Reducing ZnO to Zn: Thermal vs. Electrowinning

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SUMMARY

The discussion centers on the two primary methods for reducing zinc oxide (ZnO) to zinc (Zn): thermal reduction using carbon and electrowinning with sulfuric acid followed by electrolysis. The participants explore the feasibility of directly reducing ZnO through electrolysis in alkaline electrolytes, akin to charging a zinc-air battery. While electrowinning yields high-purity zinc, the thermal method produces less pure zinc. The economic viability of direct electrolysis is questioned, with calculations suggesting a cost of approximately $0.12 per kg of zinc, which is significantly lower than the market price of zinc at $2.1/kg.

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  • Understanding of thermal reduction processes in metallurgy
  • Knowledge of electrowinning techniques and sulfuric acid applications
  • Familiarity with electrolysis principles and electrochemical reactions
  • Basic chemistry of zinc and its compounds, particularly zinc oxide
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mheslep
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The two commercial methods of reducing ZnO to Zn appear to be
Thermal, in the presence of C:
2 ZnO + C → 2 Zn + CO2
and electrowinning:
ZnO + H2SO4 → ZnSO4 + H2O (followed by electrolysis on the ZnSO4)

But what is the effect of straight electrolysis on ZnO in the presence of some electrolyte to begin with? That is, doesn't electrolysis directly reduce ZnO (as in a charging a depleted Zn-Air battery), and if that's the case why isn't ZnO electrolysis an economic way of producing Zn from ore?
 
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zinc oxide is nearly insoluble in water or non-acidic electrolyte.

I'm not sure about the economics of the two processes you reference. I would imagine the electrowinning process produces very pure material and the carbon reduction would produce less pure product.
 
Probably is possible to get Zn from electrolysis of melted ZnO at high temperatures using a flux, as the way Al is produced from Al2O3 using Na3AlF6 as flux. In the case of Al there is quite no other way (you don't get Al from the oxide reducing it with C and you don't get Al from electrolysis of acqueous solutions of its salts); in the case of Zn the two processes you described are certainly much more simple and cheap, so I presume it's for this reason they are used.
 
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Probably my OP question is ill phrased. Let me try again.

Given a Zn anode, who's surface is largely oxidized to ZnO, and the ZnO is in contact with some alkaline electrolyte, should not the application of an electric potential to the electrode force reduction of the ZnO? Assume anything you like for the cathode, i.e. air via some porous material:

ZnO + 2e + H2O → Zn(OH)2 → 2OH- + Zn

This is basically a Zinc Air battery being charged. The Zn need never enter solution, and no high temperatures required. It should be inexpensive?
 
Oh, I see that's a non trivial amount of charge per kg of Zn:

Zn @ 65g/mole
1 mole e = 96485 C, 3600 C / amp-hour
1 mole e = 26 amp-hours, or
52 amp-hours per mole of Zn,
800 amp-hours per kg of Zn @ 2V = 1.6 kWh per kg of Zn.

That's about $0.12 per kg Zn, with see Zinc @ $2.1/kg, about 6% of the cost. Seems reasonable.
 

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