Method for recovering mercury from waste mercury catalyst
A waste mercury catalyst and leaching technology, applied in the direction of improving process efficiency, can solve the problems of high investment and operation cost of production equipment, low recovery rate, low mercury recovery rate, etc., and achieves low operating cost and equipment cost, operating conditions Mild effect with short procedure
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Embodiment 1
[0013] A method for recycling mercury in waste mercury catalysts, comprising the following steps:
[0014] 1) Using HgCl 2 water solubility, pretreat the waste mercury catalyst with water, the leaching reaction time is 80.0min, the leaching reaction temperature is 50.0℃, the liquid-solid ratio is 20.0:1.0, the magnetic stirring speed is 200.0 r / min, and the pH value is 0.5. At this time, Hg in waste mercury catalyst 2+ The leaching rate is 85.5%;
[0015] 2) The Hg-containing product obtained by filtering the above steps 2+ The leachate, select suitable mobile carrier, surfactant, solvent, surfactant is xanthate adsorbent, the concentration of xanthate adsorbent is 2.0%, carry out milk making under high-speed stirring mixing, its stirring time 30.0 min, stirring speed 280.0 r / min, with Hg 2+ The external water phase was stirred and mass-transferred at a low speed for a period of time. The stirring time was 10.0 min, and the stirring speed was 120.0 r / min. 2+ content, comp...
Embodiment 2
[0019] A method for recycling mercury in waste mercury catalysts, comprising the following steps:
[0020] 1) Using HgCl 2 Water solubility, pretreatment of waste mercury catalyst with water, leaching reaction time at 82.0 min, leaching reaction temperature at 65.0°C, liquid-solid ratio at 18.0:1.0, magnetic stirring speed at 200.0 r / min, pH value at 0.7, at this time, Hg in waste mercury catalyst 2+ The leaching rate is 86.0%;
[0021] 2) The Hg-containing product obtained by filtering the above steps 2+ The leachate, select suitable mobile carrier, surfactant, solvent, surfactant is xanthate ester adsorbent, the concentration of xanthate ester adsorbent is 4.0%, carry out milk making under high-speed stirring mixing, its stirring time is 40.0 min, the stirring speed is 280.0 r / min, and contains Hg 2+ The external water phase was stirred and mass-transferred at a low speed for a period of time, the stirring time was 15.0min, and the stirring speed was 120.0 r / min. 2+ con...
Embodiment 3
[0025] A method for recycling mercury in waste mercury catalysts, comprising the following steps:
[0026] 1) Using HgCl 2 Water solubility, pretreatment of waste mercury catalyst with water, leaching reaction time at 84.0 min, leaching reaction temperature at 75.0°C, liquid-solid ratio at 16.0:1.0, magnetic stirring speed at 200.0 r / min, pH value 0.9, at this time, Hg in waste mercury catalyst 2+ The leaching rate is 88.5%;
[0027] 2) Obtain Hg by filtering through the above steps 2+ The leachate, select suitable flow carrier, surfactant, solvent, surfactant is xanthate adsorbent, the concentration of xanthate adsorbent is 6.0%, carry out milk making under high-speed stirring mixing, its stirring time is 50.0 min, the stirring speed is 280.0 r / min, and contains Hg 2+ The external water phase was stirred and mass-transferred at a low speed for a period of time. The stirring time was 20.0 min, and the stirring speed was 120.0 r / min. 2+ content, compared with the original ...
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