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Supported catalyst for efficiently catalyzing decomposition of N2O as well as preparation method and application of supported catalyst

A supported catalyst, catalytic decomposition technology, applied in catalyst activation/preparation, physical/chemical process catalyst, separation method, etc., can solve the problems of secondary pollution, poor catalytic activity, complex preparation method, etc. Simple preparation method and high catalytic activity

Inactive Publication Date: 2018-09-07
BEIJING INSTITUTE OF PETROCHEMICAL TECHNOLOGY
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the existing supported composite metal oxide catalysts need to support a large amount of active components in order to have the catalytic decomposition efficiency equivalent to that of noble metal catalysts, and the catalytic activity is poor in the presence of oxygen and water vapor, and the preparation method is relatively complicated, which is easy to cause secondary secondary pollution

Method used

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  • Supported catalyst for efficiently catalyzing decomposition of N2O as well as preparation method and application of supported catalyst
  • Supported catalyst for efficiently catalyzing decomposition of N2O as well as preparation method and application of supported catalyst

Examples

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preparation example Construction

[0025] Specifically, the efficient catalytic decomposition of N 2 The preparation method of the loaded catalyst of O may comprise the following steps:

[0026] Step A, carrier preparation: put the pseudo-boehmite in a muffle furnace, raise the temperature to 200°C at 5°C / min and keep the temperature for 2h, then raise the temperature to 550°C at 5°C / min and roast for 4h to obtain the pseudo-boehmite γ-Al calcined with diaspore 2 o 3 carrier. Wherein, the pseudo-boehmite is preferably P-DF-03 ordinary pseudo-boehmite.

[0027] Step B, preparation and impregnation of precursor solution: γ-Al roasted per 5 g of pseudo-boehmite 2 o 3The carrier uses the ratio of 0.76-2.27g copper nitrate, 0.84-2.54g yttrium nitrate, 0-1.50g additive and 3-5mL deionized water. Add copper nitrate, yttrium nitrate, and additive into deionized water, dissolve and Mix evenly to obtain a precursor solution; then the γ-Al of the pseudo-boehmite roasted 2 o 3 The carrier is added into the precurso...

Embodiment 1

[0035] A highly efficient catalytic decomposition of N 2 The supported catalyst of O, its preparation method can comprise the following steps:

[0036] Step a1, adding 1.82g of copper nitrate and 1.35g of yttrium nitrate to 4mL of deionized water, dissolving and mixing uniformly to obtain a precursor solution; then roasting 5g of pseudo-boehmite γ-Al 2 o 3 The carrier was added into the precursor solution, stirred and mixed evenly, and then immersed in a constant temperature water bath at 40° C. for 8 hours to obtain the impregnated precursor.

[0037] Step b1, drying: put the impregnated precursor into a drying oven, and dry at 110° C. for 12 hours to obtain a dried precursor.

[0038] Step c1, roasting: put the dried precursor into a muffle furnace, raise the temperature to 200°C at 5°C / min and keep the temperature constant for 2h, then raise the temperature to 550°C at 5°C / min and roast for 4h to obtain the roasted post catalyst powder.

[0039] Step d1, tabletting and ...

Embodiment 2

[0045] A highly efficient catalytic decomposition of N 2 The supported catalyst of O, its preparation method can comprise the following steps:

[0046] Step a2, adding 1.82g of copper nitrate and 2.25g of yttrium nitrate to 4mL of deionized water, dissolving and mixing uniformly to obtain a precursor solution; then roasting 5g of pseudo-boehmite γ-Al 2 o 3 The carrier was added into the precursor solution, stirred and mixed evenly, and then immersed in a constant temperature water bath at 40° C. for 8 hours to obtain the impregnated precursor.

[0047] Step b2, drying: put the impregnated precursor into a drying oven, and dry at 110° C. for 12 hours to obtain a dried precursor.

[0048] Step c2, roasting: put the dried precursor into a muffle furnace, raise the temperature to 200°C at 5°C / min and keep the temperature constant for 2h, then raise the temperature to 550°C at 5°C / min and roast for 4h to obtain the roasted post catalyst powder.

[0049] Step d2, tabletting and ...

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Abstract

The invention discloses a supported catalyst for efficiently catalyzing decomposition of N2O as well as a preparation method and application of the supported catalyst. The supported catalyst comprises5-15wt% of CuO, 5-15wt% of Y2O3, 0.5-10wt% of an additive, and the balance of a pseudo-boehmite roasted gamma-Al2O3 supporter, wherein the additive and CuO2 and Y2O3 which are used as the active components are loaded on the pseudo-boehmite roasted gamma-Al2O3 supporter. The preparation method comprises the following steps: feeding the pseudo-boehmite roasted gamma-Al2O3 supporter into a precursorsolution containing cupric nitrate and yttrium nitrate according to an incipient-wetness impregnation method; then drying, roasting, tabletting and screening to obtain the product. The supported catalyst can be used for catalyzing decomposition of N2O under the temperature of 400-500 DEG C; few active components are loaded, and the decomposing efficiency is high; in addition, the supported catalyst remains high catalyzing activity in the presence of oxygen and water steam; the preparation method is simple; the catalyzing cost is low; secondary pollution is avoided.

Description

technical field [0001] The invention relates to the field of supported composite metal oxide catalysts, in particular to a high-efficiency catalytic decomposition of N 2 Supported catalysts for O and their preparation methods and applications. Background technique [0002] Adipic acid and nitric acid are two important raw materials in the chemical industry, but most of the tail gases discharged from adipic acid plants and nitric acid plants contain relatively high concentrations of N 2 O. while N 2 O is a serious greenhouse gas and has a serious destructive effect on the ozone layer in the stratosphere. According to statistics, the annual emissions of N from adipic acid plants and nitric acid plants 2 The amount of O accounted for about the global N 2 5% to 10% of O emissions, so N 2 O Emission reduction work is urgent. [0003] At present, industrial reduction of N in tail gas 2 There are three main methods for O: ① pyrolysis method: the N 2 O and combustible gas a...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/83B01J23/889B01J37/02B01J37/08B01D53/86B01D53/56
CPCB01D53/8628B01D2257/402B01J23/002B01J23/83B01J23/8892B01J37/0201B01J37/088B01J2523/00B01J2523/17B01J2523/31B01J2523/36B01J2523/3712Y02C20/10
Inventor 宋永吉仇杨君黄思齐王新承李翠清王虹
Owner BEIJING INSTITUTE OF PETROCHEMICAL TECHNOLOGY