阅读说明：本技术 一种燃尽含碳飞灰的双床复合煤气化炉 (Double-bed composite coal gasifier for burning off carbon-containing fly ash ) 是由 张连华 张晖 沈法华 陈习中 于 2021-09-05 设计创作，主要内容包括：本发明涉及一种燃尽含碳飞灰的双床复合煤气化炉,它将上部循环流化床内产生的含碳飞灰分离后用飞灰分散盘送入同一炉腔下部设置的热解固定床的高温渣焦层中燃烧气化,直至燃尽。飞灰分散盘由一级分灰管、分灰圈、二级分灰管、分灰圈与喷灰圈组成,飞灰输入管通过一级分灰管与分灰圈相连通,分灰圈通过二级分灰管与喷灰圈相连通,喷灰圈与炉芯连体,喷灰圈上设有喷灰孔,喷灰孔将含碳飞灰送入固定床高温焦渣层。本发明具有节能环保、飞灰输送顺畅、进入炉腔分布均匀、燃烧气化彻底等优点。(The invention relates to a double-bed composite coal gasifier for burning off carbon-containing fly ash, which separates the carbon-containing fly ash generated in an upper circulating fluidized bed and sends the separated carbon-containing fly ash into a high-temperature slag coke layer of a pyrolysis fixed bed arranged at the lower part of the same furnace chamber for combustion and gasification until the carbon-containing fly ash is burnt off. The fly ash dispersion disc consists of a first-level ash separating pipe, an ash separating ring, a second-level ash separating pipe, an ash separating ring and an ash spraying ring, wherein a fly ash input pipe is communicated with the ash separating ring through the first-level ash separating pipe, the ash separating ring is communicated with the ash spraying ring through the second-level ash separating pipe, the ash spraying ring is connected with the furnace core, an ash spraying hole is formed in the ash spraying ring, and the ash spraying hole sends carbon-containing fly ash into a high-temperature coke residue layer of the fixed bed. The invention has the advantages of energy saving, environmental protection, smooth fly ash conveying, even distribution in the furnace chamber, complete combustion and gasification and the like.)

1. The utility model provides a burn out double-bed composite coal gasifier of carbonaceous flying ash, it includes composite gasification stove, composite gasification stove's furnace chamber upper portion is circulating fluidized bed, and the lower part is the pyrolysis fixed bed, the pyrolysis fixed bed is equipped with the stove core, the stove core inner chamber is gasification agent passageway, its characterized in that:

the carbon-containing fly ash is sprayed into the high-temperature coke residue layer of the pyrolysis fixed bed after being dispersed by a fly ash dispersion disc, the fly ash dispersion disc is arranged in the gasifying agent channel, the fly ash dispersion disc comprises a fly ash input pipe, an ash separating ring and an ash spraying ring, the ash separating pipe is provided with a first-level ash separating pipe and a second-level ash separating pipe, the first-level ash separating pipe is arranged between the fly ash input pipe and the ash separating ring, the second-level ash separating pipe is arranged between the ash separating ring and the ash spraying ring, the fly ash input pipe is communicated with the ash separating ring through the first-level ash separating pipe, the ash separating ring is communicated with the ash spraying ring through the second-level ash separating pipe, the ash spraying ring is connected with the furnace core, and the ash spraying ring is provided with ash spraying holes which are communicated with the high-temperature coke residue layer.

2. The dual-bed composite coal gasifier for burning off carbon-containing fly ash according to claim 1, wherein: the fly ash dispersion disc is arranged in the middle of the furnace core.

3. The dual-bed composite coal gasifier for burning off carbon-containing fly ash according to claim 1, wherein: the fly ash input pipe, the ash separating ring and the ash spraying ring are arranged in the same plane.

4. The dual-bed composite coal gasifier for burning off carbon-containing fly ash according to claim 1, wherein: the fly ash input pipe, the ash separating ring and the ash spraying ring are arranged into a cone, the fly ash input pipe is positioned at the top of the cone, and the ash spraying ring is positioned at the bottom of the cone.

