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Catalyst for eliminating hydrocarbon impurity from CO2 and its prepn and application

A carbon dioxide and catalyst technology, which is used in the catalyst, preparation and application fields for removing hydrocarbon impurities in carbon dioxide, can solve the problems of incompatibility, high space velocity, large catalyst bed resistance, etc., and achieves high purification rate and uniform distribution. , the effect of physical stability

Active Publication Date: 2006-05-17
PETROCHINA CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although this type of catalyst has good activity, it is not suitable for high space velocity, and the resistance drop of the catalyst bed is relatively large at high space velocity.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0027] Weigh 200g Al 2 o 3 The dried rubber powder was mixed with 8g scallop powder, poured into the kneader and mixed for 5 minutes. Dissolve 10 g of SnCl in deionized water 4 ·5H 2 O and 5g citric acid, and add 1.5ml nitric acid. Adding Sn-containing solution to Al 2 o 3 In the mixture, with Al 2 o 3 The powder is kneaded for about 15 minutes, and extruded into a φ4 toothed ball with 6 teeth and a 0.5 hole in the middle of the toothed ball. Blow drying at 100-120°C for 5 hours, and calcining at 980-990°C for 4 hours to make a carrier.

[0028] Weigh 100g of the prepared carrier and immerse it in a solution containing 0.32g of Pd, take it out after 30 minutes, drain the water, dry at 100-110°C for 5 hours, and bake in a muffle furnace at 500°C for 3 hours. Prepare the catalyst of the present invention. In the catalyst, Pd accounts for 0.3% of the catalyst weight, Sn accounts for 2.3% of the catalyst weight, and the carrier is θ, δ-Al 2 o 3 Mixed crystal forms. Ca...

Embodiment 2

[0032] Weigh 200g Al 2 o 3 Dry rubber powder is mixed with 10g of starch, poured into the kneader and mixed for 5 minutes. Dissolve 12g of SnCl in deionized water 4 ·5H 2 O, and add 2.0ml acetic acid and 15ml 25% silica sol. Adding Sn-containing solution to Al 2 o 3 In the mixture, with Al 2 o 3 The powder is kneaded for about 15 minutes, and extruded into a φ4 toothed ball with 6 teeth and a 0.5 hole in the middle of the toothed ball. Blast drying at 100-120°C for 5 hours, and calcining at 1000-1010°C for 4 hours to make a carrier.

[0033] Weigh 100g of the prepared carrier and immerse it in an aqueous solution containing palladium chloride, take it out after 30 minutes, drain the water, dry it at 100-110°C for 5 hours, and bake it in a muffle furnace at 500°C for 3 hours. The carrier impregnated with palladium is then immersed in an aqueous solution containing chloroplatinic acid, taken out after 20 minutes, dried at 100-110°C for 5 hours, and calcined at 500°C in ...

Embodiment 3

[0037] Weigh 200g Al 2 o 3 The dried rubber powder was mixed with 8 g of scallop powder, and mixed in a kneader for 5 minutes. Dissolve 12g of SnCl in deionized water 4 ·5H 2 O and 5g La(NO 3 ) 3 ·nH 2 O, and add 2.0ml acetic acid. with Al 2 o 3 The powder is kneaded for about 15 minutes, and extruded into a φ3.2 trilobal strip. Blast drying at 100-120°C for 5 hours, and calcining at 1000-1010°C for 4 hours to make a carrier.

[0038] Weigh 100g of the carrier prepared by the above method, immerse in the mixed solution containing Pd and Pt, take it out after 40 minutes, drain the water, dry at 100-110°C for 5 hours, and bake in a muffle furnace at 500°C for 3 hours. Prepare the catalyst of the present invention. In the catalyst, Pd accounts for 0.15% of the catalyst weight, Pt accounts for 0.15% of the catalyst weight, Sn accounts for 2.4% of the catalyst weight, and the carrier is θ, δ-Al 2 o 3 Mixed crystal form, catalyst specific surface area 110m 2 / g, pore v...

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Abstract

The catalyst suitable for eliminating hydrocarbon impurity from high concentration CO2 waste gas exhausted from industrial plant contains carrier of mixed theta- and delta-alumina crystal mainly, active component in 0.01-3.0 wt% and co-catalyst 0.10-20 wt%, and has specific surface area one 60-140 sq m / g and pore volume of 0.50-0.70 ml / g. The present invention provides also the preparation process of the catalyst. The catalyst has relatively high oxidation activity on CO and hydrocarbon, and under the conditions of space velocity of 10,000 / hr and reaction temperature below 420 deg.c, it may reduce hydrocarbon content in CO2 from 6,000 ppm to below 10 ppm, with residual O2 being 0.2-0.3 %.

Description

technical field [0001] The invention relates to a catalyst for removing hydrocarbon impurities in carbon dioxide and its preparation method and application. The catalyst is especially suitable for removing hydrocarbons and carbon monoxide in industrial carbon dioxide waste gas to obtain food-grade carbon dioxide. The catalyst can also be used for purification treatment of other organic waste gases. Background technique [0002] The exhaust gas emitted by certain production devices contains a large amount of high-concentration carbon dioxide, such as hydrogen production units in oil refineries, synthetic ammonia units, ethylene glycol units, coal-to-gas, fermentation processes, etc. The concentration of carbon dioxide emitted by some devices is above 95%, of which It contains a small amount of combustible impurities such as hydrocarbons and carbon monoxide, which can be removed by catalytic combustion to obtain high-purity carbon dioxide containing less than 10 ppm of hydroca...

Claims

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Application Information

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IPC IPC(8): B01J23/62C01B32/50
Inventor 吴美岩李赫顾青赵兴富
Owner PETROCHINA CO LTD