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Waste water treatment catalyst and preparation method thereof

A wastewater treatment and catalyst technology, applied in the direction of catalyst activation/preparation, physical/chemical process catalysts, chemical instruments and methods, etc., can solve the problems of uneven dispersion of active metals, long time, cumbersome preparation process, etc., and achieve high activity The effect of uniform distribution of components, high content of active components, and simple preparation process

Active Publication Date: 2011-05-11
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0008] However, the analysis of the above catalyst impregnation or spray-dipping preparation methods shows that this conventional catalyst preparation method has problems such as low loading of active components, poor uniform dispersion, raw material utilization, cumbersome preparation process and long time.
The main reason is that conventional activated carbon carriers are mostly micropores, mesopores, and macropores, and the area of ​​micropores with a pore size less than 10 Å accounts for more than 80% of the total surface area, resulting in many macromolecular inorganic salts containing active metal components, Organic salts or oxides are blocked due to the sieving effect. Even if they maintain a long residence time, it is difficult to adsorb and deposit on the inner surface through the micropores of activated carbon, so that the absolute majority of the inner pore surface is not fully utilized. The loading rate is low; and some active metals with low molecular or ion diameters and strong adsorption can be freely deposited and adsorbed in the micropores of activated carbon, but due to the large number of irregular particles in the process of molecular or ion movement Large pores and hollow, limited by the movement resistance, the amount of active components that will be adsorbed or deposited will also be greatly reduced, and will require a longer residence time; due to the uneven distribution of the activated carbon carrier pore size, it determines the activity of the loaded carbon. The dispersion of the metal is uneven; in addition, in order to remove the impurities in the micropores of the active carrier, it is necessary to carry out repeated acid washing, alkali washing and deionized water washing, which makes the catalyst preparation process long and expensive, and there are subsequent environmental protection problems. a series of questions, etc.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0029] Weigh 10g Cu(NO 3 ) 2 Dissolve it in 200mL of deionized water, and form a solution after fully stirring as catalyst impregnation solution A, and place it in a closed container with nitrogen protection.

[0030] Commercially available coconut shell granular activated carbon is selected as the catalyst carrier. The main properties of the activated carbon are: moisture content 5.8%, specific surface area 928m 2 / g, average pore diameter 8.8A, iodine adsorption value 700mg / g, particle size 3mm. Weigh 15g of this kind of activated carbon and place it in a tubular electric heating furnace, and heat it to 420°C at a heating rate of 15-20°C / min under the protection of nitrogen. Quickly move the activated carbon to an airtight container filled with catalyst impregnation solution A, and let it stand for 3 minutes. With the rapid decrease of temperature, the copper nitrate in the catalyst impregnation solution A was fully loaded and deposited on the activated carbon support. Af...

Embodiment 2

[0032] Weigh 10g ZnCL 2 Dissolve in 200mL of deionized solution, and form a solution after fully stirring as catalyst impregnation solution B, and place it in a closed container with nitrogen protection.

[0033] Weigh 30 g of commercially available nut shell granular carbonized material and place it in a tubular heating furnace, and heat it to 900 °C at a heating rate of 10 °C to 20 °C / min under the protection of nitrogen. Start the steam valve of the steam generator to feed superheated steam into the inner tube of the heating furnace containing the carbonized material, and maintain the temperature of the inner tube at 850°C to 900°C for 8 minutes to activate the carbonized material. Stop heating, increase the flow rate of nitrogen to cool down, and when the temperature of the inner tube of the heating furnace drops to 500 °C, quickly move the activated carbon to a closed container with catalyst impregnation solution B and let it stand for 1 min. With the rapid drop of tempe...

Embodiment 3

[0035] Weigh 5g Cu(NO 3 ) 2 , 5g Mn(NO 3 ) 2 .4H 2 O was dissolved in 250 mL of deionized water, and after being fully stirred, a solution was formed as catalyst impregnation solution C, which was placed in a closed container with nitrogen protection.

[0036] Commercially available apricot shell granular activated carbon was selected as the catalyst carrier. The main properties of the activated carbon were: moisture content 6.2%, specific surface area 780m 2 / g, average pore diameter 10A, iodine adsorption value 690mg / g, particle size 3mm. Weigh 15g of this activated carbon and place it in a tubular electric heating furnace, and heat it to 500°C at a heating rate of 15-20°C / min under the protection of nitrogen. Quickly move the activated carbon to an airtight container filled with catalyst impregnation solution C, and let it stand for 2.5 minutes. Copper nitrate and manganese nitrate in catalyst impregnation solution C were fully loaded and deposited on the activated ca...

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PUM

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Abstract

The invention relates to a waste water treatment catalyst and a preparation method thereof. The catalyst of the invention takes active carbon as a carrier and one or several of oxides of metals such as copper, iron, manganese, vanadium, zinc and titanium as an active ingredient. The preparation method comprises: firstly, preparing high-temperature active carbon carrier at 350 to 700 DEG C; secondly, immersing the high-temperature active carbon carrier in the immersion liquor containing active metal components or spraying immersion liquor containing active metal components to immerse the high-temperature active carbon carrier so as to load a catalytic active component onto the active carbon carrier quickly; and finally, cooling, washing and drying to obtain the catalyst. The catalyst prepared by the method has the advantages that the content of the active metal components is high, and the active metal components are insusceptible to loss in waste water. The catalyst is mainly used in the catalytic oxidization treatment process of waste water.

Description

technical field [0001] The invention relates to a preparation method of a wastewater treatment catalyst, in particular to a preparation method of a catalytic oxidation catalyst for wastewater treatment. Background technique [0002] With the increasingly stringent global environmental protection regulations, the control indicators for sewage discharge standards are getting higher and higher. Under this form, wastewater catalytic oxidation treatment methods have been paid more and more attention to and adopted by people, such as the catalytic wet method of high-concentration sewage Oxidation, electrolytic catalytic oxidation, photocatalytic oxidation, advanced oxidation, etc. In the process of catalytic oxidation of wastewater, in order to obtain the ideal treatment effect and keep the cost of wastewater treatment low by reducing the reaction temperature and pressure, the preparation of cheap catalysts with high active components, high strength and high stability has undoubte...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/72B01J23/06B01J23/889B01J37/02C02F1/78
Inventor 郭宏山朱卫
Owner CHINA PETROLEUM & CHEM CORP
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