Peak shaving system coupling surplus energy consumption with solid-waste treatment

Abstract

The present invention relates to the technical field of energy storage with solid-waste treatment. Provided is a peak shaving system coupling surplus energy consumption and solid-waste treatment. The system comprises: a solar concentration tower, wherein a heat absorber can supply heat to a gasifier, and the gasifier can pyrolyze solid waste into primary fuel gas, pyrolytic fuel oil and pyrolysis char; a gas storage tank is in communication with the gasifier and is configured to collect the primary fuel gas; a tar storage mechanism is in communication with the gasifier and is configured to store the pyrolytic fuel oil and the pyrolysis char; and a microwave pyrolysis apparatus is powered by a thermal power generation unit, and the microwave pyrolysis apparatus can pyrolyze the pyrolytic fuel oil and the pyrolysis char to form secondary fuel gas and collect the secondary fuel gas into the gas storage tank. By coupling solid waste treatment with the thermal power generation unit, during an off-peak period of electricity consumption, surplus electric energy of the thermal power generation unit is used for solid-waste treatment, allowing the thermal power generation unit to maintain operation at a sufficiently high load, and during a peak period of electricity consumption, the fuel gas generated from solid-waste treatment is used for power generation to reduce the load of the thermal power generation unit, thereby realizing a valley-filling and peak-shaving function.

Description

Peak regulation system coupled with excess energy accommodation and solid waste treatment TECHNICAL FIELD

[0001] The present application relates to the technical field of energy storage and solid waste treatment, in particular to a peak regulation system coupled with excess energy accommodation and solid waste treatment. BACKGROUND

[0002] Preparation of fuel gas from solid waste is an effective energy recovery and environmental protection method, especially in the aspect of valley electricity peak regulation, which has potential application value. By converting solid waste into combustible gas, not only can the accumulation of waste and environmental pollution be reduced, but also a flexible energy supplement can be provided, which helps the power grid store energy during low demand periods and release energy during peak periods, thereby achieving stable operation of the power system.

[0003] At present, pyrolysis equipment mostly adopts solar photo-thermal coupling biomass pyrolysis reaction device, such as patent CN116240040 A uses self-driven solar photo-thermal to make biomass pyrolysis, which can not completely rely on solar energy to pyrolyze biomass.

[0004] In addition to the solar photo-thermal coupling biomass pyrolysis reaction device, vertical microwave pyrolysis can also be used to increase the production of fuel gas, such as patent CN116162498A under inert atmosphere, the products obtained by microwave pyrolysis are separated vertically, which improves the production of fuel gas. In addition, "Experimental research and mechanism analysis of corn straw catalytic pyrolysis for preparing hydrogen-rich fuel gas" discloses a scheme for improving the photo-thermal pyrolysis process by increasing the pyrolysis temperature and adding catalysts.

[0005] The above-mentioned pyrolysis equipment has the following defects:

[0006] (1) The self-driven solar photo-thermal system can not completely rely on solar energy to pyrolyze biomass, but the self-driven solar photo-thermal device has insufficient production capacity and cannot meet the requirements of large-scale solid waste pyrolysis.

[0007] (2) The existing vertical microwave pyrolysis of solid waste for preparing fuel gas adopts a one-time pyrolysis method, which requires pyrolysis of solid waste to 1000-1100℃ to completely pyrolyze, and the microwave heating consumes high power and has low efficiency and low fuel gas conversion rate.

[0008] Therefore, how to provide a pyrolysis equipment that can partially or completely solve the above-mentioned defects is a technical problem that needs to be solved by those skilled in the art. SUMMARY

[0009] The purpose of the present application is to provide a peak regulation system coupled with excess energy accommodation and solid waste treatment to solve the problems existing in the prior art, meet the requirements of large-scale solid waste pyrolysis, reduce energy consumption, and improve the fuel gas conversion rate of the solid waste pyrolysis system.

