A method for producing synthesis gas by dry reforming of methane

A methane dry reforming and synthesis gas technology, which is applied in chemical instruments and methods, inorganic chemistry, bulk chemical production, etc., can solve the problems of poor anti-coking performance of catalysts, short service life of catalysts, and low reaction space velocity, etc. Achieve the effect of improving catalytic stability, uniform temperature distribution and high catalytic activity

Active Publication Date: 2019-01-08
CHINA PETROLEUM & CHEM CORP +1
View PDF6 Cites 0 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0008] The purpose of the present invention is to overcome the short service life of the catalyst due to the low reaction space velocity or the poor anti-coking performance of the catalyst in the methane dry reforming reaction of the prior art, and to provide a catalyst with a relatively high reaction space velocity and New long-lived methane dry reforming method to synthesis gas

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 method for producing synthesis gas by dry reforming of methane
  • A method for producing synthesis gas by dry reforming of methane
  • A method for producing synthesis gas by dry reforming of methane

Examples

Experimental program
Comparison scheme
Effect test

Embodiment approach

[0023] According to a preferred embodiment of the present invention, the carrier is La and / or Mg modified Al 2 o 3 carrier, and relative to 100 parts by weight of Al modified with additives 2 o 3 As for the carrier, the content of additives La and / or Mg is 3-13 parts by weight, preferably 6-12 parts by weight, based on oxides.

[0024] According to a preferred embodiment of the present invention, relative to 100 parts by weight of the catalyst, the content of the active metal component is 4.5-6.5 parts by weight in terms of metal elements.

[0025] In the present invention, the impregnation method in the carrier modification method is not particularly limited, for example, it can be an equal-volume impregnation method commonly used in the art, or a supersaturated impregnation method, or a combination of the above methods. The temperature and time of the immersion treatment are not particularly limited, as long as the desired auxiliary ingredients can be loaded on the carrie...

Embodiment 1

[0043] This example is used to illustrate the method for producing synthesis gas by dry reforming of methane provided by the present invention.

[0044] (1) Preparation of catalyst carrier

[0045] Weigh 5.53g of Mg(NO 3 ) 2 ·6H 2 O was dissolved in 14g of deionized water to prepare carrier impregnation solution; after the dissolution was completed, it was impregnated in 10g of Al 2 o 3 On the carrier, the immersion temperature is 25°C, and it is allowed to stand for 2 hours. The strips are then extruded on an extruder. The obtained wet strip was dried at 120° C. for 8 hours, and then put into a muffle furnace for sintering at 800° C. for 3 hours. The resulting support is denoted as 8Mg-Al 2 o 3 .

[0046] (2) Preparation of catalyst

[0047] Weigh 1.06g of Ni(NO 3 ) 2 ·6H 2 O and 0.211g of P123 were dissolved in 5.2g of deionized water and stirred to dissolve, and the impregnating solution was impregnated in 4g of the above carrier 8Mg-Al 2 o 3 After standing f...

Embodiment 2

[0051] This example is used to illustrate the method for producing synthesis gas by dry reforming of methane provided by the present invention.

[0052] (1) Preparation of catalyst carrier

[0053] Weigh 1.7g of La(NO 3 ) 3 ·6H 2 O was dissolved in 14g of deionized water to prepare carrier impregnation solution; after the dissolution was completed, it was impregnated in 10g of Al 2 o 3 On the carrier, the immersion temperature is 35°C, and it is allowed to stand still for 1 hour. The strips are then extruded on an extruder. The obtained wet strip was dried at 90° C. for 10 hours, and then put into a muffle furnace for sintering at 1000° C. for 2 hours. The resulting support is denoted as 6La-Al 2 o 3 .

[0054] (2) Preparation of catalyst

[0055] Weigh 0.84g of Ni(NO 3 ) 2 ·6H 2 O and 0.166g of P123 were put into 5.2g of deionized water and stirred and dissolved; this catalyst impregnation solution was impregnated in 4g of the above-mentioned carrier 6La-Al 2 o ...

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 invention relates to the field of preparation of synthetic gas through dry reforming of methane, and discloses a method for preparing synthetic gas through dry reforming of methane. The loading amount of an active metal component Ni in a catalyst in a catalyst bed of a dry reforming reaction of methane is controlled, and a Al2O3 carrier and / or a Al2O3 carrier modified with an auxiliary agent is adopted. Even in relatively high reaction velocity, temperature dispersion of the catalyst bed is basically uniform, and an area where carbon is easily thermodynamically accumulated can be avoided, so that the catalytic stability of a catalyst is greatly improved and the service life of the catalyst can be prolonged.

Description

technical field [0001] The invention relates to the research field of producing synthesis gas by dry reforming of methane, in particular to a method for producing synthesis gas by dry reforming of methane. Background technique [0002] Methane dry reforming is CH 4 and CO 2 Under the action of a catalyst, the reaction produces CO and H 2 (synthesis gas) reaction process, the reaction formula is as follows: [0003] CH 4 +CO 2 →2CO+2H 2 , ΔH 298K =247.3kJ / mol (1) [0004] CO 2 +H 2 →CO+H 2 O,ΔH 298K =40.96kJ / mol (2) [0005] Among them, the reaction formula (1) is the main reaction, and the reaction formula (2) is the side reaction, that is, the reverse water gas shift reaction, and it is because of the existence of the reverse water gas shift reaction that the H in the product 2 / CO ratio is less than 1. [0006] The methane dry reforming reaction converts two of the cheapest carbon-containing compounds in nature, CH 4 and CO 2 It is transformed into chemical...

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): C01B3/40
CPCY02P20/52
Inventor 张荣俊夏国富李明丰侯朝鹏晋超聂红李大东
Owner CHINA PETROLEUM & CHEM CORP
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

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

© 2024 PatSnap. All rights reserved.Legal|Privacy policy|Modern Slavery Act Transparency Statement|Sitemap