CN1865775A - Composite circulating fluidized bed system for high performance clean burning of urban domestic garbage - Google Patents
Composite circulating fluidized bed system for high performance clean burning of urban domestic garbage Download PDFInfo
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- CN1865775A CN1865775A CN 200610042955 CN200610042955A CN1865775A CN 1865775 A CN1865775 A CN 1865775A CN 200610042955 CN200610042955 CN 200610042955 CN 200610042955 A CN200610042955 A CN 200610042955A CN 1865775 A CN1865775 A CN 1865775A
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- fluid bed
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- burner hearth
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Abstract
The invention relates to a compound cycle fluid bed system for burning the city life waste. Wherein, the furnace bottom of fluid bed has a slag outlet, and a taper wind plate; the middle of wall cool wall of furnace is a reducing water cool water; the upper part of reducing water cool water has a concave fuel cycle strengthen plate; secondary wind is arranged above said concave fuel cycle strengthen plate via four-angle tangent round burning; the most upper outlet of furnace has one high-temperature gas-solid separator while a material channel is under it; the most lower end of material channel has a feedback device; the lower end of material channel via tube is connected to the feedback port inside the furnace; the smoke channel is above the high-temperature gas-solid separator, while it is connected to the tail smoke channel; said tail smoke channel has a high-temperature over heater, a low-temperature over heater, a high-temperature coal reducer, a high-temperature air pre-heater, a low-temperature coal reducer, and a low-temperature air pre-heater. The invention has high burning efficiency.
Description
Technical field
The invention belongs to the environment-friendly highly efficient combustion system, particularly realize the NEW TYPE OF COMPOSITE circulating fluidized bed system with the burning of dilute-phase zone swirling eddy of the clean efficient burning of domestic waste.
Prior art
At present, the annual production of the domestic waste of China has reached about 1.5 hundred million tons, and cumulant is then more than 6,000,000,000 tons, and Chinese city rubbish will reach 3.7 hundred million tons during by 2010.According to existing 668 cities, the expert statistics whole nation, 2/3rds all in the encirclement of rubbish endless belt.At present, China's domestic waste year generation is increasing rapidly on the one hand, the method of our effective disposal of refuse is also few on the other hand, and technology of garbage disposal is also very backward, and the rubbish processing to be harmless rate that really meets National Environmental control criterion and construction criteria only has about 25%.And the long-term bulk deposition of rubbish, brought great harm to environment.
Waste incineration is to reduce combustible waste by high-temp combustion, and rubbish is become inert residue.Waste incineration is disposed has outstanding feature, and it is obvious promptly to subtract appearance decrement effect, generally subtracts and holds 80%～90%; Incapability is eliminated bacterium, virus, ammonia, organic waste gas up hill and dale, and can make pernicious gas and flue dust reach environmental requirement by purified treatment; Adaptive capacity is stronger, just has value more than the 3344kJ/kg as long as the calorific value of rubbish reaches; Save the place, operating cost is low.But also there are some shortcomings in waste incineration, as: one-time investment is big, and investment is long return period; Traditional incineration technology is difficult to guarantee the innoxious degree of burning disposal, also is difficult to adapt to house refuse causes calorific value in the house refuse, moisture because of season and climate change variation; And, if incineration technology is not advanced, the corollary equipment imperfection, the burning of house refuse is easy to generate serious secondary pollution, this pollution is mainly reflected in the discharging of tail gas after incineration, as pollutant severe overweights such as the flue dust in the discharging waste gas, oke exhaust blackness, carbon monoxide, sulfur dioxide, more alarming is De dioxins materials severe overweight in the incineration plant discharging waste gas.
At present, the main flow equipment of the large-scale domestic waste incineration of most countries is stoker fired grate formula incinerator and fluidized bed incinerator in the world.In general, the former is suitable for incinerating combustion value than higher house refuse, and efficiency of combustion is lower, steam production is low, involve great expense, the maintenance cost height; The latter is good to low-calorie rubbish adaptability, and efficiency of combustion is higher, but if adopt traditional fluidized combustion technology then to be easy to generate secondary pollution, main cause is that fire box temperature is low excessively, generally about 850 degrees centigrade, gas residence time is short, causes the generation as bioxin easily.
Summary of the invention
In order to overcome above-mentioned the deficiencies in the prior art part, the present invention proposes a kind of composite circulating fluidized bed system that is used for high performance clean burning of urban domestic garbage, is used to realize efficient, the clean incineration of domestic waste.
