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Dehydrogenation catalyst and method for preparing same

A technology of catalysts and additives, which is applied in the field of dehydrogenation catalysts and its preparation, can solve the problems of not completely solving the problem of wet water, large amount of precious metals, and low dispersion, and achieves obvious dehydrogenation effect, strong anti-toxicity, High catalytic activity at low temperature

Active Publication Date: 2012-05-30
ZHEJIANG UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] It is the most effective and convenient method to remove hydrogen by catalytically combining hydrogen and oxygen into water. In order to ensure its high efficiency, catalysts with noble metals Pt and Pd are generally used as the main active components. However, in order to ensure the high efficiency, long life and low cost of the catalyst, Still need to solve the following problems from the prior art: 1, because the hydrogen-oxygen recombination reaction is a gas-solid heterogeneous catalytic reaction, in order to keep the activity of the catalyst, the surface of the catalyst cannot be wetted by liquid water (i.e. wet water problem), while the product of the reaction is It is water, so how to control the temperature of the reaction system is extremely critical, neither too high nor too low. Proper reaction temperature control can make the product water leave the reaction system in gaseous form to ensure the effective operation of the catalyst
[0004] Existing hydrogen elimination catalysts have patent reports (US4459270, CN1040156A, etc.), but generally all use two kinds of noble metals, Pt and Pd, as the main agent, and due to the limitation of its preparation method, there is not high dispersion and the amount of noble metals (≥ 1wt %) are larger and more costly, and do not fully address the wet water problem

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0021] Weigh the dried Al 2 o 3 10 grams (20 mL, measured with a graduated cylinder) of the carrier is set aside. Add 2ml of heptanol, 6ml of ethanol, and 5.0ml of H with a concentration of 0.010gPd / ml into a 100ml three-necked flask. 2 PdCl 6 Solution, 5.0ml concentration of 0.0080gNi / ml Ni(NO 3 ) 2 Solution, 5.0ml concentration of 0.0080gSm / ml Sm(NO 3 ) 3 Solution, placed under 40kHz ultrasonic vibration, stirred at 30°C for 1 hour to form a mixed solution, and then Al 2 o 3 The carrier was added to the mixture and soaked for 3 hours. The above-mentioned processes are all carried out under the action of ultrasonic vibration. After the impregnation, the entire reaction mixture is dried at 110°C (weight gain ≤ 5%), and then placed in a muffle furnace for 450°C roasting for 4 hours, and then reduced by hydrogen. The temperature was controlled at 400° C., the time was 4 hours, the space velocity was 800 / hour (volume), and 20 ml of finished light gray catalyst was obtain...

example 2

[0024] Weigh the dried Al 2 o 3 10 grams (20 mL, measured with a graduated cylinder) of the carrier is set aside. Add 2ml of heptanol, 6ml of ethanol, and 5.0ml of H with a concentration of 0.010gPd / ml into a 100ml three-necked flask. 2 PdCl 6 Solution, 5.0ml concentration of 0.0080gNi / ml Ni(NO 3 ) 2 Solution, 5.0ml of La(NO 3 ) 3 Solution, placed under 50Hz ultrasonic vibration, stirred at 30°C for 1 hour to form a mixed solution, and then Al 2 o 3 The carrier was added to the mixture and soaked for 4 hours. The above processes are all carried out under the action of ultrasonic vibration. After the impregnation, the entire reaction mixture is dried at 120°C, then placed in a muffle furnace for 450°C roasting for 4 hours, and then reduced by hydrogen. The reduction temperature is controlled at 300°C for 5 hour, airspeed 800h -1 (volume), obtain light gray catalyst finished product 20ml.

[0025] 3ml of the above-mentioned catalyst is loaded into the catalyst activit...

example 3

[0027] Weigh the dried Al 2 o 3 10 grams (20 mL, measured with a graduated cylinder) of the carrier is set aside. Add 2ml of heptanol, 6ml of ethanol, and 5.0ml of H with a concentration of 0.010gPd / ml into a 100ml three-necked flask. 2 PdCl 6 Solution, 5.0ml concentration of 0.0080gFe / ml Fe(NO 3 ) 2 Solution, 5.0ml concentration of 0.0080gSm / ml Sm(NO 3 ) 3 Solution, placed under 60Hz ultrasonic vibration, stirred at 50°C for 1 hour to form a mixed solution, and then Al 2 o 3 The carrier was added to the mixture and soaked for 4 hours. The above processes are all carried out under the action of ultrasonic vibration. After the impregnation, all the reaction mixture is dried at 100°C, then placed in a muffle furnace for 5 hours at 450°C, and then reduced by hydrogen. The reduction temperature is controlled at 300°C for 5 hours. hour, airspeed 800h -1 (volume), obtain light gray catalyst finished product 20ml.

[0028] 3ml of the above-mentioned catalyst is loaded into t...

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PUM

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Abstract

The invention discloses a dehydrogenation catalyst, which comprises a carrier, and an active component and an accessory ingredient which are carried on the carrier, wherein the carrier is Al2O3; the active component is a noble metal Pd; the accessory ingredient is a metal accessory ingredient which is the mixture of any two or more than three of Ni, Fe, Ba, Ce, La, Sm or Pr; the load of the noblemetal Pd is 0.25 to 1.0 weight percent; and the ratio of the amount of the noble metal Pd to the total amount of metallic substances in the metal accessory ingredient is 0.3-1.5:1. The invention alsodiscloses a method for preparing the dehydrogenation catalyst and an oxyhydrogen complex reaction applied to a dehydrogenation process in an environment with little hydrogen. The dehydrogenation catalyst has the following advantages that: due to the adoption of special preparation technology, the obtained dehydrogenation catalyst of the invention has the characteristics of high dispersity, high low-temperature activity, high poison resistance, high moisture resistance and the like; and as the load of the heavy metal Pd is only 0.25 to 1.0 weight percent, high activity and low cost are achieved.

Description

(1) Technical field [0001] The invention relates to a hydrogen-removing catalyst used in a hydrogen-containing environment and a preparation method thereof. The working principle is to eliminate trace amounts of hydrogen in the environment by catalyzing hydrogen-oxygen recombination into water. (2) Background technology [0002] With the widespread use of organic hydrogenation synthesis processes, there are more and more micro-hydrogen environments. Such as various hydrogen laboratories; during the charging and discharging process of lead-acid batteries, part of the water is decomposed to produce hydrogen; in nuclear submarines, the water electrolysis oxygen generator is used to produce oxygen for the submarine crew to breathe, and the hydrogen is discharged out of the boat; nuclear power plant containment Inside, hydrogen gas is also produced due to the reaction of high-temperature metals with water. All these places where hydrogen is used and where traces of hydrogen are ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/89B01J23/44B01J37/34C01B5/00
Inventor 祝一锋铙国武吴庆安单尚
Owner ZHEJIANG UNIV OF TECH
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