A kind of Fe2+ anodic oxidation and cathodic reduction parallel production method of H2

A technology of anodic oxidation and process method, which is applied in the direction of chemical instruments and methods, photographic process, photographic auxiliary process, etc., and can solve the problems of difficult regeneration, high production cost, system pollution, etc.

Active Publication Date: 2018-06-15
YANGZHOU UNIV
View PDF8 Cites 0 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In order to improve I 2 Solubility, organic solvents such as benzene and toluene can also be used, but it will cause SO 2 The absorption conversion process becomes a liquid-liquid heterogeneous reaction process, which brings problems of liquid-liquid dispersion mixing and separation of the liquid-liquid dispersion system after the reaction, and the introduction of organic solvents will also bring problems such as solvent recovery and system pollution.
[0020] (3) Fe 3+ easily regenerated, while I 2 Difficulty regenerating
[0034] (1) High production cost: Because in the process of hydrogen production by electrolysis of water, only the target product hydrogen is generated by the cathode reaction, and the oxygen generated by the anode is of little use, so the production cost is relatively high
[0035] (2) The cell voltage is high and the energy consumption is large: due to the relatively high potential of the oxygen evolution at the anode, the operating cell voltage during the electrolysis process is relatively high and the energy consumption is large
[0036] (3) There are potential safety hazards: In the isolation membrane electrochemical reactor, the anode generates oxygen and the cathode generates hydrogen. If the operation is not done properly, the mixture of oxygen and hydrogen will occur and there is a risk of explosion.

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • A kind of Fe2+ anodic oxidation and cathodic reduction parallel production method of H2
  • A kind of Fe2+ anodic oxidation and cathodic reduction parallel production method of H2

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0092] like figure 1 and figure 2 As shown, a Fe 2+ Anodic oxidation and cathodic reduction co-produce H 2 The process method, the concrete steps are as follows:

[0093] (1) Preparation of anolyte: mix sulfuric acid with water to obtain an aqueous solution of sulfuric acid, then dissolve ferrous sulfate in the aqueous solution of sulfuric acid to obtain a solution containing 0.2mol / L H 2 SO 4 and 0.2mol / L Fe 2+ The anolyte, the operating temperature is 20 ℃.

[0094] (2) catholyte preparation: will contain Fe 3+ The sulfuric acid aqueous solution is mixed with sulfuric acid and water, and then the ferrous sulfate is dissolved in the sulfuric acid aqueous solution to obtain 8.0mol / L H 2 SO 4 , 2.0mol / L Fe 2+ and 0.02mol / L Fe 3+ The catholyte, the operating temperature is 20 ℃.

[0095] (3) Fe 2+ Anodic oxidation and cathodic reduction co-produce H 2 : In an electrochemical reactor with a sulfonic acid type cation exchange membrane as the isolation membrane, sulfu...

Embodiment 2

[0097] like figure 1 and figure 2 As shown, a Fe 2+ Anodic oxidation and cathodic reduction co-produce H 2 The process method, the concrete steps are as follows:

[0098] (1) Anolyte preparation: will contain Fe3+ The sulfuric acid aqueous solution is mixed with sulfuric acid and water, and then ferrous sulfate is dissolved in the solution to obtain 8.0mol / L H 2 SO 4 , 2.0mol / L Fe 2+ and Fe 3+ For anolyte with concentration ≤0.2mol / L, the operating temperature is 60°C.

[0099] (2) catholyte preparation: will contain Fe 3+ The sulfuric acid aqueous solution is mixed with sulfuric acid and water, and then ferrous sulfate is dissolved in the solution to obtain 8.0mol / L H 2 SO 4 , 2.0mol / L Fe 2+ and 0.02mol / L Fe 3+ The catholyte operating temperature is 60°C;

[0100] (3) Fe 2+ Anodic oxidation and cathodic reduction co-produce H 2 : In an electrochemical reactor with a sulfonic acid type cation exchange membrane as a separator, sulfuric acid as a supporting electr...

Embodiment 3

[0102] like figure 1 and figure 2 As shown, a Fe 2+ Anodic oxidation and cathodic reduction co-produce H 2 The process method, the concrete steps are as follows:

[0103] (1) Anolyte preparation: will contain Fe 2+ and Fe 3+ The sulfuric acid aqueous solution is directly used as the anolyte, and the solution composition is 6.0mol / L H 2 SO 4 , 0.8mol / L Fe 2+ and 0.1mol / L Fe 3+ , operating temperature is 40°C.

[0104] (2) catholyte preparation: will contain Fe 2+ and Fe 3+ The sulfuric acid aqueous solution is directly used as the catholyte, and the solution composition is 8.0mol / L H 2 SO 4 , 1.0mol / L Fe 2+ and 0.02mol / L Fe 3+ , operating temperature is 40°C.

[0105] (3) Fe 2+ Anodic oxidation and cathodic reduction co-produce H 2 : In a three-dimensional fixed-bed electrode electrochemical reactor with a sulfonic acid-type cation-exchange membrane as a separator, sulfuric acid as a supporting electrolyte, and a graphite electrode as an anode, the operating c...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

PUM

No PUM Login to view more

Abstract

The present invention provides a kind of Fe2+ anodic oxidation and cathodic reduction and co-produced H2 process method, this method is in sulfuric acid aqueous solution, Fe2+ is oxidized at anodic to obtain Fe3+, Fe2+ is reduced at cathode to generate Fe, at the same time H+ in catholyte is reduced to generate H2 . The process method of the present invention realizes the regeneration of Fe3+ at the anode, the removal of Fe2+ and the co-production of H2 at the cathode, and realizes the paired electrochemical synthesis of the target product at the cathode and the anode at the same time, so that the double-chamber electrodes are effectively obtained. use. The technological process of the present invention is simple, easy to operate and control, high in process efficiency and energy utilization rate, low in equipment investment and production cost, safe and reliable in process, and conducive to large-scale industrialization.

Description

technical field [0001] The present invention relates to a kind of Fe 2+ Anodic oxidation and cathodic reduction co-produce H 2 The process method belongs to the field of inorganic chemical preparation technology, also belongs to the field of hydrogen and sulfuric acid preparation technology, especially the field of hydrogen energy preparation technology; also belongs to the field of electrochemical reaction engineering and chemical separation technology. Background technique [0002] 1. Fe in sulfuric acid medium 3+ Features of use as an oxidizing agent [0003] In acidic medium, Fe 3+ and Fe 2+ can exist stably, Fe 3+ with Fe 2+ The following reactions can occur between: [0004] 2Fe 2+ →2Fe 3+ +2e - [0005] Standard electrode potential for this reaction At 1.0mol / LH 2 SO 4 solution, Therefore, Fe 3+ is an oxidizing agent with moderate oxidation ability, and Fe 2+ It is a reducing agent with moderate reducing ability. Fe 3+ able to I - 、H 2 Oxidation...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

Application Information

Patent Timeline
no application Login to view more
Patent Type & Authority Patents(China)
IPC IPC(8): C25B1/02C25B9/08C25C1/06C01B17/74C25B9/19
CPCC25B1/02C25C1/06C01B17/74C25B9/19Y02P10/20
Inventor 王雅琼李宝同王大为许文林
Owner YANGZHOU UNIV
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Try Eureka
PatSnap group products