CN211600709U - Integrated fixed bed garbage high-efficiency gasification combustion furnace - Google Patents

Abstract

The utility model provides an integral type fixed bed rubbish high efficiency gasification fires burning furnace, furnace body from up coaxial fixed bed gasification section, dry pyrolysis section, the combustible gas burning section of setting up. Garbage gets into dry pyrolysis section from the feed inlet, utilizes the radiant heat of circulation hot flue gas and combustible gas burning section to carry out drying, pyrolysis to garbage, and the solid after the pyrolysis falls into the gasification section and gasifies, and the combustible gas that the gasification produced mixes with pyrolysis gas at dry pyrolysis section, gets into the combustible gas burning section afterwards and carries out the high temperature combustion. Because pyrolysis and gasification are carried out under the anoxic condition, the generated combustible gas is rich in hydrogen, and the generation of dioxin precursors is avoided under the hydrogen-rich condition, so that the emission of dioxin is reduced from the source. The utility model discloses when realizing resourceization, innoxiousness, minimizing and the stabilization of rubbish, solved the high problem of msw incineration process dioxin emission.

Description

Integrated fixed bed garbage high-efficiency gasification combustion furnace

Technical Field

The utility model relates to an integral type fixed bed rubbish high efficiency gasification fires burning furnace belongs to solid waste processing technology field.

Background

China is the country with the highest garbage burden, the total quantity of garbage stacked in disorder throughout the country over the years is as much as 160 hundred million tons, 9 hundred million square meters of land is occupied, air and underground water resources are seriously polluted, and the rapid harmonious development of urban economy and environment is seriously hindered. In addition, China is a country with resource and energy shortage, how to realize the resource and energy utilization of urban garbage, and the method develops circular economy while solving the problem of urban garbage, and is an effective way for realizing the change of economic development modes.

In order to solve the serious problems, a plurality of solutions are provided for garbage treatment at home and abroad, such as landfill after sorting, fertilizer preparation, cracking oil preparation, biochemical treatment and the like. Among them, incineration disposal, sanitary landfill, and composting, which have been already put into practice, have certain disadvantages. For example, in the incineration technology, heat energy is obtained while waste reduction is realized, but more dioxin (also called dioxin is a fat-soluble substance with no color, no taste and serious toxicity) is generated, and smoke hardly reaches the emission standard after being specially treated.

Developed countries such as europe, the united states, japan and the like are actively developing the application of a garbage gasification technology, which directly generates combustible gas with a certain calorific value by high-temperature heat treatment of garbage in an oxygen-poor atmosphere or a small amount of steam atmosphere, and burns the combustible gas for power generation or heat supply. Compare in the direct incineration disposal of traditional rubbish, the gasification technique turns into the combustible gas with rubbish, and under the gasification condition, the production volume of dioxin reduces by a wide margin, can reduce the emission of dioxin from the source, is regarded as a more environmental protection efficient treatment way.

SUMMERY OF THE UTILITY MODEL

The to-be-solved technical problem of the utility model is how to reduce the discharge of dioxin in the garbage heat treatment process.

In order to solve the technical problem, the technical scheme of the utility model is to provide an integrated fixed bed garbage high-efficiency gasification combustion furnace, which is characterized in that a furnace body is coaxially provided with a fixed bed gasification section, a drying pyrolysis section and a combustible gas combustion section from bottom to top; the bottom of the fixed bed gasification section is provided with a slag discharge port, the side surfaces of the drying pyrolysis section are symmetrically provided with 2 garbage feed ports, and the upper part of the combustible gas combustion section is provided with a high-temperature flue gas outlet.