Technical scheme of the present invention is achieved in that and the present invention includes fluid bed burner hearth and furnace wall water-cooling wall, fluid bed burner hearth bottom is provided with slag-drip opening, the fluid bed burner hearth is provided with the taper air distribution plate in the bottom, furnace wall water-cooling wall middle part is the waisting water-cooling wall, waisting water-cooling wall top is provided with the concave shape fuel recycle and strengthens plate, above strengthening plate, the concave shape fuel recycle adopt the mode of corner tangential firing to arrange secondary wind, the High Temperature Gas solid separator is set the exit topmost at the fluid bed burner hearth, there is material channel High Temperature Gas solid separator below, material channel is provided with material returning device bottom, the lower end of material channel is communicated to feedback outlet in the fluid bed burner hearth by pipeline, there is exhaust gases passes High Temperature Gas solid separator top, exhaust gases passes is connected with back-end ductwork, sets gradually high temperature superheater in back-end ductwork from top to bottom, low temperature superheater, high-temperature economizer, high-temperature air preheater, low-level (stack-gas) economizer, low-temperature air preheater.
Be provided with the circulation of two briquette fuels at emulsion zone and strengthen plate, this plate is a concave shape, and its cross section is circular-arc, and two boards is symmetric arrangement in the horizontal direction.
The waisting water-cooling wall is that the base angle is 27-33 ° a isosceles triangle.
The taper air distribution plate is selected blast cap formula air distribution plate for use, at the intensive relatively blast cap of its edge placement, arranges sparse relatively blast cap therebetween, leaves the space between taper air distribution plate and the furnace wall water-cooling wall.
The present invention has the following advantages:
(1) the present invention strengthens plate, water-cooling wall waisting, taper air distribution plate three's comprehensive function by the concave shape fuel recycle, form interior circulation at emulsion zone, fuel forms the rising solid particle flows in the both sides of taper air distribution plate, strengthen under the effect of plate in the concave shape fuel recycle then, directly over taper air distribution plate centre position, form sinking, when the solid particle that descends falls back on the taper air distribution plate, a part is not fired particle and slide into slag notch under air distribution plate, circulation in another part continues to participate in; And at the same time, the solid particle that refluxes by the water-cooling wall waisting also participates in the interior circulation, has so just formed two materials circulations.
(2) can fully prolong the residing time in furnace of high-temperature flue gas and solid particle,, reduce the phosphorus content of flying dust, have more superior environmental-protecting performance keeping to significantly reduce the generation of bioxin under the situation of fire box temperature more than 850 ℃;
(3) because circulation on the basis of outer circulation, having set up effectively, and utilize the mode that is similar to corner tangential firing to make secondary wind form the high-temperature flue gas swirl flow combustion at dilute-phase zone, turbulivity increases in the stove, the high-temperature region time of staying prolongs, be very beneficial for the abundant after-flame of high-temperature flue gas and solids, therefore comparing traditional this system of circulating fluid bed garbage system has higher efficiency of combustion and heat transfer efficiency;
(4) design of combined-circulation prolongs the time of staying of rubbish in stove, and some firing-difficult matters are also burnt, thereby make this scheme wider to the adaptability of fuel; And, the C in emission, NOx, SO
2, the content of HCl and flue dust discharge capacity reduce on, kept the advantage of general recirculating fluidized bed CIU, reduce greatly than coal-powder boiler, have more the feature of environmental protection.
Description of drawings
Fig. 1 is a structural representation of the present invention.
Fig. 2 is the A-A sectional view.
The specific embodiment
With reference to Fig. 1, shown in 2, burner hearth 6 exterior bottom are provided with slag-drip opening 1, fluid bed burner hearth 6 inside bottom are provided with taper air distribution plate 2, the middle part is a waisting water-cooling wall 3, waisting water-cooling wall 3 tops are provided with the concave shape fuel recycle and strengthen plate 5, above strengthening plate 5, the concave shape fuel recycle adopt the mode of corner tangential firing to arrange overfiren air port 4, High Temperature Gas solid separator 7 is set the exit topmost at fluid bed burner hearth 6, High Temperature Gas solid separator 7 belows are material channel 16, material channel 16 is provided with material returning device 17 bottom, the lower end of material channel 16 is communicated to by pipeline and forms feedback outlet 18 in the fluid bed burner hearth 6, High Temperature Gas solid separator 7 tops are exhaust gases passes 8, exhaust gases passes 8 is connected with back-end ductwork 15, has set gradually high temperature superheater 9 in back-end ductwork 15 from top to bottom, low temperature superheater 10, high-temperature economizer 11, high-temperature air preheater 12, low-level (stack-gas) economizer 13, low-temperature air preheater 14.
Be provided with two concave shape fuel recycles at emulsion zone and strengthen plate 5, this plate is a concave shape, and its cross section is circular-arc, and two boards is symmetric arrangement in the horizontal direction.
Waisting water-cooling wall 3 is that the base angle is 27-33 ° a isosceles triangle.
Taper air distribution plate 2 is selected blast cap formula air distribution plate for use, at the intensive relatively blast cap of its edge placement, arranges sparse relatively blast cap therebetween, and leave the space between furnace wall water-cooling wall and taper air distribution plate 2.
