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Gasification furnace and gasification method thereof

A gasifier and mixed gas technology, applied in the field of coal gasification, can solve problems such as low effective gas content

Active Publication Date: 2020-04-03
ENN SCI & TECH DEV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In the existing entrained gasifier technology, the effective gas composition is about 80%-90%, the effective gas content is low, and the carbon dioxide gas generated is about 10%-20%, which brings a lot of greenhouse gases to the environment

Method used

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  • Gasification furnace and gasification method thereof

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Experimental program
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Effect test

Embodiment 1

[0054] Applied to the top single burner 3 gasifier, combined with figure 1 , figure 2 and image 3 As shown, the designed coal input (dry basis) is 1000t / d, the pressure is 4.0MPa, and the first insulation layer 12 is made of refractory bricks. The top of the gasifier is a three-channel burner 3, and the burner 3 channels (from inside to outside) are respectively central oxygen, coal water slurry and annular oxygen, wherein the central oxygen accounts for about 20% of the total oxygen. The above-mentioned primary reaction chamber 1 is a fully mixed flow reactor, and the height H of the primary reaction chamber 1 1 4m, diameter φ 1 is 2.134m, the aspect ratio is 1.87, and the volume is 15m 3 . The secondary reaction chamber 2 is a plug flow reactor with a height H 2 3m, diameter φ 2 is 0.91m, the aspect ratio is 3.29, α is 15°, and the volume is 2.4m 3 .

[0055] Such as image 3 As shown, the periphery of the primary reaction chamber 1 is provided with eight first h...

Embodiment 2

[0059] Applied to top-mounted single-burner 3 gasifiers, such as Figure 4 As shown, the designed coal input (dry basis) is 1500t / d, the pressure is 4.0MPa, the first heat insulation layer 12 adopts a water wall; the top is a two-channel burner 3, and the burner 3 channels (from the inside to the outside) are respectively For oxygen and pulverized coal. The primary reaction chamber 1 is a fully mixed flow reactor with a height H 1 4m, diameter φ 1 2.7m, height-to-diameter ratio 1.48, volume 25m 3 . The secondary reaction chamber 2 is a plug flow reactor with a height H 2 3.5m, diameter φ 2 is 0.96m, the aspect ratio is 3.64, α is 15°, and the volume is 3m 3 , the second heat insulation layer 18 is made of a water-cooled wall.

[0060] The primary reaction chamber 1 is provided with eight first high-temperature thermocouples 16, every four first high-temperature thermocouples 16 are on the same plane, and a pair of first high-temperature thermocouples 16 on the upper and...

Embodiment 3

[0062] Applied to side multi-burner 3 gasifiers, combined with Figure 5 and Figure 6As shown, the designed coal input (dry basis) is 1500t / d, the pressure is 6.5MPa, the first insulation layer 12 is made of refractory bricks; the side part is four three-channel burners 3, and the burner 3 channels (from inside to Outer) are central oxygen, coal water slurry and annular gap oxygen respectively, wherein central oxygen accounts for about 18% of the total oxygen. Primary reaction chamber 1 is a fully mixed flow reactor with high H 1 5m, φ 1 is 2.4m, the aspect ratio is 2.08, and the volume is 24m 3 ; The secondary reaction chamber 2 is a plug-flow reactor, and the second insulation layer 18 selects refractory bricks, and the high H of the secondary reaction chamber 2 2 3.5m, diameter φ 2 is 0.96m, the aspect ratio is 3.64, α is 15°, and the volume is 3m 3 .

[0063] Such as Figure 6 As shown, the outer circumference of the primary reaction chamber 1 is provided with nin...

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Abstract

The invention relates to the technical field of coal gasification, and provides a gasification furnace and a gasification method thereof. The gasification furnace comprises a primary reaction chamber,a secondary reaction chamber and a chilling chamber, a first contraction section is arranged at the bottom of the primary reaction chamber, and an expansion section is arranged at the top of the secondary reaction chamber. The gasification method comprises the following steps: a burner injects a material and an oxidizing agent into the primary reaction chamber, the flow velocity of a gas in the primary reaction chamber is controlled to be 0.6-1.2 m / s, and the standing time of the gas is controlled to be 3-6 s; a mixed gas passes through the first contraction section at a speed of 8-12 m / s; the speed of a gas in the secondary reaction chamber is 3-8 m / s, and the standing time is 0.2-0.8 s; and the mixed gas generated by a secondary reaction enters the chilling chamber. A combustion chamberis divided into the primary reaction chamber and the secondary reaction chamber, the first contraction section is arranged at the bottom of the primary reaction chamber to prevent the material and the oxidizing agent from escaping, enhance the back-mixing state and increase the conversion rate of carbon, and the expansion section is arranged at the secondary reaction chamber to avoid gas backflow, increase the intensity of the secondary reaction and increase the content of effective gas.

Description

technical field [0001] The invention relates to the technical field of coal gasification, in particular to a gasification furnace and a gasification method thereof. Background technique [0002] At present, coal-water slurry gasification technology and pulverized coal gasification technology are two mainstream entrained bed gasification technologies. After gasification reaction between coal-water slurry or pulverized coal and oxidant, synthesis gas containing CO and H2 is generated, which is then purified, Conversion and synthesis processes to produce high value-added chemicals such as methanol, ethylene glycol, and urea. The reactor is the core device of the gasification reaction. The common ones are fully mixed flow reactor and plug flow reactor. The fully mixed flow reactor refers to the reactor that reacts after mixing the media with different residence times, while the plug flow reactor refers to the The medium enters and exits at the same time, and the reactor has the...

Claims

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Application Information

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IPC IPC(8): C10J3/48
CPCC10J3/48
Inventor 王向龙侯祥生李克忠高明刘刚徐国壮付伟贤彭知顺
Owner ENN SCI & TECH DEV