CN205026683U - Burn burning furnace heat transfer system - Google Patents
Burn burning furnace heat transfer system Download PDFInfo
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- CN205026683U CN205026683U CN201520651412.1U CN201520651412U CN205026683U CN 205026683 U CN205026683 U CN 205026683U CN 201520651412 U CN201520651412 U CN 201520651412U CN 205026683 U CN205026683 U CN 205026683U
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- incinerator
- heat exchanger
- chimney
- spray
- air heat
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Abstract
The utility model relates to a burn burning furnace heat transfer system burns burning furnace and is connected with air heat exchanger, and air heat exchanger is connected with the dust remover, and the dust remover is connected with the spray absorber, last cold wind import and the hot air exitus of being equipped with of air heat exchanger, cold wind import and blower connection, the top surface of dust remover is equipped with the sampling point, and the side of dust remover is equipped with the water tank, the top of spray absorber is equipped with the chimney, and the side of chimney is equipped with the trompil, and the opening of chimney side is connected with luring the fan, be equipped with the equipment of spraying in the spray absorber, the equipment of spraying through the pipeline with spray the pump and be connected, spray the pump and be connected with the sprayed circulation pond, the bottom surface of spray absorber is equipped with the waste liquid discharge hole and is connected with the sprayed circulation pond. The utility model relates to a burn burning furnace heat transfer system through increasing the way that oxygen was supplied with, reduces the loss of the energy relatively, has greatly reduced msw incineration's cost, and the structure is simple relatively, and manufacturing cost is lower, easily extensive the popularization.
Description
Technical field
The utility model relates to field of garbage disposal, particularly relates to waste incineration processing system.
Background technology
Incinerator is a kind of innocent treatment equipment being usually used in medical treatment and life waste product, animal harmless treatment aspect.Its principle is the burning utilizing the fuel such as coal, fuel oil, combustion gas, object to be processed is carried out the carbonization of destroying by fire of high temperature, to reach the object of sterilization.
Along with the develop rapidly of producing and economic rapid emergence, China has stepped into the ranks of domestic waste high yield state.According to statistics, nineteen ninety the total output of Chinese MSW research be 6,900 ten thousand tons, wherein Shanghai whole city Municipal Garbage Yield is 2,700,000 tons (every days about 7500 tons), ranks first in the country.Nineteen ninety-five, the total output of National urban rubbish reached 100,000,000 tons. according to the investigation statistics to 418 big or middle cities, the Municipal Garbage Yield in China city with annual 10% speed increase, expect rubbish annual production in 2010 and will reach about 200,000,000 tons. to 2014, the volume of cargo in storage over the years of whole nation rubbish has reached more than 60 hundred million tons, and appropriation of land area reaches 500,000,000 m2 (closing 750,000 mu).In more than 600 city, the whole nation, there is more than 200 by garbage mountain is surrounded.Areas in Shanghai City 1260km
2nearly 2000 of the rubbish heap of more than 50m2 is had, floor space about 7900 mu in scope.The long-term air storage of rubbish has caused atmospheric environment, underground water and soil etc. and has significantly threatened and harm.
The temperature of existing incinerator when carrying out burning operation in incinerator needs to reach 850 DEG C, only having in-furnace temperature to reach this high temperature just can make rubbish fully burn, but want the prerequisite reached a high temperature to be need to consume a large amount of energy, the a large amount of consumption of the energy mean waste incineration cost raising, and then improve the expense of whole garbage disposal.
Utility model content
The technical problems to be solved in the utility model overcomes existing indulging to fall into, and provides reliably a set of, greatly can improve the incinerator system of firing efficiency.
