1. The utility model provides a high-parameter msw incineration boiler of large capacity high load, including furnace (200), grate system (100) that is located furnace (200) below, the cigarette wind system that is linked together with furnace (200), feed inlet (400) that is linked together with furnace (200) and lime-ash export (500) that is linked together with furnace (200), lime-ash export (500) are used for the discharge of lime-ash after the rubbish burning, a serial communication port, grate system (100) include independent be used for carrying out drying pyrolysis to rubbish drying section (110), be used for burning rubbish drying section (110) and be used for burning out the burn out section (130) of rubbish, drying section (110), burning section (120) and burn out section (130) slope are arranged and are connected in proper order, provide the primary air that the required as the oxidant of combustion process by cigarette wind system, primary air is through independent drying section primary air entry (111), The combustion section primary air inlet (121) and the burnout section primary air inlet (131) adopt different control strategies to be respectively sent into the drying section (110), the combustion section (120) and the burnout section (130), and the primary air sent into the drying section (110), the combustion section (120) and the burnout section (130) is different oxidants, wherein: the oxidant which is sent into the drying section (110) through the drying section primary air inlet (111) is mixed gas of high-temperature circulating flue gas from a flue gas air system and externally input primary air preheated by an air preheater; the oxidant which is fed into the combustion section (120) through the combustion section primary air inlet (121) is oxygen-enriched oxidant which is input externally; the oxidant fed into the burnout section (130) via the burnout section primary air inlet (131) is externally input primary air preheated by an air preheater.

2. The large-capacity high-load high-parameter waste incineration boiler according to claim 1, wherein the concentration of oxygen in the mixed gas is 10% -15%, the range of the high-temperature circulating flue gas from a flue gas and air system is 450 ℃ -650 ℃, the source selects the flue position without a high-temperature heating surface in the flue gas and air system, and a circulating flue gas fan selected for conveying the high-temperature circulating flue gas adopts a variable frequency design to adjust the flow and speed of the high-temperature circulating flue gas; the oxygen-enriched oxidant is sourced from high-temperature air at the outlet of the air preheater and high-concentration oxygen, the concentration of the oxygen is 25-35%, and the temperature range is 150-350 ℃.

3. A large capacity high load high parameter waste incineration boiler as in claim 2, characterized in that the wind rate of the primary wind passing through the drying section primary wind inlet (111) is in the range of 25% -35%; the air rate range of the primary air passing through the primary air inlet (121) of the combustion section is 55-75%; the air rate range of the primary air passing through the primary air inlet (131) of the burnout section is 5% -10%.

4. A large capacity high load high parameter waste incineration boiler according to claim 1, characterised in that the temperature of the flue gas above the drying section (110) and the burnout section (130) is in the range 900 ℃ to 1100 ℃, and the temperature of the flue gas above the combustion section (120) is controlled in the range 1200 ℃ to 1400 ℃.

5. A large capacity high load high parameter waste incineration boiler as in claim 1, characterized in that said furnace (200) comprises a front arch wall (201), a rear arch wall (202) and side walls (203) surrounded by membrane water walls, the inner sides of the water walls being coated with refractory material; the front arch wall (201) is positioned above the drying section (110) and is used for reflecting heat released by garbage combustion to a material layer on the drying section (110) and guiding smoke below the front arch wall (201) in the hearth (200) to flow into a flue (303) of the smoke and air system; the rear arch wall (202) is positioned above the combustion section (120) and the burnout section (130) and is used for reflecting heat released by garbage combustion to a material layer on the combustion section (120) and the burnout section (130), and the rear arch wall (202) is used for guiding smoke below the rear arch wall (202) in the hearth (200) to flow into a flue (303) of the smoke and air system; the side wall (203) is positioned above the grate system (100), and the side wall (203), the front arch wall (201) and the rear arch wall (202) jointly form a combustion and heat exchange space of the hearth (200).

