Chain type hydrogen and oxygen production integrated method and device

A chain and oxidation reaction technology, applied in chemical instruments and methods, hydrogen, iron compounds, etc., can solve the problems of high energy consumption, purity, long construction period, complicated operation, etc., and achieve the effect of wide distribution, low price and low price

Inactive Publication Date: 2010-10-27
HUAZHONG UNIV OF SCI & TECH
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Problems solved by technology

Cryogenic rectification is mainly based on the N in the air 2 and O 2 The difference in boiling point, the air is compressed and liquefied, and low-temperature rectification is carried out to make O 2 It is separated from the air. Although this method has a long history and mature technology, it has large investment, high energy consumption, long

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  • Chain type hydrogen and oxygen production integrated method and device
  • Chain type hydrogen and oxygen production integrated method and device
  • Chain type hydrogen and oxygen production integrated method and device

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Embodiment Construction

[0054] The chain-type hydrogen and oxygen production integrated device proposed by the present invention, such as structure figure 1 As shown, the oxygen carrier reduction reactor system A is composed of the bubbling bed reduction reactor 1, the cyclone separator 2 for separating the oxygen carrier fine powder and its coke particles, the sealing valve 3 and the sealing valve 4; The hydrogen reactor 5, the cyclone separator 6 and the sealing valve 7 form the hydrogen production system B; furthermore, the bubbling bed primary oxygen production reactor 8, the cyclone separator 9, the sealing valve 10, and the bubbling bed secondary oxygen production reactor 11. The cyclone separator 12 and the sealing valve 13 form the oxygen production system C; finally, the fast fluidized bed air reactor 14, the cyclone separator 15 and the sealing valve 16 form the oxygen carrier regeneration system.

[0055] In view of the residual coke and CuFe remaining after the gasification of carbon-cont...

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Abstract

The invention provides a chain type hydrogen and oxygen production integrated method, comprising the following steps: CuFe2O4 and solid carbonaceous matters are subjected to reduction reaction to obtain reduction products of Cu, Fe and FeO, wherein the Fe, the FeO and vapour are subjected to oxidation reaction to generate H2 and Fe3O4, and the residual Cu is in oxidation reaction with the Fe3O4 and air to generate CuFe2O4 by oxidation; and the CuFe2O4 is heated and decomposed to generate O2 and CuFeO2, and the CuFeO2 and air are in oxidation reaction to generate CuFe2O4 once again. The invention also provides a device for realizing the method, which comprises the main assemblies of a bubbling fluidized bed reactor, a cyclone separator, a sealing valve and a rapid fluidized bed. The invention can obtain H2 and O2 by chain type continuous preparation, has simple process and low energy consumption, can obtain H2 and O2 with the high purity approximate to 100%, realizes CO2 zero emission in the hydrogen production process and has broad application prospect.

Description

technical field [0001] The present invention relates to hydrogen H 2 and O 2 Preparation field, specifically related to a simultaneous and continuous preparation of high-purity H 2 and O 2 methods and devices. Background technique [0002] h 2 It is not only an important chemical raw material, but also an efficient and clean energy carrier, which is widely used in petroleum, chemical industry, transportation, electric power and other fields. At present, the preparation of hydrogen has received close attention. There are many methods for the preparation of hydrogen, but most of the hydrogen used in industry 2 It is still derived from the electrolysis of water, or using hydrocarbon gas fuel as raw material, and reforming hydrocarbon gas fuel, water vapor reforming, CO 2 removal and H 2 It is obtained through many processes such as separation and purification, but due to the electrolysis of water to produce H 2 High energy consumption, while reforming hydrocarbon gas fu...

Claims

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Application Information

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IPC IPC(8): C01B3/06C01B3/10C01B13/02C01G49/00
CPCY02E60/36
Inventor 王保文赵海波郑瑛张少华郑楚光
Owner HUAZHONG UNIV OF SCI & TECH
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