Zn(g) + CO2(g) = ZnO(s) + CO(g)

Figure 1. Imperial Smelting Furnace
Table 1 below summarizes the gas amounts entering and exiting the quencher.
Liquid Zn is recovered from the liquation unit by phase separation upon cooling
of the Pb-Zn alloy from the quencher.
| TABLE 1. Gas amounts entering and exiting the quencher. | |||
|
Item
|
Top Gas
|
Gas Out
|
|
|
N2 (g)
|
48.29 lb moles
|
57.43 %
|
48.29 lb moles
|
| CO2 (g) |
3.61 lb moles
|
3.61 %
|
3.47 lb moles
|
| CO (g) |
25.82 lb moles
|
30.71 %
|
25.96 lb moles
|
| Zn (g) |
6.37 lb moles
|
7.58 %
|
0.09 lb moles
|
| ZnO (solid) |
|
-
|
-
|
| Volume @STP |
30,188 ft3
|
|
27,934 ft3
|
| T |
1000 °C
|
|
650 °C
|
Data:
CO2(g) + Zn(g)
= ZnO(s) + CO(g)
DG°(cal/gmole) = - 45065+28.289*(T, Kelvin)
| TABLE 2. Zinc Vapor Pressure | |
|
T, ºC
|
P°Zn,
atm
|
|
377
|
5.5×10-5
|
| 650 |
0.045
|
| 923 |
1.16
|
| TABLE 3. Heats of Formation at 77ºF and Heat Capacities | ||
|
Gas
|
DH°Formation, 77 °°F
(BTU/(lbmole) |
Cp
(BTU/ (lbmole*°F) |
|
N2 (gas)
|
-
|
7.0
|
| CO2 (gas) |
-169,290
|
11.0
|
| CO (gas) |
-47,556
|
7.2
|
| O2 (gas) |
-
|
7.1
|
| Zn (gas) |
56,104
|
5.0
|
| ZnO (solid) |
-149,706
|
12.0
|
| TABLE 4. Data for Liquid Pb-Zn Alloys at 650 °C | ||
|
Mole Fraction of Zn
|
Activity of Zn in Liquid Pb-Zn Alloys
Relative to Pure, Liquid Zn |
Activity Coefficient
|
|
0
|
0
|
7.94
|
| 0.1 |
0.627
|
6.273
|
| 0.2 |
0.942
|
4.709
|

Figure 2. Sketch of the Pb-Zn Phase Diagram
What conditions would make the reaction below LESS likely?
CO2(g) + Zn(g) = ZnO(s) + CO(g)
|
(A)
|
Higher T & Higher Ptotal
|
|
(B)
|
Lower T & Lower Ptotal
|
|
(C)
|
Higher T & Lower Ptotal
|
|
(D)
|
Lower T & Higher Ptotal
|
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