6. A high capacity, high load, high parameter waste incineration boiler as in claim 5, characterized in that said front arch wall (201), said rear arch wall (202) and said side walls (203) are all in the form of water cooled walls, no air cooled walls are provided, and the fire facing surfaces are made of SiC type refractory.

7. A large capacity high load high parameter waste incineration boiler as in claim 5, characterized by, that said flue gas system further comprises a secondary air nozzle for providing secondary air (302) used as over-fire air, the source of secondary air (302) is air, the secondary air nozzle is located at the outlet of said furnace (200) and at the upper region of said furnace (200), the secondary air nozzle is arranged in N layers, N is more than or equal to 3; the secondary air nozzles of the bottom layer are arranged on the front arch wall (201) and the rear arch wall (202), and the secondary air nozzles of other layers except the bottom layer are arranged on a vertical flue (303) of the smoke and air system.

8. The large-capacity high-load high-parameter waste incineration boiler according to claim 7, wherein CaO powder (308) enters the hearth (200) through the secondary air nozzles arranged on the front arch wall (201) and the rear arch wall (202), and the CaO powder (308) enters the hearth (200) under the entrainment of gravity and fluid and reacts with acid gases in flue gas; the secondary air nozzles arranged on the front arch wall (201) and the rear arch wall (202) are uniformly arranged in a plurality of rows in the width direction.

9. A high capacity, high load and high parameter waste incineration boiler according to claim 6, characterized in that the flue (303) is located right above the combustion section (120), the central axis of the flue (303) is located above the combustion zone in the furnace (200), the vertical projection thereof completely covers the combustion section (120), and the vertical projection covers 1/4 larger than the sum of the areas of the drying section (110) and the burnout section (130).

10. A high capacity high load high parameter waste incineration boiler as in claim 6, characterized by, that said flue (303) is in the form of a full water wall, surrounded by membrane walls, connected to the water wall outlets of said front arch wall (201), said rear arch wall (202) and said side walls (203) in the form of a header; the fire facing side of the flue (303) is laid by SiC type refractory materials;

the ash outlet (500) is connected with the front arch wall (201), the rear arch wall (202) and the side wall (203).

Background

With the development of society and economy, the method of landfill and composting for treating municipal domestic waste cannot meet the requirement of waste treatment capacity. The urban domestic garbage incineration power generation technology recovers heat in high-temperature flue gas after garbage incineration and converts the heat into electric energy. The technology can realize the reduction, harmlessness and reclamation of garbage treatment, obtain the dual benefits of economy and environment, and belongs to the clean and renewable power generation technology. However, due to the common low heat value of domestic garbage, the large amount of corrosive gas contained in the flue gas after combustion and the like, the main steam parameters of the existing garbage generator set are mostly lower than 6.5MPa/450 ℃, the garbage treatment capacity is less than 1000t/d, the heat generated in a hearth is not enough to support the improvement of steam-water system parameters, and the method is a key factor causing that the garbage power generation technology is difficult to achieve large capacity, high parameters and high load all the time. In addition, the diversity of garbage components and heat values has obvious influence on the operation of the boiler. Along with the improvement of unit parameters and capacity, the challenge of the diversity of garbage components and heat values on the safe operation of equipment is more severe, so that a garbage incineration boiler which is stable in combustion and has flexible and effective adjusting means is required. In addition, pollutant emission has been a concern of waste incineration plants, and the control of dioxin is more difficult and important. The current theory considers that the main sources of dioxin in flue gas are waste components, the formation in a hearth and the low-temperature resynthesis outside the hearth. Dioxin and precursors are generated in large quantities due to poor combustion conditions in the hearth, low oxygen concentration, low hearth temperature, and the like. The 3T principle proposed by the existing garbage incinerator can inhibit and reduce the emission of dioxin to a great extent. Reasonable furnace structure and combustion process control are economical and effective measures for controlling the emission of the pollutants from the source.

Disclosure of Invention

The purpose of the invention is: provides a high-load high-parameter incineration boiler with large capacity, flexibility and adjustability.

