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Preparation and application of Pt QDs-CeO2/Co modified Y-type molecular sieve hydrogenation catalyst

A hydrogenation catalyst and molecular sieve technology, applied in the direction of molecular sieve catalyst, catalyst activation/preparation, physical/chemical process catalyst, etc., can solve the problems of poor catalytic effect and high cost, and achieve the goal of reducing price, increasing activity and reducing electron density. Effect

Inactive Publication Date: 2021-02-05
杭州靖舒新材料有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] In view of the shortcomings of the existing hydrogenation catalysts in the application of direct coal liquefaction oil products to prepare industrial white oil, the catalytic effect is not good and the cost is high, the present invention provides a Pt QDs-CeO 2 Preparation and Application of Hydrogenation Catalyst of / Co Modified Y Molecular Sieve

Method used

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  • Preparation and application of Pt QDs-CeO2/Co modified Y-type molecular sieve hydrogenation catalyst
  • Preparation and application of Pt QDs-CeO2/Co modified Y-type molecular sieve hydrogenation catalyst

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0027] (1) Preparation of catalyst

[0028] Step 1: Add NaY-type molecular sieves to deionized water, sonicate for 20 minutes at room temperature, and then add Co(NO 3 ) 2 ·6H 2 O, continue to stir for 3h, filter after stirring and place the filtered product in a 100% water vapor atmosphere at a temperature of 570°C for 2h, then use NH 4 The Cl solution was exchanged and washed for 6 times, and then placed in a muffle furnace for calcination at 400 °C for 3 h; then the calcined sample was placed in EDTA-2Na solution, stirred vigorously in a water bath at 85 °C for 5 h, after the stirring was completed, it was filtered and used The filtered product was washed with deionized water until neutral, and then the product was dried in a vacuum oven at 100°C for 12 hours to obtain a Co-modified Y-type molecular sieve. Among them, Co(NO 3 ) 2 ·6H 2 The consumption ratio of O and NaY type molecular sieve is 0.32g:1g, and the consumption ratio of NaY type molecular sieve and EDTA-2N...

Embodiment 2

[0034] (1) Preparation of catalyst

[0035] Step 1: Add NaY molecular sieves into deionized water, sonicate for 30 minutes at room temperature, and then add Co(NO 3 ) 2 ·6H 2 O, continue to stir for 4h, filter after the stirring is over and place the filtered product in a 100% water vapor atmosphere at a temperature of 570°C for 3h, then filter the molecular sieve with NH 4 The Cl solution was exchanged and washed 7 times, and then placed in a muffle furnace for calcination at 400 °C for 4 h; then the calcined sample was placed in EDTA-2Na solution, stirred vigorously in a water bath at 90 °C for 5 h, filtered after the stirring was completed, and used The filtered product was washed with deionized water until neutral, and then the product was dried in a vacuum oven at 92°C for 14 hours to obtain a Co-modified Y-type molecular sieve. Among them, Co(NO 3 ) 2 ·6H 2 The consumption ratio of O and NaY type molecular sieve is 0.46g:1g, and the consumption ratio of NaY type mo...

Embodiment 3

[0041] (1) Preparation of catalyst

[0042] Step 1: Add NaY molecular sieves into deionized water, sonicate for 25 minutes at room temperature, and then add Co(NO 3 ) 2 ·6H 2 O, continue to stir for 4h, filter after the stirring is over and place the filtered product in a 100% water vapor atmosphere at a temperature of 570°C for 3h, then filter the molecular sieve with NH 4 The Cl solution was exchanged and washed 8 times, and then placed in a muffle furnace for calcination at 400 °C for 3 h; then the calcined sample was placed in EDTA-2Na solution, stirred vigorously in a water bath at 86 °C for 4 h, filtered and used The filtered product was washed with deionized water until neutral, and then the product was dried in a vacuum oven at 96°C for 15 hours to obtain a Co-modified Y-type molecular sieve. Among them, Co(NO 3 ) 2 ·6H 2 The consumption ratio of O and NaY type molecular sieve is 0.42g:1g, and the consumption ratio of NaY type molecular sieve and EDTA-2Na solutio...

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Abstract

The invention belongs to a white oil processing technology, and particularly relates to preparation and application of a Pt QDs-CeO2 / Co modified Y-type molecular sieve hydrogenation catalyst. The preparation method of the molecular sieve comprises the following steps: carrying out Co modification on a NaY type molecular sieve by using an aqueous solution ion exchange method, carrying out aftertreatment on the molecular sieve by using disodium ethylenediaminetetraacetate, loading CeO2 on the surface of the Co modified Y type molecular sieve by using Ce(NO3)3.6H2O as a raw material, and depositing Pt QDs on the surface of the CeO2 / Co modified Y type molecular sieve to obtain the Pt QDs-CeO2 / Co modified Y type molecular sieve hydrogenation catalyst. The catalyst disclosed by the invention islow in cost and good in catalytic effect in the application of preparing industrial white oil from direct coal liquefaction oil products.

Description

technical field [0001] The invention belongs to white oil processing technology, in particular to a Pt QDs-CeO 2 Preparation and application of Co-modified Y-type molecular sieve hydrogenation catalyst. Background technique [0002] White oil is a colorless, odorless, non-corrosive special mineral oil obtained through deep refining to remove impurities such as aromatics, oxygen, sulfur and nitrogen. It is colorless, odorless, chemically inert and has good light stability. Its basic composition is a saturated hydrocarbon structure, and its average relative molecular weight is usually in the range of 250-450; the composition of white oil is basically saturated hydrocarbons (cycloalkanes and alkanes). my country's white oil is divided into three types: industrial grade, cosmetic grade, and food and pharmaceutical grade. [0003] There are two main production methods for white oil: one is to use the lubricating oil fraction of low-sulfur paraffin base or naphthenic crude oil a...

Claims

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Application Information

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IPC IPC(8): B01J29/14B01J37/30B01J35/10C10G45/12
CPCB01J29/146B01J37/30C10G45/12B01J2229/186B01J2229/24C10G2300/201C10G2300/302C10G2300/70C10G2400/14B01J35/394B01J35/61
Inventor 戈锐林
Owner 杭州靖舒新材料有限公司