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A method and equipment for multi-stage entrained entrained bed coal gasification coupled with high temperature shift

A high-temperature conversion and entrained bed technology, which is applied in the gasification of granular/powdered fuels, chemical industry, and the manufacture of combustible gases, can solve the problems of high-temperature sensible heat utilization, large CO conversion load, and large sensible heat loss of gas. , to achieve the effects of improving the adaptability of coal types, reducing the system switching load, reducing system investment and operating costs

Active Publication Date: 2018-03-02
SHANXI INST OF COAL CHEM CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] Although dry coal powder entrained bed gasification technology has been industrialized and maturely applied, there are still some disadvantages: (1) Coal gas high-temperature quenching process is commonly used, and the crude gas at 1200-1500 °C is quenched and cooled to 200-250 °C, and the sensible heat of gas Large loss; (2) The CO concentration in the crude gas is over 65%, and the H 2 Low content, for chemical synthesis processes that require hydrogen, such as synthetic ammonia, synthetic methanol, and synthetic oil, the post-system CO conversion load is large; (3) For coals with high coal ash melting point and high viscosity-temperature characteristics, it is easy to cause blockage of the ash discharge port , so it is generally only suitable for coals whose ash melting point is less than 1300°C
However, the multi-nozzle feeding method also makes the control system complex, increases the difficulty of operation, and cannot solve the technical problem of high-temperature sensible heat utilization

Method used

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  • A method and equipment for multi-stage entrained entrained bed coal gasification coupled with high temperature shift
  • A method and equipment for multi-stage entrained entrained bed coal gasification coupled with high temperature shift
  • A method and equipment for multi-stage entrained entrained bed coal gasification coupled with high temperature shift

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Experimental program
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Effect test

Embodiment 1

[0032]A multi-stage entrained entrained gasifier, which includes a furnace body 1, a high-temperature gasification section 2, a high-temperature transformation section 3 and a quenching section 4, and is characterized in that the furnace body 1 is divided into a high-temperature gasification section 2, a high-temperature transformation section 3 and a quenching section. Section 4, the inner wall of the high-temperature gasification section 2 is a water-cooled wall 6, the outer wall is a cylindrical shell 7, the top of the high-temperature gasification section 2 has coal powder and gasification agent inlet 5, and the lower part of the high-temperature gasification section 2 passes through the flaring section 8 and The high-temperature conversion section 3 is connected, and the conical surface of the flared section 8 is evenly distributed to change the atomizing nozzle 10 for spraying water or low-temperature steam. It is a refractory lining 11, the outer wall is a cylindrical sh...

Embodiment 2

[0042] The total height of the multi-stage entrained-bed coal gasifier is 13800mm. Among them, the height of the high-temperature gasification section is 5200mm, the inner diameter is 450mm, and the wall is a coiled water-cooled wall structure; the height of the high-temperature transformation section is 4100mm, the inner diameter is 900mm, and the wall is a corundum refractory lining structure; the height of the chilling section is 4500mm, and the inner diameter is 900mm; The apex angle α of the section cone is 60°, and 8 nozzles are evenly distributed along the circumference of the conical surface of the flaring section, and are arranged opposite to each other at 45° horizontally downward; 10 layers of baffles are arranged in the chilling section, The included angle between the plate blade and the horizontal plane is 60°, and the rest of the multi-stage entrained-bed coal gasifier is the same as that in Embodiment 1.

[0043] The properties of the experimental coal are as de...

Embodiment 3

[0049] The total height of the multi-stage entrained bed coal gasifier is 14300mm. Among them, the height of the high-temperature gasification section is 5500mm, the inner diameter is 800mm, and the wall is a coiled water-cooled wall structure; the height of the high-temperature transformation section is 3700mm, the inner diameter is 1200mm, and the wall is a corundum refractory lining structure; the height of the chilling section is 5100mm, and the inner diameter is 1200mm; The apex angle α of the section cone is 150°, and there are 12 spray water atomization nozzles evenly distributed along the circumference of the cone surface of the flaring section, which are arranged opposite to each other at 60° horizontally downward; 15 layers of baffles are arranged in the chilling section, The included angle between the plate blade and the horizontal plane is 75°, and the rest of the multi-stage entrained-bed coal gasifier is the same as that in Embodiment 1.

[0050] The experimental...

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Abstract

A multi-stage entrained-flow coal gasification method capable of realizing coupling high temperature shift comprises the following steps: dry coal powder and a gasifying agent are vertically sprayed into a high-temperature gasification section from a burner of a multi-stage entrained-flow gasifier for coal gasification reaction, generated hot coal gas and molten slag flow downwards into a high-temperature conversion section, converted spray water or low-temperature steam is sprayed into the gasifier from an atomization spray head to be subjected to high-temperature water vapor shift reaction to generate H2, coal gas and ash enter a chilling section through a flow guide pipe, and the coal gas is cooled, washed, discharged out of the gasifier from a crude coal gas outlet, and fed into a post-system to be purified. The method has the advantages that the operation is easy, the thermal efficiency is high, the hydrogen content in coal gas is high, and the adaptability to coal type is good.

Description

technical field [0001] The invention relates to a dry coal pulverized entrained bed gasification technology, in particular to a multi-stage entrained entrained bed coal gasification method coupled with high temperature conversion and its equipment. Background technique [0002] Coal gasification technology is the core and leading technology of the coal chemical industry, and it is also one of the key technologies to realize efficient and clean utilization of coal. The rapid expansion of the coal chemical market has further promoted the considerable progress of coal gasification technology. Pressurization, large-scale, and strong adaptability of raw materials are the development directions of advanced gasification technology. [0003] Gasification technology can be divided into fixed bed, fluidized bed and entrained bed gasifier according to the way of gas-solid contact. Among them, the entrained bed gasifier has the advantages of large production capacity, high carbon conve...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10J3/46C10J3/48C10J3/72
CPCY02P20/10
Inventor 赵建涛房倚天黄戒介陈寒石张林仙李春玉郭金霞方惠斌张磊
Owner SHANXI INST OF COAL CHEM CHINESE ACAD OF SCI
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