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

A Catalytic Heating Coupling Methanol Hydrogen Production Process

A methanol hydrogen production and process technology, which is applied in the fields of hydrogen, inorganic chemistry, chemical instruments and methods, etc., can solve the problems of the need to discharge combustible tail gas, large area, unsafe, etc., and achieves small area and equipment area. Small, emission-safe effect

Active Publication Date: 2021-03-02
四川蜀泰化工科技有限公司
View PDF3 Cites 1 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The purpose of the present invention is to provide a catalytic heating coupled methanol hydrogen production process to solve the problem that the existing methanol hydrogen production process requires external heating to start, requires additional equipment, high energy consumption, and occupies a large area. In addition, it can also solve the existing problems. There is a defect that methanol hydrogen production process needs to discharge combustible tail gas, which is unsafe and environmentally friendly

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 Catalytic Heating Coupling Methanol Hydrogen Production Process
  • A Catalytic Heating Coupling Methanol Hydrogen Production Process
  • A Catalytic Heating Coupling Methanol Hydrogen Production Process

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0045] Such as Figure 1-2 , a catalytic heating coupled methanol hydrogen production process, including a catalytic oxidation reactor 2 and a methanol hydrogen production system, in the catalytic oxidation reactor 2, methanol and air in the raw material are oxidized at a constant temperature at a catalyst layer under the condition of above 10°C The catalytic oxidation reaction occurs, and the heat generated provides heat energy for the start-up of the methanol hydrogen production system.

Embodiment 2

[0047] On the basis of Example 1, such as Figure 1-3 , the catalytic oxidation reactor 2 includes a reactor cylinder with both ends closed and connected with a plurality of inlet and outlet pipes, a central pipe 4 is arranged in the reactor cylinder, and the central pipe 4 extends to the reactor cylinder Outside the top of the body, a mixer 19 is arranged on the upper part of the center tube 4 in the reaction cylinder, and a plurality of reaction tubes 5 are evenly arranged around the center tube 4, and each reaction tube 5 is provided with a A combined catalyst layer, the combined catalyst layer includes the normal temperature oxidation catalyst layer at the lower part and the medium temperature oxidation catalyst layer located at the upper part of the normal temperature oxidation catalyst layer, both ends of the central tube 4 and the reaction tube 5 are open, A heat transfer medium outlet 8 and a heat transfer medium inlet 9 are provided on the wall of the reaction cylinde...

Embodiment 3

[0049] On the basis of Example 2, the normal temperature oxidation catalyst layer includes a first catalyst, the shape of the first catalyst is spherical and / or honeycomb cylinder, and the medium temperature oxidation catalyst layer includes a second catalyst, the second The shape of the catalyst is spherical and / or honeycomb cylindrical; the volume ratio of the first catalyst to the second catalyst is 1:1-1:5.

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
particle sizeaaaaaaaaaa
specific surface areaaaaaaaaaaa
specific surface areaaaaaaaaaaa
Login to View More

Abstract

The invention discloses a catalytic heating coupled methanol hydrogen production process, which belongs to the field of hydrogen production, and specifically relates to the technical field of methanol hydrogen production, in order to solve the problem that the existing methanol hydrogen production process requires external heating to start, additional equipment is required, and energy consumption is high. It covers a large area, including a catalytic oxidation reactor and a methanol hydrogen production system. In the catalytic oxidation reactor, methanol and air in the raw material are oxidized at a temperature above 10°C, and the catalyst layer is oxidized at normal temperature, and the catalytic oxidation reaction occurs. The generated heat provides thermal energy for the start-up of the methanol hydrogen production system. Under the condition of no heat source, the raw material methanol and air undergo a catalytic oxidation reaction in the catalytic oxidation reactor under the action of the combined catalyst layer, and the heat generated provides heat energy for the start-up of the methanol hydrogen production system, making the entire methanol hydrogen production process run at room temperature It starts from the bottom, does not require external heating to start, and does not require additional external heat source equipment. The equipment occupies a small area and consumes low energy.

Description

technical field [0001] A catalytic heating coupled methanol hydrogen production process, the invention belongs to the field of hydrogen production, and specifically relates to the technical field of methanol hydrogen production. Background technique [0002] After the reformed gas of the traditional methanol steam reforming hydrogen production process passes through pressure swing adsorption or membrane hydrogen extraction, the required product H is obtained. 2 In addition, the rest is analytical gas, and the H in the analytical gas 2 The content is 30%-40%; the product H of the current common methanol direct cracking process 2 , CO, used tail gas H 2 The content is above 95%. There are generally two ways to deal with it. One is to send it into the boiler combustion system for boiler combustion. Due to the unstable gas source, there are obvious safety hazards to the boiler combustion system; Great and also cause a waste of clean energy. The treatment of this combustible...

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): C01B3/32C01B3/22
CPCC01B3/22C01B3/326C01B2203/0233C01B2203/0277C01B2203/0805C01B2203/1005C01B2203/1023C01B2203/1041C01B2203/107C01B2203/1082C01B2203/1223
Inventor 许云波严会成吴小强李龙李德胜孙瑜
Owner 四川蜀泰化工科技有限公司
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

Browse by: Latest US Patents, China's latest patents, Technical Efficacy Thesaurus, Application Domain, Technology Topic, Popular Technical Reports.

© 2024 PatSnap. All rights reserved.Legal|Privacy policy|Modern Slavery Act Transparency Statement|Sitemap|About US| Contact US: help@patsnap.com