Coal gasification method

A technology for coal gasification and gasification furnace, applied in the field of coal gasification, can solve the problems of high content, unfavorable hydrogen, and high cost of oxygen production, and achieve the effects of good flow characteristics, reduced vibration, and reduced escape

Active Publication Date: 2015-04-08
铜陵市世纪朝阳数码科技有限责任公司
View PDF4 Cites 4 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] (1) The oxygen used in this process requires the construction of an air separation unit, which requires high investment and high cost of oxygen production. This is the main reason for restricting the development of continuous oxygen-enriched gasification and the fact that small and medium-sized synthetic ammonia plants use this process.
[0005] (2) The composition of oxygen-enriched continuous gasification gas is poor, with carbon dioxide content as high as 15-20%, methane content as high as 2%, and the gas contains organic substances such as benzene and naphthalene
Bring great problems to the follow-up section
Especially the problem of methane and organic matter, there is no good solution at present
[0006] (3) It is difficult to control the oxygen content in the oxygen-enriched continuous gasification gas composition, which brings safety hazards to the subsequent sections
[0010] The gasifier adopts a water-cooled wall structure, and its disadvantage is that the CH in the syngas 4 The content is high, which is unfavorable for the production of ammonia, methanol and hydrogen

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

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0028] A coal gasification method, the specific preparation steps are as follows:

[0029] (1) Coal grinding and drying unit

[0030] After the lignite with particle size ≤ 30mm is pre-dried, the broken lignite particle size is less than 15mm. The above-mentioned pre-dried lignite is lifted to a height of 45 meters through the bucket elevator, and enters the raw material coal storage of the gasification device through the closed coal delivery trestle under the protection of nitrogen. The warehouse, under the action of gravity, enters the coal mill through the coal feeder and grinds it into powder. The primary air from the hot blast stove enters the coal mill in a circular distribution, and at the same time controls the flow of the primary air entering the coal mill. The temperature is not higher than the conversion temperature of lignite. Control the temperature of the inert airflow generated by the inert gas generator when it enters the coal mill inlet to about 150°C, and the...

Embodiment 2

[0039] A coal gasification method, the specific preparation steps are as follows:

[0040] (1) Coal grinding and drying unit

[0041] After the lignite with particle size ≤ 30mm is pre-dried, the broken lignite particle size is less than 15mm. The above-mentioned pre-dried lignite is lifted to a height of 45 meters through the bucket elevator, and enters the raw material coal storage of the gasification device through the closed coal delivery trestle under the protection of nitrogen. The warehouse, under the action of gravity, enters the coal mill through the coal feeder and grinds it into powder. The primary air from the hot blast stove enters the coal mill in a circular distribution, and at the same time controls the flow of the primary air entering the coal mill. The temperature is not higher than the conversion temperature of lignite. Control the temperature of the inert airflow generated by the inert gas generator when it enters the coal mill inlet to about 200°C, and the...

Embodiment 3

[0050] A coal gasification method, the specific preparation steps are as follows:

[0051] (1) Coal grinding and drying unit

[0052] After the lignite with particle size ≤ 30mm is pre-dried, the broken lignite particle size is less than 15mm. The above-mentioned pre-dried lignite is lifted to a height of 45 meters through the bucket elevator, and enters the raw material coal storage of the gasification device through the closed coal delivery trestle under the protection of nitrogen. The warehouse, under the action of gravity, enters the coal mill through the coal feeder and grinds it into powder. The primary air from the hot blast stove enters the coal mill in a circular distribution, and at the same time controls the flow of the primary air entering the coal mill. The temperature is not higher than the conversion temperature of lignite. Control the temperature of the inert airflow generated by the inert gas generator when it enters the coal mill inlet to about 250°C, and the...

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
sizeaaaaaaaaaa
sizeaaaaaaaaaa
particle sizeaaaaaaaaaa
Login to view more

Abstract

The invention provides a coal gasification method. The coal gasification method comprises the following steps: grinding the coal, drying, pressurizing and transporting the pulverized coal, and gasifying the pulverized coal in a gasification furnace. On the model selection of a coal grinder, primary air entering the coal grinder from a hot blast heater is annularly distributed, the temperature of the hot air entering the coal grinder is ensured to be higher than the conversion temperature of brown coal, the local surface of the brown coal is ensured not to be overheated, and the escape of volatile components in the brown coal can be reduced; the high-volatility brown coal is adopted as a raw material, the coal grinding system is controlled, the maximum concentration of oxygen is 4 percent, a new flow of low-pressure nitrogen is supplemented to a coal grinder sealing system, an nitrogen inlet in the system is also increased, the impact on a grinding roll is reduced, and the vibration of the coal grinder is reduced; the combustion temperature in the gasification furnace is 150 to 200 DEG C higher than the flowing temperature of lime-ash. Under the temperature and pressure, not only can the conversion rate of carbon in the gasification furnace be ensured to reach 99 percent, but also the lime-ash is good in flow characteristic.

Description

technical field [0001] The invention relates to a coal gasification method, which belongs to the field of coal chemical industry. Background technique [0002] Coal is an abundant resource. Coal gasification is an efficient and clean coal utilization method. Coal gasification technologies commonly used today include oxygen-enriched continuous gasification, fluidized bed gasification, and two-stage pressurized gasification of dry pulverized coal. But above-mentioned technology all has defect. [0003] Oxygen-enriched continuous gasification has the following disadvantages: [0004] (1) The oxygen used in this process requires the construction of an air separation unit, which requires high investment and high cost of oxygen production. This is the most important reason for restricting the development of continuous oxygen-enriched gasification and the small and medium-sized synthetic ammonia plants adopting this process. [0005] (2) The composition of oxygen-enriched conti...

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): C10J3/48C10J3/50C10J3/84C10J3/72
CPCC10J3/48C10J3/50C10J3/723C10J3/84C10J2300/0906C10J2300/0909C10J2300/0936C10J2300/1615
Inventor 李程伟
Owner 铜陵市世纪朝阳数码科技有限责任公司
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