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An Efficient Methanol Decomposition Copper-Based Catalyst for Hydrogen Production

A copper-based catalyst, methanol decomposition technology, applied in the direction of catalyst activation/preparation, metal/metal oxide/metal hydroxide catalyst, physical/chemical process catalyst, etc., can solve the problem of poor catalyst stability and poor catalyst selectivity Excellent, narrow catalyst reaction temperature zone, etc., to achieve the effects of easy washing, long service life, and good low-temperature activity

Active Publication Date: 2020-05-12
SHANDONG QILU KELI CHEMICAL RESEARCH INSTITUTE CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, Cu-based catalysts still have the following disadvantages: (1) The reaction temperature zone of the catalyst is relatively narrow, and the optimum active zone is 260°C-280°C; the reaction temperature is too low, and the activity is poor; the reaction temperature is too high, and the Cu grains in the catalyst grow. The speed is fast, causing the stability of the catalyst to deteriorate and the life-span to be short; (2) Cu-Zn-Al catalyst selectivity is not good, mainly due to ZnO and Al 2 o 3 All belong to amphoteric compounds, which are easy to form acid centers under the influence of various conditions; according to literature reports, the incompletely coordinated aluminum atoms on the surface are connected to form acid centers, which can convert methanol to form hydrocarbons and other by-products; (3) residual sodium content in the catalyst High, affecting catalyst activity
[0008] The active temperature range and selectivity of the catalyst prepared by the above method still need to be further improved

Method used

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  • An Efficient Methanol Decomposition Copper-Based Catalyst for Hydrogen Production
  • An Efficient Methanol Decomposition Copper-Based Catalyst for Hydrogen Production
  • An Efficient Methanol Decomposition Copper-Based Catalyst for Hydrogen Production

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0052] 110g aluminum nitrate (Al(NO 3 ) 3 9H 2 O) and 32g magnesium nitrate (Mg(NO 3 ) 2 ·6H 2 O) adding 415mL deionized water to make molar concentration is 1mol / L mixed salt solution A; 123g copper nitrate (Cu(NO 3 ) 2 ·3H 2 O), 148g zinc nitrate (Zn(NO 3 ) 2 ·6H 2 O) add 1.0L deionized water to form solution B; Take by weighing 190g sodium carbonate (Na 2 CO 3 ) was dissolved in 1.5L of water to form solution C.

[0053] Put solution A and 0.4L of solution C into the precipitation container at the same time under stirring, add 100mL deionized water into the container in advance, and heat it to 35°C, control the temperature of the reaction process at 35°C, and control the reaction pH value at about 8.5 , aged under reaction conditions for 3h after precipitation. After aging, add 0.5 mol of methanol to it and raise the temperature to 40°C. Solution B and the remaining 1.1L solution C are simultaneously dripped into the precipitation container under stirring. The ...

Embodiment 2

[0056] 170g aluminum nitrate (Al(NO 3 ) 3 9H 2 O) and 26g magnesium nitrate (Mg(NO 3 ) 2 ·6H 2 O) adding 550mL deionized water to make molar concentration is 1mol / L mixed salt solution A; 157g copper nitrate (Cu(NO 3 ) 2 ·3H 2 O), 75g zinc nitrate (Zn(NO 3 ) 2 ·6H 2 O) add 0.8L deionized water to form solution B; Take by weighing 270g potassium carbonate (K 2 CO 3 ) was dissolved in 1.5L of water to form solution C.

[0057] Put solution A and 0.7L of solution C into the precipitation container while stirring, add 100mL of deionized water in advance, and heat it to 50°C. The temperature of the reaction process is controlled at 50°C, and the reaction pH value is controlled at 7.5 After precipitation, it was aged for 3h under the reaction conditions. After aging, add 0.98 mol of ethanol to it, and raise the temperature to 60°C. Solution B and 0.7L of solution C are simultaneously dripped into the precipitation container under stirring. The temperature of the reactio...

Embodiment 3

[0060] 235g aluminum nitrate (Al(NO 3 ) 3 9H 2 O) and 23g calcium nitrate (Ca(NO 3 ) 2 ) was added with 770mL deionized water to form a molar concentration of 1mol / L mixed salt solution A; 93g copper nitrate (Cu(NO 3 ) 2 ·3H 2 O), 112g zinc nitrate (Zn(NO 3 ) 2 ·6H 2 O) add 1.0L deionized water to form solution B; Take by weighing 106g sodium carbonate (Na 2 CO 3 ) and 164g sodium bicarbonate (NaHCO 3 ) was dissolved in 1.5L of water to form solution C.

[0061] Put solution A and 1L of solution C into the sedimentation container while stirring, add 100mL deionized water in advance, and heat it to 600°C. The temperature of the reaction process is controlled at 60°C, and the reaction pH value is controlled at about 6.5 , aged under reaction conditions for 3h after precipitation. After aging, add 0.4mol propanol to it, and raise the temperature to 80°C, and drop solution B and 0.5L solution C into the precipitation container simultaneously under stirring, control th...

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Abstract

An efficient copper-based catalyst for hydrogen production from methol, the catalyst is CuO, ZnO, Al 2 O 3 ,M x O Y The mixture, the weight percentage content of each component is as follows: CuO is 10-60%, ZnO is 10-60%, Al 2 O 3 is 5‑50%, M x O Y It is 1-10%, in which the alkaline earth metal M is selected from one of Mg, Ca, Ce and Sr, and the following preparation method is adopted: (1) Al-M modification is prepared by modifying the alumina support by adding alkaline earth metals Carrier; (2) Add low-molecular alcohol to the mother liquor of the modified carrier, and then add active metal salt solution and alkaline precipitant to perform a precipitation reaction. After the reaction is completed, solid-liquid separation, washing, drying, and roasting are performed to obtain the catalyst. The catalyst prepared by the preparation method provided by the invention not only has high catalytic activity, wide reaction temperature range and good low-temperature activity, but also has good selectivity, few by-products and long service life.

Description

technical field [0001] The invention relates to the technical field of hydrogen production by methanol decomposition, in particular to an efficient copper-based catalyst for hydrogen production by methanol decomposition. Background technique [0002] Hydrogen production by methanol decomposition is a relatively economical hydrogen production method. The reaction process couples the endothermic methanol decomposition reaction and the exothermic carbon monoxide shift reaction, which not only overcomes the danger that the catalyst may be sintered, but also solves the need for external Defects that provide more energy. [0003] The core of methanol hydrogen production technology is the catalyst. At present, the methanol decomposition hydrogen production catalyst widely used in industry is Cu-based catalyst. This type of catalyst has relative advantages in terms of methanol conversion activity, reaction selectivity, operating temperature and raw material cost. . However, Cu-bas...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/80B01J23/83C01B3/32
CPCC01B3/326B01J23/002B01J23/80B01J23/83B01J37/03B01J37/031B01J37/08B01J2523/00B01J35/394B01J35/613B01J35/633B01J35/647B01J35/615B01J2523/17B01J2523/24B01J2523/27B01J2523/31B01J2523/3712B01J2523/23B01J2523/22
Inventor 郭瑞孙晓明李永超翟西平张路平
Owner SHANDONG QILU KELI CHEMICAL RESEARCH INSTITUTE CO LTD