Unlock instant, AI-driven research and patent intelligence for your innovation.

Fluidized bed reaction device and reaction method for producing methane-rich synthesis gas by catalytic coal gasification

A methane synthesis gas and coal catalytic gasification technology, which is applied to the gasification of granular/powdered fuels, the manufacture of combustible gases, and the production of bulk chemicals. It can solve the problems of low carbon conversion rate, complex structure, and low methane yield.

Active Publication Date: 2021-05-11
CHINA PETROLEUM & CHEM CORP +1
View PDF6 Cites 0 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] One of the technical problems mainly solved by the present invention is the problems of low carbon conversion rate, low methane yield, high energy consumption and complicated structure in the prior art. Fluidized bed reaction device for syngas, which is composed of gasification reaction section and methanation reaction section, which simplifies the furnace structure, reduces equipment investment, realizes self-heating reaction and full utilization of energy, and improves carbon conversion rate and methane yield

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
  • Fluidized bed reaction device and reaction method for producing methane-rich synthesis gas by catalytic coal gasification
  • Fluidized bed reaction device and reaction method for producing methane-rich synthesis gas by catalytic coal gasification

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0036]In this embodiment, the lower space of the gasification apparatus is 0.1m, the height 5m, the upper space inside diameter is 0.2m, the height is 6m, the set two-layer gas distributor, the air hole is uniformly arranged along the circumference, provided with a 10-lap gas hole, open hole The rate is 2%, and the angle of the inclined surface of the gas distributor is 30 °, and a auxiliary feed port is set for replenishing the catalyst. Inner Mongolish coal was used to obtain 1 mm or less, and the catalyst can be used with potassium carbonate, and 10% of the potassium carbonate catalysts and the pulverized coal were mixed. After drying 24h, it obtained a mixture of less than 5% water content, supplemented The potassium carbonate catalyst is 10% of the lower space catalyst. The mixture of pulverized coal and catalyst was added to the gasifier, high temperature water vapor and preheating oxygen passed from the level gas distributor into the gasifier, and carried out under pressure o...

Embodiment 2

[0038]In this embodiment, the lower space of the gasification device is 0.1m, the height 5m, the upper space inner diameter is 0.3m, the height is 6m, the set two-layer gas distributor, the pores are uniformly arranged along the circumference, and 10, opening, opening The rate is 2%, and the angle of the inclined surface of the gas distributor is 30 °, and a auxiliary feed port is set for replenishing the catalyst. Inner Mongolish coal was used to obtain 1 mm or less, and the catalyst can be used with potassium carbonate, and 10% of the potassium carbonate catalysts and the pulverized coal were mixed. After drying 24h, it obtained a mixture of less than 5% water content, supplemented The potassium carbonate catalyst is 10% of the lower space catalyst. The mixture of pulverized coal and catalyst was added to the gasifier, high temperature water vapor and preheating oxygen passed from the level gas distributor into the gasifier, and carried out under pressure of 3.5 MPa, temperature 8...

Embodiment 3

[0040]In this embodiment, the lower space of the gasification device is 0.1m, the height 5m, the upper space inner diameter of 0.3m, the height is 6m, the set two-layer gas distributor, and the pores are evenly arranged along the circumference, and 20 lap gas holes, open holes The rate is 2%, and the angle of the inclined surface of the gas distributor is 30 °, and a auxiliary feed port is set for replenishing the catalyst. Inner Mongolish coal was used to obtain 1 mm or less, and the catalyst can be used with potassium carbonate, and 10% of the potassium carbonate catalysts and the pulverized coal were mixed. After drying 24h, it obtained a mixture of less than 5% water content, supplemented The potassium carbonate catalyst is 10% of the lower space catalyst. The mixture of pulverized coal and catalyst was added to the gasifier, high temperature water vapor and preheating oxygen passed from the level gas distributor into the gasifier, and carried out under pressure of 3.5 MPa, temp...

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 a fluidized bed reaction device and a reaction method for producing methane-rich syngas by catalytic coal gasification, which solves the problems of low carbon conversion rate, low methane yield, high energy consumption and complex structure in the prior art , the present invention is formed by the gasification reaction section of the lower space and the methane synthesis section of the upper space, and is characterized in that the inner diameter of the upper space is larger than that of the lower space, and the bottoms of the two spaces are respectively provided with a first-level and a second-level gas distributor; mainly comprising the following steps : Raw coal and catalyst are burned and gasified with oxygen-containing gas and water vapor in the lower space, and the synthesis gas produced by the gasification reaction is mixed with part of the recycled synthesis gas in the upper space for methanation reaction, thereby producing a synthetic gas rich in methane The technical solution of natural gas can better solve the above problems and can be applied in the field of coal-to-natural gas.

Description

Technical field[0001]The present invention relates to a reaction apparatus and method of gas-modified methane, and in particular, the present invention relates to a device and method for producing a gas-rich gasification gasification of gasification and methanated reaction segments.Background technique[0002]Natural gas is a high-quality fuel and an important chemical raw material, which has the advantages of safe and reliable and green environment. With the rapid development of my country and the acceleration of urbanization, the demand for natural gas is increasing. my country's own natural gas production is unable to reach the demand for natural gas, the supply and demand contradiction is increasingly prominent, and the supply gap is only able to rely on imports to compensate, and it is largely affected my country's energy security. Given that my country is a coal big country, coal production is rich, coal consumption accounts for about 70% of total energy resources, and coal as t...

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): C10J3/54C10J3/56C10J3/84C10J3/72
CPCY02P20/52
Inventor 金渭龙顾松园钟思青金永明
Owner CHINA PETROLEUM & CHEM CORP