Device and method for autothermal production of high-purity hydrogen by catalytic cracking of methane

A methane catalysis and methane gas technology, applied in chemical instruments and methods, hydrogen production, hydrogen/synthesis gas production, etc., can solve the problems of low hydrogen concentration, high operating cost, low methane cracking conversion rate, etc., to save production Cost, reduced energy consumption, simple installation effect

Active Publication Date: 2021-07-16
CHINA UNIV OF MINING & TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0004] There are two main problems in the existing methane catalytic cracking hydrogen production process. One is that the catalyst is easily deactivated during the reaction process, resulting in low methane cracking conversion rate and low hydrogen concentration. The other is that the system generally requires an external heat source and cannot Self-heating operation, resulting in complex system and high operating cost
Therefore, methods for the catalytic cracking of methane to produce hydrogen remain to be further developed

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  • Device and method for autothermal production of high-purity hydrogen by catalytic cracking of methane

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Embodiment 2

[0047] This embodiment also provides a method for the autothermal production of high-purity hydrogen by catalytic cracking of methane. The method uses an activated carbon catalyst and the device in Example 1. The specific steps of the method are the same as in Example 1. The reaction conditions of the method : The catalytic cracking temperature is 1050°C, the pressure is normal pressure, the flow rate of methane gas is 16kg / h, the residence time of methane gas in the cracking reactor is 2.9s, the preheating temperature of the regeneration medium is 150°C, and the regeneration starting temperature is 760°C. The pressure is normal pressure, the flow rate of water vapor is 12.3kg / h, the flow rate of oxygen is 24.1kg / h, and the residence time of the regeneration medium in the regeneration reactor is 1.5s.

[0048] The reaction results are: methane cracking single-pass conversion rate reaches 100%, the volume percentage of hydrogen in the product gas reaches 100%, and the CO / H in th...

Embodiment 3

[0050] This embodiment also provides a method for the autothermal production of high-purity hydrogen by catalytic cracking of methane. The method uses an activated carbon catalyst and the device in Example 1. The specific steps of the method are the same as in Example 1. The reaction conditions of the method : The catalytic cracking temperature is 1100°C, the pressure is normal pressure, the flow rate of methane gas is 16kg / h, the residence time of methane gas in the cracking reactor is 2.8s, the preheating temperature of the regeneration medium is 300°C, and the regeneration starting temperature is 850°C. The pressure is normal pressure, the flow rate of water vapor is 13.5kg / h, the flow rate of oxygen is 21.9kg / h, and the residence time of the regeneration medium in the regeneration reactor is 1.5s.

[0051] The reaction results are: methane cracking single-pass conversion rate reaches 100%, the volume percentage of hydrogen in the product gas reaches 100%, and the CO / H in th...

Embodiment 4

[0053] This embodiment also provides a method for autothermal production of high-purity hydrogen by catalytic cracking of methane, which uses coke and the device in Example 1 (the cracking reactor adopts a moving bed, and the regenerative reactor adopts a fast fluidized bed). The specific steps of the method are the same as in Example 1, and the reaction conditions of the method: the catalytic cracking temperature is 1100°C, the pressure is normal pressure, the methane gas flow rate is 16kg / h, and the residence time of the methane gas in the cracking reactor is 3.2s, The preheating temperature of regeneration medium is 300°C, the starting temperature of regeneration is 830°C, the pressure is normal pressure, the flow rate of water vapor is 12.3kg / h, the flow rate of oxygen is 21.9kg / h, and the residence time of regeneration medium in the regeneration reactor is 1.5s.

[0054] The reaction results are: methane cracking single-pass conversion rate reaches 100%, the volume percen...

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Abstract

The invention discloses a device and method for autothermally producing high-purity hydrogen by catalytic cracking of methane. The device mainly includes a cracking reactor, a regeneration reactor, a riser, a cyclone separator, a filter device and a flow sealing valve; the method includes: Methane goes backwards with the catalyst in the cracking reactor and undergoes a catalytic cracking reaction to obtain hydrogen and deactivated catalyst. After impurity removal and separation, high-purity hydrogen is obtained. The catalyst carries carbon deposits into the regeneration reactor for regeneration to generate syngas and regenerated catalyst. The regenerated catalyst is transported to the cyclone separator through the riser, and then re-enters the cracking reactor for recycling after removing impurities. The present invention can not only fully recover the catalytic activity of the deactivated catalyst, produce high-purity hydrogen, but also use the heat released by the combustion of carbon deposits on the deactivated catalyst to provide heat for the regeneration reactor, and use the heat carried by the regenerated catalyst to provide heat for the cracking reactor. Heat, so that the system runs by self-heating, reducing energy consumption and saving costs.

Description

technical field [0001] The invention belongs to the technical field of hydrogen production, and in particular relates to a device and method for autothermally producing high-purity hydrogen by catalytic cracking of methane. Background technique [0002] There are two main ways to produce hydrogen from methane: one is through the preparation of synthesis gas (H 2 and CO), and then physically or chemically remove CO to obtain H 2 , including steam methane reforming (SRM), partial oxidation (POM), autothermal reforming (ATR), carbon dioxide reforming, and combined reforming processes; the other is direct catalytic cracking of methane to obtain hydrogen and carbon black. [0003] SRM is currently the most widely used hydrogen production method in industry, but this method needs to go through three stages of synthesis gas preparation, water gas shift and decarbonization to obtain high-purity hydrogen. The process is relatively complicated and produces a large amount of carbon di...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01B3/26C01B3/06
CPCC01B3/06C01B3/26C01B2203/0277C01B2203/0805C01B2203/1241Y02E60/36Y02P20/584
Inventor 刘方杨丽刘磊刘阳何建龙
Owner CHINA UNIV OF MINING & TECH
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