Process and device for preparing hydrogen from hydrogen iodide in iodine-sulfur circulation

A hydrogen iodide and process technology, which is applied in the field of hydrogen iodide production process and equipment in the iodine-sulfur cycle, can solve the problems of reduced hydrogen production efficiency, increased hydrogen production cost, and high energy consumption for electrochemical decomposition, achieving improved The effect of recovery rate, investment and energy consumption reduction, improvement of quality and energy utilization rate

Active Publication Date: 2021-08-10
DALIAN UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

However, there are many disadvantages in the traditional hydrogen production method: fossil fuel dry gas hydrogen production process CO 2 There are many emissions, the prepared hydrogen contains sulfur, and high-purity hydrogen needs to be desulfurized and purified; the electrolytic hydrogen production process has low efficiency and high cost; the hydrogen obtained by biomass decomposition hydrogen production is limited and cannot be used in large-scale industries, etc.
The process of producing hydrogen from hydrogen iodide in the traditional iodine-sulfur cycle is complex, and the HIX decomposition process mainly includes phosphoric acid extraction, electrochemical decomposition and high-pressure reactive distillation
The process of the phosphoric acid extraction unit is complicated, and the introduction of impurities will affect the circulation and separation of the system; the electrochemical decomposition consumes a lot of energy, the hydrogen production efficiency is low, and it cannot be applied industrially. It is currently in the laboratory research stage; high-pressure reactive distillation, temperature High energy consumption, using traditiona

Method used

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  • Process and device for preparing hydrogen from hydrogen iodide in iodine-sulfur circulation
  • Process and device for preparing hydrogen from hydrogen iodide in iodine-sulfur circulation
  • Process and device for preparing hydrogen from hydrogen iodide in iodine-sulfur circulation

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Effect test

Embodiment 1

[0081] Using the process described in the present invention, HIX enters the thermal integration composite tower C101. The outer diameter of the new composite tower is 250mm, the height of the composite tower section is 680mm, and the material of the composite tower is corrosion-resistant and high-temperature-resistant stainless steel. The stripping section and the reaction section of heat integrated composite tower C101 are 8 trays respectively, and the water washing section contains 6 trays. The pressure of the stripping section is 1 bar, and the temperature of the stripping tower is 120°C. The pressure in the reaction section is 10 bar, the feed position is the second plate, the feed temperature is 447°C, the tower top temperature is 207°C, the tower bottom temperature is 477°C, and the reflux ratio is 3. The pressure of the washing section is 1 bar, the washing water enters the washing section at the top of the tower, and the water temperature is 5°C. o 2 Washing tower C1...

Embodiment 2

[0090] Using the process described in the present invention, HIX enters the thermal integration composite tower C101. The outer diameter of the new composite tower is 250mm, the height of the composite tower section is 680mm, and the material of the composite tower is corrosion-resistant and high-temperature-resistant stainless steel. The stripping section and the reaction section of heat integrated composite tower C101 are 8 trays respectively, and the water washing section contains 6 trays. The pressure of the stripping section is 1 bar, and the temperature of the stripping tower is 120°C. The pressure in the reaction section is 10 bar, the feed position is the second plate, the feed temperature is 447°C, the tower top temperature is 207°C, the tower bottom temperature is 477°C, and the reflux ratio is 3. The pressure of the washing section is 1 bar, the washing water enters the washing section at the top of the tower, and the water temperature is 5°C. o 2 Washing tower C102...

Embodiment 3

[0095] Using the process described in the present invention, HIX enters the thermal integration composite tower C101. The outer diameter of the new composite tower is 250mm, the height of the composite tower section is 680mm, and the material of the composite tower is corrosion-resistant and high-temperature-resistant stainless steel. The stripping section and the reaction section of heat integrated composite tower C101 are 8 trays respectively, and the water washing section contains 6 trays. The pressure of the stripping section is 1 bar, and the temperature of the stripping tower is 120°C. The pressure in the reaction section is 10 bar, the feed position is the second plate, the feed temperature is 447°C, the tower top temperature is 207°C, the tower bottom temperature is 477°C, and the reflux ratio is 3. The pressure of the washing section is 1 bar, the washing water enters the washing section at the top of the tower, and the water temperature is 5°C. o 2 Washing tower C1...

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Abstract

The invention belongs to the related technical field of hydrogen preparation through thermochemical circulation, and provides a process and a device for preparing hydrogen from hydrogen iodide in iodine-sulfur circulation. The device comprises an HIX steam stripping section, a reaction rectifying section, a reaction gas washing section and a steam stripping gas washing process and device. A shell pass and a tube pass of a novel shell-and-tube heat integration composite tower are filled with a 1# filler and a 2# filler respectively, N tower sections of a composite section are coaxially and hermetically connected, and the HIX steam stripping section, the reaction rectifying section and a water washing section are coupled together, so that gradient utilization of energy is realized; the system mixed gas containing O2 and SO2 is used as the circulating stripping gas of the stripping section of the composite tower, so that the generation of S, H2S and a small amount of H2SO4 mingled in an HIX system is inhibited, and the recovery rate of SO2 in HIX is improved; and the tower bottom material liquid of the reaction section of the heat integration composite tower and the acidic water of the washing section and the stripping gas washing tower are returned to the front mixing tank of the Bensen reactor, so that the quality utilization rate of the system is improved.

Description

technical field [0001] The invention relates to a process and a device for preparing hydrogen from hydrogen iodide in an iodine-sulfur cycle, and belongs to the related technical field of thermochemical cycle preparation of hydrogen. Background technique [0002] The main energy supply in the world today comes from fossil fuels. However, fossil fuels are non-renewable and pollute the environment, which does not meet the requirements of carbon neutrality. There are solutions to reduce the environmental impact of fossil fuels, such as carbon capture, storage, and thermal decarbonization. However, while carbon capture can save environmental costs, it cannot be a long-term solution for energy sustainability. Due to the high energy density, cleanness and non-toxicity of hydrogen energy, the formation of more compounds and large reserves, hydrogen energy is considered to be an alternative energy carrier in the future. However, there are many disadvantages in the traditional hydr...

Claims

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Application Information

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IPC IPC(8): C01B3/04C01B7/13
CPCC01B3/04C01B7/135C01B2203/1205C01B2203/1258C01B2203/80Y02P20/129Y02E60/36
Inventor 刘宏吕文东董宏光候国新
Owner DALIAN UNIV OF TECH
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