In order to solve the problems of the technologies described above, the utility model provides following technical scheme:
A kind of incinerator heat-exchange system, comprise incinerator, air heat exchanger, deduster and spray absorber, described incinerator is connected with air heat exchanger, and described empty heat exchanger is connected with deduster, and described deduster is connected with spray absorber; Described air heat exchanger is provided with cold wind import and hot-blast outlet, and described cold wind import is connected with air blast; The end face of described deduster is provided with sampled point, and the side of described deduster is provided with water tank; The top of described spray absorber is provided with chimney, and the side of described chimney is provided with perforate, and the opening of chimney side is connected with luring blower fan; Be provided with sprinkling equipment in described spray absorber, sprinkling equipment is connected by Guan Shouyu spray pump, and spray pump is connected with Sprayer Circulation pond; The bottom surface of described spray absorber is provided with waste liquid tap and is connected with Sprayer Circulation pond.
Further, described incinerator is vertical incinerator.
Further, the hot-blast outlet of described air heat exchanger is connected with incinerator.
Further, be provided with liquid level gauge in described water tank, the side of water tank is provided with running water inlet.
Further, described chimney is provided with collection point.
A kind of incinerator heat-exchange system of the utility model, by increasing the way of oxygen supply, the loss of the relative minimizing energy, namely energy demand of the present utility model is being reached under identical high temperature prerequisite much smaller than legacy equipment, considerably reduce the cost of waste incineration, structure is relatively simple, and production cost is lower, is easy to large-scale promotion.
Accompanying drawing explanation
Accompanying drawing is used to provide further understanding of the present utility model, and forms a part for description, is used from explanation the utility model, does not form restriction of the present utility model with embodiment one of the present utility model.In the accompanying drawings:
Fig. 1 is structural representation of the present utility model.
Detailed description of the invention
Below in conjunction with accompanying drawing, preferred embodiment of the present utility model is described, should be appreciated that preferred embodiment described herein is only for instruction and explanation of the utility model, and be not used in restriction the utility model.
As shown in Figure 1, a kind of incinerator heat-exchange system of the utility model, comprise incinerator 1, air heat exchanger 2, deduster 3 and spray absorber 4, described incinerator 1 is connected with air heat exchanger 2, described air heat exchanger 2 is connected with deduster 3, and described deduster 3 is connected with spray absorber 4; Described air heat exchanger 2 is provided with cold wind import 21 and hot-blast outlet 22, and described cold wind import 21 is connected with air blast 23; The end face of described deduster 3 is provided with sampled point 32, and the side of described deduster 3 is provided with water tank 31; The top of described spray absorber 4 is provided with chimney 41, and the side of described chimney 41 is provided with perforate, and the opening of chimney 41 side is connected with luring blower fan 42; Be provided with sprinkling equipment in described spray absorber 4, sprinkling equipment is connected with spray pump 43 by pipeline, and spray pump 43 is connected with Sprayer Circulation pond 44; The bottom surface of described spray absorber 4 is provided with waste liquid tap and is connected with Sprayer Circulation pond 44; Described incinerator 1 is vertical incinerator; The hot-blast outlet 22 of described air heat exchanger 2 is connected with incinerator 1; Be provided with liquid level gauge 311 in described water tank 31, the side of water tank 31 is provided with running water inlet 312; Described chimney 41 is provided with collection point 411.
When carrying out waste incineration operation, first the preheating carrying out incinerator 1 is heated, open air heat exchanger 2, by air blast 23 to air heat exchanger 2 cold wind import air blast, air heat exchanger 2 heats the air entered, and is entered in incinerator 1 by hot-blast outlet 22, and then improves the firing efficiency of incinerator 1, the heat that incinerator 1 combustion is got rid of simultaneously passes in air heat exchanger 2, also improves the heat exchange efficiency of air heat exchanger 2; After incinerator 1 temperature is up to standard, rubbish is put into incinerator 1, the burning of rubbish must bring the generation of ashes, a large amount of ashes enter air heat exchanger 2 with hot-air, ashes enter in deduster 3 subsequently, by water tank 31, who is injected in deduster 3, carry out rough dusting by the mode of water-cooled, and sampled by sampled point 32 pairs of deduster inside at deduster 3 top; Remaining the dust do not eliminated subsequently enters in spray absorber 4 by pipeline, now startup spray pump 43 extracts the water in Sprayer Circulation pond 44, the sprinkling equipment that the water be extracted is entered in spray absorber 4 by pipeline sprays dust, namely carries out final dedusting; Gas after spray is discharged by chimney 41, and carries out implementing monitoring by 411 pairs, the collection point on chimney 41 Exhaust Gas; The waste liquid that spray brings is provided with waste liquid tap by the bottom surface of spray absorber 4 and enters in Sprayer Circulation pond 44.
