Double-circulation fluidized bed two-section coupled powdered coal pressure gasification device and method

Pending Publication Date: 2018-04-20
SHAANXI YANCHANG PETROLEUM GRP
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Problems solved by technology

At present, there are relatively large reserves of medium and high-rank coals in China. How to make the gasification technology only suitable for low-rank coals solve the problems of low carbon conversion rate, high methane content in syngas and coal tar in medium and high-rank coals Defects, increasing throughput and reducing energy consumption have become key issues
[0003] The circula

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  • Double-circulation fluidized bed two-section coupled powdered coal pressure gasification device and method

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Embodiment Construction

[0031] A pulverized coal pressurized gasification device and method with double circulating fluidized bed and two-stage coupling of the present invention will be described in detail below with reference to the accompanying drawings and embodiments.

[0032] A pulverized coal pressurized gasification device with a double circulating fluidized bed coupled in two stages according to the present invention, such as figure 1 As shown, it includes two parts: a first-stage reactor (A) and a second-stage reactor (B); the first-stage reactor (A) includes a reaction system (1), a carbonaceous material recovery system (2) and a return material Conveying system (3); the second-stage reactor (B) includes a secondary reaction system (4), a fine ash capture device (5) and a return conveying system (6) connected end to end; the first-stage reactor ( A) is connected with the second-stage reactor (B) through a pipeline (7).

[0033]In the pulverized coal pressurized gasification device with dou...

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Abstract

The invention discloses a double-circulation fluidized bed two-section coupled powdered coal pressure gasification device and method and belongs to the technical field of coal gasification. The deviceis characterized by comprising two parts, namely a first section reactor and a second section reactor, wherein the first section reactor comprises a reaction system, a carbon-containing material recycling system and a returned material conveying system which are connected in a head to end manner; the second section reactor comprises a secondary reaction system, a fine ash capturing device and a returned material conveying system which are connected in the head to end manner; the first section reactor is connected with the second section reactor through a pipeline. The improved device is rapidin solid circulation velocity and gas circulation speed, large in treatment capacity, sufficient in reaction medium heat exchange, high in heat exchange efficiency, small in overall temperature difference of fluidized beds and large in coal type application range, that is, from low-rank coal to medium/high-rank coal which is rich in reserve in China, the contents of effective gas components and the carbon conversion rate in coal gases are increased, a generated synthesis gas is free of tar, and later gas purification can be relatively simple.

Description

technical field [0001] The invention belongs to the technical field of coal gasification, and in particular relates to a pulverized coal pressurized gasification device and method with two-stage coupling of a double circulating fluidized bed. Background technique [0002] China's resource endowment is more coal and less oil and gas. Coal has played an important role in my country's economic development, but its extensive use has also produced many negative effects. Coal gasification, as an important technology for coal conversion and utilization, has received more and more attention. However, the existing coal chemical technology has limited applicability of coal types, and has not been able to better solve the problems of large-scale, clean, and high-efficiency. At present, there are relatively large reserves of medium and high-rank coals in China. How to make the gasification technology only suitable for low-rank coals solve the problems of low carbon conversion rate, high...

Claims

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Application Information

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IPC IPC(8): C10J3/56C10J3/72C10J3/80C10J3/84
CPCC10J3/56C10J3/72C10J3/721C10J3/80C10J3/84C10J2300/0936C10J2300/0959C10J2300/0976C10J2200/152C10J2300/1807
Inventor 李晓宏权亚文杜鹏鹏张飞高伟赵金萍何淑梅
Owner SHAANXI YANCHANG PETROLEUM GRP
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