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Monolithic catalyst and preparation and application thereof

A monolithic catalyst, monolithic catalyst technology, applied in the field of coal chemical industry, can solve the problems of low reaction activity, low operating space velocity, high energy consumption and material consumption, etc.

Active Publication Date: 2018-02-16
DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Due to the low reaction activity and low operating space velocity, in order to meet the demand for raw material gas in the downstream link, it is necessary to invest in a huge production device, which increases the input cost, and the energy consumption and material consumption are relatively high.

Method used

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  • Monolithic catalyst and preparation and application thereof
  • Monolithic catalyst and preparation and application thereof
  • Monolithic catalyst and preparation and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0055] a) Coating preparation: 10g of hydroxyapatite Ca 5 (PO 4 ) 3 (OH) and 60 g of deionized water were mixed in a 100 ml ball mill tank, the speed of the ball mill was adjusted to 500 r / min, and the catalyst coating carrier slurry was obtained after ball milling for 6 hours. Select a monolithic catalyst carrier with a pore size of 400 holes / square inch, dip the coating carrier slurry for 3 minutes, then use compressed air to remove excess liquid slurry in the channel of the monolithic catalyst carrier, and repeat the above coating after drying. The coating step was carried out 3 times, and the weight of the coated catalyst promoter was weighed to be 20% of the overall catalyst carrier, and it was placed in a muffle furnace for calcination at 400° C. for 2 h.

[0056] b) Take 0.03g Nd(NO 3 ) 3 ﹒ 6H 2 O dissolved in 5ml of water to form Nd(NO 3 ) 3 solution, impregnating the above-mentioned additive-free carrier in the solution for 2 hours, and then drying at 80° C. f...

Embodiment 2

[0062] a) Coating preparation: 10g of hydroxyapatite Ca 5 (PO 4 ) 3 (OH) and 60 g of deionized water were mixed in a 100 ml ball mill tank, the speed of the ball mill was adjusted to 500 r / min, and the catalyst coating carrier slurry was obtained after ball milling for 6 hours. Select a monolithic catalyst carrier with a pore size of 400 holes / square inch, dip the coating carrier slurry for 3 minutes, then use compressed air to remove excess liquid slurry in the channel of the monolithic catalyst carrier, and repeat the above coating after drying. The coating step was carried out 3 times, and the weight of the coated catalyst promoter was weighed to be 20% of the overall catalyst carrier, and it was placed in a muffle furnace for calcination at 400° C. for 2 h.

[0063] b) Take 0.03g Nd(NO 3 ) 3 ﹒ 6H 2 O dissolved in 5ml of water to form Nd(NO 3 ) 3 solution, impregnating the above-mentioned additive-free carrier in the solution for 2 hours, and then drying at 80° C. f...

Embodiment 3

[0068] a) Coating preparation: 10 g of Beta molecular sieve and 60 g of deionized water were mixed, ultrasonically treated for 30 min and then stirred for 2 h to obtain catalyst coating carrier slurry. Select an integral catalyst carrier with a channel mesh number of 600 holes / square inch, dip the coating carrier slurry for 3 minutes, then use compressed air to remove excess liquid slurry in the channel of the integral catalyst carrier, and repeat the above coating after drying. The coating step was carried out 3 times, and the weight of the coated catalyst promoter was weighed to be 20% of the overall catalyst carrier, and it was placed in a muffle furnace for calcination at 400° C. for 2 h.

[0069] b) take 1.92g (NH 4 ) 2 HPO 4 Dissolve in 10ml of water to form a solution, impregnate the additive-free carrier prepared in the above steps in this solution for 2 hours, then dry it at 80°C for 12 hours, place it in a muffle furnace and bake it at 400°C for 2 hours to obtain a...

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Abstract

The invention provides a high-dispersion monolithic catalyst for selectively catalytic oxidization of H2 in the atmosphere of high-concentration CO and a preparation method and application of the high-dispersion monolithic catalyst. The catalyst is suitable for a fixed bed reactor and has a multilayer structure, wherein the multilayer structure includes but not limited to a shell layer, an activecomponent layer, a carrier coating and a honeycomb carrier layer. The catalyst can be applied to the process of the selectively catalytic oxidization of H2 in the atmosphere of the high-concentrationCO, wherein the ratio of H2 to O2 in feed gas is 1:1 to 1:3, the reaction temperature is 150-250 DEG C, and the pressure is 0.3-0.6 MPa; besides, when the airspeed is 3000-20000h<-1>, the content of output H2 is less than 100 ppm, so that the reaction requirements of subsequent vapor catalytic coupling synthesis of oxalate by using CO are met.

Description

technical field [0001] The invention belongs to the field of coal chemical industry, in particular to a H 2 Highly dispersed monolithic catalyst for selective catalytic oxidation, its preparation method and application. Background technique [0002] Ethylene glycol is an important chemical basic raw material used in the production of various polyesters and antifreeze agents. At present, the ethylene glycol demanded by my country needs to rely heavily on imports, and the synthesis gas (CO+H) is produced through coal gasification. 2 ), the "coal-to-ethylene glycol" technology, which combines oxalate with CO catalytic coupling and hydrogenation to generate ethylene glycol, can make full use of my country's relatively abundant coal resources to produce ethylene glycol, and may gradually replace the "petroleum route "technology. Then reduce my country's dependence on oil imports, and change the current situation in which ethylene glycol is in short supply due to lack of oil res...

Claims

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Application Information

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IPC IPC(8): B01J23/44B01J23/652B01J23/89B01J27/185B01J29/22B01J29/74B01J29/85B01J37/02C01B32/40B01J35/02
CPCB01J23/44B01J23/6525B01J23/894B01J27/1856B01J29/22B01J29/7415B01J29/85B01J37/0232C01B2210/0004C01B2210/0053B01J35/394B01J35/396B01J35/393
Inventor 王树东苏宏久李晓彤李德意
Owner DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI
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