Preferably, the fixed bed gasification section comprises a heat insulation furnace wall section, ash discharging necking arranged at two sides and connected with the heat insulation furnace wall section and a fire grate arranged at the center, and a material layer supporting platform is arranged at the lower part of the heat insulation furnace wall section; the grate is of a 3-7-layer pagoda-shaped ventilation structure, a grate supporting platform and a grate driving shaft opening are arranged on the inner inclined surface of the ash discharge throat, and the grate driving shaft opening extends downwards to penetrate out of the inclined surface of the ash discharge throat; the center of the upper part of the grate supporting platform is provided with a gasifying agent runner pipe, the upper part of the gasifying agent runner pipe is vertically arranged at the center of the grate, and the inlet bending section at the lower part of the gasifying agent runner pipe extends out of the furnace body.

Preferably, a wear-resisting plate is arranged on the inner side of the material layer supporting platform; the included angle beta between the inclined plane of the ash slag discharge necking and the vertical line is 15-60 degrees; the included angle theta between the pagoda inclined plane and the vertical line of the fire grate is 30-75 degrees, ash scraping knives are arranged on the lowermost layer of the fire grate, and the number of the ash scraping knives is 1-6; the height H2 from the material layer supporting platform to the outlet of the fixed bed gasification section is 2-6 m.

Preferably, the gasification agent circulated by the gasification agent circulation pipe is any one of air, oxygen-enriched air and pure oxygen or a mixed gas of any one of air, oxygen-enriched air and pure oxygen and steam.

Preferably, the dry pyrolysis section comprises a heat insulation furnace wall, and the bottom of the dry pyrolysis section is symmetrically provided with 2 inclined grates; an air chamber is arranged below the grate, and an air inlet and an ash leakage outlet are arranged on the air chamber.

Preferably, the fire grate is a fixed fire grate or a movable fire grate, and the inclination angle alpha of the fire grate is 15-60 degrees; the width of the grate is equal to the inner diameter D2 of the gasification section of the fixed bed, and the length L is 1-3 times of the width; the angle between the upper inclined plane and the vertical plane of the heat insulation furnace wall is 30-80 degrees.

Preferably, the air introduced from the air inlet is air or hot flue gas.

Preferably, the combustible gas combustion section comprises a combined furnace wall of a heat insulation furnace wall and a water-cooling or air-cooling furnace wall; the lower part of the combustible gas combustion section is provided with at least 2 layers of air nozzles.

Preferably, the air nozzles are arranged in a 4-degree tangent circle mode or in a front-rear wall opposite impact mode, the number of layers is an even number in a range from 2 to 16, the number of clockwise tangent circles in the layers is equal to the number of anticlockwise tangent circles in the layers, and the height from the uppermost layer of the air nozzles to the high-temperature flue gas outlet is 4-12 m.

Preferably, the inner diameter D1 of the combustible gas combustion section is 1-4 times of the inner diameter D2 of the fixed bed gasification section.

The utility model has the advantages of through the combination of trick of grate, combustible gas combustion mode, realized 3 processes of dry pyrolysis of rubbish, waste gasification, combustible gas burning in a stove, overcome rubbish and directly burned the high shortcoming of dioxin emission, reach the purpose of the clean thermal conversion of rubbish. Because the drying section in the furnace is arranged, the utility model can treat the garbage with higher water content. In addition, fixed bed gasification is comparatively wide in range to the requirement of rubbish granularity, the utility model discloses it is loose to rubbish pretreatment requirement, only need simple letter sorting broken can.

Drawings

FIG. 1 is a schematic front view of an integrated fixed bed waste high efficiency gasification combustion furnace;

FIG. 2 is a schematic side view of an integrated fixed bed garbage high efficiency gasification combustion furnace;

FIG. 3 is a first cross-sectional view taken along line A-A of FIG. 1;

FIG. 4 is a second cross-sectional top view taken along line A-A of FIG. 1;

FIG. 5 is a sectional top view of B-B shown in FIG. 1;

FIG. 6 is a detailed view of FIG. 1 at I; in the figure, 6a represents a garbage layer and 6b represents hot flue gas;

FIG. 7 is a detail view of FIG. 2 at point II; in the figure, 7a represents a garbage layer, 7b and 7d represent ash, and 7c represents a gasifying agent;

description of reference numerals:

100-a combustible gas combustion section; 200-drying the pyrolysis section; 300-a grate; 400-fixed bed gasification stage; 500-grate; 101-combined furnace wall; 102-air jets; 103-high temperature flue gas outlet; 201-heat insulation furnace wall; 202-a feed inlet; 203-air/hot flue gas inlet; 204-an air chamber; 205-ash leakage and discharge port; 401-an insulated furnace wall section; 402-ash outlet; 403-material bed supporting platform; 404-a wear plate; 405-discharging ash slag and necking; 406-a grate support platform; 407-grate drive shaft port; 408-a gasifying agent circulation pipe; 501-ash scraping knife.

Detailed Description

The present invention will be further described with reference to the following specific examples.

In order to make the present invention more comprehensible, preferred embodiments are described in detail below with reference to the accompanying drawings.

The utility model relates to an integrated fixed bed garbage high-efficiency gasification combustion furnace, as shown in figure 1 and figure 2. Comprises 5 main components, namely a fixed bed gasification section 400, a grate 500, a drying pyrolysis section 200, a grate 300 and a combustible gas combustion section 100; the fixed bed gasification section 400 comprises a heat insulation furnace wall section 401, ash discharging necking 405 arranged at two sides and connected with the heat insulation furnace wall section 401 and a fire grate 500 arranged at the center, and a material layer supporting platform 403 is arranged at the lower part of the heat insulation furnace wall section 401; the grate 500 is a 3-7-layer pagoda-shaped ventilation structure, a grate supporting platform 406 and a grate driving shaft port 407 are arranged on the inner side inclined surface of the ash discharge throat 405, and the grate driving shaft port 407 extends downwards to penetrate out of the inclined surface of the ash discharge throat 405; the center of the upper part of the grate supporting platform 406 is provided with a gasification agent circulation pipe 408, the upper part of the gasification agent circulation pipe 408 is vertically arranged at the center of the grate 500, and the inlet bending section at the lower part of the gasification agent circulation pipe 408 extends out of the furnace body; the dry pyrolysis section 200 comprises an insulating furnace wall 201, and the bottom of the dry pyrolysis section 200 is symmetrically provided with 2 inclined grates 300; an air chamber 204 is arranged below the grate 300, and an air inlet 203 and an ash leakage outlet 205 are arranged on the air chamber 204; the combustible gas combustion section 100 comprises a combined furnace wall 101 of a heat insulation furnace wall and a water-cooling or air-cooling furnace wall; the lower portion of the combustible gas combustion section 100 is provided with at least 2 layers of air jets 102.

The utility model discloses an internal work region is 3 regions, describes respectively as follows:

a dry pyrolysis zone: the waste enters the grate 300 arranged at the bottom of the pyrolysis drying section in an inclined way from 2 feed ports 202 through an external feeding system, as shown in figure 5. Because the grate 300 has a certain gradient, the garbage is freely spread downwards on the grate 300, and a material layer with a certain thickness is formed on the grate 300. The hot flue gas from the plenum 204 flows out from the gas distribution holes of the grate 300 and horizontally penetrates through the garbage layer, so that the garbage has certain heating, drying, ventilating and pushing effects, the upper part of the garbage layer receives high-temperature radiation from the combustible gas combustion section 100, and the garbage is dried and pyrolyzed, as shown in fig. 6. Pyrolysis gas and water vapor generated by the drying pyrolysis section 200 are mixed with combustible gas from the fixed bed gasification section 400, and then enter the combustible gas combustion section 100 for combustion, and garbage after drying pyrolysis falls into the fixed bed gasification section 400 for gasification reaction. Because the flow area of the dry pyrolysis section 200 is much larger than that of the fixed bed gasification section 400, the flow rate of the gas is significantly reduced when the gas flows through the dry pyrolysis section 200, and the particles carried by the fixed bed gasification section 400 fall into the fixed bed gasification section 400 again to continue gasification, so that the dust content of the flue gas discharged from the high-temperature flue gas outlet 103 is greatly reduced. On the other hand, the combustible gas generated by gasification is rich in hydrogen, and after the flow rate of the combustible gas flowing through the drying pyrolysis section 200 is reduced, the residence time is prolonged, the reaction time of the hydrogen and the dioxin precursor is prolonged, and the reduction of the emission of the dioxin from the source is facilitated.