5. The dual-bed composite coal gasifier for burning off carbon-containing fly ash according to claim 1, wherein: and a slag stopping brim is arranged on the ash spraying ring above the ash spraying hole.

Technical Field

The invention relates to a gasification furnace, in particular to a double-bed composite coal gasification furnace for recycling gasified burnout of carbon-containing fly ash, belonging to the technical field of coal gasification.

Background

In recent years, although clean energy such as wind power, hydropower, nuclear power, photovoltaic and the like is rapidly developed and utilized, the method still cannot adapt to social development requirements, on one hand, the total amount of developed energy cannot be met, and on the other hand, the method is high in price and high in use cost. Because of large inventory and low price, coal is still the main heat energy source in the industries of smelting, chemical engineering, ceramics and the like in China at present and in a certain period in future. Around the efficient and clean utilization of coal, people design various coal gasification furnaces, the most widely used are fixed bed gasification furnaces and fluidized bed gasification furnaces, which have the advantages and disadvantages that the carbon conversion rate and the thermal efficiency of the fixed bed gasification furnaces are high, but tar and phenol water exist in the production process; the latter can produce clean coal gas, but the fly ash containing carbon produced in the gas production process is difficult to treat, and in addition, a large amount of semicoke is discharged with slag, so that the carbon conversion rate is reduced, and the environment is polluted. In order to solve the problem of semicoke discharge, the applicant of the present invention has proposed a circulating fluidized bed (202110944641.2) in which a fluidized combustion and moving pyrolysis furnace are combined, wherein the upper part of a gasification furnace is provided with a fluidized bed and the lower part thereof is provided with a fixed bed, so that the advantages of the fluidized bed and the fixed bed are utilized, thereby not only producing clean coal gas, but also burning out semicoke and improving the conversion rate of coal. However, the treatment of the fly ash is not satisfactory, the fly ash is often matched with the construction of a power plant for treating the fly ash, the investment is large, the cost is high, and the fly ash is not suitable for the technical transformation and equipment transformation upgrading of small and medium-sized enterprises. In order to solve the problem of difficult treatment of the carbon-containing fly ash, the existing carbon-containing fly ash combustion equipment and process of the circulating fluidized bed must be further optimized.

Disclosure of Invention

The invention provides a double-bed composite coal gasifier for burning off carbon-containing fly ash, aiming at the problem that the carbon-containing fly ash generated by a circulating fluidized bed in the background art is difficult to treat. By arranging the fly ash dispersion disc, carbon-containing fly ash is sprayed into a high-temperature coke slag layer of the pyrolysis fixed bed by pneumatic transmission to be burnt out.

In order to achieve the purpose, the invention provides the following technical scheme that the double-bed composite coal gasification furnace for burning off the carbon-containing fly ash comprises a composite gasification furnace, wherein the upper part of a furnace chamber of the composite gasification furnace is a circulating fluidized bed, the lower part of the furnace chamber of the composite gasification furnace is a pyrolysis fixed bed, the pyrolysis fixed bed is provided with a furnace core, the inner cavity of the furnace core is a gasification agent channel, the circulating fluidized bed generates coal gas, semicoke and the carbon-containing fly ash, the semicoke enters a solid bed gasification furnace for pyrolysis gasification, and the coal gas enters gas equipment.

And the carbon-containing fly ash is sprayed into the pyrolysis fixed bed high-temperature coke slag layer after being dispersed by a fly ash dispersion disc, and the fly ash dispersion disc is arranged in the gasifying agent channel. The fly ash dispersion disc comprises a fly ash input pipe, an ash separating ring and an ash spraying ring, wherein the ash separating pipe is provided with a first-stage ash separating pipe and a second-stage ash separating pipe, the first-stage ash separating pipe is arranged between the fly ash input pipe and the ash separating ring, the second-stage ash separating pipe is arranged between the ash separating ring and the ash spraying ring, the fly ash input pipe is communicated with the ash separating ring through the first-stage ash separating pipe, the ash separating ring is communicated with the ash spraying ring through the second-stage ash separating pipe, the ash spraying ring is connected with the furnace core, an ash spraying hole is formed in the ash spraying ring, and the ash spraying hole is communicated with the high-temperature coke residue layer.

