Unlock instant, AI-driven research and patent intelligence for your innovation.

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 the problem of low COD removal rate and achieve good The effect of technical effects

Active Publication Date: 2020-01-03
CHINA PETROLEUM & CHEM CORP +1
View PDF6 Cites 0 Cited by
  • 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 low removal rate of COD in the heterogeneous catalytic wet oxidation reaction in the prior art, and a new heterogeneous catalytic wet oxidation catalyst is provided

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Heterogeneous Catalytic Wet Oxidation Catalyst
  • Heterogeneous Catalytic Wet Oxidation Catalyst

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0037] 1. Vector preparation

[0038] Put 110g of finished MWCNTs powder (particle size 30 μm) and 110 g of finished graphite powder (particle size 30 μm) into a kneader and mix, pour 20 g of PEG400 aqueous solution with a concentration of 15 wt % and 50 g of water, knead, extrude, and roll into balls. Dry at 100° C. for 12 hours to obtain a spherical carrier with a diameter of 3 mm.

[0039] 2. Catalyst preparation

[0040] Mix 198g spherical carrier with 300g RuCl containing 2gRu 3 The methanol solution was mixed for impregnation. Stand at room temperature for 6h, then dry in an oven at 110°C for 16h, and then calcinate in a muffle furnace at 450°C for 2.5h to obtain a catalyst precursor. 400°C in H 2 -N 2 Reduction in the atmosphere for 4h to obtain the catalyst, wherein H 2 :N 2 The volume ratio is 4:96.

[0041] 3. Catalyst evaluation

[0042] Take 100g of catalyst and put it into a wet oxidation reactor for reaction. The reaction temperature is 280°C, the press...

Embodiment 2

[0045] 1. Vector preparation

[0046]Put 132g of finished MWCNTs powder (particle size 30 μm) and 88g finished graphite powder (particle size 30 μm) into a kneader and mix, pour 20g of 15wt% PEG400 aqueous solution and 50g of water for kneading, extruding, and rolling ball molding. Dry at 100° C. for 12 hours to obtain a spherical carrier with a diameter of 3 mm.

[0047] 2. Catalyst preparation

[0048] Mix 198g spherical carrier with 300g RuCl containing 2gRu 3 The methanol solution was mixed for impregnation. Stand at room temperature for 6h, then dry in an oven at 110°C for 16h, and then calcinate in a muffle furnace at 450°C for 2.5h to obtain a catalyst precursor. 400°C in H 2 -N 2 Reduction in the atmosphere for 4h to obtain the catalyst, wherein H 2 :N 2 The volume ratio is 4:96.

[0049] 3. Catalyst evaluation

[0050] Take 100g of catalyst and put it into a wet oxidation reactor for reaction. The reaction temperature is 280°C, the pressure is 9.0MPa, the vo...

Embodiment 3

[0053] 1. Vector preparation

[0054] Put 88g of finished MWCNTs powder (particle size 30 μm) and 132g finished graphite powder (particle size 30 μm) into a kneader and mix them, pour 20g of 15wt% PEG400 aqueous solution and 50g of water, knead, extrude, and roll into balls. Dry at 100° C. for 12 hours to obtain a spherical carrier with a diameter of 3 mm.

[0055] 2. Catalyst preparation

[0056] Mix 198g spherical carrier with 300g RuCl containing 2gRu 3 The methanol solution was mixed for impregnation. Stand at room temperature for 6h, then dry in an oven at 110°C for 16h, and then calcinate in a muffle furnace at 450°C for 2.5h to obtain a catalyst precursor. 400°C in H 2 -N 2 Reduction in the atmosphere for 4h to obtain the catalyst, wherein H 2 :N 2 The volume ratio is 4:96.

[0057] 3. Catalyst evaluation

[0058] Take 100g of catalyst and put it into a wet oxidation reactor for reaction. The reaction temperature is 280°C, the pressure is 9.0MPa, the volume ra...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

No PUM Login to View More

Abstract

The invention relates to a multiphase catalysis wet type oxidation catalyst, and a preparation method and a purpose thereof, and mainly solves the problem of low COD removal rate in the prior art. The multiphase catalysis wet type oxidation catalyst has the technical scheme that the multiphase catalysis wet type oxidation catalyst is prepared from the following ingredients in parts by weight: (a) 98.0 to 99.8 parts of carriers and (b) 0.2 to 2.0 parts of ingredients which are carried on the carriers and are selected from at least one kind of materials from Ru, Pd, Pt and Rh; the carriers are selected from at least one kind of materials from silicon dioxide, aluminum oxide, titanium oxide, multiwalled carbon nanotubes and graphite. The catalyst well solves the problem and can be used for 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

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/42B01J23/46B01J23/44C02F1/72C02F103/36
CPCB01J23/42B01J23/44B01J23/462C02F1/725C02F1/727C02F2103/36
Inventor 郑育元陈航宁郭宗英吴粮华顾松园
Owner CHINA PETROLEUM & CHEM CORP