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Mixed metal oxide catalysts for ammonia decomposition

An oxide and catalyst technology, applied in the system field of ammonia decomposition catalyst, can solve the problems of infeasibility and poor catalyst performance.

Inactive Publication Date: 2017-02-22
SABIC GLOBAL TECH BV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, these techniques are often not commercially viable under fuel cell operating conditions due to poor catalyst performance

Method used

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  • Mixed metal oxide catalysts for ammonia decomposition
  • Mixed metal oxide catalysts for ammonia decomposition
  • Mixed metal oxide catalysts for ammonia decomposition

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0042] Example 1. Preparation of cobalt-containing catalyst

[0043] The co-precipitation method is used to prepare cobalt-containing mixed metal oxide compounds.

[0044] In an exemplary method, the precursor solution is obtained by dissolving the purity grade nitrate of the corresponding metal in distilled water: 2.47g Co(NO 3 ) 2 6H 2 O, 18.7g Mg(NO 3 ) 3 , 10.4g Al(NO 3 ) 3 And 2.238g La(NO 3 ) 3 . A solution of 0.1M NaOH used as a precipitant was prepared.

[0045] The metal salt solution is mixed to form a first solution. This produces a mixed Co, Al, La and Mg metal salt solution.

[0046] Put a certain volume of distilled water into a beaker, heat to 65°C and adjust the pH with 0.1M NaOH to reach pH=8.0. This is called the second solution. The first solution (mixed Co, Al, La and Mg metal salt solutions) and the precipitate are simultaneously introduced into the second solution under vigorous stirring. Obtain a slurry. The resulting slurry was aged in mother liquor for 2...

Embodiment 2

[0047] Example 2. Test for catalytic activity for ammonia decomposition

[0048] A test of a catalyst for decomposing ammonia into hydrogen and nitrogen was performed in a Microactivity-Reference (PID Eng&Tech, Madrid, Spain). A 0.5-1.0 g sample with a particle size of 125-250 μm was introduced into a quartz reactor (ID 6.0 mm) and activated with pure hydrogen flow at 600° C. for 5 h. After the reduction process is completed, the reactor temperature is lowered to 350°C and passed through for 1200h -1 The gas hourly space velocity (GHSV) replaces the hydrogen stream with a pure ammonia stream. Change the reaction temperature between 350°C and 600°C.

[0049] The inlet and outlet gases of the reactor were analyzed by a gas chromatograph (GC-450Varian, USA) equipped with a thermal conductivity detector and a Poropak Q column connected online.

[0050] in figure 1 In, the experimental data of the catalytic property test of the catalyst prepared in Example 1 in the ammonia decomposition...

Embodiment approach 1

[0055] Embodiment 1. A method for preparing a catalyst for ammonia decomposition, the method comprising: providing a first solution comprising: selected from cobalt soluble salt, nickel soluble salt, iron soluble salt and combinations thereof First metal soluble salt; second metal soluble salt selected from magnesium soluble salt, calcium soluble salt, strontium soluble salt, barium soluble salt and combinations thereof; selected from lanthanide soluble salt and combinations thereof And optionally, a fourth metal soluble salt selected from aluminum soluble salts, transition metal soluble salts, alkali metal soluble salts and combinations thereof; between about 6.0 and about 11.0 Co-precipitating the first metal oxide, the second metal oxide, the third metal oxide, and the optional fourth metal oxide from the first solution at pH to form a hydrotalcite-like structure material; and decompose the hydrotalcite-like structure Material to form a catalyst.

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Abstract

Systems and methods for ammonia decomposition catalysts are described. Systems and methods may include providing a first solution, where the first solution includes a first metal soluble salt of cobalt, nickel, iron, and a combination thereof; a second metal soluble salt of magnesium, calcium, strontium, barium, and a combination thereof; a third metal soluble salt of lanthanide elements, and a combination thereof; and a fourth metal soluble salt of aluminum, transition metals, alkali metals, and a combination thereof. The first metal oxide, the second metal oxide, the third metal oxide, and the fourth metal oxide may be co-precipitated from the first solution at a pH between approximately 6.0 and approximately 11.0 to form a hydrotalcite- like structured material. The co-precipitated material may be aged and dried. The aged, dried, co-precipitated material may be decomposed to form a final catalyst product.

Description

Technical field [0001] The present invention relates to systems and methods for ammonia decomposition catalysts, and more specifically to mixed metal oxide catalysts and methods for producing mixed metal oxide catalysts. Background technique [0002] Fuel cells are emerging as one of the most promising clean energy sources due to high efficiency and low environmental pollution. Fuel cells have been widely used in many fields including automobiles, electronic equipment, military, aerospace and so on. Some of the main obstacles to the widespread adoption of commercial fuel cell applications include clean hydrogen production, hydrogen storage, hydrogen transportation and cost. The generation of onboard hydrogen from a liquid source with a high hydrogen density would be a desirable method to overcome one or more of these obstacles. However, the current technology does not provide suitable on-board hydrogen generated from a liquid source with high hydrogen density. [0003] Liquid am...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/83C01B3/04
CPCB01J23/002B01J23/83C01B3/047B01J2523/00B01J2523/22B01J2523/31B01J2523/3706B01J2523/845B01J37/031Y02E60/36B01J37/0236B01J37/082
Inventor 张辉拉切扎·安格洛夫·彼得罗夫叶海亚·阿布巴科尔·艾尔哈米德阿卜杜勒拉希姆·阿梅德·艾尔查拉尼穆罕默德·阿卜杜勒拉赫曼·达乌斯穆罕默德·H·艾尔哈兹米
Owner SABIC GLOBAL TECH BV