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Heterogeneous Catalytic Wet Oxidation Catalyst

A technology of wet oxidation and heterogeneous catalysis, applied in physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, oxidized water/sewage treatment, etc., can solve low COD removal rate, low catalyst strength, etc. problem, to achieve the effect of COD removal rate improvement, catalyst strength improvement and good technical effect

Active Publication Date: 2019-01-25
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0008] One of the technical problems to be solved by the present invention is the problem of low COD removal rate and low catalyst strength in the heterogeneous catalytic wet oxidation reaction in the prior art, and a new heterogeneous catalytic wet oxidation catalyst is provided

Method used

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  • Heterogeneous Catalytic Wet Oxidation Catalyst
  • Heterogeneous Catalytic Wet Oxidation Catalyst
  • Heterogeneous Catalytic Wet Oxidation Catalyst

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0029] step 1)

[0030] Prepare 0.2mol / l Ti(SO 4 ) 2 1000ml of aqueous solution and 1000mL of 0.6mol / l ammonia water. Co-precipitation of titanium salt and ammonia water is used to form a gel precipitate, which is filtered, washed, dried, kneaded, extruded, pelletized, and roasted at 750°C for 5.5h to make TiO 2 spherical carrier.

[0031] Step 2)

[0032] 20g TiO 2 The spherical carrier was impregnated with 0.53g RuCl 3 ·nH 2 O solution. Impregnated at room temperature for 6h, then dried in an oven at 110°C for 16h, and then calcined in a muffle furnace at 480°C for 2.5h to obtain a catalyst precursor.

[0033] step 3)

[0034] Reduction with hydrogen at 400°C for 4 hours to obtain the finished catalyst C1.

[0035] The ratio of anatase:rutile in the catalyst was determined to be 90:10 by XRD peak area.

[0036] The catalyst composition is shown in Table 1, and the preparation conditions are shown in Table 2.

Embodiment 2

[0038] step 1)

[0039] Prepare 0.2mol / l Ti(SO4) 2 1000ml of aqueous solution and 1000mL of 0.6mol / l ammonia water. Co-precipitation of titanium salt and ammonia water is used to form a gel precipitate, which is filtered, washed, dried, kneaded, extruded, pelletized, and roasted at 780°C for 5.0h to make TiO 2 spherical carrier.

[0040] Step 2)

[0041] 20g TiO 2 The spherical carrier was impregnated with 0.34g PdCl 2in solution. Impregnated at room temperature for 6h, then dried in an oven at 110°C for 16h, and then calcined in a muffle furnace at 420°C for 3.6h to obtain a catalyst precursor.

[0042] step 3)

[0043] Reduction with hydrogen at 400°C for 3.5 hours to obtain the finished catalyst C2.

[0044] The ratio of anatase:rutile in the catalyst was determined to be 90:10 by XRD peak area.

[0045] The catalyst composition is shown in Table 1, and the preparation conditions are shown in Table 2.

Embodiment 3

[0047] step 1)

[0048] Prepare 0.2mol / l Ti(SO 4 ) 2 1000ml of aqueous solution and 1000mL of 0.6mol / l ammonia water. Co-precipitation of titanium salt and ammonia water is used to form a gel precipitate, which is filtered, washed, dried, kneaded, extruded, pelletized, and roasted at 800°C for 4.0h to make TiO 2 spherical carrier.

[0049] Step 2)

[0050] 20g TiO 2 The spherical carrier is impregnated with 0.56g H 2 PtCl 6 ·6H 2 O solution. Impregnated at room temperature for 6h, then dried in an oven at 110°C for 16h, and then calcined in a muffle furnace at 550°C for 2.2h to obtain a catalyst precursor.

[0051] step 3)

[0052] Reduction with hydrogen at 520° C. for 3 h gave the finished catalyst C3.

[0053] The ratio of anatase:rutile in the catalyst was determined to be 90:10 by XRD peak area.

[0054] The catalyst composition is shown in Table 1, and the preparation conditions are shown in Table 2.

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Abstract

The present invention relates to a heterogeneous catalysis wet oxidation catalyst, a preparation method and uses thereof. A purpose of the present invention is mainly to solve the problems of low COD removal rate and low catalyst strength in the prior art. The technical scheme of the present invention comprises that a heterogeneous catalysis wet oxidation catalyst is used, and the components comprise, by weight, a) 98.0-99.8 parts of a TiO2 carrier, and b) 0.2-2.0 parts of at least one selected from Ru, Pd, Pt and loaded on the TiO2 carrier. With the technical scheme, the problems in the prior art are well solved, and the method can be used for the industrial acrylonitrile wastewater treatment.

Description

technical field [0001] The invention relates to a heterogeneous catalytic wet oxidation catalyst and its preparation method and application. Background technique [0002] Due to the characteristics of water (such as non-toxic, cheap, wide sources, etc.), it is often used as a reaction solvent, medium or heat carrier in the chemical production process, so the water quality of the water body is inevitably damaged. With the vigorous development of the chemical industry, water pollution is increasing year by year, and the pollution of toxic organic substances to water is particularly serious. This kind of pollutant has the characteristics of large discharge, wide pollution area and refractory biodegradation, which has seriously threatened human life and restricted the development of chemical industry. Therefore, research on how to treat industrial organic wastewater with high efficiency and energy saving has become an urgent problem to be solved. [0003] Industrial wastewater...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/46B01J23/44B01J23/42C02F1/72
Inventor 郑育元郭宗英陈航宁汪国军
Owner CHINA PETROLEUM & CHEM CORP