RTO high-temperature incineration system and method

Abstract

The invention discloses an RTO high-temperature incineration system and method, and relates to the technical field of waste gas treatment. Comprising a pretreatment system, an adsorption system and a catalytic combustion system, the pretreatment system comprises a surface air cooler cooling module; the adsorption system comprises a dust filtering module and a continuous adsorption module; the catalytic combustion system comprises a waste heat utilization module, a power equipment module, a catalytic combustion module, a control room module and a tool box module. By optimizing the heat recovery and waste gas treatment process, the treatment efficiency and the energy utilization rate are improved, through intelligent control, a novel catalyst, higher catalytic activity and longer operation life, the waste gas treatment efficiency is improved, the operation cost and the environmental influence are reduced, and a solution is provided for the field of waste gas treatment.

Description

Technical Field

[0001] The invention relates to the technical field of waste gas treatment, and in particular to an RTO high-temperature incineration system and method. Background Art

[0002] With the acceleration of industrialization, a large amount of waste gas generated in the industrial production process, especially waste gas containing volatile organic compounds (VOCs), poses a serious threat to the environment and human health. In order to reduce the emission of these harmful substances, the traditional high-temperature incineration system is used to treat volatile organic compounds, but it also faces problems such as high energy consumption and low treatment efficiency. RTO (Regenerative Thermal Oxidizer) is an efficient waste gas treatment technology. It is widely used because it can oxidize and decompose VOCs in waste gas into harmless CO2 and H2O at high temperature and has a high heat recovery efficiency.

[0003] Although the existing RTO system performs well in waste gas treatment, its heat recovery efficiency and long-term stability under high-temperature operation still need to be further improved; a certain amount of energy is still required to start and maintain the high-temperature oxidation reaction, especially when treating low-concentration VOCs waste gas, the energy consumption problem is more prominent; the catalyst is expensive and has poor performance. Summary of the invention

[0004] The object of the present invention is to provide a RTO high temperature incineration system and method to solve the problems raised in the above background technology.

[0005] In order to solve the above technical problems, the present invention provides the following technical solutions: an RTO high temperature incineration system, comprising: a pretreatment system, an adsorption system, and a catalytic combustion system; the pretreatment system comprises a surface cooler cooling module; the adsorption system comprises a dust filtration module and a continuous adsorption module; the catalytic combustion system comprises a waste heat utilization module, a power equipment module, a catalytic combustion module, a control room module, and a tool box module;

[0006] The surface cooler cooling module effectively reduces the exhaust gas temperature through heat exchange between cooling water and exhaust gas, and cools the high-temperature exhaust gas for subsequent treatment;

[0007] The dust filtration module is provided with three-stage filtration, including a primary filter and a medium filter, which are used to remove dust harmful to the rotor, ensure that the dust content in the exhaust gas meets environmental protection standards, and reduce pollution to the environment;

[0008] The continuous adsorption module effectively removes volatile organic compounds (VOCs) in the exhaust gas through continuous adsorption and regeneration processes, thereby improving the exhaust gas purification effect;

[0009] In the waste heat utilization module, the high-temperature airflow generated by oxidation flows through the heat storage body to heat it up and "storage heat", and is used to preheat the subsequent organic waste gas, so as to save fuel consumption caused by the waste gas heating and improve energy utilization efficiency;

[0010] The power equipment modules include fans, pumps, and motors to ensure smooth flow of exhaust gas in the system and maintain normal operation of each module;

[0011] The catalytic combustion module burns the organic pollutants in the exhaust gas at high temperature under the action of a catalyst, converting them into harmless carbon dioxide and water, ensuring that the organic pollutants are completely decomposed, reducing energy consumption and secondary pollution;

[0012] The control room module adopts a programmable controller system PLC, which is equipped with centralized control and local control. It is responsible for power supply and automatic control of various power equipment in the exhaust gas treatment facility, real-time monitoring of system operation status and parameters, and timely adjustment of control strategies to ensure safe, stable and efficient operation of the system;

[0013] The toolbox module, through a complete toolbox configuration, provides the necessary tools and spare parts for the maintenance and overhaul of the RTO high temperature incineration system, ensuring that when a failure occurs or maintenance is required, it can be handled quickly, reducing downtime and ensuring production continuity.