In order to achieve the aim, the technical scheme of the invention is to provide a large-capacity high-load high-parameter waste incineration boiler which comprises a hearth, a grate system positioned below the hearth, a smoke air system communicated with the hearth, a feeding hole communicated with the hearth and an ash residue outlet communicated with the hearth, wherein the ash residue outlet is used for discharging ash residues after waste combustion The primary air of the combustion section and the burnout section, which is sent into the drying section, the combustion section and the burnout section, is different oxidants, wherein: the oxidant fed into the drying section through the primary air inlet of the drying section is a mixed gas of high-temperature circulating flue gas from a flue gas system and externally input primary air preheated by an air preheater; the oxidant fed into the combustion section through the primary air inlet of the combustion section is oxygen-enriched oxidant input from the outside; the oxidant fed into the burnout section via the burnout section primary air inlet is externally input primary air preheated by an air preheater.

Preferably, the concentration of oxygen in the mixed gas is 10% -15%, the range of the high-temperature circulating flue gas from a flue gas and air system is 450 ℃ -650 ℃, the source selects the flue position without a high-temperature heating surface in the flue gas and air system, and a circulating flue gas fan selected for conveying the high-temperature circulating flue gas adopts a variable frequency design to adjust the flow and speed of the high-temperature circulating flue gas; the oxygen-enriched oxidant is sourced from high-temperature air at the outlet of the air preheater and high-concentration oxygen, the concentration of the oxygen is 25-35%, and the temperature range is 150-350 ℃.

Preferably, the air rate of the primary air passing through the primary air inlet of the drying section is 25% -35%; the air rate range of the primary air passing through the primary air inlet of the combustion section is 55-75%; the air rate range of the primary air passing through the primary air inlet of the burnout section is 5% -10%.

Preferably, the temperature interval of the flue gas above the drying section and the burnout section is 900-1100 ℃, and the temperature of the flue gas above the combustion section is controlled at 1200-1400 ℃.

Preferably, the hearth comprises a front arch wall, a rear arch wall and side walls which are enclosed by membrane type water-cooled walls, and the inner sides of the water-cooled walls are coated with refractory materials; the front arch wall is positioned above the drying section and used for reflecting heat released by garbage combustion to a material layer on the drying section and guiding smoke below the front arch wall in the hearth to flow into a flue of the smoke and air system; the rear arch wall is positioned above the combustion section and the burnout section and used for reflecting heat released by garbage combustion to a material layer on the combustion section and the burnout section, and the rear arch wall is used for guiding smoke below the rear arch wall in the hearth to flow into a flue of the smoke and air system; the side wall is positioned above the fire grate system, and the side wall, the front arch wall and the rear arch wall jointly form a combustion and heat exchange space of the hearth.

Preferably, the front arch wall, the rear arch wall and the side walls are all in the form of water-cooled walls, no air-cooled wall is arranged, and the fire facing surfaces of the front arch wall, the rear arch wall and the side walls are laid by SiC type refractory materials.

Preferably, the flue gas and air system further comprises a secondary air nozzle for providing secondary air used as over-fire air, the secondary air is sourced from air, the secondary air nozzle is positioned at the outlet of the hearth and at the upper area of the hearth, the secondary air nozzle is arranged in N layers, and N is more than or equal to 3; the secondary air nozzles at the bottom layer are arranged on the front arch wall and the rear arch wall, and the secondary air nozzles at other layers except the bottom layer are arranged on the vertical flue of the smoke and air system.

Preferably, CaO powder enters the hearth through the secondary air nozzles arranged on the front arch wall and the rear arch wall, and enters the hearth under the gravity and the fluid entrainment, and reacts with acid gas in the flue gas; the secondary air nozzles arranged on the front arch wall and the rear arch wall are uniformly arranged in a plurality of rows along the width direction.