[0010] To achieve the above object, the application provides the following scheme: the application provides a peak regulation system coupled with energy consumption and solid waste treatment, comprising:

[0011] A solar light tower has a heat absorber;

[0012] A gasification furnace, the heat absorber can supply heat to the gasification furnace, and the gasification furnace can pyrolyze solid waste into primary fuel gas, hot fuel oil and pyrolysis coke;

[0013] A gas storage tank, which is in communication with the gasification furnace, is used to collect primary fuel gas;

[0014] A tar storage mechanism, which is in communication with the gasification furnace, is used to store hot fuel oil and pyrolysis coke;

[0015] A microwave pyrolysis device, the feeding end of which is in communication with the tar storage mechanism, is powered by a thermal power generator set, and the microwave pyrolysis device can pyrolyze hot fuel oil and pyrolysis coke to form secondary fuel gas and collect it into the gas storage tank.

[0016] Further, the pyrolysis temperature of the gasification furnace is 500-600℃, and the pyrolysis temperature of the microwave pyrolysis device is 1000-1100℃.

[0017] Further, it further comprises a pretreatment chamber, the heat absorber can supply heat to the pretreatment chamber, and the pretreatment chamber can preheat solid waste at a temperature of 100-200℃, and the preheated solid waste is transported to the gasification furnace by a first crawler conveyor.

[0018] Further, the gasification furnace comprises:

[0019] A furnace body, one side of which is provided with a feeding port, and the feeding port is connected with the first crawler conveyor;

[0020] A stirring device, which is arranged at the bottom of the gasification furnace;

[0021] A heating assembly, which is arranged on the inner surface of the gasification furnace and is heated by the heat absorber;

[0022] An air inlet pipeline, which is in communication with the furnace body and is used to convey inert gas and carbon dioxide gas into the furnace body;

[0023] The solid waste is pyrolyzed into primary gas, hot fuel oil and pyrolysis coke in the furnace body, and the primary gas, hot fuel oil and pyrolysis coke are distributed from top to bottom; the furnace body is provided with a first gas collecting pipeline corresponding to the region where the primary gas is distributed, the first gas collecting pipeline is communicated with the gas storage tank, and the furnace body is provided with a tar collecting mechanism corresponding to the region where the hot fuel oil and pyrolysis coke are distributed, and the tar collecting mechanism is communicated with the tar storage mechanism.

[0024] Further, the tar storage mechanism comprises a pyrolysis coke storage room and an oil storage tank, the tar collecting mechanism comprises an oil outlet pipeline and a second crawler belt conveying device, the oil outlet pipeline is used for collecting the pyrolysis oil from the furnace body into the oil storage tank, and the second crawler belt conveying device is used for collecting the pyrolysis coke from the furnace body into the pyrolysis coke storage room; the pyrolysis coke storage room and the oil storage tank are communicated with the microwave pyrolysis equipment.

[0025] Further, the heat collecting mechanism is further provided, and a heat collecting end of the heat collecting mechanism is connected with the first gas collecting pipeline and / or the oil outlet pipeline and / or the second crawler belt conveying device, so as to collect the heat energy of the primary gas, hot fuel oil and pyrolysis coke; and the heat collecting mechanism can supply heat to the gasification furnace and / or the pretreatment chamber.

[0026] Further, the microwave pyrolysis equipment is communicated with the gas storage tank through a second gas collecting pipeline, and the heat collecting end of the heat collecting mechanism is connected with the second gas collecting pipeline, so as to collect the heat energy of the secondary gas.

[0027] Further, the air inlet pipeline is provided with an air inlet adjusting device, and the air inlet adjusting device is used for adjusting the proportion of the inert gas and the carbon dioxide gas entering the furnace body.

[0028] Further, the control center is further provided, the microwave pyrolysis equipment is provided with a gravity sensor, the control center is communicated with the gravity sensor, the gravity sensor can monitor the weight of the hot fuel oil and the pyrolysis coke in the microwave pyrolysis equipment and send the control center, and the control center controls the power distribution of the thermal power generator set to the microwave pyrolysis equipment according to the weight of the hot fuel oil and the pyrolysis coke; if the thermal power generator set has redundant power, the gasification furnace is supplied with power and heat energy is generated.

