CN216667697U - Household garbage incineration and waste tire pyrolysis co-production device - Google Patents
Household garbage incineration and waste tire pyrolysis co-production device Download PDFInfo
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- CN216667697U CN216667697U CN202122934143.8U CN202122934143U CN216667697U CN 216667697 U CN216667697 U CN 216667697U CN 202122934143 U CN202122934143 U CN 202122934143U CN 216667697 U CN216667697 U CN 216667697U
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Abstract
The utility model relates to the technical field of solid waste treatment, in particular to a domestic waste incineration and waste tire pyrolysis cogeneration device which comprises a waste incineration boiler, a tire pyrolysis furnace, a waste heat boiler, a steam turbine and a generator, wherein a pyrolysis gas pipeline is fixedly communicated between a pyrolysis gas discharge end of the tire pyrolysis furnace and a gas inlet end of the waste incineration boiler, a first high-temperature flue gas pipeline is fixedly communicated between a first gas outlet end of the waste incineration boiler and a gas inlet end of the tire pyrolysis furnace, a second high-temperature flue gas pipeline is fixedly communicated between a second gas outlet end of the waste incineration boiler and the gas inlet end of the waste heat boiler, and a steam pipeline is fixedly communicated between the gas outlet end of the waste heat boiler and a steam inlet end of the steam turbine. The utility model can realize the reutilization of the flue gas and the waste steam waste heat of the waste incineration power plant, effectively reduces the heat loss of the discharged flue gas, provides a good way for the treatment of the waste tires, achieves the purposes of energy saving and consumption reduction, realizes the full utilization of energy, and has the characteristics of safety, labor saving, simplicity, convenience and high efficiency.
Description
Technical Field
The utility model relates to the technical field of solid waste treatment, in particular to a device for co-producing household garbage incineration and waste tire pyrolysis.
Background
With the rapid development of national economy and the increasing improvement of the living standard of people, the domestic garbage is increased gradually, and the dilemma of 'garbage enclosing city' is highlighted. The reasonable treatment of the garbage plays an increasingly important role in practicing a green development idea and promoting the ecological civilization construction process. At present, the treatment mode of the household garbage has three types: direct incineration, sanitary landfills and composting. Compared with landfill which is easy to cause secondary pollution and waste compost which is difficult to sell, the household garbage incineration power generation technology is gradually a mainstream way for treating household garbage in China as a method for utilizing solid waste resources. The heat in the purified and dedusted flue gas at the tail part of the waste heat boiler of the waste incineration power station is recycled, and the reduction of the smoke discharge loss has very important significance for improving the boiler efficiency and the power generation economy of the whole plant.
In recent years, the automobile yield in China is rapidly increased, so that the development of the tire industry is driven, and a large amount of waste tires are brought. From 2012 onwards, the annual global tire production has broken through 2000 ten thousand tons, with the tire production in our country being 1000 ten thousand tons. The main methods for recycling waste tires are divided into physical treatment and chemical treatment. The physical treatment mainly comprises retreaded tires, reclaimed rubber and rubber powder, and most of the physical treatment technologies have high energy consumption and low profit. Therefore, most rubber powder enterprises are in a loss state at present. The chemical treatment is mainly a waste tyre thermochemical treatment technology, comprising pyrolysis, incineration and gasification technologies. However, incineration and gasification both cause different levels of environmental damage. The pyrolysis technology has low energy consumption, and products of the pyrolysis oil, the carbonaceous materials and the like have great utilization value. Therefore, the pyrolysis technology becomes an important method for solving the problem of recycling the waste tires.
The main products of the pyrolysis of the waste tires are pyrolysis gas, pyrolysis oil and pyrolysis carbon black. The pyrolysis gas is non-pour-point depression waste gas formed in the process of pyrolysis and condensation of the waste tire, and mainly comprises CO2、CO、H2、CH4、C2H6、C3H8、C4H6And the amount of the pyrolysis gas is about 30 to 53 percent of the total amount of the pyrolysis gas. The calorific value of the pyrolysis gas is similar to that of natural gas, so that the pyrolysis gas can be directly used as fuel gas. The high-calorific-value pyrolysis gas is used for heat generation and power generation, has considerable economic benefit, can make up the current situation of coal shortage as a high-calorific-value energy source, and has good development prospect. Therefore, the recycled flue gas enters the waste heat boiler, the circulating water absorbing the waste heat of the discharged flue gas is used as the working medium of the steam cycle power generation system, and the feed water is evaporated in the waste heat boiler and then enters the steam turbine to do work to drive the generator to generate power. Pyrolysis oil and pyrolytic carbon in the pyrolysis product can be stored and utilized, and the whole system realizes high-efficiency synergy of energy conservation, environmental protection and economy.
