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Catalyst for ammonia decomposition, process for producing same, and method of treating ammonia

A catalyst, ammonia decomposition technology, applied in catalyst activation/preparation, separation methods, chemical instruments and methods, etc., can solve the problems of high catalyst performance, low space velocity, low ammonia concentration, etc.

Active Publication Date: 2011-08-17
NIPPON SHOKUBAI CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0008] However, these catalysts all have a low ammonia concentration in the process gas (specifically, 5% by volume in Patent Document 4, and 50% by volume in Patent Document 5), or low space velocity based on ammonia (specifically, Patent Document 5 4 for 642h -1 , patent document 5 is 1000h -1 , Non-Patent Document 1 is 430h -1 ) conditions, the ammonia decomposition rate was measured. Therefore, even if the ammonia decomposition rate is 100% at a relatively low temperature, it is not necessarily caused by the high performance of the catalyst.
[0009] In this way, the conventional ammonia decomposition catalysts have the problem that they cannot effectively decompose ammonia at a relatively low temperature and at a high space velocity to obtain high-purity hydrogen.

Method used

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  • Catalyst for ammonia decomposition, process for producing same, and method of treating ammonia
  • Catalyst for ammonia decomposition, process for producing same, and method of treating ammonia
  • Catalyst for ammonia decomposition, process for producing same, and method of treating ammonia

Examples

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preparation example Construction

[0062] "The preparation method of ammonia decomposition catalyst (I)"

[0063] Hereinafter, preferred specific examples of the method for producing the ammonia decomposition catalyst (I) of the present invention will be given, but the method is not limited to the following production method as long as the subject of the present invention can be achieved.

[0064] (1) An oxide of component A, a mixture of an oxide of component A and an oxide of component B, a composite oxide of component A and component B, a mixture of oxides of component C added to these, or a mixture of these A method in which a calcined product obtained by calcining the aqueous solution of the C component and drying the mixture is used as a catalyst;

[0065] (2) A method of further treating the calcined product of (1) at a temperature of 300-800° C. with ammonia gas or nitrogen-hydrogen mixed gas (nitridation treatment);

[0066] (3) A method of roasting an aqueous solution of a salt containing component A...

Embodiment

[0146] Hereinafter, the present invention will be described in more detail by citing experimental examples, but the present invention is not limited to the following experimental examples, and appropriate changes can be added to the range appropriately obtained from the gist described before and after. Implementation, these are included in the technical scope of the present invention.

[0147] Ammonia decomposition catalyst (I)

[0148] First, a production example and performance evaluation of the ammonia decomposition catalyst (I) will be described. In addition, an X-ray diffractometer (product name "RINT-2400", manufactured by Rigaku Corporation) was used for the X-ray diffraction measurement. The X-ray source uses CuKα (0.154nm), and it is carried out under the following measurement conditions, that is, the X-ray output power is 50kV, 300mA, the divergence slit is 1.0mm, and the divergence slit length (dissipation limit slit) is 10mm, The scanning speed is 5 degrees per m...

experiment example I-1

[0150] Dissolve 80.00 g of cobalt nitrate hexahydrate in 400.00 g of distilled water. Separately, 48.53 g of ammonium molybdate was slowly added and dissolved in 250 g of boiling distilled water. After mixing the two aqueous solutions, heat and stir, and evaporate to dryness. The obtained solid was dried at 120° C. for 10 hours, then baked at 350° C. for 5 hours under a nitrogen stream, and 3 hours at 500° C. under an air stream. Confirmed as α-CoMoO by X-ray diffraction measurement 4 .

[0151] Furthermore, 0.5-1.0 mL of α-CoMoO was filled in a reaction tube made of SUS316 4 , the temperature was raised to 400° C. under nitrogen gas (hereinafter referred to as “nitrogen”) at a rate of 30-50 mL / min. Then, the temperature was raised to 700° C. under feeding ammonia gas (hereinafter referred to as “ammonia”) at 50-100 mL / min, and the treatment (nitridation treatment) was carried out at 700° C. for 5 hours to obtain an ammonia decomposition catalyst (hereinafter referred to a...

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Abstract

The present invention relates to a catalyst for ammonia decomposition which is a catalyst for decomposing ammonia into nitrogen and hydrogen. The catalyst includes an active catalyst ingredient which comprises at least one transition metal selected from a group consisting of molybdenum, tungsten, vanadium, chromium, manganese, iron, cobalt, and nickel. It is preferred that (I) the active catalyst ingredient comprise at least one member selected from a group consisting of molybdenum, tungsten, and vanadium, or (II) the active catalyst ingredient comprise a nitride of at least one transition metal selected from a group consisting of molybdenum, tungsten, vanadium, chromium, manganese, iron, cobalt, and nickel, or (III) the active catalyst ingredient contain at least one iron-family metal selected from a group consisting of iron, cobalt, and nickel and further contain a metal oxide. This catalyst enables ammonia to be efficiently decomposed into nitrogen and hydrogen at a relatively low temperature and a high space velocity, whereby high-purity hydrogen is acquired.

Description

technical field [0001] The present invention relates to a catalyst for decomposing ammonia into nitrogen and hydrogen, a preparation method thereof, and an ammonia treatment method using the catalyst. Background technique [0002] Ammonia has odor, especially irritating odor, so when the content in the gas is above the odor threshold, it needs to be treated. Therefore, various ammonia treatment methods have been studied. For example, a method of oxidizing ammonia into nitrogen and water by contacting it with oxygen, a method of decomposing ammonia into nitrogen and hydrogen, and the like have been proposed. [0003] For example, Patent Document 1 discloses that when ammonia produced from a coke oven is oxidized to nitrogen and water, for example, a platinum-alumina catalyst, a manganese-alumina catalyst, a cobalt-alumina catalyst, etc. are used, and ammonia produced from a coke oven When ammonia is decomposed into nitrogen and hydrogen, for example, an ammonia treatment me...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/88B01D53/86B01J23/28B01J23/34B01J23/75B01J23/755B01J23/76B01J23/78B01J23/80B01J23/85B01J27/24
CPCB01J23/75B01J27/053Y02E60/364B01J23/8872B01J23/755B01J27/24B01J23/74B01J23/002B01J23/28B01J23/78B01D2255/20707B01J23/88B01D2257/406B01D53/8634B01D2255/202B01J23/34B01D2255/20753B01J37/0236B01J23/83B01J23/888B01J2523/00Y02E60/36B01J2523/3712B01J2523/48B01J2523/845B01J2523/842B01J2523/27B01J2523/31B01J2523/69B01J2523/847B01J2523/13B01J2523/25B01J2523/24B01J2523/3706B01J2523/15B01J2523/68B01J2523/36B01J2523/22B01J23/889C01B21/02C01B3/04
Inventor 冈村淳志桐敷贤吉宗壮基常木英昭
Owner NIPPON SHOKUBAI CO LTD
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