Because the dry pyrolysis section 200 that adopts the grate 300 has been set up in the stove, the utility model discloses can handle the higher rubbish of water content, when the rubbish low grade calorific value that goes into the stove reaches 5200kJ/kg, the highest water content of rubbish that goes into the stove can relax to 52%. The utility model discloses require simply to rubbish preliminary treatment, only need simply sort to broken to the particle diameter be less than 100mm can.

A gasification area: the garbage dried and partially pyrolyzed in the drying pyrolysis section falls into the fixed bed gasification section 400 for gasification reaction. After the refuse falls into this area, a bed of material of a certain thickness is formed above the grate 500. The gasifying agent (air + superheated steam) is distributed evenly through the grate 500 and then passes up through the bed as shown in fig. 7. The gasification agent is in countercurrent contact with the garbage through the material layer, the garbage is sequentially subjected to drying, dry distillation, gasification and combustion reaction from top to bottom, the residual ash after the reaction is cooled by the gasification agent, and under the condition that the grate 500 rotates, the ash and slag scraping knife 501 arranged on the outer edge of the bottom of the grate scrapes into the ash and slag discharge throat 405 and is discharged out of the furnace from the ash and slag outlet 402.

Because the residence time of the garbage in the fixed bed gasification section 400 is longer than 1 hour, the highest temperature reaches 1000 ℃, the combustible in the garbage can be completely gasified, the ignition loss of the discharged ash is very low, and the typical value is less than 3%.

Combustible gas combustion zone: the gasification section produces 600 ℃ combustible gas and carries a small amount of particles to enter the dry pyrolysis section 200, because the flow area enlarges suddenly, the flow rate reduces remarkably, the particles carried by the air current fall into the gasification section again, and the combustible gas and the pyrolysis gas and the steam generated by the dry pyrolysis section 200 are mixed and then enter the combustible gas combustion area 100. In the upward flowing process of the gas, the temperature is reduced firstly, then the gas is heated gradually by high-temperature radiant heat in a combustion area, the temperature is gradually increased to about 700 ℃, the gas is combusted with hot air sprayed from the air nozzle 102, the temperature is further increased to 870 ℃, and the residence time of the smoke in a high-temperature area is more than 2S, so that pollutants and macromolecular substances in the combustible gas are thoroughly decomposed. When the calorific value of the garbage cannot reach the calorific value required by the design, a afterburning burner is arranged in the area to maintain the temperature to be higher than 870 ℃. The high-temperature flue gas is discharged from the high-temperature flue gas outlet 103, enters a waste heat recovery boiler of a subsequent system, and generates steam for power generation or heat supply.

In order to enhance the mixing of air and combustible gas, the air nozzles 102 in this area are arranged in 4 corner tangential circles, 4 layers are arranged from bottom to top, the tangential circle diameter of each layer is equal, and the layers are respectively a clockwise tangential circle, an anticlockwise tangential circle, a clockwise tangential circle and an anticlockwise tangential circle from bottom to top, as shown in fig. 3. The principle of the arrangement of the air nozzles is to fully mix and burn the air and the combustible gas as far as possible, and besides the mode of 4-degree tangent circles, the opposite arrangement mode of the front wall and the rear wall can achieve similar effects, as shown in figure 4.

The utility model discloses can show the emission that has reduced dioxin from the source, realize the high-efficient clean thermal conversion of rubbish, reach the minimizing of rubbish, stabilization, resourceization and innoxious purpose.

The effect of the present invention will be described below by taking an integrated fixed bed garbage high efficiency gasification combustion furnace with a daily garbage disposal amount of 600 tons as an example.