Disclosure of Invention
The utility model provides a household garbage incineration and waste tire pyrolysis co-production device, overcomes the defects of the prior art, and can effectively solve the problems of heat in the flue gas of a garbage incineration power station and waste tire pyrolysis gas recycling in the prior art.
The technical scheme of the utility model is realized by the following measures: the utility model provides a domestic waste burns and junked tire pyrolysis coproduction device, including the msw incineration boiler, the tire pyrolysis stove, exhaust-heat boiler, steam turbine and generator, the tire pyrolysis stove is provided with pyrolysis oil discharge end, pyrolysis carbon discharge end and pyrolysis gas discharge end, it has pyrolysis gas pipeline to fix the intercommunication between tire pyrolysis stove pyrolysis gas discharge end and the msw incineration boiler inlet end, it has first high temperature flue gas pipeline to fix the intercommunication between msw incineration boiler first end of giving vent to anger and the tire pyrolysis stove inlet end, it has second high temperature flue gas pipeline to fix the intercommunication between msw incineration boiler second end of giving vent to anger and the exhaust-heat boiler inlet end, exhaust-heat boiler inlet end intercommunication has the air inlet pipeline, it has the vapor pipeline to fix the intercommunication between exhaust-heat boiler end of giving vent to anger and the steam turbine inlet end, the output shaft of steam turbine is connected with the input shaft transmission of generator.
The following are further optimization or/and improvement of the technical scheme of the utility model:
the household garbage incineration and waste tire pyrolysis co-production device further comprises a condenser, a low-pressure heater and a deaerator, a first steam extraction pipeline is fixedly communicated between a first steam extraction end of the steam turbine and a steam inlet end of the deaerator, a second steam extraction pipeline is fixedly communicated between a second steam extraction end of the steam turbine and a steam inlet end of the low-pressure heater, a steam exhaust pipeline is fixedly communicated between a steam exhaust steam outlet end of the steam turbine and a steam inlet end of the condenser, a condensate water pipeline is fixedly communicated between a condensate water outlet end of the condenser and a liquid inlet end of the low-pressure heater, a low-temperature heat source pipeline is fixedly communicated between a first liquid outlet end of the low-pressure heater and a liquid inlet end of the deaerator, and a circulating water pipeline is fixedly communicated between a liquid outlet end of the deaerator and a liquid inlet end of the waste tire boiler.
And a return pipeline is fixedly communicated between the second liquid outlet end of the low-pressure heater and the liquid inlet end of the condenser.
And the condensate water pipeline and the circulating water pipeline are respectively provided with a conveying pump.
The utility model can realize the reutilization of the flue gas and the waste steam waste heat of the waste incineration power plant, effectively reduces the heat loss of the discharged flue gas, provides a good way for the treatment of the waste tires, achieves the purposes of energy saving and consumption reduction, realizes the full utilization of energy, and has the characteristics of safety, labor saving, simplicity, convenience and high efficiency.
Drawings
FIG. 1 is a schematic process flow diagram of the present invention.
The codes in the figures are respectively: 1 is the msw incineration boiler, 2 is the tire pyrolysis stove, 3 is exhaust-heat boiler, 4 is the steam turbine, 5 is the generator, 6 is the pyrolysis gas pipeline, 7 is first high temperature flue gas pipeline, 8 is second high temperature flue gas pipeline, 9 is the air admission pipeline, 10 is the steam pipeline, 11 is the condenser, 12 is low pressure feed water heater, 13 is the oxygen-eliminating device, 14 is first extraction steam pipeline, 15 is the second extraction steam pipeline, 16 is the exhaust steam pipeline, 17 is the condensate water pipeline, 18 is low temperature heat source pipeline, 19 is circulating water pipeline, 20 is the backflow pipeline, 21 is the delivery pump.
