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Sulfur-tolerant catalyst for gas deoxidation as well as preparation method and application thereof

A catalyst and gas technology, applied in the field of catalyst for gas deoxidation and its preparation, can solve the problems of easy deactivation of palladium, high catalyst cost, easy loss of palladium and the like

Active Publication Date: 2012-07-11
XINDI ENERGY ENG TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The catalyst has good activity, but the cost of the catalyst is relatively high. Palladium as the main active component is easily deactivated in a sulfur environment. At the same time, palladium is easily lost at high temperatures, and its hydrothermal stability is not outstanding.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

preparation example Construction

[0038] The preparation method of deoxidation catalyst of the present invention is as follows:

[0039] (1) Select a suitable inert carrier material as the catalyst skeleton.

[0040] (2) Mix aluminum hydroxide with commercially available or self-made cerium-zirconium composite oxides according to a molar ratio of 0.5 to 5, add 0.1 to 2% by volume of dilute nitric acid solution, the volume of dilute nitric acid added is equal to cerium-zirconium composite oxide and 2 to 20 times the mixing volume of aluminum hydroxide, wet ball milling into slurry.

[0041] (3) Coating the prepared slurry onto an inert catalyst carrier.

[0042] (4) Drying, such as drying at 80-150°C for 6-15 hours, then at 500-900°C, calcining for 2-6 hours, and heating up to 500-900°C can be temperature-programmed within 2-5 hours, thus obtaining the obtained Catalyst support is required.

[0043] (5) The above steps can be repeated until the desired loading is obtained.

[0044] (6) Prepare molybdenum-co...

Embodiment 1

[0061] Preparation of cerium-zirconium composite oxide: Weigh 64.4 g of zirconium oxychloride and 86.8 g of cerium nitrate, respectively, and dissolve them in 500 ml of deionized water, and mix the two solutions after complete dissolution. Under stirring conditions, add ammonia solution with a concentration of 25% to the mixed solution dropwise, and control the pH value of the end point of the titration to be 9.5 to 10. After the titration is completed, the precipitate is allowed to stand for 12 hours, and the precipitate is filtered and washed until the pH value is reached. 7, dried at 100°C for 6 hours, and ground into powder. The temperature was programmed to rise to 900°C within 3 hours, and calcined for 4 hours to obtain the structural formula CeO 2 · ZrO 2 57.89 g of cerium-zirconium composite oxides are used for subsequent use.

[0062] Weigh 100 g of alumina pellets (volume 66 ml) as an inert carrier for the catalyst. Weigh 30g of cerium-zirconium composite oxide an...

Embodiment 2

[0067] The carrier preparation process is the same as in Example 1.

[0068] Weigh 50 g of ammonium dimolybdate, dissolve it in 100 ml of 15% ammonia solution in deionized water, and prepare ammonium dimolybdate solution. The prepared catalyst carrier was impregnated therein for 3 hours, dried at 100° C. for 12 hours, and the above experiment was repeated twice.

[0069] Weigh 10 g of lanthanum nitrate, dissolve it in 100 ml of deionized water to prepare a lanthanum nitrate solution, impregnate the catalyst precursor loaded with ammonium dimolybdate in it for 3 hours, and dry at 100° C. for 12 hours.

[0070] The catalyst precursor loaded with molybdenum and lanthanum was programmed to heat up to 700° C. within 3 hours, and calcined for 2 hours to obtain a catalyst precursor loaded with molybdenum trioxide and lanthanum oxide.

[0071] Measure 66ml of chloroplatinic acid solution with a concentration of 10mg / ml, soak the prepared catalyst pellets for 30 minutes, dry at 100°C ...

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PUM

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Abstract

The invention provides a sulfur-tolerant catalyst for gas deoxidation as well as a preparation method and an application thereof. The catalyst contains a catalyst carrier, noble metal Pt, transition metal Mo and rare earth metal oxides, wherein the noble metal Pt and transition metal Mo serve as catalyst active components and are loaded on the catalyst carrier, and the rare earth metal oxides serve as catalyst promoter and are loaded on the catalyst carrier; and the catalyst carrier is formed by an inert first carrier with porous structure and a metal oxide second carrier applied onto the first carrier. The deoxidation catalyst has the advantages of low noble metal loading capacity, good low-temperature activity and high hydrothermal stability, and further has good sulfur tolerance.

Description

technical field [0001] The invention relates to the fields of gas treatment and energy utilization, in particular to a catalyst for gas deoxidation and its preparation method and application Background technique [0002] Gas refers to the coalbed methane extracted from underground mines by using underground extraction technology in the process of coal mining for the sake of coal mining safety. Due to the large amount of air mixed in during the pumping process, the general volume concentration of methane is ≤40%, while the highest concentration of oxygen volume can reach about 15%. The combustion products of gas are water and carbon dioxide, which will not pollute the environment, and is recognized as a high-quality clean energy by the world. [0003] In my country, most of the gas can only be used locally as civil fuel, and most of it is burned and vented. According to statistics, the gas emitted by coal mining in my country is as high as 20 billion m3 every year. 3 , acco...

Claims

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Application Information

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IPC IPC(8): B01J23/652C10L3/10
Inventor 王义于建涛常俊石雷志祥孙树英
Owner XINDI ENERGY ENG TECH