Transport of Zn (II) by TDDA-Polypropylene Supported Liquid Membranes and Recovery from Waste Discharge Liquor of Galvanizing Plant of Zn (II)

<div>Effect of HCl concentration in feed solution on flux (<svg height="10.5647pt" id="M41" style="vertical-align:-1.928801pt" version="1.1" viewbox="-0.0498162 -8.6359 5.99765 10.5647" width="5.99765pt" xmlns="http://www.w3.org/2000/svg" xmlns:xlink="http://www.w3.org/1999/xlink"><g transform="matrix(.013,0,0,-0.013,0,0)"><path d="M429 650H175L169 622C251 614 259 612 244 532L174 152C163 91 152 37 135 -6C109 -72 67 -101 23 -113L33 -144C45 -143 73 -134 102 -119C186 -76 229 -1 254 133L327 532C341 609 347 613 423 622L429 650Z" id="g113-75"></path></g></svg>) of Zn (II). [HCl] in feed solution = 0.50 mol/dm<sup>3</sup> to 3.0 mol/dm<sup>3</sup>, [TDDA] in membrane phase = 0.80 mol/dm<sup>3</sup>, [NaOH] in stripping solution = 2.0 mol/dm<sup>3</sup>, time = 5.0 h.</div>

Journal of Chemistry

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Figure 4

Figure 4: Transport of Zn (II) by TDDA-Polypropylene Supported Liquid Membranes and Recovery from Waste Discharge Liquor of Galvanizing Plant of Zn (II) 

Figure 4 | Transport of Zn (II) by TDDA-Polypropylene Supported Liquid Membranes and Recovery from Waste Discharge Liquor of Galvanizing Plant of Zn (II) 