CO sulfur resistant transformation catalyst and its preparation method
A sulfur-resistant shift and catalyst technology, applied in chemical instruments and methods, inorganic chemistry, bulk chemical production, etc., can solve the problems of low low temperature activity, poor dispersion performance of active components and additives, and high strength, and achieve optimization. Pore structure, ensuring active stability, improving strength and stability
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Embodiment 1
[0026] The preparation of embodiment 1 catalyst
[0027] Listed in table 1 are industrial Co-Mo sulfur-resistant shift catalyst QCS-01 (Qilu Petrochemical Company Research Institute production, carried out large-scale industrial application at home) and the composition of the catalyst prepared by the present invention:
[0028]
catalyst
Chemical composition, %(m / m)
Al 2 o 3
TiO 2
MgO
NiO
MnO 2
CoO
MoO 3
La 2 o 3
Ce 2 o 3
QCS-01
45.7
11.0
21.4
4.5
3.5
8.9
0.25
0.25
A
45.5
11.5
22.3
0.5
3.6
8.7
B
39.5
11.8
22.1
3
3
3.7
12
C
38.1
12.3
21.9
5.9
3
1
3.5
10
D
33.1
11.8
22.4
14
3.4
8.7
...
Embodiment 2
[0040] Embodiment 2 catalyst performance evaluation
[0041] Catalyst activity tests were carried out on the normal pressure micro-reaction evaluation device and the pressurized particle size evaluation device respectively. Among them, the evaluation conditions of the atmospheric pressure micro-reaction evaluation device are:
[0042] Catalyst loading: 0.3g Catalyst particle size: 40-60 mesh
[0043] h 2 O / dry gas: 1.0 (molar ratio) Dry gas space velocity: 10000h -1
[0044] h 2 S concentration: 0.3~0.4% (v / v) Vulcanization temperature: 250℃
[0045] Vulcanization time: 4 hours
[0046] The evaluation conditions of the pressurized raw particle size evaluation device are:
[0047] Catalyst loading: 50mlφ4mmα-Al 2 o 3 Ball 1:1 dilution
[0048] Catalyst particle size: φ4×4mm H 2 O / dry gas: 1.2 (molar ratio)
[0049] h 2 S concentration: 0.2~0.4% (v / v)
[0050] Vulcanization temperature: 250℃ Vulcanization time: 20hr
[0051] Vulcanization space velocity: 2000h-1 V...
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