[0029] Further, the fuel cell station is further provided, and the gas storage tank can deliver the primary gas and the secondary gas to the fuel cell station.

[0030] The following technical effects are disclosed in the application:

[0031] 1. This invention couples solid waste treatment with thermal power generating units. During off-peak electricity demand periods, the thermal power generating units are required to operate at a forced low load. At this time, the redundant electrical energy of the thermal power generating units can be used for solid waste treatment, allowing the thermal power generating units to maintain a sufficiently high load operation and avoiding problems such as unstable operation and shutdown that are prone to occur when thermal power generating units operate at low loads. During peak electricity demand periods, the gas generated from solid waste treatment is used for power generation, reducing the load on the thermal power generating units, thereby achieving the function of peak shaving during off-peak hours.

[0032] 2. Solid waste treatment adopts a two-stage pyrolysis method of gasification furnace pyrolysis and microwave pyrolysis. The gasification furnace pyrolysis temperature is 500-600℃, and the microwave pyrolysis temperature is 1000-1100℃. Compared with traditional one-time microwave pyrolysis, the pyrolysis time is reduced, the energy consumption is reduced, and the conversion rate of fuel gas is improved.

[0033] 3. The energy storage material used in this application is solid waste, which is a renewable energy source that can reduce carbon emissions. The energy is converted into chemical energy (gas) and stored in a gas storage tank, which can flexibly meet electricity demand and absorb the lowest off-peak electricity during peak shaving. Compared with the commonly used battery storage, it can reduce the use of batteries. In addition, batteries have a limited lifespan, while the system used in this application has no energy storage lifespan limit, which can reduce the amount of coal used during peak periods, improve the energy structure, increase the recycling rate of solid waste, and reduce costs.

[0034] 4. This application utilizes a heat collection mechanism to supply heat to the gasifier and / or pretreatment chamber, and uses a thermal power generator set to supply heat to the gasifier. On the one hand, this can reduce the energy consumption of the pretreatment chamber, and on the other hand, it can maintain the furnace temperature at night, ensure the sustainability of gasifier operation, and avoid frequent start-ups and shutdowns. Summary of the Invention

[0035] To more clearly illustrate the technical solutions in the embodiments of the present invention or the prior art, the drawings used in the embodiments will be briefly introduced below. Obviously, the drawings described below are only some embodiments of the present invention. For those skilled in the art, other drawings can be obtained based on these drawings without creative effort.

[0036] Figure 1 is a schematic diagram of the structure of the present invention;

[0037] Figure 2 is a schematic diagram of the internal structure of the gasifier;

[0038] Figure 3 is a schematic diagram of the working principle of the optical radiation sensor;

[0039] Wherein, 1, solar light tower; 2, gasifier; 201, furnace body; 202, stirring device; 203, heating assembly; 204, gas inlet pipeline; 3, gas storage tank; 4, microwave pyrolysis equipment; 5, fuel cell station; 6, thermal power generator set; 7, pretreatment chamber; 8, first gas collection pipeline; 9, pyrolysis coke storage room; 10, oil storage tank; 11, oil outlet pipeline; 12, first crawler transmission device; 13, second crawler transmission device; 14, heat collecting mechanism; 15, second gas collection pipeline. DETAILED DESCRIPTION

[0040] The technical solutions in the embodiments of the present application will be clearly and completely described below with reference to the drawings in the embodiments of the present application. Obviously, the described embodiments are only part of the embodiments of the present application, rather than all the embodiments. Based on the embodiments in the present application, all other embodiments obtained by those skilled in the art without creative labor fall within the scope of protection of the present application.

[0041] In order to make the above-mentioned purposes, features and advantages of the present application more obvious and easy to understand, the present application will be further described in detail below with reference to the drawings and specific embodiments.