Workflow: the garbage fuel burning produces high-temperature flue gas; Flue gas heats through fluid bed burner hearth 6 and to the working medium in the water-cooling wall, arrives 6 outlets of fluid bed burner hearth; By High Temperature Gas solid separator 7 being set in fluid bed burner hearth 6 exits, a large amount of high-temp solid materials is separated from air-flow, send the combustion chamber back to via material returning device 17 again,, guarantee that fuel and desulfurizing agent repeatedly circulate, burn repeatedly and react to keep the fast fluidized condition of combustion chamber; Remaining high-temperature flue gas then order is heated to superheat state through high temperature superheater 9, low temperature superheater 10 with working medium; Pass through high-temperature economizer 11, high-temperature air preheater 12, low-level (stack-gas) economizer 13, low-temperature air preheater 14 then in order, the final discharge.
Below in conjunction with accompanying drawing the present invention is described in further detail.
At first, arrange intensive relatively blast cap in the marginal portion of taper air distribution plate 2, and, air distribution plate is divided into emulsion zone and dilute-phase zone, and the blast cap ratio in two districts is located 1:8 at the sparse relatively blast cap of mid portion layout.Form the inhomogeneous cloth wind of taper air distribution plate 2.When work, the air-supply of blast cap is all from same ajutage on the taper air distribution plate 2, thereby guarantee that a wind that enters fluid bed burner hearth 6 has identical operating mode, help the stable of blast cap operating mode like this, also help the fluidization of solid particle in the fluid bed burner hearth 6.Under the stable situation of blowing, the solid particle in the burner hearth is in fluidized state, will pressure reduction occur on taper air distribution plate 2 both sides and middle top, and strengthen under the effect of plate 5 circulation in the formation in the concave shape fuel recycle.
Owing to consider that the internal circulating load of rubbish is much bigger than the internal circulating load of the fire coal under the same parameter, fuel is strengthened plate will be subjected to very serious wearing and tearing, therefore fuel is strengthened plate and carried out the piecemeal design: according to the abrasion condition of different parts, fuel is strengthened plate be divided into several sections, adopt different steel to make respectively, fit together at last.Fuel reinforcement plate is arranged to dismountable in burner hearth, helps reducing wearing and tearing and is convenient to again change.Strengthen under the effect of plate circulation in the emulsion zone of burner hearth has formed more effectively like this at fuel.
Considered that solid particle will glide along fluid bed burner hearth 6 water-cooling walls; so strengthen plate 5 in order to cooperate the concave shape fuel recycle; designed a waisting water-cooling wall 3; can be recovered to fluid bed burner hearth 6 emulsion zones with slide the solid particle that comes along water-cooling wall on the one hand, can also reduce 6 wind of fluid bed burner hearth are strengthened gap between plate 5 and the water-cooling wall in the concave shape fuel recycle inleakage on the other hand.Strengthen the comprehensive function of plate 5, waisting water-cooling wall 3 by fluid bed burner hearth 6, concave shape fuel recycle, form interior circulation at the emulsion zone of fluid bed burner hearth 6.After flue dust enters into dilute-phase zone, on four angles of the water-cooling wall of fluid bed burner hearth 6 front-back walls, secondary wind is similar to quadrangle tangential circle to be arranged, make flue dust form the screw type combustion position, can fully prolong the high-temperature flue gas and the time of staying of solid particle in stove like this, realize the efficient burning of fuel.This will be very beneficial for the after-flame of fuel, improves efficiency of combustion; Help the removal of dioxins materials and the inhibition of other pollutants, help environmental protection.
Claims (4)
1, a kind of New Cycle fluidized system that is used for burning city domestic garbage, comprise: fluid bed burner hearth (6) and furnace wall water-cooling wall, it is characterized in that, fluid bed burner hearth (6) bottom is provided with slag-drip opening (1), fluid bed burner hearth (6) is provided with taper air distribution plate (2) in the bottom, the middle part of furnace wall water-cooling wall is waisting water-cooling wall (3), waisting water-cooling wall (3) top is provided with the concave shape fuel recycle and strengthens plate (5), strengthening plate (5) top in the concave shape fuel recycle adopts the mode of corner tangential firing to arrange overfiren air port (4), High Temperature Gas solid separator (7) is set the exit topmost at fluid bed burner hearth (6), High Temperature Gas solid separator (7) below is material channel (16), material channel (16) is provided with material returning device (17) bottom, the lower end of material channel (16) is communicated to the interior feedback outlet (18) of fluid bed burner hearth (6) by pipeline, High Temperature Gas solid separator (7) top is exhaust gases passes (8), exhaust gases passes (8) is connected with back-end ductwork (15), is disposed with high temperature superheater (9) in back-end ductwork (15) from top to bottom, low temperature superheater (10), high-temperature economizer (11), high-temperature air preheater (12), low-level (stack-gas) economizer (13), low-temperature air preheater (14).