Detailed Description
The present invention is not limited by the following examples, and specific embodiments may be determined according to the technical solutions and practical situations of the present invention.
In the present invention, for convenience of description, the description of the relative positional relationship of the components is described according to the layout pattern of fig. 1 of the specification, such as: the positional relationship of front, rear, upper, lower, left, right, etc. is determined in accordance with the layout direction of fig. 1 of the specification.
The utility model is further described with reference to the following examples and figures:
as shown in attached figure 1, the household garbage incineration and waste tire pyrolysis cogeneration device comprises a garbage incineration boiler 1, a tire pyrolysis furnace 2 and a waste heat boiler 3, the tire pyrolysis furnace 2 is provided with a pyrolysis oil discharge end, a pyrolysis carbon discharge end and a pyrolysis gas discharge end, a pyrolysis gas pipeline 6 is fixedly communicated between the pyrolysis gas discharge end of the tire pyrolysis furnace 2 and the gas inlet end of the garbage incineration boiler 1, a first high-temperature flue gas pipeline 7 is fixedly communicated between the first gas outlet end of the garbage incineration boiler 1 and the gas inlet end of the tire pyrolysis furnace 2, a second high-temperature flue gas pipeline 8 is fixedly communicated between the second gas outlet end of the garbage incineration boiler 1 and the gas inlet end of the waste heat boiler 3, a gas inlet pipeline 9 is communicated with the gas inlet end of the waste heat boiler 3, a water vapor pipeline 10 is fixedly communicated between the gas outlet end of the waste heat boiler 3 and the gas inlet end of the steam turbine 4, and an output shaft of the steam turbine 4 is in transmission connection with an input shaft of the generator 5.
The household garbage incineration and waste tire pyrolysis co-production device can be further optimized or/and improved according to actual needs:
as shown in fig. 1, the domestic garbage incineration and waste tire pyrolysis cogeneration device further comprises a condenser 11, a low-pressure heater 12 and a deaerator 13, a first steam extraction pipeline 14 is fixedly communicated between a first steam extraction end of the steam turbine 4 and a steam inlet end of the deaerator 13, a second steam extraction pipeline 15 is fixedly communicated between a second steam extraction end of the steam turbine 4 and a steam inlet end of the low-pressure heater 12, a steam exhaust pipeline 16 is fixedly communicated between a steam exhaust outlet end of the steam turbine 4 and a steam inlet end of the condenser 11, a condensate water pipeline 17 is fixedly communicated between a condensate water outlet end of the condenser 11 and a liquid inlet end of the low-pressure heater 12, a low-temperature heat source pipeline 18 is fixedly communicated between a first liquid outlet end of the low-pressure heater 12 and a liquid inlet end of the deaerator 13, and a circulating water pipeline 19 is fixedly communicated between a liquid outlet end of the deaerator 13 and a liquid inlet end of the waste heat boiler 3.
As shown in fig. 1, a return line 20 is fixedly communicated between the second liquid outlet end of the low-pressure heater 12 and the liquid inlet end of the condenser 11.
As shown in fig. 1, a transfer pump 21 is provided in each of the condensate line 17 and the circulation line 19.
According to the utility model, waste incineration high-temperature flue gas is used for carrying out high-temperature pyrolysis on the waste tires, and the obtained pyrolysis gas enters the incinerator for cyclic utilization, so that the flue gas of a waste incineration power plant and the waste heat of exhaust steam are recycled, the heat loss of the exhaust steam is effectively reduced, a good way is provided for the treatment of the waste tires, the purposes of energy conservation and consumption reduction are achieved, and the full utilization of energy is realized.
The above technical features constitute the best embodiment of the present invention, which has strong adaptability and best implementation effect, and unnecessary technical features can be increased or decreased according to actual needs to meet the requirements of different situations.
