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A self-heating hydrogen-oxygen catalytic burner and self-heating starting method

A catalytic burner, self-heating technology, applied in the direction of combustion methods, burners, gas fuel burners, etc., can solve the problems of potential safety hazards, no measures to prevent tempering, etc., achieve stable heat supply, and improve the form of catalysts , Solve the effect of tempering

Active Publication Date: 2020-05-19
武汉氢能与燃料电池产业技术研究院有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The mixed gas is sprayed into the catalytic layer through the nozzle, and there are no measures to prevent backfire, which poses a safety hazard

Method used

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  • A self-heating hydrogen-oxygen catalytic burner and self-heating starting method
  • A self-heating hydrogen-oxygen catalytic burner and self-heating starting method
  • A self-heating hydrogen-oxygen catalytic burner and self-heating starting method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0030] refer to Figure 1 to Figure 4 As shown, the present invention discloses a self-heating hydrogen-oxygen catalytic combustor, including a gas mixing chamber 1 with a cavity, and an air pipeline 2 and a hydrogen pipeline 5 vertically arranged in the gas mixing chamber 1, the hydrogen gas The pipeline 5 is arranged above the air pipeline 2, and the air pipeline 2 and the hydrogen pipeline 5 both extend outward along the tangential surface of the gas mixing chamber 1, and at the same time form an angle of 10-20° with the horizontal line, so that the air and the hydrogen are tangentially The gas flows into the gas mixing chamber 1, and the flow rate of hydrogen and air is controlled at Mach 0.2 to ensure that the hydrogen pressure is greater than the air pressure, so as to prevent oxygen (or air) from entering the hydrogen pipeline 5 and prevent hydrogen and oxygen from burning in the hydrogen pipeline 5 , the air pipeline 2 and the hydrogen pipeline 5 are respectively arran...

Embodiment 2

[0034] The gas mixing chamber 1 has a diameter of 60 mm and a height of 40 mm. The hydrogen gas pipeline 5 and the air pipeline 2 are vertically arranged, and the flow rate of the gas mixture is controlled to Mach 0.1. Nickel foam is processed into an air duct flame arrester 4 with a thickness of 5mm, a hole number of 40PPI, and a porosity of 40%. The gas distributor 6 is also processed from nickel foam, with a thickness of 7mm, a number of holes of 50PPI, and a porosity of 60%. When the catalytic plate 10 is produced, the thickness of the aluminum foil substrate is 4 mm, and the 20 μm hydrophobic γ-Al 2 o 3 For the transition layer, a 0.5 μm platinum active layer is deposited, platinum accounts for 0.8% of the mass of the transition layer, and the average diameter of platinum particles is 5 nm. The catalytic plate 10 is folded into a catalytic combustion chamber 8 with a pore size of 200 μm. The size of the catalytic combustion chamber 8 is 60mm in diameter and 130mm in le...

Embodiment 3

[0037] The gas mixing chamber 1 has a diameter of 60 mm and a height of 40 mm. The hydrogen pipeline 5 and the air pipeline 2 are vertically arranged, and the velocity of the mixed gas is controlled at Mach 0.08. Nickel foam is processed into an air duct flame arrester 4 with a thickness of 5mm, a hole number of 40PPI, and a porosity of 40%. The gas distributor 6 is also processed from nickel foam, with a thickness of 6mm, a hole number of 40PPI, and a porosity of 50%. When the catalytic plate 10 is produced, the thickness of the aluminum foil substrate is 4 mm, and the hydrophobic γ-Al is coated with 30 μm 2 o 3 For the transition layer, a 1 μm platinum active layer is deposited, platinum accounts for 1% of the mass of the transition layer, and the average diameter of platinum particles is 5 nm. The catalytic plate 10 is folded into a catalytic combustion chamber 8 with a pore size of 100 μm. The size of the catalytic combustion chamber 8 is 60mm in diameter and 130mm in l...

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PUM

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Abstract

The invention discloses a self-heating type hydrogen-oxygen catalytic burner and a self-heating start method. The self-heating type hydrogen-oxygen catalytic burner comprises a gas mixing chamber, anair pipeline and a hydrogen pipeline, wherein the air pipeline and the hydrogen pipeline are perpendicularly arranged in the gas mixing chamber. An air pipeline fire barrier and a hydrogen pipeline fire barrier are arranged in the air pipeline and the hydrogen pipeline correspondingly, a cellular catalytic burning chamber rolled by a catalytic plate is arranged below the gas mixing chamber, and agas distributor is connected between the gas mixing chamber and the catalytic burning chamber. The hydrogen-oxygen catalytic burner is applicable to heating, safe and reliable, the self-heating function is particularly applicable to field application, mixed gas is introduced in according to the ratio of hydrogen to nitrogen being 2:3-3:2, the temperature can reach 160 DEG C or above after 3-6min,and self-heating start is achieved; and when hydrogen reacts with air, the hydrogen volume ratio is controlled to be 10% or below, combustion tail gas with different temperatures is obtained by controlling the mixed gas flow and the hydrogen volume ratio so as to be used for different heating occasions.

Description

technical field [0001] The invention belongs to the field of hydrogen energy application, in particular to a self-heating hydrogen-oxygen catalytic burner and its self-heating starting method. Background technique [0002] Hydrogen has the advantages of green and pollution-free, high mass energy density, renewable, and abundant resources. It is considered as a green energy in the 21st century and has great application potential. Researches on the production, storage, transportation and application of hydrogen are in full swing around the world, in order to gain an advantage in the future technology field and new energy competition. [0003] Heating is one of the important applications of hydrogen. However, hydrogen combustion has the disadvantages of fast combustion, high temperature, easy tempering, and great safety hazards. Therefore, hydrogen combustion for heating has not been widely promoted. The complete combustion of hydrogen and oxygen at a lower temperature under t...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): F23D14/02F23D14/62F23D14/60
Inventor 李海港彭恩高吴飞程臣曾辉
Owner 武汉氢能与燃料电池产业技术研究院有限公司
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