[0042] The present application provides a peak regulation system coupled with surplus energy consumption and solid waste treatment, comprising: a solar light tower 1 having a heat absorber; a gasifier 2, the heat absorber being capable of supplying heat to the gasifier 2, the gasifier 2 being capable of pyrolyzing solid waste into primary fuel gas, hot fuel oil and pyrolysis coke; a gas storage tank 3, the gas storage tank 3 being in communication with the gasifier 2 and being used for collecting the primary fuel gas; a tar storage mechanism, the tar storage mechanism being in communication with the gasifier 2 and being used for storing the hot fuel oil and the pyrolysis coke; a microwave pyrolysis equipment 4, a feeding end of the microwave pyrolysis equipment 4 being in communication with the tar storage mechanism, the microwave pyrolysis equipment 4 being powered by a thermal power generator set 6, the microwave pyrolysis equipment 4 being capable of pyrolyzing the hot fuel oil and the pyrolysis coke to form secondary fuel gas and collecting the secondary fuel gas into the gas storage tank 3. The pyrolysis temperature of the gasifier 2 is 500-600 DEG C, and the pyrolysis temperature of the microwave pyrolysis equipment 4 is 1000-1100 DEG C.

[0043] In the present embodiment, a pretreatment chamber 7 is further included, the heat absorber is capable of supplying heat to the pretreatment chamber 7, the pretreatment chamber 7 is capable of preheating the solid waste at a temperature of 100-200 DEG C, and the preheated solid waste is transported to the gasifier 2 by a first crawler transmission device 12. The pretreatment chamber 7 is used for removing moisture in the solid waste, so that the solid waste is changed into a dry state and is convenient for subsequent pyrolysis.

[0044] The gasifier 2 comprises a furnace body 201, the furnace body 201 is provided with a feeding port on one side, the feeding port is connected with the first caterpillar conveyor 12; a stirring device 202 is arranged at the bottom of the gasifier 2; a heating assembly 203 is arranged on the inner surface of the gasifier 2 and is heated by a heat absorber; an air inlet pipeline 204 is connected with the furnace body 201 and is used for conveying inert gas and carbon dioxide gas into the furnace body 201; the solid waste is pyrolyzed into primary fuel gas, hot fuel oil and pyrolysis coke in the furnace body 201, and the primary fuel gas, the hot fuel oil and the pyrolysis coke are distributed from top to bottom in sequence; the furnace body 201 is provided with a first gas collecting pipeline 8 corresponding to the region where the primary fuel gas is distributed, the first gas collecting pipeline 8 is connected with the gas storage tank 3, and the furnace body 201 is provided with a tar collecting mechanism corresponding to the region where the hot fuel oil and the pyrolysis coke are distributed, and the tar collecting mechanism is connected with a tar storage mechanism.

[0045] The tar storage mechanism comprises a pyrolysis coke storage room 9 and an oil storage tank 10, the tar collecting mechanism comprises an oil outlet pipeline 11 and a second caterpillar conveyor 13, the oil outlet pipeline 11 is used for collecting the pyrolysis oil from the furnace body 201 into the oil storage tank 10, and the second caterpillar conveyor 13 is used for collecting the pyrolysis coke from the furnace body 201 into the pyrolysis coke storage room 9; the pyrolysis coke storage room 9 and the oil storage tank 10 are connected with the microwave pyrolysis equipment 4.

[0046] In the embodiment, a heat collecting mechanism 14 is further included, a heat collecting end of the heat collecting mechanism 14 (the heat collecting mechanism 14 can be a heat exchanger filled with a heat exchange medium and a heat storage device, the heat collecting end is a contact end of the heat exchange medium and the following structure, the heat collecting mechanism 14 can be any device capable of exchanging heat with the following structure, which is not limited here) is connected with the first gas collecting pipeline 8 and / or the oil outlet pipeline 11 and / or the second caterpillar conveyor 13, and is used for collecting the heat energy of the primary fuel gas, the hot fuel oil and the pyrolysis coke, and the heat collecting mechanism 14 can supply heat to the gasifier 2 and / or the pretreatment chamber 7. The microwave pyrolysis equipment 4 is connected with the gas storage tank 3 through a second gas collecting pipeline 15, the heat collecting end of the heat collecting mechanism 14 is connected with the second gas collecting pipeline 15, and is used for collecting the heat energy of the secondary fuel gas. In some other embodiments, the pyrolysis oil and the pyrolysis coke which are easy to exchange heat can be input into the heat collecting mechanism 14 with a large heat exchange chamber, and then are sent to the corresponding storage mechanism after heat exchange.

