CN203549845U - Grate-fired furnace co-processing dangerous waste burning system - Google Patents
Grate-fired furnace co-processing dangerous waste burning system Download PDFInfo
- Publication number
- CN203549845U CN203549845U CN201320651739.XU CN201320651739U CN203549845U CN 203549845 U CN203549845 U CN 203549845U CN 201320651739 U CN201320651739 U CN 201320651739U CN 203549845 U CN203549845 U CN 203549845U
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- Prior art keywords
- hazardous waste
- solid
- liquid
- grate
- dangerous waste
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- 239000002699 waste material Substances 0.000 title abstract description 12
- 239000007788 liquid Substances 0.000 claims abstract description 47
- 239000007787 solid Substances 0.000 claims abstract description 17
- 238000001816 cooling Methods 0.000 claims abstract description 13
- 239000007921 spray Substances 0.000 claims abstract description 8
- 239000002920 hazardous waste Substances 0.000 claims description 72
- 239000000203 mixture Substances 0.000 claims description 4
- 239000003245 coal Substances 0.000 abstract description 7
- 230000007613 environmental effect Effects 0.000 abstract description 2
- 238000007599 discharging Methods 0.000 abstract 1
- 239000002893 slag Substances 0.000 abstract 1
- 238000005516 engineering process Methods 0.000 description 6
- 239000002803 fossil fuel Substances 0.000 description 5
- 238000002485 combustion reaction Methods 0.000 description 4
- 238000004064 recycling Methods 0.000 description 4
- 239000002910 solid waste Substances 0.000 description 4
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 3
- 239000003546 flue gas Substances 0.000 description 3
- 239000000446 fuel Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000003818 cinder Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 239000005431 greenhouse gas Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000013316 zoning Methods 0.000 description 1
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Abstract
The utility model discloses a grate-fired furnace co-processing dangerous waste burning system. A water-cooling wall is arranged on the upper part of a hearth, the upper end of the hearth is provided with a steam pocket, the steam pocket is connected with the water-cooling wall, the upper part of the hearth is connected with a burn-out chamber, a fire grate is arranged below the hearth, the front end of the fire grate is provided with a front arch, the rear end of the fire grate is provided with a rear arch, the top and the bottom of the front arch are respectively provided with a liquid feeding hole and a solid feeding hole, a multilevel primary air chamber is arranged below the fire grate, two sides of the hearth are respectively provided with secondary wind gaps which are arranged on the upper part of the liquid feeding hole, and the tail part of the fire grate is provided with a slag discharging device; a liquid dangerous waste tank, a liquid dangerous waste pump, a liquid dangerous waste spray gun and the liquid feeding hole are sequentially connected with one another, a solid dangerous waste feeder and a coal feeder are respectively connected with the solid feeding hole through a closed-type mixed feeder, and the solid dangerous waste feeder is connected with a solid dangerous waste cabin. The existing grate-fired furnace is effectively used for burning dangerous waste, so that the storage expense and environmental risk caused by the fact that the dangerous waste cannot be treated in time can be reduced.
Description
Technical field
The utility model relates to the grate furnace incineration disposal technology of discarded object, relates in particular to a kind of grate furnace coexistence and puts hazardous waste burn system.
Background technology
According to the statistics of national environmental protection portion; within 2010, national industrial solid wastes generation is 240943.5 ten thousand tons; wherein hazardous waste generation is 1586.8 ten thousand tons, and volume of comprehensive utilization (containing utilizing storage capacity in former years), storage capacity, disposal amount are respectively 976.8 ten thousand tons, 166.3 ten thousand tons, 512.7 ten thousand tons.Can find out, along with the rapid growth of China's economy, the generation of industrial waste and hazardous waste is constantly soaring, and corresponding disposal facility can not meet demand far away.
Dangerous waste disposal method is various, wherein, utilizes Industrial Boiler to carry out hazardous waste and the common method of burning of design fuel, not only can make hazardous waste minimizing and innoxious, and can at utmost recycle the energy of hazardous waste.Hazardous waste and the common burning of design fuel (coal) can part substitute fossil fuels, reduced the consumption to fossil fuel, reduce the discharge of greenhouse gases and atmosphere pollution.Although rise the seventies in last century, European and American developed countries just start research and the application of the common disposal technology of being devoted to Industrial Stoves, in the production practices of decades, this technology is disposed and has been brought into play great function for the processing of hazardous waste, but the coexistence of the hazardous waste of China is put incineration technology still in the starting stage.The advantages such as industrial boilers in China is take grate furnace as main, and it is wide that grate furnace has fuel tolerance, easy to operate, and security reliability is high, and load adaptability is strong, its furnace high-temperature environment for incineration disposal hazardous waste provide may.Therefore design the incinerator that a kind of rational grate furnace coexistence puts hazardous waste necessary.
Summary of the invention
The purpose of this utility model be overcome grate furnace incinerator can only combustion of fossil fuels (as coal) and the deficiency of solid waste (as house refuse), provide a kind of grate furnace coexistence to put hazardous waste burn system.