Preferably, the flue is positioned right above the combustion section, the central axis of the flue is positioned above the combustion area in the hearth, the projection of the central axis of the flue in the vertical direction completely covers the combustion section, and the coverage area of the vertical projection is greater than 1/4 of the sum of the areas of the drying section and the burnout section.

Preferably, the flue is in a form of a full water-cooled wall, is surrounded by membrane water-cooled walls, and is connected with the front arch wall, the rear arch wall and the water-cooled wall outlets of the side walls in a form of a header; the fire facing side of the flue is laid by SiC type refractory materials;

the ash residue outlet is connected with the front arch wall, the rear arch wall and the side wall.

The invention adopts different control strategies in three stages of drying pyrolysis, combustion and burnout in the waste incineration process so as to achieve the purposes of large capacity, high load, high parameter, flexibility and adjustability. In the garbage drying and pyrolyzing section, the drying and pyrolyzing of the garbage are accelerated by adopting high-temperature circulating flue gas and flue gas thermal radiation; in the combustion section, the invention adopts oxygen-enriched air to improve the combustion reaction degree, strengthen the combustion process and increase the volume heat load in the hearth; in the burnout section, the reasonable proportion of the primary air and the secondary air is adopted to improve the burnout rate of the fuel and reduce the thermal ignition loss rate in ash slag. The invention improves the garbage treatment capacity and the volume heat load in the hearth by controlling the combustion process so as to realize the high-load high-parameter, flexible and controllable safe operation of the garbage incineration boiler.

Compared with the prior art, the invention has the following beneficial effects:

1. the waste incineration boiler with high load and high parameters has the advantages of large waste treatment capacity, high system thermal efficiency and low dioxin emission.

2. The drying, burning and burnout stages of the fire grate adopt independent control strategies, different stages adopt different oxidant combinations, the temperature and flow of the oxidant are adjusted according to the heat value of the fuel, the inlet flue gas parameters entering the high-temperature flue gas filtering equipment are effectively adjusted and controlled, and the adaptability of the unit to large load change, unstable burning and fuel diversity is improved.

3. The improvement of the heat capacity of the hearth and the heat load per unit volume provides possibility for adopting high parameters for a subsequent evaporation system.

Drawings

FIG. 1 is a schematic view of a high load high parameter waste incineration boiler;

FIG. 2 is a schematic top view of a high load high parameter waste incineration boiler furnace;

fig. 3 is a schematic diagram of a secondary air jet arrangement.

In the figure, 100-grate system, 200-hearth, 400-feed inlet, 500-ash outlet, 110-drying section, 120-combustion section, 130-burnout section, 111-drying section primary air inlet, 121-combustion section primary air inlet, 131-burnout section primary air inlet, 201-front arch wall, 202-rear arch wall, 203-side wall, 301-primary air, 302-secondary air, 303-flue, 304-flue outlet, 306-gas mixer, 307-secondary air nozzle and 308-CaO powder.

Detailed Description

The invention will be further illustrated with reference to the following specific examples. It should be understood that these examples are for illustrative purposes only and are not intended to limit the scope of the present invention. Further, it should be understood that various changes or modifications of the present invention may be made by those skilled in the art after reading the teaching of the present invention, and such equivalents may fall within the scope of the present invention as defined in the appended claims.

Referring to fig. 1, the waste incineration boiler with high capacity, high load and high parameters provided by the invention comprises a fire grate system 100, a hearth 200, a smoke and air system, a feeding hole 400 and an ash outlet 500. The household garbage enters the hearth 200 through the feeding hole 400, and the garbage is dried and pyrolyzed on the drying section 110 of the grate system 100 through the movement of the pusher and the grate system 100. With the completion of the dry pyrolysis, the waste enters the combustion section 120 for a combustion reaction. When the combustion process is completed, the fuel enters the burnout section 130 under the operation of the grate system 100, thereby increasing the burnout of the fuel. And finally out of the furnace 200 through an ash outlet 500. The hearth 200 and the flue 303 of the smoke and air system are both surrounded by a water wall structure. The flue inlet of the flue 303 is connected with the flue gas outlet of the hearth 200, and the inner wall of the flue is coated with refractory materials to ensure the safety of the water-cooled wall.

