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In the case of the MSH leachate data, thermodynamic modelling and previous leaching studies (Taylor and Lichte 1980; Jones and Gislason 2008) imply that for H2O-leached tephra samples, there may be no significant influence of tephra/water ratio or leaching time.
Furthermore, leaching time was also significative.
This will lead to reduction of Ti at longer leaching time, therefore 2 h represents an optimum leaching time of Ti by sulfuric acid [9].
Open image in new window Fig. 2 Effect of leaching time on Ti recovery.
The factors investigated included: acid concentration, leaching time, temperature and solid to liquid ratio.
The three variables studied were leaching time, concentration of sulfuric acid and sample amount.
Figure 1 illustrates an effect of leaching time on the metal leaching from the Sn Cu solder.
The addition of gravel above the herbicide layer halved the leaching time needed for peak As release from the soil.
Two variables are examined including, (1) leaching time, and (2) height of the heap, at a copper mineral treatment plant.
A two-step pH-stat leaching procedure that considers pH as well as L / S and leaching time was suggested.
The studied input variables were temperature, stirring speed, clay to acid dosage, leaching time and leachant concentration.
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