Grate furnace coexistence is put hazardous waste burn system and is comprised grate furnace incinerator and feed system; Grate furnace incinerator comprises fire grate, a multistage air compartment, face arch, rear arch, slag-draining device, burner hearth, secondary furnace, drum, water-cooling wall, feeding-in solid body mouth, liquid inlet opening and overfiren air port; Upper furnace furnace wall is furnished with water-cooling wall, burner hearth upper end is provided with drum, and drum is connected with water-cooling wall, and upper furnace is connected with secondary furnace, burner hearth below is provided with fire grate, fire grate front end is provided with face arch, and fire grate rear end is provided with rear arch, and face arch is respectively equipped with liquid inlet opening, feeding-in solid body mouth up and down, fire grate below is provided with a multistage air compartment, burner hearth both sides are provided with overfiren air port, and are positioned at liquid inlet opening top, and fire grate afterbody is provided with slag-draining device; Feed system comprises that liquid hazardous waste tank, liquid hazardous waste mix batcher to pump, liquid hazardous waste spray gun, solid-state hazardous waste feed bin, solid-state hazardous waste batcher, feeder, closed; Liquid hazardous waste tank, liquid hazardous waste are connected in turn to pump, liquid hazardous waste spray gun, liquid inlet opening, solid-state hazardous waste batcher mixes batcher by closed respectively with feeder and is connected with feeding-in solid body mouth, and solid-state hazardous waste batcher is connected with solid-state hazardous waste feed bin.
The utility model has been realized the liquid and solid-state hazardous waste grate furnace incinerator of charging respectively, having solved grate furnace incinerator can only combustion of fossil fuels (as coal) and the problem of solid waste (as house refuse), realized the innoxious and energy recycling of hazardous waste, liquid hazardous waste feed arrangement and solid-state hazardous waste feed arrangement can be distinguished isolated operation, the liquid hazardous waste of low heat value cannot also can move during independent burning simultaneously, both guaranteed the grate furnace stable operation of putting hazardous waste burn system of coexisting, also guaranteed the instant incineration disposal of solid-state and liquid hazardous waste.
Accompanying drawing explanation
Fig. 1 is that hazardous waste burn system structural representation is put in grate furnace coexistence;
In figure, fire grate 1, a multistage air compartment 2, face arch 3, rear arch 4, slag-draining device 5, burner hearth 6, secondary furnace 7, drum 8, water-cooling wall 9, feeding-in solid body mouth 10, liquid inlet opening 11, overfiren air port 12, liquid hazardous waste tank 13, liquid hazardous waste mix batcher 19 to pump 14, liquid hazardous waste spray gun 15, solid-state hazardous waste feed bin 16, solid-state hazardous waste batcher 17, feeder 18, closed.
The specific embodiment
As shown in Figure 1, grate furnace coexistence is put hazardous waste burn system and is comprised grate furnace incinerator body and feed system; Grate furnace incinerator comprises fire grate 1, a multistage air compartment 2, face arch 3, rear arch 4, slag-draining device 5, burner hearth 6, secondary furnace 7, drum 8, water-cooling wall 9, feeding-in solid body mouth 10, liquid inlet opening 11 and overfiren air port 12; Burner hearth 6 top furnace walls are furnished with water-cooling wall 9, burner hearth 6 upper ends are provided with drum 8, and drum 8 is connected with water-cooling wall 9, and burner hearth 6 tops are connected with secondary furnace 7, burner hearth 6 belows are provided with fire grate 1, fire grate 1 front end is provided with face arch 3, and fire grate 1 rear end is provided with rear arch 4, and face arch 3 is respectively equipped with liquid inlet opening 11, feeding-in solid body mouth 10 up and down, fire grate 1 below is provided with a multistage air compartment 2, burner hearth 6 both sides are provided with overfiren air port 12, and are positioned at liquid inlet opening 11 tops, and fire grate 1 afterbody is provided with slag-draining device 5; Feed system comprises that liquid hazardous waste tank 13, liquid hazardous waste mix batcher 19 to pump 14, liquid hazardous waste spray gun 15, solid-state hazardous waste feed bin 16, solid-state hazardous waste batcher 17, feeder 18, closed; Liquid hazardous waste tank 13, liquid hazardous waste are connected in turn to pump 14, liquid hazardous waste spray gun 15, liquid inlet opening 11, solid-state hazardous waste batcher 17 mixes batcher 19 by closed respectively with feeder 18 and is connected with feeding-in solid body mouth 10, and solid-state hazardous waste batcher 17 is connected with solid-state hazardous waste feed bin 16.
The incinerating method that multi phase state hazardous waste is put in grate furnace coexistence is: liquid hazardous waste enters burner hearth 6 by feeding-in solid body mouth 10 with the delivery rate in 70-150 ton/sky by liquid inlet opening 11, solid-state hazardous waste and bunker coal, by the interior high-temperature flue gas of burner hearth 6, hazardous waste is dried and is lighted; Adopt one time wind air zoning, the forward and backward wall paper of Secondary Air is put, and according to mixing the ratio adjustment secondary air flow that burns hazardous waste, secondary air flow is controlled at the 8%-15% of total blast volume; Solid dangerous waste and bunker coal burn on fire grate 1, and the flue gas of generation upwards flows, and the throat by face arch 3 and rear arch 4, to burner hearth 6 tops, enters secondary furnace 7, guarantee that flue gas is greater than 2s in the interior time of staying of burner hearth 6; In combustion process, burner hearth 6 temperature remain on more than 850 ℃, and heat is by absorbing recycling take water-cooling wall 9 as main heating surface, and on fire grate 1, the hazardous waste residue of after-flame and cinder fall into slag-draining device 5; The sufficiently long time of staying and hot environment make the abundant burning of hazardous waste, realize the innoxious and energy of hazardous waste recycling.