Examples

600 tons (water content 52%) of integral type fixed bed rubbish high efficiency gasification combustion furnace are handled to a set of day, and fixed bed gasification section 400 internal diameter D2 is 4000mm, and height H2 is 5m, and this section outside is the square, and inside is the cylinder, fills refractory material between square and the cylinder, and thickness is 200 mm.

The thickness of the refractory insulation layer of the insulation furnace wall of the dry pyrolysis section 200 is about 200mm, and the angle between the inclined plane and the vertical plane is 65 degrees. The grate 300 has a width of 4m, a length L of 4.5m and a grate inclination angle α of 25 °.

The combustible gas combustion section 100 is the square, and the internal diameter is 6m, sets up adiabatic brickwork, and the thickness of fire-resistant insulating layer is about 200mm, sets up 4 layers of 4 angle tangent circle air spout, and the topmost layer air spout is 6m apart from high temperature exhanst gas outlet 103's height H1. SNCR is arranged in the furnace, a afterburning burner (used when the low calorific value of the garbage fed into the furnace is lower than 5200 kJ/kg) is arranged in the furnace, and the total height of the gasification combustion furnace is 32 m.

The high-temperature flue gas outlet 103 is connected with a waste heat boiler, and after the heat of the high-temperature flue gas is recovered by the waste heat boiler, part of the flue gas is pressurized by a fan and then is sent to the drying pyrolysis section 200. And (3) delivering steam generated by the waste heat boiler to 1 supercritical coal-fired boiler for reheating and upgrading, and then generating power by using a supercritical unit. The steam produced by the waste heat boiler can also be used for supplying heat.

The garbage raw material is urban garbage with water content of 52%.

The garbage property parameters are as follows:

item	Unit of	Garbage collection
			C	％	15.25
H	％	2.8
			O	％	14
N	％	0.5
			S	％	0.15
Cl	％	0.3
			Moisture content	％	52
Fixed carbon	％	9
			Volatile component	％	24
Ash content	％	15
			Lower calorific value	kJ/kg	5200

The operating parameters of the gasification burner were as follows:

the main performance indexes of the gasification combustion furnace are as follows:

the emission index of the gasification combustion furnace is as follows (waste heat boiler outlet):

from above data can see, the utility model discloses compare with current waste incineration mode, the dioxin content of original emission is showing and is reducing (the utility model discloses only 12.5% of waste incinerator), and the flue gas dust content also reduces by a wide margin (the utility model discloses a 33.3% of waste incinerator), and whole thermal efficiency is equivalent (being greater than 80%) with waste incinerator. Because of the integrated furnace structure, the investment of the equipment is equivalent to that of the garbage incinerator with the same scale, and the emission index is superior to that of the garbage incinerator.

The foregoing is merely a preferred embodiment of the present invention, and is not intended to limit the present invention in any way and in any way, and it should be understood that modifications and additions may be made by those skilled in the art without departing from the method of the present invention, and such modifications and additions are also considered to be within the scope of the present invention. Those skilled in the art can make various changes, modifications and evolutions equivalent to those made by the above-disclosed technical content without departing from the spirit and scope of the present invention, and all such changes, modifications and evolutions are equivalent embodiments of the present invention; meanwhile, any changes, modifications and evolutions of equivalent changes to the above embodiments according to the actual technology of the present invention are also within the scope of the technical solution of the present invention.

Claims (10)

1. The integrated fixed bed garbage high-efficiency gasification combustion furnace is characterized in that a furnace body is coaxially provided with a fixed bed gasification section (400), a drying pyrolysis section (200) and a combustible gas combustion section (100) from bottom to top; the bottom of the fixed bed gasification section (400) is provided with a slag discharge port (402), the side surface of the drying pyrolysis section (200) is symmetrically provided with 2 garbage feed ports (202), and the upper part of the combustible gas combustion section (100) is provided with a high-temperature flue gas outlet (103).