The use process of the best embodiment of the utility model is as follows:
a part of high-temperature flue gas generated by burning the garbage in the garbage burning boiler 1 enters the tire pyrolyzing furnace 2 to be used for pyrolyzing the waste tires to generate three products of pyrolysis oil, pyrolysis carbon and pyrolysis gas, wherein the pyrolysis oil and the pyrolysis carbon are stored and utilized, and the pyrolysis gas is recycled to enter the garbage burning boiler 1 to continuously burn and release heat; the other part of the high-temperature flue gas from the waste incineration boiler 1 enters a waste heat boiler 3, air is introduced into the waste heat boiler 3 for afterburning, water is heated and supplied to the waste heat boiler to be changed into steam, and the steam enters a steam turbine 4 to drive a coaxial generator 5 to generate electricity. In addition, two steam extractions are extracted from the steam turbine 4, the first steam extraction enters the deaerator 13, the second steam extraction enters the low-pressure heater 12, and the residual exhaust steam of the steam turbine 4 enters the condenser 11 to be condensed into condensate water. And the condensed water in the condenser 11 enters the low-pressure heater 12 to exchange heat with the second steam extraction of the steam turbine 4 to raise the temperature, so that the heated feed water is obtained. The heated feed water enters a deaerator 13, deaerates and performs mixed heat exchange with the first steam extraction of the steam turbine 4 in the deaerator 13, and finally returns to the waste heat boiler 3.
Claims (5)
1. The utility model provides a domestic waste burns and junked tire pyrolysis coproduction device, a serial communication port includes the msw incineration boiler, the tire pyrolysis stove, exhaust-heat boiler, steam turbine and generator, the tire pyrolysis stove is provided with pyrolysis oil discharge end, pyrolysis carbon discharge end and pyrolysis gas discharge end, it has pyrolysis gas pipeline to fix the intercommunication between tire pyrolysis stove pyrolysis gas discharge end and the msw incineration boiler inlet end, it has first high temperature flue gas pipeline to fix the intercommunication between the first end of giving vent to anger of msw incineration boiler and the tire pyrolysis stove inlet end, it has second high temperature flue gas pipeline to fix the intercommunication between the end of giving vent to anger of msw incineration boiler second and the exhaust-heat boiler inlet end, exhaust-heat boiler inlet end intercommunication has the air inlet pipeline, it has the steam pipeline to fix the intercommunication between end of giving vent to anger of exhaust-heat boiler and the steam turbine inlet end, the output shaft of steam turbine is connected with the input shaft transmission of generator.
2. The device for co-production of household garbage incineration and waste tire pyrolysis as claimed in claim 1, wherein the device for co-production of household garbage incineration and waste tire pyrolysis further comprises a condenser, a low-pressure heater and a deaerator, a first steam extraction pipeline is fixedly communicated between a first steam extraction end of the steam turbine and a steam inlet end of the deaerator, a second steam extraction pipeline is fixedly communicated between a second steam extraction end of the steam turbine and a steam inlet end of the low-pressure heater, a steam exhaust pipeline is fixedly communicated between a steam exhaust steam outlet end of the steam turbine and a steam inlet end of the condenser, a condensate water pipeline is fixedly communicated between a condensate water outlet end of the condenser and a liquid inlet end of the low-pressure heater, a low-temperature heat source pipeline is fixedly communicated between a first liquid outlet end of the low-pressure heater and a liquid inlet end of the deaerator, and a circulating water pipeline is fixedly communicated between a liquid outlet end of the deaerator and a liquid inlet end of the waste heat boiler.
3. The domestic waste incineration and junked tire pyrolysis coproduction device as defined in claim 1 or 2, characterized in that a return line is fixedly communicated between the second liquid outlet end of the low-pressure heater and the liquid inlet end of the condenser.
4. The domestic waste incineration and junked tire pyrolysis cogeneration apparatus of claim 1 or 2, characterized in that the condensate water pipeline and the circulating water pipeline are both provided with a delivery pump.
5. The domestic waste incineration and junked tire pyrolysis cogeneration apparatus of claim 3, characterized in that the condensate water pipeline and the circulating water pipeline are both provided with a delivery pump.
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CN202122934143.8U CN216667697U (en) | 2021-11-26 | 2021-11-26 | Household garbage incineration and waste tire pyrolysis co-production device |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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CN116925803A (en) * | 2023-06-12 | 2023-10-24 | 中国联合工程有限公司 | Multi-effect recycling system for waste tires and working method thereof |
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2021
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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CN116925803A (en) * | 2023-06-12 | 2023-10-24 | 中国联合工程有限公司 | Multi-effect recycling system for waste tires and working method thereof |
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