Method of recovering noble metal from spent catalyst containing noble metal
A technology for waste catalysts and precious metals, which is applied in the field of recovering precious metals from waste catalysts containing precious metals, can solve the problems of long time consumption, low precious metal recovery rate, waste of resources, etc., so as to reduce production costs, promote industrial applications, and shorten the required time. Effect
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Embodiment 1
[0025] Put 10.0g of industrial waste catalyst containing 0.400w% Pd into a quartz tube, firstly roast at 600°C for 2h, then increase the temperature to 1000°C, keep the temperature constant for 1h, and then pass in N 2 After reaching room temperature, add 100ml of the leaching solution whose composition is shown in Table 1 to the sample, stir at 60°C for 2h, filter and fully wash the precipitate to obtain 160g of a solution containing a palladium compound, and measure the mass percentage of Pd in the solution by atomic absorption spectroscopy The concentration is 0.024w%, the calculated Pd content is 0.0384g, and the leaching rate of Pd is 96.0w%.
[0026] According to the palladium recovery method in US Patent No. 5,045,290: the total recovery rate of Pd reaches 90.2w%.
Embodiment 2
[0028] 10.0g of industrial waste catalyst containing 0.620w% Pt was put into a quartz tube, firstly roasted at 600°C in the air for 2h, then passed through nitrogen to keep the temperature for 1h, and then passed into H 2After reaching room temperature, add 100ml of the leaching solution whose composition is shown in Table 1 to the sample, stir at 60°C for 2h, filter and wash the precipitate sufficiently to obtain 173g of a solution containing Pt compounds, and measure the mass percentage of Pt in the solution by atomic absorption spectroscopy The concentration is 0.035w%, the calculated Pt content is 0.0605g, and the leaching rate of Pt is 97.5w%.
[0029] According to the method of platinum recovery in US Patent No. 5,797,977: the total recovery rate of Pt is 89.7w%.
Embodiment 3~21
[0031] The experimental process is the same as in Example 1, and the specific conditions are as shown in Table 1.
[0032] A
B
C
D
E
F
G
H
R
J
1
10.0
0.42
600(2)+1000(1)
N 2
HCl(2.8)+H 2 o 2 (1.2)+NaCl(2.5)
1000
60
4
96.0
3
10.0
0.42
600(1)+1000(2)
N 2
HCl(4.0)+H 2 o 2 (0.6)+NaCl(1.2)
1000
20
6
93.4
4
10.0
0.42
550(2)+900(2)
N 2
HCl(4.0)+H 2 o 2 (0.8)+NaCl(1.0)
1000
10
8
92.0
5
10.0
0.42
500(2)+850(4)
N 2
HCl(4.5)+H 2 o 2 (1.0)+NaCl(1.0)
800
30
6
93.3
6
10.0
0.42
600(2)+900(2)
N 2
HCl(3.5)+H 2 o 2 (2.3)+NaCl(3.0)
800
45
6
90.0
7
10.0
0.42
450(2)+1200(1)
N 2
HCl(6.0)+H 2 o 2 (2.8)+NaCl(0.5)
1200
80 ...
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