[0014] Furthermore, the catalyst used in the catalytic combustion module includes a noble metal composite rare earth oxide catalyst and a rare earth composite oxide catalyst. The noble metal composite rare earth oxide catalyst has a broad spectrum of activity against organic waste gas and is used to catalyze the oxidation reaction of various organic waste gases; 2 High selectivity ensures high efficiency and environmental protection of waste gas treatment; has extremely high adhesion and wear resistance, firm coating, and active components do not fall off; long service life; size and shape can be customized;

[0015] The rare earth composite oxide catalyst uses rare earth elements as the main active component; has a low ignition temperature for oxygen-containing and nitrogen-containing organic waste gases, high catalytic activity, and complete combustion. 2 The selectivity is high; the coating is firm and the active components do not fall off; the size and shape can be customized.

[0016] Furthermore, the control room module adopts a programmable controller system PLC for centralized control and local control, specifically including:

[0017] The centralized control specifically includes:

[0018] The operator starts the system at the PLC operation station in the central control room. After receiving the start command, the PLC starts the power equipment in sequence according to the preset start sequence.

[0019] The operator monitors the operating parameters of the equipment in real time and records them through the monitoring interface of the PLC operation station to obtain monitoring data;

[0020] Adjust the control parameters according to the monitoring data obtained, and the PLC automatically adjusts the operating status of the equipment according to the set parameters;

[0021] The PLC performs fault processing and system shutdown based on the detected fault;

[0022] The local control is specifically as follows:

[0023] The operator issues a command on the control panel attached to the equipment, and the PLC starts the equipment after receiving the start command;

[0024] The operator directly adjusts the operating parameters of the equipment through the control panel, and the PLC responds and adjusts in real time and changes the operating status of the equipment;

[0025] The operator stops or shuts down the PLC controlled equipment by pressing the emergency stop button on the control panel.

[0026] Furthermore, the programmable controller system PLC controls temperature, pressure, flow, level and composition, specifically:

[0027] Temperature and pressure control adopts PID control algorithm, and the calculation formula is:

[0028]

[0029] Among them, u(t) is the output of the controller, e(t) is the error, that is, the difference between the set temperature and the actual temperature, the difference between the set pressure and the actual pressure, K p , K i , K d are the proportional, integral and differential coefficients respectively;

[0030] Flow control is achieved by adjusting the valve opening, and the calculation formula is:

[0031]

[0032] Among them, Q is the flow rate, C v is the valve flow coefficient, ΔP is the pressure difference on both sides of the valve;

[0033] Level control is carried out by adjusting the opening of the feed and discharge valves. The calculation formula is:

[0034] L=L 0 +∫Q in dt―∫Q out dt;

[0035] Among them, L is the current liquid level, L 0 is the initial liquid level, Q in is the feed flow rate, Q out is the discharge flow rate;

[0036] Composition control involves the balance of chemical reactions and the ratio of the mixture, calculated as:

[0037]

[0038] Where C is the concentration of the mixture component, m 1 , m 2 ,…,m n is the mass of each component and V is the total volume of the mixture.

[0039] The present invention also provides a RTO high temperature incineration method, specifically:

[0040] Step S1, collecting volatile organic compound (VOCs) waste gas;

[0041] Step S2, pre-treating the collected volatile organic compound (VOCs) waste gas, including setting up three-stage filtration to remove dust harmful to the rotor, and continuous adsorption to remove volatile organic compounds (VOCs) in the waste gas;

[0042] Step S3, sending the pre-treated waste gas containing volatile organic compounds (VOCs) into the RTO incinerator and heating it to above 700° C.;

[0043] Step S4: Volatile organic compounds (VOCs) in the exhaust gas undergo oxidation reaction with oxygen to generate CO 2 and H 2 O, and release heat;

[0044] Step S5, the high-temperature gas generated by the oxidation reaction flows through the ceramic heat storage body, causing the ceramic heat storage body to heat up and "store heat" for heat recovery;

[0045] Step S6, using the heated ceramic heat storage body to preheat the waste gas that will enter later, prepare for incineration, and reduce the fuel consumption for heating the waste gas;

[0046] Step S7, exhaust gas that reaches the emission mark is discharged.

[0047] Beneficial effects of the present invention: The RTO high-temperature incineration system provided by the present invention improves the processing efficiency and energy utilization rate by optimizing the heat recovery and waste gas treatment process. The waste gas is treated by the dust filtration module and the continuous adsorption module to adsorb the volatile organic compounds (VOCs) in the waste gas, reduce the emission of harmful substances, and reduce the pollution to the atmospheric environment.

[0048] The present invention adopts a new catalyst, which can reduce costs and improve processing efficiency through efficient catalyst technology, higher catalytic activity and operating life.

