Zeolite Fenton catalyst containing isolated metal species as well as preparation method and application thereof
A catalyst and metal technology, applied in the field of catalyst preparation for wastewater treatment, can solve the problems of complex preparation method and low content of isolated metal species, etc.
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Embodiment 1
[0021] (1) Preparation of catalyst precursor. 10g4A zeolite and 2000mg / LFeCl 3 The solutions were mixed according to the mass ratio of 1:50, shaken in an air bath shaker for 3 hours, and then vacuum-filtered to collect the obtained solid as the catalyst precursor.
[0022] (2) Preparation of catalyst. After the catalyst precursor was frozen in the refrigerator for 0.5h, it was placed in a freeze dryer and frozen at -55°C for 48h to prepare a 4A zeolite Fenton catalyst containing isolated iron species.
[0023] The solid ultraviolet-visible diffuse reflectance spectrogram of the 4A zeolite Fenton catalyst containing isolated iron species is as attached figure 1 As shown, the 4A zeolite Fenton catalyst containing the isolated iron species has a sharp absorption peak at 209nm, while the absorption of the comparative catalyst is very weak at this place; The absorption intensity of the catalyst is less than that of the comparative catalyst. These phenomena indicate that in the 4...
Embodiment 2
[0026] (1) Preparation of catalyst precursor. 5g4A zeolite and 2000mg / LFeCl 3 The solutions were mixed according to the ratio of 1:5 (mass ratio), and after being shaken in an air bath shaker for 2 hours, they were vacuum-filtered, and the obtained solid was collected as the catalyst precursor.
[0027] (2) Preparation of catalyst. After the catalyst precursor was frozen in the refrigerator for 0.5 h, it was placed in a freeze dryer and frozen at -55 °C for 34 h to prepare a 4A zeolite Fenton catalyst containing isolated iron species.
[0028] When the pH value of the phenol solution was adjusted to 4.00, the 4A zeolite Fenton catalyst containing the isolated iron species of the present invention and the catalyst of the comparative example, the time required to degrade 70% phenol was 8h and 10.3h respectively, and the utilization rate of hydrogen peroxide in the degradation process They are 12.00% and 8.37% respectively.
Embodiment 3
[0030] (1) Preparation of catalyst precursor. 10g4A zeolite and 200mg / LFeCl 3 The solution was mixed according to the ratio of 1:50, and after being shaken in an air bath shaker for 5 hours, it was vacuum filtered, and the obtained solid was collected as the catalyst precursor.
[0031] (2) Preparation of catalyst. The preparation method is the same as in Example 1.
[0032] When the pH of the phenol solution was adjusted to 6.30, about 61.69% of the phenol could be degraded after 12 hours of reaction for the isolated iron species-containing 4A zeolite Fenton catalyst of the present invention, while the comparative catalyst had no degradation of phenol.
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