2. The integrated fixed bed refuse high efficiency gasification combustion furnace according to claim 1, wherein the fixed bed gasification stage (400) comprises a heat insulation furnace wall section (401), ash discharge throats (405) provided at both sides and connected to the heat insulation furnace wall section (401), and a grate (500) provided at the center, and a material bed support platform (403) is provided at the lower part of the heat insulation furnace wall section (401); the grate (500) is of a 3-7-layer pagoda-shaped ventilation structure, a grate supporting platform (406) and a grate driving shaft port (407) are arranged on the inner side inclined surface of the ash discharge throat (405), and the grate driving shaft port (407) extends downwards to penetrate out of the inclined surface of the ash discharge throat (405); the center of the upper part of the grate supporting platform (406) is provided with a gasification agent circulation pipe (408), the upper part of the gasification agent circulation pipe (408) is vertically arranged at the center of the grate (500), and the inlet bending section at the lower part of the gasification agent circulation pipe (408) extends out of the furnace body.

3. An integrated fixed bed refuse high efficiency gasification combustion furnace according to claim 2, wherein the material bed supporting platform (403) is provided with a wear plate (404) inside; the included angle beta between the inclined plane of the ash discharge necking (405) and the vertical line is 15-60 degrees; the included angle theta between the pagoda inclined plane and the vertical line of the fire grate (500) is 30-75 degrees, the lowermost layer of the fire grate (500) is provided with ash scraping knives (501), and the number of the ash scraping knives (501) is 1-6; the height H2 from the material layer supporting platform (403) to the outlet of the fixed bed gasification section (400) is 2-6 m.

4. The integrated fixed bed waste gasification burner as recited in claim 2, wherein the gasifying agent circulated through the gasifying agent circulation pipe (408) is any one of air, oxygen-enriched air and pure oxygen or a mixture of air, oxygen-enriched air and pure oxygen and steam.

5. The integrated fixed bed waste high efficiency gasification combustion furnace as set forth in claim 1, wherein the dry pyrolysis section (200) comprises an adiabatic furnace wall (201), and 2 inclined grates (300) are symmetrically arranged at the bottom of the dry pyrolysis section (200); an air chamber (204) is arranged below the grate (300), and an air inlet (203) and an ash leakage outlet (205) are arranged on the air chamber (204).

6. The integrated fixed bed refuse high efficiency gasification combustion furnace according to claim 5, characterized in that the grate (300) is a fixed grate or a movable grate, the inclination angle α of the grate (300) is 15-60 °; the width of the grate (300) is equal to the inner diameter D2 of the fixed bed gasification section (400), and the length L is 1-3 times of the width; the angle between the upper inclined plane of the heat insulation furnace wall (201) and the vertical plane is 30-80 degrees.

7. The integrated fixed bed garbage high efficiency gasification combustion furnace as set forth in claim 5, characterized in that the wind introduced from the wind inlet (203) is air or hot flue gas.

8. An integrated fixed bed refuse high efficiency gasification combustion furnace according to claim 1, wherein said combustible gas combustion section (100) comprises a combined furnace wall (101) of a heat insulating furnace wall and a water-cooled or air-cooled furnace wall; the lower part of the combustible gas combustion section (100) is provided with at least 2 layers of air nozzles (102).

9. The integrated fixed bed waste gasification burner as recited in claim 8, wherein the air nozzles (102) are arranged in 4-degree tangential circles or in front-rear wall opposite direction, the number of layers is an even number of 2 to 16, the number of clockwise tangential circles in the layers is equal to the number of counterclockwise tangential circles in the layers, and the height from the uppermost layer of the air nozzles (102) to the high temperature flue gas outlet (103) is 4 to 12 m.

10. The integrated fixed bed waste high efficiency gasification combustion furnace as set forth in claim 8, wherein the inner diameter D1 of the combustible gas combustion section (100) is 1-4 times the inner diameter D2 of the fixed bed gasification section (400).

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