Preparation method of iron-based composite catalyst for catalytic ozonation treatment of coal chemical wastewater

A composite catalyst, coal chemical wastewater technology, applied in catalyst activation/preparation, oxidized water/sewage treatment, metal/metal oxide/metal hydroxide catalyst, etc., can solve the problem of low efficiency, utilization of active substances and active sites Reduce the rate of loading, the amount of loaded active substances and low dispersibility, etc., to increase the amount of loading, the catalyst is effective, and the stability and dispersibility are improved.

Pending Publication Date: 2021-08-17
CCTEG CHINA COAL RES INST +1
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0005] Catalyst loading methods commonly used in industrial production are mainly divided into two categories: surface precipitation method and granulation method, however, traditional catalyst loading methods are often inefficient, and the amount and dispersion of loaded active substances are very low
In addition, in some cases, the traditional loading method will cause the active species to form clusters on the surface of the catalyst support, which reduces the utilization of active species and active sites.

Method used

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  • Preparation method of iron-based composite catalyst for catalytic ozonation treatment of coal chemical wastewater
  • Preparation method of iron-based composite catalyst for catalytic ozonation treatment of coal chemical wastewater
  • Preparation method of iron-based composite catalyst for catalytic ozonation treatment of coal chemical wastewater

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Embodiment 1

[0036] Embodiment 1: A kind of preparation method of the iron-based composite catalyst that is used for the catalytic ozonation treatment of coal chemical industry wastewater, comprises the following steps: Activation / pretreatment carrier: carrier is immersed in NaOH solution, and carrier is Al2O3 particle, NaOH in NaOH solution and The weight ratio of Al2O3 particles is 10:1, and then washed with pure water until the pH of the carrier supernatant becomes neutral; the washed carrier is dried at 90°C for 12 hours; and it is observed whether bubbles are formed on the carrier, if If bubble formation is not observed or bubbling stops, the mass transfer rate of NaOH should be increased, for example, by stirring to increase the cross-flow velocity of the NaOH solution. Preparation of metal precursor solution: Fe(NO3)3 and urea were dissolved in pure water to prepare metal precursor solution, the concentration of Fe(NO3)3 in the metal precursor solution was 10 mM, and the concentratio...

Embodiment 2

[0037]Embodiment 2: A kind of preparation method of the iron-based composite catalyst that is used for the catalytic ozonation treatment of coal chemical industry wastewater, comprises the following steps: Activation / pretreatment carrier: carrier is immersed in NaOH solution, and carrier is Al2O3 particle, NaOH in NaOH solution and The weight ratio of Al2O3 particles is 151, and then washed with pure water until the pH of the carrier supernatant becomes neutral; dry the washed carrier at 115 °C for 14 hours; and observe whether air bubbles are formed on the carrier, if not observed When the bubbles are formed or the bubbles stop, the mass transfer rate of NaOH should be increased, for example, the cross-flow velocity of NaOH solution can be increased by shaking. Preparation of metal precursor solution: Fe(NO3)3 and urea were dissolved in pure water to prepare metal precursor solution, the concentration of Fe(NO3)3 in the metal precursor solution was 15 mM, and the concentration...

Embodiment 3

[0038] Embodiment 3: A kind of preparation method of the iron-based composite catalyst that is used for the catalytic ozonation treatment of coal chemical industry wastewater, comprises the following steps: Activation / pretreatment carrier: the carrier is immersed in NaOH solution, carrier is Al2O3 particles, NaOH in NaOH solution and The weight ratio of Al2O3 particles is 20:1, and then washed with pure water until the pH of the carrier supernatant becomes neutral; the washed carrier is dried at 120°C for 16 hours; and it is observed whether bubbles are formed on the carrier, if If no bubble formation is observed or the bubbling stops, the mass transfer rate of NaOH should be increased, for example, by aeration to increase the cross-flow velocity of the NaOH solution. Preparation of metal precursor solution: Fe(NO3)3 and urea were dissolved in pure water to prepare metal precursor solution, the concentration of Fe(NO3)3 in the metal precursor solution was 20 mM, and the concent...

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Abstract

The invention discloses a preparation method of an iron-based composite catalyst for catalytic ozonation treatment of coal chemical wastewater. The preparation method comprises the following steps: activating / pretreating a carrier, preparing a metal precursor solution, loading Fe onto an Al2O3 carrier, and performing oscillating, aging, drying and washing. According to the preparation method, the aluminum oxide is taken as the carrier, urea is taken as a self-sacrifice template, so that iron oxide is loaded on the surface of aluminum oxide, and the existence of urea is beneficial to precipitation of iron on the carrier; when heating is carried out at 90-120 DEG C, urea can be decomposed very slowly to form hydroxyl groups, and the hydroxyl groups are uniformly distributed on the surface and pores of the Al2O3 carrier; then, ferric hydroxide and ferric oxyhydroxide are precipitated on the surface of the carrier. The active substance directly grows on the surface of the carrier, so that the stability and dispersity of Fe are obviously improved, and meanwhile, the loading amount of Fe on the carrier is increased.

Description

technical field [0001] The invention relates to the field of catalyst preparation, in particular to a method for preparing an iron-based composite catalyst used for catalytic ozonation treatment of coal chemical wastewater. Background technique [0002] Despite the recent reform measures and regulations formulated by the Chinese government in terms of energy consumption and environmental protection, which have promoted the deployment of non-fossil energy (e.g., solar, wind, nuclear energy) and the development of electric vehicles nationwide, coal is still China's The main energy source, for example, in 2018, coal accounted for about 60% of domestic energy consumption, equivalent to one-half of the world's annual coal consumption. Therefore, the huge demand for coal energy makes the coal chemical industry an important contributor to wastewater discharge, and the coal chemical wastewater discharged by it contains high concentrations of toxic and harmful compounds, such as poly...

Claims

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Application Information

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IPC IPC(8): B01J23/74B01J37/02B01J37/03B01J37/08C02F1/78
CPCB01J23/74B01J23/002B01J37/0207B01J37/035B01J37/082C02F1/78C02F1/725
Inventor 孔祥瞳李文博高明龙陈贵锋马金星大卫·韦特钟金龙王吉坤
Owner CCTEG CHINA COAL RES INST
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