[0049] While treating the waste gas, the present invention can also recover part of the heat for preheating the waste gas entering the system or other process, thereby improving energy utilization efficiency and reducing operating costs. BRIEF DESCRIPTION OF THE DRAWINGS

[0050] Figure 1 It is a schematic diagram of the RTO high temperature incineration system of the present invention.

[0051] Figure 2 It is a schematic diagram of the catalyst shape.

[0052] Figure 3 It is a flow chart of the RTO high temperature incineration method. DETAILED DESCRIPTION

[0053] In the following description, a large number of specific details are provided to provide a more thorough understanding of the present invention. However, it is apparent to those skilled in the art that the present invention can be implemented without one or more of these details. In other examples, in order to avoid confusion with the present invention, some technical features well known in the art are not described.

[0054] The present invention provides a RTO high temperature incineration system, referring to Figure 1 , including a pretreatment system, an adsorption system, and a catalytic combustion system; the pretreatment system includes a surface cooler cooling module; the adsorption system includes a dust filtration module and a continuous adsorption module; the catalytic combustion system includes a waste heat utilization module, a power equipment module, a catalytic combustion module, a control room module, and a tool box module.

[0055] The pretreatment system includes a surface cooler cooling module, which effectively reduces the exhaust gas temperature through heat exchange between cooling water and exhaust gas, and cools the high-temperature exhaust gas for subsequent treatment.

[0056] The adsorption system includes a dust filtration module and a continuous adsorption module. The dust filtration module is a pre-treatment filter, which is equipped with three-stage filtration, including a primary filter G4 and medium-efficiency filters ACF, F7, and F9. The filter is equipped with a differential pressure gauge, which will give an alarm and replace the filter material in time when overpressure is detected; the pre-treatment filter is mainly used to remove dust that is harmful to the rotor.

[0057] The primary filter is used to remove particles larger than 5μm in the exhaust gas. When the resistance reaches the set value, it is taken out and replaced. It is used as a disposable product with a replacement cycle of about half a month.

[0058] The parameters of the primary G4 filter are: filtration efficiency is 95%, and the air volume is 3000m 3 / h, size is 595×595×46mm, initial resistance is 40Pa, final resistance is 250Pa;

[0059] The medium efficiency filter is used to remove particles of 1 to 5 μm in the exhaust gas. When the resistance reaches the set value, it is taken out and replaced. It is used as a disposable product with a replacement cycle of about 2 months. The parameters of the F7 / F9 filter used in the medium efficiency filter are:

[0060] name Filtration efficiency <![CDATA[Processing air volume (m 3 / h)]]> Dimensions (mm) Dosage (sheets) Initial resistance (Pa) ACF 95 3000 595×595×600 28 600 F7 Filter 90％ 3000 595×595×600 28 105 F9 Filter 90％ 3000 595×595×600 28 105

[0061] The continuous adsorption module can effectively remove volatile organic compounds (VOCs) from exhaust gas through continuous adsorption and regeneration processes, thereby improving the exhaust gas purification effect.

[0062] In this embodiment, through three-stage filtration including primary filter G4, medium filter ACF, F7, and F9, the system can effectively remove particulate matter of different particle sizes in the exhaust gas, remove dust that is harmful to the rotor, and protect the rotor in the continuous adsorption module from damage, thereby improving the purification efficiency and extending the service life of the equipment; the filter is provided with a differential pressure gauge, which can alarm when overpressure is detected to ensure timely replacement of the filter material and avoid system performance degradation due to filter clogging; the primary filter is replaced every half a month and the medium filter is replaced approximately every two months to regularly replace the filter to reduce system downtime caused by filter clogging and reduce maintenance costs; the continuous adsorption module effectively removes volatile organic compounds (VOCs) in the exhaust gas through continuous adsorption and regeneration processes, thereby improving the exhaust gas purification effect, and at the same time, it is possible to improve energy efficiency by optimizing the adsorption and regeneration processes.

[0063] In a further embodiment, the catalytic combustion system includes a waste heat utilization module, a power equipment module, a catalytic combustion module, a control room module, and a tool box module.

[0064] The power equipment module, including fans, pumps, and motors, ensures that exhaust gas flows smoothly in the system and maintains the normal operation of each module.

[0065] The toolbox module provides the necessary tools and spare parts for the maintenance and overhaul of the RTO high temperature incineration system through a complete toolbox configuration, ensuring that when a failure occurs or maintenance is required, it can be handled quickly, reducing downtime and ensuring production continuity.

