Catalyst for CO2 decomposition and preparantion process thereof
A catalyst, supported catalyst technology, applied in separation methods, chemical instruments and methods, physical/chemical process catalysts, etc., can solve problems such as low industrial application value
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Embodiment 1
[0018] Preparation of Catalyst Pd / SrCo of the Invention by Equal Volume Impregnation Method 0.4 Fe 0.5 Zr 0.1 o 3-δ
[0019] Follow these steps:
[0020] (1) Weigh 0.6685g of PdCl 2 In a beaker, add excess ammonia water (about 10mL) to the beaker while stirring until the metal salt is completely dissolved to prepare the corresponding complex solution as the impregnating solution;
[0021] (2) Then add 7.6g of carrier perovskite mixed conductor (SrCo 0.4 Fe 0.5 Zr 0.1 o 3-δ , where δ represents the number of oxygen lattice vacancies) powder impregnation for 30min;
[0022] (3) Aging at room temperature for 60 minutes, drying at 120°C for 6 hours, then roasting at 500°C for 5 hours, grinding and sieving to obtain a 300-mesh catalyst, wherein the weight content of the active component Pd is 5%.
Embodiment 2
[0024] Catalyst Pd / SrCo 0.4 Fe 0.5 Zr 0.1 o 3-δ to CO 2 Experiment of catalytic activation effect:
[0025] In the reactor shown in Figure 4 is equipped with SrCo 0.4 Fe 0.5 Zr 0.1 o 3-δ Oxygen permeable membrane (1), the upper side of this oxygen permeable membrane is equipped with the present invention Pd / SrCo 0.4 Fe 0.5 Zr 0.1 o 3-δ Catalyst (2). Carbon dioxide is passed into the reactor from the upper side at an intake rate of 4ml / min, and at the same time diluted with 26ml / min of helium; the permeation side uses helium as a sweeping gas, and the intake rate of helium is controlled at 30ml / min. The on-line detection of decomposition products by gas chromatography is shown in Figure 3. In Figure 3, the characteristic peak of CO appeared at 7.034min, proving that CO was generated. At the reaction temperatures of 950°C, 900°C, 850°C, and 800°C, the catalytic activation of CO by the catalyst was investigated. 2 The results are shown in Figure 1.
[0026] As can...
Embodiment 3
[0028] Catalyst Pd / SrCo 0.4 Fe 0.5 Zr 0.1 o 3-δ to CO 2 Stability test of catalytic activity
[0029] at SrCo 0.4 Fe 0.5 Zr 0.1 o 3-δ In the oxygen-permeable membrane reactor, the experimental conditions were the same as in Example 1, and the stability time of the catalytic activity of the catalyst was investigated at 950° C., and the results are shown in FIG. 2 .
[0030] It can be seen from Figure 2 that after the catalytic activity of the catalyst was stable for 20 hours, the CO 2 The decomposition rate has decreased, but its catalytic effect is still obvious. The results show that the catalytic activity of the catalyst can be maintained for more than 20 hours.
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