Looking for breakthrough ideas for innovation challenges? Try Patsnap Eureka!

Integrated device for preparing hydrogen by the recapitalization of dimethyl ether aqueous vapor and method

A technology of steam reforming and hydrogen production equipment, which is applied in the direction of chemical instruments and methods, hydrogen, bulk chemical production, etc. It can solve the problems of complex gas components, high energy consumption, and difficulty in obtaining hydrogen, so as to improve the reaction Effects of conversion rate and hydrogen yield improvement

Inactive Publication Date: 2008-05-14
TSINGHUA UNIV
View PDF4 Cites 12 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0009] The steam reforming reaction of dimethyl ether produces hydrogen with high hydrogen content, and the reaction conditions are mild. The disadvantage is that the steam reforming reaction of dimethyl ether is a strong endothermic reaction, and the reaction itself and the vaporization of raw material water need absorption. Heat, when hydrogen production needs to burn part of the fuel for heating
Patents CN1126709C and CN1044896C propose a method for catalyzing hydrogen production by dimethyl ether in the presence of steam. In this patent, dimethyl ether is first hydrolyzed to produce a mixture containing carbon oxides and hydrogen, and then the reaction product is subjected to a water gas change reaction to make a large amount of carbon monoxide Converted into carbon dioxide, and the product is rich in carbon monoxide, which makes the hydrogen production process of dimethyl ether complicated and high in energy consumption; although the patent CN1123530C proposes a method of generating rich hydrogen by steam reforming dimethyl ether and using part of the hydrogen to oxidize for heat , but the patent preferably uses a fluidized bed reactor, the reaction operating pressure is high, the gas components in the reaction product are complex, and it is difficult to obtain hydrogen with high purity. The above patents are not suitable for mobile hydrogen production or hydrogen production from small hydrogen sources

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
  • Integrated device for preparing hydrogen by the recapitalization of dimethyl ether aqueous vapor and method
  • Integrated device for preparing hydrogen by the recapitalization of dimethyl ether aqueous vapor and method
  • Integrated device for preparing hydrogen by the recapitalization of dimethyl ether aqueous vapor and method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0036] 0.02m 3 / h Dimethyl ether hydrogen production unit

[0037] The reaction device is constructed as shown in Figure 2. The membrane reactor is used, the reaction temperature is 200°C, the reaction pressure is 0.1MPa, the center tube is made of palladium-silver alloy, the mass percentage of palladium and silver is 3:1, and the pressure in the center tube is normal pressure. The feed amount of ether is 500ml / min, the molar ratio of water to dimethyl ether is 3:1; the reforming catalyst adopts a mixture of molecular sieve ZSM-5 and copper-based catalyst, totaling 10g, and the ratio of molecular sieve catalyst ZSM-5 and copper-based catalyst is 10g. The weight ratio is 1:1, and the combustion-supporting catalyst adopts Pd / Al 2 O 3 Noble metal catalyst 5g, center tube assembly tube length 300mm, tube diameter 10mm, film thickness 0.06mm, 5 center tubes, the conversion rate of dimethyl ether is 60%, and the scale of hydrogen production is 0.02m 3 / h, the hydrogen recovery rate is 8...

Embodiment 2

[0039] 0.03m 3 / h Dimethyl ether hydrogen production unit

[0040] The reaction device is constructed as shown in Figure 2. The membrane reactor of Example 1 is used, the reaction temperature is 300°C, the reaction pressure is 0.1MPa, the center tube is made of palladium-silver alloy, and the mass percentage of palladium and silver is 9:1. The pressure in the center tube is normal pressure. , The feed rate of dimethyl ether is 500ml / min, the molar ratio of water to dimethyl ether is 3:1, the reforming catalyst adopts a mixture of molecular sieve catalyst ZSM-5 and copper-based catalyst totaling 10g, molecular sieve ZSM-5 and copper The weight ratio of the base catalyst is 2:1, and the combustion-supporting catalyst adopts Pd / Al 2 O 3 Noble metal catalyst 5g, center tube assembly tube length 300mm, tube diameter 10mm, film thickness 0.06mm, 5 center tubes, the conversion rate of dimethyl ether obtained is 80%, and the scale of hydrogen production is 0.03m 3 / h, the hydrogen recover...

Embodiment 3

[0042] 0.3m 3 / h Dimethyl ether hydrogen production unit

[0043] The reaction device is constructed as shown in Figure 2. The membrane reactor of Example 1 is used, the reaction temperature is 300°C, the reaction pressure is 0.5MPa, the center tube uses a composite palladium membrane, the pressure in the center tube is normal pressure, and the feed volume of dimethyl ether is 5000ml / min, the molar ratio of water to dimethyl ether is 6:1, the catalyst is solid acid Al 2 O 3 100g of mixture with precious metal platinum catalyst, solid acid Al 2 O 3 The weight ratio to the precious metal platinum catalyst is 5:1, and the combustion-supporting catalyst adopts Pd / Al 2 O 3 Noble metal catalyst 50g, central tube assembly tube length 300mm, tube diameter 20mm, film thickness 0.01mm, 15 central tubes, the conversion rate of dimethyl ether obtained is 80%, and the hydrogen production scale is 0.3m 3 / h, the hydrogen recovery rate is 83%, the hydrogen purity is 99.5%, and the system therma...

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

PropertyMeasurementUnit
diameteraaaaaaaaaa
thicknessaaaaaaaaaa
diameteraaaaaaaaaa
Login to View More

Abstract

The invention discloses an integrated dimethyl ether steam reforming hydrogen-production device and a method, belonging to the hydrogen-production equipment and the method. The invention utilizes a dual-jacketed membrane reactor to realize the coupling of an exothermic reaction and an endothermic reaction and the coupling of a catalytic reaction and a product separation. The invention is characterized in that the central tube of the double cannula is a hydrogen permeation membrane made of palladium silver alloy for in-situ separation of H2, the product of the reaction system; two reforming catalysts are filled in a jacket of the double cannula and the dimethyl ether steam reforming hydrogen production is carried out in the jacket of the tube side; a combustion supporting catalyst is filledin the shell side out of the double cannula to supply heat for the dimethyl ether steam reforming reaction. The invention has the advantages of greatly promoting the steam reforming reaction rate ofthe dimethyl ether, the heat utilization rate and the product purity. The invention obtains high purity hydrogen at lower reaction temperature and pressure, in which the conversion of dimethyl ether canreach 80%, the hydrogen recovery rate 85%, the hydrogen production rate 0.05 to 0.6 m<3> / h, the hydrogen purity 99.5% and the thermal efficiency of the system is above 80%.

Description

Technical field [0001] The invention relates to a device and a method for preparing hydrogen by using dimethyl ether as a raw material, in particular to an integrated dimethyl ether steam reforming hydrogen production device and a method. Background technique [0002] Hydrogen energy is regarded as the most promising energy source in this century because of its cleanness, high efficiency, and renewable energy. At present, it is still an ideal low-pollution or zero-pollution energy for vehicles. At present, the research and development of the mobile hydrogen production process of liquid hydrocarbons (such as methanol) based on chemical processes has become one of the current hot topics in the field of fuel cells. Using methanol as fuel can solve the problems of storage and transportation, but the specific energy density of methanol is still unsatisfactory, and it is more toxic. Once leaked, it will cause great harm to the human body and the environment. In addition, the infrastruc...

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 Applications(China)
IPC IPC(8): C01B3/38
CPCY02P20/52
Inventor 王金福冯冬梅王铁峰王德峥
Owner TSINGHUA UNIV
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Patsnap Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Patsnap Eureka Blog
Learn More
PatSnap group products