High-temperature gas cooled nuclear reactor coupled iodine selenium thermochemical cycle phosphorous reduction hydrogen production method

A thermochemical cycle and high-temperature gas-cooled reactor technology, applied in chemical instruments and methods, inorganic chemistry, hydrogen, etc., can solve the problems of high energy consumption, heat, high temperature, etc., and achieve the effect of reducing production costs

Active Publication Date: 2019-11-05
CHINERGY CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The disadvantage of the sulfur-iodide cycle hydrogen production method is that the decomposition reaction of sulfuric acid still requires a relatively high temperature, and it is still on a laboratory scale, which consumes a lot of energy and heat.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0058] (1) Take water as raw material, add selenium and iodine, react under normal pressure, the mol ratio of water, selenium and iodine is: water: selenium: iodine=1: 0.4: 1, and reaction temperature is 25 ℃, and reaction time is 60min, the complete mark of reaction is no longer producing gas, and the reaction obtains selenous acid solution and hydroiodic acid, and the reaction equation is as follows:

[0059] 3H 2 O+Se+2I 2 →H 2 SeO 3 +4HI

[0060] The hydriodic acid and selenous acid generated above are obviously layered due to different densities, the hydriodic acid is in the upper layer, and the selenous acid solution is in the lower layer. Using a liquid-liquid separation method, the selenous acid solution and hydroiodic acid are subjected to liquid-liquid separation to obtain the selenous acid solution and hydroiodic acid;

[0061] (2) contain following component in the hydroiodic acid that step (1) obtains: 1 2 , HI and H 2 0, the mixed ternary solution is recor...

Embodiment 2

[0069] (1) Take water as raw material, add selenium and iodine, react under normal pressure, the mol ratio of water, selenium and iodine is: water: selenium: iodine=1: 0.5: 1.2, and reaction temperature is 28 ℃, and the reaction time is 50min, the complete mark of reaction is no longer producing gas, and the reaction obtains selenous acid solution and hydroiodic acid, and the reaction equation is as follows:

[0070] 3H 2 O+Se+2I 2 →H 2 SeO 3 +4HI

[0071] The hydriodic acid and selenous acid generated above are obviously layered due to different densities, the hydriodic acid is in the upper layer, and the selenous acid solution is in the lower layer. Using a liquid-liquid separation method, the selenous acid solution and hydroiodic acid are subjected to liquid-liquid separation to obtain the selenous acid solution and hydroiodic acid;

[0072] (2) contain following component in the hydroiodic acid that step (1) obtains: 1 2 , HI and H 2 O, the mixed ternary solution is...

Embodiment 3

[0080] (1) Take water as raw material, add selenium and iodine, react under normal pressure, the mol ratio of water, selenium and iodine is: water: selenium: iodine=1: 1: 2, and reaction temperature is 28 ℃, and reaction time is 48min, the complete mark of reaction is no longer producing gas, and the reaction obtains selenous acid solution and hydroiodic acid, and the reaction equation is as follows:

[0081] 3H 2 O+Se+2I 2 →H 2 SeO 3 +4HI

[0082] The hydriodic acid and selenous acid generated above are obviously layered due to different densities, the hydriodic acid is in the upper layer, and the selenous acid solution is in the lower layer. Using a liquid-liquid separation method, the selenous acid solution and hydroiodic acid are subjected to liquid-liquid separation to obtain the selenous acid solution and hydroiodic acid;

[0083] (2) contain following component in the hydroiodic acid that step (1) obtains: 1 2 , HI and H 2 O, the mixed ternary solution is recorde...

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PUM

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Abstract

The invention relates to an iodine selenium thermochemical cycle phosphorous reduction hydrogen production method, and belongs to the technical field of hydrogen energy. The method comprises the stepsthat water serves as a raw material, selenium and iodine are added for a reaction under normal pressure, and a seleninic acid solution and hydroiodic acid are obtained; the hydroiodic acid is rectified and concentrated, the rectified and concentrated hydroiodic acid is decomposed, hydrogen obtained after decomposition is output as a product, and iodine is recycled; a reducing agent white phosphorus or red phosphorus or phosphorus trioxide are added into the obtained seleninic acid solution, selenium and a by-product are obtained and output, and the selenium as the raw material is recycled. The highest temperature required by the reaction process in the method is 400-500 DEG C, and the problem is avoided that due to too high reaction temperature, large-scaled hydrogen production cannot beconducted. The reacting agent iodine and selenium in the method can be recycled, and accordingly, the hydrogen production cost is greatly reduced. The method can be well coupled with the latest cleanenergy, namely a high-temperature gas cooled nuclear reactor, the heat energy, electric energy and mechanical energy of the high-temperature gas cooled nuclear reactor can be utilized by the iodine selenium thermochemical cycle hydrogen production process.

Description

technical field [0001] The invention relates to a high-temperature gas-cooled reactor coupled iodine-selenium thermochemical cycle phosphorus reduction hydrogen production method, which belongs to the technical field of hydrogen energy. Background technique [0002] Hydrogen energy is an ideal clean secondary energy source. It is widely distributed and does not cause pollution when burned. Compared with electricity, hydrogen energy is easier to store and transport, and can be directly used as fuel. The energy system centered on hydrogen energy is increasingly valued. One of the most promising approaches is thermochemical cycle splitting of water to produce hydrogen. The current common thermochemical cycle hydrogen production method is sulfur iodine cycle hydrogen production, such as Chinese patent application (application publication number is CN104817057) discloses a method for thermochemical cycle hydrogen production, the method includes 3 chemical reactions, as follows S...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B3/04
CPCC01B3/04C01B2203/025C01B2203/0266C01B2203/0805Y02E60/36C01B3/068C01B25/16C01B3/066C01B7/14
Inventor 孟东旺齐乃烨王春铭
Owner CHINERGY CO LTD
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