[0047] In the embodiment, an air inlet adjusting device is arranged on the air inlet pipeline 204, and is used for adjusting the proportion of the inert gas and the carbon dioxide gas entering the furnace body 201. Specifically, the inert gas and the carbon dioxide are loaded by different gas cylinders respectively, the flow valves are arranged at the outlets of the gas cylinders, the air inlet amounts of the two are uniformly adjusted by the air inlet adjusting device, and the atmosphere in the furnace is changed. A good atmosphere in the furnace can ensure that the solid waste is fully pyrolyzed, and improve the fuel gas conversion rate and the overall power generation efficiency.

[0048] In the embodiment, a control center is further included, the microwave pyrolysis device 4 is provided with a gravity sensor, the control center is in communication connection with the gravity sensor, the gravity sensor can monitor the weight of the hot fuel oil and the pyrolysis coke in the microwave pyrolysis device 4 and send the control center, and the control center controls the power distribution of the thermal power generator set 6 to the microwave pyrolysis device 4 according to the weight of the hot fuel oil and the pyrolysis coke; if the thermal power generator set 6 has redundant power, the gasification furnace 2 and / or the pretreatment chamber 7 are supplied with power and heat energy is generated. A light radiation sensor is arranged on the solar energy light tower 1, the light radiation sensor is in communication connection with the control center, when the light intensity is sufficient, the heat collecting mechanism 14 does not need to supply heat to the gasification furnace 2 or the pretreatment chamber 7, when the light intensity is insufficient, the heat collecting mechanism 14 supplies heat to the gasification furnace 2 or the pretreatment chamber 7, and the pyrolysis function of the gasification furnace 2 and the preheating and drying functions of the pretreatment chamber 7 are maintained.

[0049] In the embodiment, a fuel cell station 5 is further included, and the gas storage tank 3 can deliver the primary fuel gas and the secondary fuel gas to the fuel cell station 5. During the peak power consumption period, the primary fuel gas and the secondary fuel gas are fully combusted in the fuel cell station 5 to generate water vapor to drive the steam turbine to work and generate power.

[0050] The specific working process is as follows:

[0051] During the day, the solar energy light tower 1 absorbs solar energy through the heat absorber and generates heat. The solid waste is first sent into the pretreatment chamber 7, the heat absorber supplies heat to the pretreatment chamber 7 to generate a preheating temperature of 100-200 DEG C, evaporates the moisture in the solid waste, and the solid waste is dried. The dried solid waste is transported into the gasification furnace 2 through the first crawler transport device.

[0052] The heat absorber supplies heat to the gasification furnace 2, and the gasification furnace 2 pyrolyzes the solid waste at a temperature of 500 DEG C, the stirring device 202 is used to ensure the uniformity of pyrolysis during the pyrolysis process, the pyrolysis time is about 1 hour, and the pyrolyzed solid waste becomes primary fuel gas, hot fuel oil and pyrolysis coke, wherein the primary fuel gas is in the uppermost layer, the hot fuel oil is in the middle layer, and the pyrolysis coke is in the lowermost layer. The primary fuel gas is directly collected into the gas storage tank 3 through the first gas collecting pipeline 8, the hot fuel oil and the pyrolysis coke are collected into the oil storage tank 10 and the pyrolysis coke storage room 9 respectively, and the primary fuel gas, the hot fuel oil and the pyrolysis coke still have a temperature of above 400 DEG C during the process of being transported to the corresponding collecting device. The heat collecting end of the heat collecting mechanism 14 collects the heat of the primary fuel gas, the hot fuel oil and the pyrolysis coke by heat exchange.