2, system according to claim 1 is characterized in that, plate (5) is strengthened in the concave shape fuel recycle two, and it is that the cross section of concave shape is circular-arc, and plates (5) symmetric arrangement is in the horizontal direction strengthened in two concave shape fuel recycles.
3, system according to claim 1 is characterized in that, water-cooling wall waisting (3) is that the base angle is 27-33 ° a isosceles triangle.
4, system according to claim 1, it is characterized in that taper air distribution plate (2) is selected blast cap formula air distribution plate for use, at the intensive relatively blast cap of its edge placement, arrange sparse relatively blast cap therebetween, leave the space between taper air distribution plate (2) and the furnace wall water-cooling wall.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006100429559A CN100441952C (en) | 2006-06-09 | 2006-06-09 | Composite circulating fluidized bed system for high performance clean burning of urban domestic garbage |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006100429559A CN100441952C (en) | 2006-06-09 | 2006-06-09 | Composite circulating fluidized bed system for high performance clean burning of urban domestic garbage |
Publications (2)
| Publication Number | Publication Date |
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| CN1865775A true CN1865775A (en) | 2006-11-22 |
| CN100441952C CN100441952C (en) | 2008-12-10 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2006100429559A Expired - Fee Related CN100441952C (en) | 2006-06-09 | 2006-06-09 | Composite circulating fluidized bed system for high performance clean burning of urban domestic garbage |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101846308A (en) * | 2010-06-13 | 2010-09-29 | 山西蓝天环保设备有限公司 | Circulating fluidized bed domestic waste incineration power generation boiler |
| CN103277782A (en) * | 2013-05-24 | 2013-09-04 | 太原锅炉集团有限公司 | Carbon black tail gas combusting boiler |
| CN111237745A (en) * | 2020-01-13 | 2020-06-05 | 洛阳建材建筑设计研究院有限公司 | Non-uniform air distribution fluidized bed and non-uniform air distribution fluidized bed boiling decomposition device |
| CN112432183A (en) * | 2020-10-23 | 2021-03-02 | 清华大学 | Waste incineration coupling boiler system |
Family Cites Families (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA1285375C (en) * | 1986-01-21 | 1991-07-02 | Takahiro Ohshita | Thermal reactor |
| CA1291322C (en) * | 1987-12-17 | 1991-10-29 | John V. Allen | Fluidized bed reactor with two zone combustion |
| CN2283188Y (en) * | 1996-09-24 | 1998-06-03 | 中国科学院工程热物理研究所 | circulating fluidized bed garbage incinerator |
| CN2377450Y (en) * | 1999-07-12 | 2000-05-10 | 中国科学院工程热物理研究所 | Vortex circulation fluidised bed refuse incinerator |
| CN2432452Y (en) * | 2000-05-10 | 2001-05-30 | 清华大学煤燃烧工程研究中心 | constant pressure combined recirculating fluidized bed garbage incinerator |
| CN2428695Y (en) * | 2000-05-25 | 2001-05-02 | 中国科学院工程热物理研究所 | Circulation fluidizing-bed garbage incineration furnace with novel external heat-exchanger |
| CN2494931Y (en) * | 2001-08-16 | 2002-06-12 | 江西锅炉化工石油机械联合有限责任公司 | Differential fluidized-bed boiler for incinerating waste |
| CN1696569A (en) * | 2004-05-12 | 2005-11-16 | 清华大学 | Boiler of circulating fluid bed for burning household garbage |
-
2006
- 2006-06-09 CN CNB2006100429559A patent/CN100441952C/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101846308A (en) * | 2010-06-13 | 2010-09-29 | 山西蓝天环保设备有限公司 | Circulating fluidized bed domestic waste incineration power generation boiler |
| CN101846308B (en) * | 2010-06-13 | 2012-01-25 | 山西蓝天环保设备有限公司 | Circulating fluidized bed domestic waste incineration power generation boiler |
| CN103277782A (en) * | 2013-05-24 | 2013-09-04 | 太原锅炉集团有限公司 | Carbon black tail gas combusting boiler |
| CN111237745A (en) * | 2020-01-13 | 2020-06-05 | 洛阳建材建筑设计研究院有限公司 | Non-uniform air distribution fluidized bed and non-uniform air distribution fluidized bed boiling decomposition device |
| CN112432183A (en) * | 2020-10-23 | 2021-03-02 | 清华大学 | Waste incineration coupling boiler system |
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| Publication number | Publication date |
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| CN100441952C (en) | 2008-12-10 |
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Granted publication date: 20081210 Termination date: 20110609 |