Therefore, the grate furnace incineration technology that the utility model provides, the grate furnace of having realized liquid and solid-state hazardous waste burns, having solved grate furnace incinerator can only combustion of fossil fuels (as coal) and the problem of solid waste (as house refuse), has realized the innoxious and energy recycling of hazardous waste.
Claims (1)
1. a hazardous waste burn system is put in grate furnace coexistence, it is characterized in that comprising grate furnace incinerator and feed system, grate furnace incinerator comprises fire grate (1), a multistage air compartment (2), face arch (3), rear arch (4), slag-draining device (5), burner hearth (6), secondary furnace (7), drum (8), water-cooling wall (9), feeding-in solid body mouth (10), liquid inlet opening (11) and overfiren air port (12), burner hearth (6) top furnace wall is furnished with water-cooling wall (9), burner hearth (6) upper end is provided with drum (8), drum (8) is connected with water-cooling wall (9), burner hearth (6) top is connected with secondary furnace (7), burner hearth (6) below is provided with fire grate (1), fire grate (1) front end is provided with face arch (3), fire grate (1) rear end is provided with rear arch (4), face arch (3) is respectively equipped with liquid inlet opening (11) up and down, feeding-in solid body mouth (10), fire grate (1) below is provided with a multistage air compartment (2), burner hearth (6) both sides are provided with overfiren air port (12), and be positioned at liquid inlet opening (11) top, fire grate (1) afterbody is provided with slag-draining device (5), feed system comprises that liquid hazardous waste tank (13), liquid hazardous waste mix batcher (19) to pump (14), liquid hazardous waste spray gun (15), solid-state hazardous waste feed bin (16), solid-state hazardous waste batcher (17), feeder (18), closed, liquid hazardous waste tank (13), liquid hazardous waste are connected in turn to pump (14), liquid hazardous waste spray gun (15), liquid inlet opening (11), solid-state hazardous waste batcher (17) mixes batcher (19) by closed respectively with feeder (18) and is connected with feeding-in solid body mouth (10), and solid-state hazardous waste batcher (17) is connected with solid-state hazardous waste feed bin (16).
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CN201320651739.XU CN203549845U (en) | 2013-10-22 | 2013-10-22 | Grate-fired furnace co-processing dangerous waste burning system |
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CN201320651739.XU CN203549845U (en) | 2013-10-22 | 2013-10-22 | Grate-fired furnace co-processing dangerous waste burning system |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103604126A (en) * | 2013-10-22 | 2014-02-26 | 浙江大学 | Common treatment hazardous waste combustion system of grate-fired furnace and method thereof |
CN106801877A (en) * | 2017-01-04 | 2017-06-06 | 浙江大学 | Hazardous waste burn system and its method are put in a kind of room burner coexistence |
CN106838910A (en) * | 2017-02-14 | 2017-06-13 | 西安山岳环保科技有限公司 | One kind useless solid and liquid waste incineration and exhaust heat recovering method |
CN107420904A (en) * | 2016-12-26 | 2017-12-01 | 浙江春晖环保能源股份有限公司 | Garbage burning system |
-
2013
- 2013-10-22 CN CN201320651739.XU patent/CN203549845U/en not_active Expired - Lifetime
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103604126A (en) * | 2013-10-22 | 2014-02-26 | 浙江大学 | Common treatment hazardous waste combustion system of grate-fired furnace and method thereof |
CN103604126B (en) * | 2013-10-22 | 2016-03-02 | 浙江大学 | Hazardous waste burn system and method thereof are put in grate furnace coexistence |
CN107420904A (en) * | 2016-12-26 | 2017-12-01 | 浙江春晖环保能源股份有限公司 | Garbage burning system |
CN107420904B (en) * | 2016-12-26 | 2019-01-25 | 浙江春晖环保能源股份有限公司 | Garbage burning system |
CN106801877A (en) * | 2017-01-04 | 2017-06-06 | 浙江大学 | Hazardous waste burn system and its method are put in a kind of room burner coexistence |
CN106838910A (en) * | 2017-02-14 | 2017-06-13 | 西安山岳环保科技有限公司 | One kind useless solid and liquid waste incineration and exhaust heat recovering method |
CN106838910B (en) * | 2017-02-14 | 2019-08-27 | 西安山岳环保科技有限公司 | The useless solid and liquid waste incineration of one kind and exhaust heat recovering method |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
AV01 | Patent right actively abandoned |
Granted publication date: 20140416 Effective date of abandoning: 20160302 |
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C25 | Abandonment of patent right or utility model to avoid double patenting |