[0066] The catalytic combustion module burns the organic pollutants in the exhaust gas at high temperatures under the action of a catalyst, converting them into harmless carbon dioxide and water, ensuring that the organic pollutants are completely decomposed, reducing energy consumption and secondary pollution. Figure 2In this embodiment, two types of catalysts are used: precious metal composite rare earth oxide catalyst and rare earth composite oxide catalyst. The precious metal composite rare earth oxide catalyst has high activity and a broad spectrum of activity against various organic waste gases. The combustion is thorough and the CO 2 The selectivity reaches more than 98%; the coating is firm and the active components do not fall off; the service life is long, and its normal operating life is more than 3 years; the honeycomb and particle size and shape can be customized. The rare earth composite oxide catalyst has low cost and is lower than the precious metal catalyst on the market; the catalyst has high activity, especially for oxygen-containing and nitrogen-containing organic waste gases, the ignition temperature is less than 200 degrees; the catalyst burns thoroughly and has no effect on CO 2 The selectivity reaches over 99%; the coating is firm and the active components do not fall off; the honeycomb and particle size and shape can be customized.

[0067] The waste heat utilization module allows the high-temperature airflow generated by oxidation to flow through the ceramic heat storage body to store heat. When the waste gas containing organic matter enters the RTO high-temperature incineration system, it first flows through the ceramic heat storage body, which releases the stored heat to heat it up and "storage heat", preheating the waste gas to a temperature close to that required for the oxidation reaction, and then the preheated waste gas enters the combustion chamber. The preheating module can save fuel consumption caused by the temperature rise of the waste gas and improve energy utilization efficiency.

[0068] In this embodiment, two types of catalysts, namely precious metal composite rare earth oxide catalysts and rare earth composite oxide catalysts, are used to promote the oxidation rate of organic pollutants and improve the exhaust gas purification efficiency. Since the temperature required for catalytic combustion is relatively low, the thermal stress on the internal materials of the RTO system can be reduced and the service life of the equipment can be extended. The waste heat utilization module recovers and stores heat in the high-temperature airflow through a ceramic heat storage body, releases heat before the exhaust gas enters the combustion chamber, and preheats the exhaust gas to a temperature close to that required for the oxidation reaction, thereby reducing the additional fuel consumed to reach the reaction temperature. By preheating the exhaust gas, the use of fuel is reduced and the operating cost is reduced.

[0069] In a further embodiment, the control room module adopts a programmable controller system PLC, which is equipped with centralized control and local control. It is responsible for power supply and automatic control of various power equipment in the exhaust gas treatment facility, real-time monitoring of system operating status and parameters, and timely adjustment of control strategies to ensure safe, stable and efficient operation of the system.

[0070] The specific operations of centralized control are:

[0071] The operator starts the system at the PLC operation station in the central control room. After receiving the start command, the PLC starts the power equipment in sequence according to the preset start sequence.

[0072] The operator monitors the operating parameters of the equipment in real time and records them through the monitoring interface of the PLC operation station to obtain monitoring data;

[0073] Adjust the control parameters according to the monitoring data obtained, and the PLC automatically adjusts the operating status of the equipment according to the set parameters;

[0074] The PLC performs fault processing and system shutdown based on the detected fault;

[0075] The specific operations of local control are:

[0076] The operator issues a command on the control panel attached to the equipment, and the PLC starts the equipment after receiving the start command;

[0077] The operator directly adjusts the operating parameters of the equipment through the control panel, and the PLC responds and adjusts in real time and changes the operating status of the equipment;

[0078] The operator stops or shuts down the PLC controlled equipment by pressing the emergency stop button on the control panel.

[0079] In a further embodiment, the programmable controller system PLC mainly controls temperature, pressure, flow, level, and composition, specifically:

[0080] Temperature and pressure control adopts PID control algorithm, and the calculation formula is:

[0081]

[0082] Among them, u(t) is the output of the controller, e(t) is the error, that is, the difference between the set temperature and the actual temperature, the difference between the set pressure and the actual pressure, K p , K i , K d are the proportional, integral and differential coefficients respectively;

[0083] Flow control is achieved by adjusting the valve opening, and the calculation formula is:

[0084]

[0085] Among them, Q is the flow rate, C v is the valve flow coefficient, ΔP is the pressure difference on both sides of the valve;

[0086] Level control is carried out by adjusting the opening of the feed and discharge valves. The calculation formula is:

[0087] L=L 0 +∫Q in dt―∫Q out dt;

[0088] Among them, L is the current liquid level, L 0 is the initial liquid level, Q in is the feed flow rate, Q outis the discharge flow rate;

[0089] Composition control involves the balance of chemical reactions and the ratio of the mixture, calculated as:

[0090]

[0091] Where C is the concentration of the mixture component, m 1 , m 2 ,…,m n is the mass of each component and V is the total volume of the mixture.