Preferably, the fly ash dispersion plate is arranged in the middle of the furnace core.

Preferably, the fly ash input pipe, the ash separating ring and the ash spraying ring are arranged in the same plane.

Preferably, the fly ash input pipe, the ash separating ring and the ash spraying ring are arranged into a cone, the fly ash input pipe is positioned at the top of the cone, and the ash spraying ring is positioned at the bottom of the cone.

Furthermore, a slag stopping brim is arranged on the ash spraying ring above the ash spraying hole.

The invention arranges a fly ash dispersion disk in the furnace core of the pyrolysis fixed bed, and an ash spraying ring of the fly ash dispersion disk is connected with the furnace core. The fly ash dispersion disc gradually disperses the carbon-containing fly ash and sprays the carbon-containing fly ash into the high-temperature coke residue layer of the pyrolysis fixed bed from the ash spraying holes arranged on the ash spraying ring to burn out.

The invention has the advantages of energy saving, environmental protection, smooth transportation of carbon-containing fly ash, uniform distribution in the furnace chamber, complete combustion and gasification and the like.

Drawings

FIG. 1 is a main sectional structure diagram of the present invention,

figure 2 is an enlarged view of portion I of figure 1,

fig. 3 is a cross-sectional view taken along line a-a of fig. 2.

In the attached drawing, 1 is a gasification furnace, 2 is a fly ash dispersion disc, 3 is a furnace core, 4 is a positioning seat, 5 is a gasification agent conduit, 6 is a fly ash conveying pipe, 7 is an air distribution grate, 8 is an air distribution plate, 9 is a slag stopping eave, 201 is a fly ash input pipe, 202 is an ash separating ring, 203 is an ash spraying ring, 204 is an ash spraying hole, 205 is a first-stage ash separating pipe and 206 a second-stage ash separating pipe.

Detailed Description

The figure shows an embodiment in which the fly ash dispersing disks 2 are arranged in a planar mesh. As shown in figure 1, raw material coal is combusted and gasified in a gasification furnace 1 to generate semicoke, carbon-containing fly ash and coal gas, the semicoke enters a solid bed gasification furnace for pyrolysis and gasification, the coal gas enters gas-using equipment, separated carbon-containing fly ash is gathered to form fly ash airflow under the action of high-pressure nitrogen, the fly ash airflow enters a fly ash conveying pipeline 6 and then enters a fly ash input pipe 201 from the fly ash conveying pipeline 6, the fly ash airflow is conveyed into a primary ash separating pipe 205 by the fly ash input pipe 201, the fly ash airflow is conveyed into an ash separating ring 202 by the primary ash separating pipe 205, the fly ash airflow is conveyed into a secondary ash separating pipe 206 by the ash separating ring 202, the fly ash airflow is conveyed into an ash spraying ring 203 by the secondary ash separating pipe 206, and the fly ash airflow is sprayed into a high-temperature slag coke layer above an air distribution grate 7 from an ash spraying hole 204 and is combusted until the coal gas is completely gasified. A slag blocking eave 9 is arranged above the ash spraying hole 204 to prevent coal slag from reversely entering the ash spraying ring 203 from the ash spraying hole 204.

The fly ash dispersion disc 2 is arranged in a gasifying agent channel below the air distribution plate 8 of the circulating fluidized bed, an ash spraying ring of the fly ash dispersion disc is connected with a furnace core 3 of the pyrolysis fixed bed, and the furnace core 3 is arranged on the positioning seat 4 and supported by the positioning seat 4.

In the figure, a gasifying agent conduit 6 sends a gasifying agent into a gasifying agent channel to provide the gasifying agent for the circulating fluidized bed and the pyrolysis fixed bed.