greyed portion basically is a perforated titanium distributor pipe which causes immense gurgling noises plus after say 2 months or so when we take it out generally its end blind is broken (see the fig). It runs throughout the diameter (1.5m) of tank

Now what if I increase the number of holes either by perforating the other side of pipe, or increasing the dia or existing holes (or some holes) & finally what is the optimal orientation of this pipe I mean holes facing bottom of tank/ top of tank or just sideways
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