[0092] The PLC system of this embodiment helps to optimize the combustion process by accurately controlling parameters such as temperature, pressure, and flow. Based on the real-time monitoring of parameters such as temperature and pressure, once an abnormal situation is detected, an alarm can be immediately issued and corresponding measures can be taken to prevent equipment damage or safety accidents. The PLC system can also monitor the operating status of the RTO system in real time, adjust control parameters in a timely manner, ensure stable operation of the system, avoid system failures caused by parameter fluctuations, and use the recorded data to analyze the system operating status to help maintenance personnel discover potential problems in a timely manner.

[0093] The present invention also provides a RTO high temperature incineration method, the specific steps are:

[0094] Step S1, collecting volatile organic compound (VOCs) waste gas;

[0095] Step S2, pre-treating the collected volatile organic compound (VOCs) waste gas, including setting up three-stage filtration to remove dust harmful to the rotor, and continuously adsorbing through an adsorbent to remove volatile organic compounds (VOCs) in the waste gas and reduce the pollutant load entering the RTO;

[0096] Step S3, sending the pre-treated waste gas containing volatile organic compounds (VOCs) into the RTO incinerator and heating it to above 700° C.;

[0097] Step S4: Volatile organic compounds (VOCs) in the exhaust gas undergo oxidation reaction with oxygen to generate CO 2 and H 2 O, and release heat;

[0098] Step S5, the high-temperature gas generated by the oxidation reaction flows through the ceramic heat storage body, causing the ceramic heat storage body to heat up and "storage" heat for heat recovery;

[0099] Step S6, using the heated ceramic heat storage body to preheat the waste gas that enters later to prepare for incineration, thereby reducing the extra fuel consumption when the waste gas reaches the temperature required for the oxidation reaction and improving energy utilization efficiency;

[0100] Step S7, exhaust gas that reaches the emission mark is discharged.

[0101] In this embodiment, the pretreatment stage removes dust that is harmful to the rotor, protects the key components of the continuous adsorption module and the RTO incinerator, and extends the service life of the equipment; the ceramic heat storage body is used to recover and utilize the heat in the exhaust gas for preheating the subsequent exhaust gas, thereby reducing fuel consumption, improving energy utilization efficiency, and reducing the operating cost of the RTO system; the method provided in this embodiment removes VOCs in the exhaust gas, and the RTO system helps to reduce pollution to the atmospheric environment and plays a huge role in environmental protection.

[0102] As described above, although the present invention has been shown and described with reference to specific preferred embodiments, it should not be construed as limiting the present invention itself. Various changes may be made to it in form and detail without departing from the spirit and scope of the present invention as defined in the appended claims.

Claims

1. An RTO high temperature incineration system, characterized in that: include: Pretreatment system, adsorption system, catalytic combustion system; The pretreatment system includes a surface cooler cooling module; the adsorption system includes a dust filtration module and a continuous adsorption module; The catalytic combustion system includes a waste heat utilization module, a power equipment module, a catalytic combustion module, a control room module, and a tool box module; The surface cooler cooling module effectively reduces the exhaust gas temperature through heat exchange between cooling water and exhaust gas, and cools the high-temperature exhaust gas for subsequent treatment; The dust filtration module is provided with three-stage filtration, including a primary filter and a medium filter, which are used to remove dust harmful to the rotor, ensure that the dust content in the exhaust gas meets environmental protection standards, and reduce pollution to the environment; The continuous adsorption module effectively removes volatile organic compounds (VOCs) in the exhaust gas through continuous adsorption and regeneration processes, thereby improving the exhaust gas purification effect; The waste heat utilization module, the high-temperature airflow generated by oxidation flows through the heat storage body, so that it heats up and "storages heat", and is used to preheat the subsequent organic waste gas, so as to save fuel consumption caused by the waste gas heating and improve energy utilization efficiency; The power equipment modules include fans, pumps, and motors to ensure smooth flow of exhaust gas in the system and maintain normal operation of each module; The catalytic combustion module burns the organic pollutants in the exhaust gas at high temperature under the action of a catalyst, converting them into harmless carbon dioxide and water, ensuring that the organic pollutants are completely decomposed, reducing energy consumption and secondary pollution; The control room module adopts a programmable controller system PLC, which is equipped with centralized control and local control. It is responsible for power supply and automatic control of various power equipment in the exhaust gas treatment facility, real-time monitoring of system operation status and parameters, and timely adjustment of control strategies to ensure safe, stable and efficient operation of the system; The toolbox module, through a complete toolbox configuration, provides the necessary tools and spare parts for the maintenance and overhaul of the RTO high temperature incineration system, ensuring that when a failure occurs or maintenance is required, it can be handled quickly, reducing downtime and ensuring production continuity.