The whole combustion process of the household garbage is divided into three independent processes of drying pyrolysis, combustion and burnout, and different oxidants and control strategies are adopted respectively. Oxidant primary air required by the combustion process enters the drying section 110, the combustion section 120 and the burnout section 130 of the fire grate through a drying section primary air inlet 111, a combustion section primary air inlet 121 and a burnout section primary air inlet 131 which are arranged on the slag leakage hopper. Wherein, in order to improve the garbage drying process of the drying section 110, the drying section 110 adopts the combined action of high-temperature circulating flue gas and front arch wall radiation heat exchange. High temperature flue gas recirculation can also increase the average temperature in the furnace 200, prevent stagnant areas of flow, increase the heat load in the furnace 200. The primary air of the oxidant fed into the drying section 110 through the primary air inlet 111 of the drying section is derived from a high-temperature circulating flue gas and a primary air mixed gas from an air preheater, the concentration of oxygen in the primary air mixed gas is 10% -15%, the range of the high-temperature flue gas is 450 ℃ -650 ℃, and the range of the air rate is 25% -35%. The main process of combustion takes place in the combustion section 120, the primary air of oxidant fed into the combustion section 120 through the primary air inlet 121 of the combustion section is oxygen-enriched oxidant, the concentration of oxygen in the oxygen-enriched oxidant is 25% -35%, the temperature range is 150-350 ℃, and the air rate range is 55% -75%. The combustion intensity of the combustion area is improved by improving the oxygen concentration in the oxygen-enriched oxidant, and the temperature of the flue gas after combustion is improved. Oxygen-enriched airThe combustion can be obviously enhanced, and the central temperature of a combustion area is improved. The burned garbage moves to the burnout section 130 under the action of the grate system 100, the heat in the ash is recovered through the primary air of the oxidant fed through the primary air inlet 131 of the burnout section, the air rate ranges from 5% to 10%, and the burnout rate is improved by prolonging the residence time, so that the thermal ignition reduction rate of the ash is reduced. The primary oxidant air fed through the burnout section primary air inlet 131 is conventional high-temperature primary air from an air preheater, and the flue gas temperature is 180-250 ℃. By controlling the circulating flue gas volume and the oxygen concentration in the oxygen-enriched combustion, the problem of large temperature fluctuation of a flue gas outlet caused by the change of a garbage heat value can be solved. Meanwhile, the increase of the oxygen concentration in the combustion section can strengthen the combustion process, improve the temperature of the combustion center and reduce the generation of hydrocarbon (C) caused by insufficient oxygen, insufficient mixing or low temperature_mH_n) The dioxin and the water are completely decomposed into carbon dioxide and water, and the combination of the carbon dioxide and the chloride in the garbage is reduced to form the dioxin or the precursor thereof, so that the aim of controlling the generation of the dioxin in the combustion process is fulfilled.

Besides using the high-temperature circulating flue gas and the oxygen concentration to control the combustion temperature in the center of the hearth 200, the temperature of a flue gas outlet can be controlled by the secondary air flow, and the burnout rate is improved.

CaO powder 308 enters the hearth 200 through bottom layer secondary air nozzles 307 arranged on the front arch and the rear arch, enters the hearth region of the hearth 200 to form a W-shaped motion track, and enters the subsequent flow from the flue outlet 304. The addition of the CaO powder 308 can control the content of acid gases in the flue gas in the combustion process, and prevent the water-cooled wall and the subsequent high-temperature heating surface from being corroded by the acid gases. The method provides possibility for subsequently arranging high-temperature heating surfaces such as a superheater and a reheater and improving steam parameters of the system.

The circulating flue gas fan adopted by the circulating flue gas system adopts a variable frequency design, and the flow and the speed of the circulating flue gas can be adjusted.