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Flame-retardant porous matrix supported non-noble metal catalyst as well as preparation method and application thereof

A porous matrix, non-precious metal technology, applied in the direction of catalyst activation/preparation, metal/metal oxide/metal hydroxide catalyst, combustion method, etc., can solve the problem of increasing uncontrollable factors in the reaction and increasing the pressure drop of the fixed bed layer , affecting catalyst life and other issues, to achieve excellent stability, long service life, and good hydrothermal properties

Pending Publication Date: 2022-07-29
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0004] In the above published patents, alumina and titanium oxide are used as the primary coating components in the catalyst coating process, and then the active metal or active metal oxide is loaded. The stability of the coating not only affects the life of the catalyst, but also affects the life of the catalyst. The powdering of the cracked and peeled coating will also increase the pressure drop of the fixed bed layer and increase the uncontrollable factors of the reaction

Method used

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  • Flame-retardant porous matrix supported non-noble metal catalyst as well as preparation method and application thereof
  • Flame-retardant porous matrix supported non-noble metal catalyst as well as preparation method and application thereof

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preparation example Construction

[0053] The present invention also provides a method for preparing a flame-retardant porous matrix-supported non-precious metal catalyst, which is characterized by comprising the following steps:

[0054](1) mixing and contacting at least one original matrix selected from attapulgite and kaolin, at least one inorganic material selected from inorganic porous solids, a peptizer, and water to make a plastic mixed contact body; wherein, relative to The total amount of the original matrix and the inorganic material, the content of the original matrix is ​​10-99.5 mass %, preferably 20-99 mass %, the inorganic material content is 0.5-90 mass %, preferably 1-80 mass %, More preferably 5-80 mass %, more preferably 8-70 mass %, still more preferably the remainder;

[0055] (2) optionally subjecting the plastic mixed contact body to molding to obtain a porous matrix blank;

[0056] (3) calcining the mixed contact body of step (1) or the porous substrate blank of step (2) to obtain a fla...

Embodiment 1

[0115] Mix attapulgite, 13X molecular sieve, 65% mass concentration of nitric acid, methylcellulose, and magnesium stearate in a kneader in a mass ratio of 10:4:0.02:0.2:0.001, and stir evenly, add an appropriate amount of water, Knead into a plastic mixed contact body, put the contact body into an extruder, and extrude it under the conditions of a temperature of 25 ° C and a pressure of 5 MPa to make a square honeycomb body, a square honeycomb body. The length and height of the four bottom sides are respectively 80 cm and 100 cm, and the honeycomb green body is calcined at 300° C. for 2 hours under air conditions to obtain a flame-retardant honeycomb matrix A. The Co content of each cubic honeycomb substrate A is 160kg / m 3 The polyethylene glycol-400 aqueous solution of cobalt nitrate is configured in the proportion of 3 , Mo content is 15kg / m 3 The aqueous solution of cerium nitrate and ammonium molybdate was prepared in the proportion of cerium nitrate and ammonium molybd...

Embodiment 2

[0117] Mix attapulgite, kaolin, Y molecular sieve, 65% mass concentration of nitric acid, methylcellulose, and magnesium stearate in a kneader in a mass ratio of 8:2:2:0.02:0.2:0.03, Add an appropriate amount of water, knead into a plastic mixed contact body, put the contact body into an extruder, and extrude it at a temperature of 25 ° C and a pressure of 5 MPa to make a blank with square honeycomb holes. The length and height of the four bottom sides of the green body are respectively 80 cm and 100 cm, and the honeycomb green body is calcined at 500° C. for 2 hours under air conditions to obtain a flame-retardant honeycomb matrix B. According to the content of Co on each cubic honeycomb matrix B is 130kg / m 3 The proportion of citric acid aqueous solution of cobalt nitrate is configured, wherein the mass ratio of citric acid and cobalt nitrate is 0.1:1, and the Ce content on each cubic honeycomb matrix B is 40kg / m 3 , Mn content is 29kg / m 3 The aqueous solution of cerium ni...

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Abstract

The invention relates to a flame-retardant porous matrix supported non-noble metal catalyst as well as a preparation method and application thereof. The flame-retardant porous matrix supported non-noble metal catalyst has the advantages of simple preparation method, high mechanical strength, strong water-resistant thermal stability, good volatile organic compound catalytic performance in treatment of VOCs, long service life and the like, and is also applicable to catalytic wet oxidation of wastewater.

Description

technical field [0001] The invention relates to a flame-retardant porous matrix-supported non-precious metal catalyst. More specifically, the present invention relates to a flame-retardant porous matrix-supported non-precious metal catalyst and a method for preparing the same. The invention also relates to the application of the flame-retardant porous matrix-supported non-precious metal catalyst in the catalytic oxidation treatment of volatile organic compounds (VOCs or VOC) and wastewater with high chemical oxygen demand (COD). Background technique [0002] In recent years, with the increasing requirements of the country for environmental protection, adsorption methods, absorption methods, condensation methods, membrane separation methods, high-temperature incineration methods and catalytic oxidation methods have been widely used in various waste gases containing volatile organic compounds (VOCs). Recycling / Remediation. Among them, the adsorption method is suitable for 50...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/16B01J29/03B01J29/76B01J29/85B01J23/847B01J23/889B01J23/83B01J23/843B01J37/04B01J37/08B01J37/02B01J35/10B01J35/04F23G7/07C02F1/74C02F101/34
CPCB01J29/03B01J29/85B01J23/83B01J29/163B01J29/166B01J29/7607B01J23/8472B01J23/8892B01J23/8437B01J37/04B01J37/08B01J37/0201B01J37/0203F23G7/07C02F1/74C02F1/725B01J2229/186B01J2229/20C02F2101/34B01J35/56B01J35/635B01J35/633B01J35/647B01J35/615
Inventor 刘经伟朱伟孟杰李泽壮徐骏
Owner CHINA PETROLEUM & CHEM CORP