[0053] At night, the power consumption is greatly reduced, and the thermal power generator set 6 is forced to reduce the load. In order to ensure that the thermal power generator set 6 maintains a safe load, the hot fuel oil and the pyrolysis coke are mixed without limitation of the mixing ratio, the mixed hot fuel oil and pyrolysis coke are placed into the microwave pyrolysis equipment 4, the redundant power of the thermal power generator set 6 is supplied to the microwave pyrolysis equipment 4, the hot fuel oil and the pyrolysis coke are pyrolyzed at a temperature of 1000 DEG C, and the pyrolysis time is about 0.5 hours. The pyrolysis coke and the hot fuel oil are completely pyrolyzed to form secondary fuel gas, which is collected into the gas storage tank 3 through the second gas collecting pipeline 15. The temperature of the secondary fuel gas still has a temperature of 900 DEG C or above, and the heat collecting end of the heat collecting mechanism 14 collects the heat of the secondary fuel gas through heat exchange.

[0054] During the peak power consumption period, the fuel gas is delivered to the fuel cell station 5 through the gas storage tank 3 to generate power, reduce the load of the thermal power generator set, and realize the function of valley power peak shaving.

[0055] In the above process, when the light intensity is sufficient, the heat collecting mechanism 14 does not need to supply heat to the gasification furnace 2 or the pretreatment chamber 7; when the light intensity is insufficient, the heat collecting mechanism 14 supplies heat to the gasification furnace 2 or the pretreatment chamber 7 to maintain the pyrolysis function of the gasification furnace 2 and the preheating and drying function of the pretreatment chamber 7, and fully utilize the heat storage energy of the heat collecting mechanism 14 and the heat storage energy generated by the solar tower 1.

[0056] In the above process, since the solar tower 1 cannot work in the night scene, in addition to the heat collecting mechanism 14 which can supply heat to the gasification furnace 2 and the pretreatment chamber 7, the redundant power of the thermal power generator set 6 can also be used to supply heat to the gasification furnace 2 and the pretreatment chamber 7, and the valley power consumption is fully utilized.

[0057] The total length of completely pyrolyzing solid waste by using the embodiment is 1.5 hours, and the total length of completely pyrolyzing solid waste by using the traditional one-time microwave pyrolysis method is more than 2 hours. Compared with the traditional one-time microwave pyrolysis method, the application not only shortens the pyrolysis time, but also reduces the pyrolysis energy consumption.

[0058] In the description of the present application, it should be understood that the terms "longitudinal", "transverse", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer" and the like indicate the orientation or positional relationship based on the orientation or positional relationship shown in the drawings, and are only used to facilitate the description of the present application, and do not indicate or imply that the device or element referred to must have a particular orientation, be constructed and operated in a particular orientation, and therefore cannot be understood as a limitation of the present application.

[0059] The above described embodiments are only to illustrate the preferred modes of the present application, and are not intended to limit the scope of the present application. Any modification and improvement made by those skilled in the art to the technical solutions of the present application without departing from the design spirit of the present application shall fall within the protection scope of the present application as defined by the claims.