2. The RTO high temperature incineration system according to claim 1, characterized in that: The catalyst used in the catalytic combustion module includes a precious metal composite rare earth oxide catalyst and a rare earth composite oxide catalyst. The precious metal composite rare earth oxide catalyst has a broad spectrum of activity to organic waste gas and is used to catalyze the oxidation reaction of various organic waste gases. It has high selectivity to CO2, ensuring the high efficiency and environmental protection of waste gas treatment. It has extremely high adhesion and wear resistance, a firm coating, and active components do not fall off. It has a long operating life and can be customized in size and shape. The rare earth composite oxide catalyst uses rare earth elements as the main active component; has a low ignition temperature for oxygen-containing and nitrogen-containing organic waste gases, high catalytic activity, complete combustion, and high selectivity for CO2; The coating is strong and the active components will not fall off; the size and shape can be customized.

3. The RTO high temperature incineration system according to claim 1, characterized in that: The control room module adopts a programmable controller system PLC for centralized control and local control, specifically including: The centralized control specifically includes: The operator starts the system at the PLC operation station in the central control room. After receiving the start command, the PLC starts the power equipment in sequence according to the preset start sequence. The operator monitors the operating parameters of the equipment in real time and records them through the monitoring interface of the PLC operation station to obtain monitoring data; Adjust the control parameters according to the monitoring data obtained, and the PLC automatically adjusts the operating status of the equipment according to the set parameters; The PLC performs fault processing and system shutdown based on the detected fault; The local control is specifically as follows: The operator issues a command on the control panel attached to the equipment, and the PLC starts the equipment after receiving the start command; The operator directly adjusts the operating parameters of the equipment through the control panel, and the PLC responds and adjusts in real time and changes the operating status of the equipment; The operator stops or shuts down the PLC controlled equipment by pressing the emergency stop button on the control panel.

4. The RTO high temperature incineration system according to claim 1, characterized in that: The programmable controller system PLC controls temperature, pressure, flow, level and composition, specifically: Temperature and pressure control adopts PID control algorithm, and the calculation formula is: Among them, u(t) is the output of the controller, e(t) is the error, that is, the difference between the set temperature and the actual temperature, the difference between the set pressure and the actual pressure, K p , K i , K d are the proportional, integral and differential coefficients respectively; Flow control is achieved by adjusting the valve opening, and the calculation formula is: Among them, Q is the flow rate, C v is the valve flow coefficient, ΔP is the pressure difference on both sides of the valve; Level control is carried out by adjusting the opening of the feed and discharge valves. The calculation formula is: L=L0+∫Q in dt―∫Q out dt; Among them, L is the current liquid level, L0 is the initial liquid level, Q in is the feed flow rate, Q out is the discharge flow rate; Composition control involves the balance of chemical reactions and the ratio of the mixture, calculated as: Where C is the concentration of the components of the mixture, m1, m2, ..., m n is the mass of each component and V is the total volume of the mixture.

5. A RTO high temperature incineration method, characterized in that: Specifically: Step S1, collecting volatile organic compound (VOCs) waste gas; Step S2, pre-treating the collected volatile organic compound (VOCs) waste gas, including setting up three-stage filtration to remove dust harmful to the rotor, and continuous adsorption to remove volatile organic compounds (VOCs) in the waste gas; Step S3, sending the pre-treated waste gas containing volatile organic compounds (VOCs) into the RTO incinerator and heating it to above 700° C.; Step S4, volatile organic compounds (VOCs) in the exhaust gas undergo an oxidation reaction with oxygen to generate CO2 and H2O, and release heat; Step S5, the high-temperature gas generated by the oxidation reaction flows through the ceramic heat storage body, causing the ceramic heat storage body to heat up and "store heat" for heat recovery; Step S6, using the heated ceramic heat storage body to preheat the waste gas that will enter later, prepare for incineration, and reduce the fuel consumption for heating the waste gas; Step S7, exhaust gas that reaches the emission mark is discharged.

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