A kind of incinerator heat-exchange system of the utility model, by increasing the way of oxygen supply, the loss of the relative minimizing energy, namely energy demand of the present utility model is being reached under identical high temperature prerequisite much smaller than legacy equipment, and achieve recycling of heat and water, considerably reduce the cost of waste incineration, structure is relatively simple, production cost is lower, is easy to large-scale promotion.
The foregoing is only preferred embodiment of the present utility model, be not limited to the utility model, although be described in detail the utility model with reference to previous embodiment, for a person skilled in the art, it still can be modified to the technical scheme described in foregoing embodiments, or carries out equivalent replacement to wherein portion of techniques feature.All within spirit of the present utility model and principle, any amendment done, equivalent replacement, improvement etc., all should be included within protection domain of the present utility model.
Claims (5)
1. an incinerator heat-exchange system, comprises incinerator, air heat exchanger, deduster and spray absorber, it is characterized in that: described incinerator is connected with air heat exchanger, and described air heat exchanger is connected with deduster, and described deduster is connected with spray absorber;
Described air heat exchanger is provided with cold wind import and hot-blast outlet, and described cold wind import is connected with air blast;
The end face of described deduster is provided with sampled point, and the side of described deduster is provided with water tank;
The top of described spray absorber is provided with chimney, and the side of described chimney is provided with perforate, and the opening of chimney side is connected with luring blower fan;
Be provided with sprinkling equipment in described spray absorber, sprinkling equipment is connected with spray pump by pipeline, and spray pump is connected with Sprayer Circulation pond;
The bottom surface of described spray absorber is provided with waste liquid tap and is connected with Sprayer Circulation pond.
2. a kind of incinerator heat-exchange system according to claim 1, is characterized in that: described incinerator is vertical incinerator.
3. a kind of incinerator heat-exchange system according to claim 1, is characterized in that: the hot-blast outlet of described air heat exchanger is connected with incinerator.
4. a kind of incinerator heat-exchange system according to claim 1, is characterized in that: be provided with liquid level gauge in described water tank, and the side of water tank is provided with running water inlet.
5. a kind of incinerator heat-exchange system according to claim 1, is characterized in that: described chimney is provided with collection point.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520651412.1U CN205026683U (en) | 2015-08-26 | 2015-08-26 | Burn burning furnace heat transfer system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520651412.1U CN205026683U (en) | 2015-08-26 | 2015-08-26 | Burn burning furnace heat transfer system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205026683U true CN205026683U (en) | 2016-02-10 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520651412.1U Active CN205026683U (en) | 2015-08-26 | 2015-08-26 | Burn burning furnace heat transfer system |
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| CN (1) | CN205026683U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US11014037B2 (en) * | 2017-07-27 | 2021-05-25 | Jiangsu Jiulang High-Tech Co., Ltd. | Membrane method processing system and process for high-concentration salt-containing organic waste liquid incineration exhaust gas |
-
2015
- 2015-08-26 CN CN201520651412.1U patent/CN205026683U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US11014037B2 (en) * | 2017-07-27 | 2021-05-25 | Jiangsu Jiulang High-Tech Co., Ltd. | Membrane method processing system and process for high-concentration salt-containing organic waste liquid incineration exhaust gas |
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