Fluidized bed reactor for gasifying inferior coal with high ash content and low activity

A fluidized bed reactor and reactor technology are applied in the field of fluidized bed gasification, and can solve problems affecting the long-cycle stable operation time of the fluidized bed reactor, corrosion and wear of slag discharge pipes, jet pipe classifiers, fluidized bed The reactor theory is complex and other problems, to achieve the effect of improving the secondary agglomeration rate and the conversion rate of raw coal, shortening the manufacturing cycle, and wide adaptability of coal types

Pending Publication Date: 2020-03-20
上海浦名能源科技有限公司
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] my country's steam coal and low-quality anthracite account for a very large proportion. This part of coal has a large ash content and poor activity, so it is not suitable for fixed-bed reactors and entrained-bed reactors.
Therefore, there is a wide living space for fluidized bed reactors with wider adaptability to coal types, but the theory of fluidized bed reactors is more complicated and the operation is more difficult. At present, industrialized fluidized bed reactors are mainly based on gas Gasification of high-activity lignite and long-flame coal, and few examples of gasification of high-ash and low-activity bituminous coal
[0008] For gasifying bituminous coal with high ash content and low activity, the fluidized bed reactor still has the following problems: First, the gasification agent distribution plate is very easy to leak ash, resulting in ash accumulation in the gas chamber, which affects the gas distribution effect of the gasification agent. It brings safety hazards to the equipment; secondly, the ash discharge intensity of the lower slag outlet is very high, and the current two-in-one structure of the slag discharge pipe and the gasification agent jet pipe can easily cause corrosion and wear of the slag discharge pipe, jet pipe, and classifier , causing the shutdown of the device, seriously affecting the long-term stable running time of the fluidized bed reactor
This method mainly uses chemical methods to process raw coal. For large-scale coal chemical plants, the workload is relatively large.

Method used

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  • Fluidized bed reactor for gasifying inferior coal with high ash content and low activity
  • Fluidized bed reactor for gasifying inferior coal with high ash content and low activity

Examples

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Embodiment 1

[0041] like figure 1 As shown, the fluidized bed reactor used in this embodiment to gasify high-ash, low-activity low-quality coal includes: a reactor main body 1, a gas distribution plate 9 is arranged inside the reactor main body 1, and the gas distribution plate 9 Divide the reactor main body 1 into two parts: a dense-phase area 11 and a gas chamber 4; wherein, the gasification agent jet pipe 7 and a slag discharge pipe 5 are also provided on the gas distribution plate 9; the dense-phase area 11 One of the positions is provided with pulverized coal inlet 6.

[0042] In this embodiment, a suitable position of the dense phase zone 11 is selected to be provided with a pulverized coal inlet 6 (such as figure 1 shown). According to the amount of coal input, preferably, 2 to 3 pulverized coal inlets 6 can be provided. Among them, the pulverized coal can enter the dense phase zone 11 through the pulverized coal inlet 6 by using a pneumatic conveying device.

[0043] Wherein, t...

Embodiment 2

[0059] The difference between this embodiment and Embodiment 1 is that in this embodiment, N partition plates 17 are arranged in the air chamber 4, wherein, N≥1, and the air chamber 4 is surrounded by the partition plates 17 is divided into N+1 sub-air chambers.

[0060] In this embodiment, N=1 is used for further explanation, and those skilled in the art can understand the specific implementation manner of N>1 on the basis of this embodiment.

[0061] like figure 2 As shown, the air chamber 4 is provided with a partition plate 17 , and the air chamber 4 is divided into a first sub-air chamber 20 and a second sub-air chamber 18 by the partition plate 17 . The fluidized bed reactor in this embodiment is provided with two sub-gas chambers according to the up-and-down arrangement. By adjusting the gasification agent flow rate and oxygen concentration in different sub-gas chambers, the strong back-mixing of coal char particles in the upper area of ​​the distribution plate is rea...

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Abstract

The invention discloses a fluidized bed reactor for gasifying inferior coal with high ash content and low activity. The fluidized bed reactor comprises a reactor main body, which is internally provided with a gas distribution plate, wherein the gas distribution plate divides the reactor main body into a dense phase zone and a gas chamber, a gasifying agent jet pipe and a residue discharge pipe arealso arranged on the gas distribution plate, and a powder coal inlet is formed in one position of the dense phase zone. According to the invention, by independently arranging the gasifying agent jetpipe and the residue discharge pipe, the adaptability to high-ash coal is improved; and by arranging the residual carbon combustion burner for discharging residue and circulating coke powder, the carbon conversion rate of low-activity inferior coal is greatly improved, and the efficient gasification of low-activity inferior coal is realized.

Description

technical field [0001] The application belongs to the technical field of fluidized bed gasification, and in particular relates to a fluidized bed reactor for gasifying inferior coal with high ash content and low activity. Background technique [0002] my country's energy structure is more coal and less oil. Therefore, using coal-based raw materials to produce chemical products plays a vital role in reducing the country's dependence on oil and improving energy security. Coal-to-gas is an important technology to realize coal-based chemical industry Rely on. [0003] So far, there have been a large number of coal gasification reactors of different schools at home and abroad. According to reaction time and reaction intensity, coal gasification reactors are divided into fixed-bed reactors, entrained-bed reactors and fluidized-bed reactors. [0004] Fixed-bed reactors are mainly represented by Lurgi furnaces, which need to use high-quality lump coal or chemical coke as raw materi...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10J3/56C10J3/50C10J3/72
CPCC10J3/50C10J3/56C10J3/72C10J2300/093C10J2300/0946
Inventor 马凌河雷会娇吴明曾海英游春华牛强
Owner 上海浦名能源科技有限公司
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