Claims

1. A peak shaving system coupled with excess energy accommodation and solid waste treatment, characterized in that, The application relates to a solar energy concentrating tower (1) with a heat absorber, a gasification furnace (2) which can be heated by the heat absorber, the gasification furnace (2) can pyrolyze solid waste into primary fuel gas, hot fuel oil and pyrolysis coke, a gas storage tank (3) which is communicated with the gasification furnace (2) and is used for collecting the primary fuel gas, a coke storage mechanism which is communicated with the gasification furnace (2) and is used for storing the hot fuel oil and the pyrolysis coke, a microwave pyrolysis device (4) whose feeding end is communicated with the coke storage mechanism, the microwave pyrolysis device (4) is powered by a thermal power generator set (6), the microwave pyrolysis device (4) can pyrolyze the hot fuel oil and the pyrolysis coke into secondary fuel gas and collect the secondary fuel gas into the gas storage tank (3), a pretreatment chamber (7) which can be heated by the heat absorber and can preheat the solid waste at a temperature of 100-200 DEG C, the preheated solid waste is transported to the gasification furnace (2) through a first crawler belt conveying device (12), the gasification furnace (2) comprises a furnace body (201) which is provided with a feeding port on one side and is connected with the first crawler belt conveying device (12), a stirring device (202) which is arranged on the furnace bottom of the gasification furnace (2), a heating assembly (203) which is arranged on the inner surface of the gasification furnace (2) and is heated by the heat absorber, and an air inlet pipeline (204) which is communicated with the furnace body (201) and is used for conveying inert gas and carbon dioxide gas into the furnace body (201), the solid waste is pyrolyzed into the primary fuel gas, the hot fuel oil and the pyrolysis coke in the furnace body (201), the primary fuel gas, the hot fuel oil and the pyrolysis coke are distributed from top to bottom, the furnace body (201) is provided with a first gas collecting pipeline (8) corresponding to the region where the primary fuel gas is distributed, the first gas collecting pipeline (8) is communicated with the gas storage tank (3), the furnace body (201) is provided with a coke collecting mechanism corresponding to the region where the hot fuel oil and the pyrolysis coke are distributed, and the coke collecting mechanism is communicated with the coke storage mechanism, the coke storage mechanism comprises a pyrolysis coke storage chamber (9) and an oil storage tank (10), the coke collecting mechanism comprises an oil outlet pipeline (11) and a second crawler belt conveying device (13), the oil outlet pipeline (11) is used for collecting the pyrolysis oil from the furnace body (201) into the oil storage tank (10), and the second crawler belt conveying device (13) is used for collecting the pyrolysis coke from the furnace body (201) into the pyrolysis coke storage chamber (9), the pyrolysis coke storage chamber (9) and the oil storage tank (10) are both communicated with the microwave pyrolysis device (4), and the gas storage tank (3) can deliver the primary fuel gas and the secondary fuel gas to a fuel cell station (5). The pyrolysis temperature of the gasification furnace (2) is 500-600 DEG C, and the pyrolysis temperature of the microwave pyrolysis device (4) is 1000-1100 DEG C. ​ ​ ​ ​ ​ ​ ​ ​ ​ ​ ​ ​ 2. The peak shaving system of claim 1, wherein, ​ 3. The peak shaving system for coupling waste energy absorption and solid waste treatment according to claim 1, characterized in that, Further comprising a heat collecting mechanism (14), a heat collecting end of the heat collecting mechanism (14) is connected with the first gas collecting pipeline (8) and / or oil outlet pipeline (11) and / or second crawler belt conveying device (13), for collecting heat energy of primary fuel gas, hot fuel oil and pyrolysis coke, the heat collecting mechanism (14) can supply heat to the gasifier (2) and / or pretreatment chamber (7).

4. The coupled waste-to-energy absorption and solid waste treatment peak shaving system of claim 3, wherein, The microwave pyrolysis equipment (4) is communicated with the gas storage tank (3) through a second gas collecting pipeline (15), a heat collecting end of the heat collecting mechanism (14) is connected with the second gas collecting pipeline (15), for collecting heat energy of secondary fuel gas.

5. The coupled waste-to-energy and solid waste disposal peak-shaving system of claim 1, wherein, An air inlet adjusting device is arranged on the air inlet pipeline (204), the air inlet adjusting device is used for adjusting the proportion of inert gas and carbon dioxide gas entering into the furnace body (201).

6. The coupled waste-to-energy absorption and solid waste treatment peak shaving system of claim 1, wherein, Further comprising a control center, the microwave pyrolysis equipment (4) has a gravity sensor, the control center is communicatively connected with the gravity sensor, the gravity sensor can monitor the weight of hot fuel oil and pyrolysis coke in the microwave pyrolysis equipment (4) and send the control center, the control center controls the power distribution of the thermal power generator set (6) to the microwave pyrolysis equipment (4) according to the weight of the hot fuel oil and pyrolysis coke; if the thermal power generator set (6) has redundant power, the thermal power generator set (6) supplies power to the gasifier (2) and generates heat energy.

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