76 results about "Thermochemical reaction" patented technology

A thermochemical reactor for receiving a source of atmospheric carbon dioxide and reducing the atmospheric carbon dioxide is provided. In one or more embodiments, the thermochemical reactor may be part of an atmospheric carbon capture system that includes a solid sorbent and an exchange fluid that is cycled between the solid sorbent and the thermochemical reactor.

The invention provides a tip Raman-based metal oxide nanoparticle in-situ detection method, which comprises: S1, dispersing metal oxide nanoparticles in a nanoparticle dispersion liquid, focusing laser to the tip of a nanometer tip through an objective lens, capturing a single nanoparticle by using an optical tweezers technology, and attaching the single nanoparticle to the nanometer tip; s2, focusing Raman laser on a nano needle tip-particle interface, generating a local high-temperature field through a photo-thermal near-field coupling effect, triggering a thermal chemical reaction of nano particles, and synchronously collecting a Raman spectrum; and S3, carrying out pretreatment and characteristic peak analysis on the collected Raman signal of the Raman spectrum, and determining the reaction critical temperature and the dynamic process in combination with temperature calibration data. According to the invention, capture and accurate heating of the nanoparticles are realized through photo-thermal coupling of the optical tweezers and the needle tip, and thermal chemical reaction monitoring of the nanoparticles is realized.

The invention discloses a cabin multi-dimensional fire simulation method and system for fire personnel training, and the method comprises the steps: carrying out the modeling of a cabin, generating a digital twinborn body of the cabin, carrying out the initialization, and constructing a thermal fluid dynamic field, the digital twinborn body comprises a cabin geometric structure, a combustible material distribution condition and a linkage control interface of fire fighting equipment, and the cabin geometric structure is divided into a plurality of grids; fire information is obtained in real time through a sensor arranged in a cabin and mapped to the corresponding position of the digital twinborn body, a dynamic fire evolution cognitive model used for describing dynamic fire evolution is set, and the dynamic fire evolution cognitive model comprises a thermochemical reaction potential operator and a space coupling operator of flame propagation; and simulating the combustion condition of each grid through a dynamic fire evolution cognitive model, generating a final digital twinborn body, mapping the final digital twinborn body to virtual reality equipment, and completing fire training in a cabin by a user through the virtual reality equipment.

The application discloses a medical waste pyrolysis system and a pyrolysis method based on low-temperature pyrolysis, which comprises a pyrolysis furnace, one end of the pyrolysis furnace is connected with a feeding unit, the other end of the pyrolysis furnace is connected with a slag discharging unit, the front end and the rear end of the pyrolysis furnace are respectively connected with a front distributor and a rear distributor, and the gas outlet of the front distributor and / or the rear distributor is connected with a burner; the burner is connected with the pyrolysis furnace for providing heat; and the burner is connected with a tail gas treatment device through a waste heat boiler. The medical waste is indirectly heated under an oxygen-free or oxygen-deficient working condition, the continuous endothermic and exothermic reactions are utilized, the organic components in the medical waste are subjected to thermal cracking and thermal chemical reactions, the original molecular structure is changed, the medical waste is changed into different phase-state substances, pyrolysis gas and pyrolysis carbon are generated, the continuous pyrolysis treatment of the medical waste is realized, the heat is recycled, and the cost is reduced; and the system has high comprehensive heat energy utilization rate and high waste resource utilization rate.

The invention discloses a lithium battery thermal runaway early detection device and method based on gas spectrum analysis, and relates to the technical field of thermal runaway detection.A miniature gas sampling channel is arranged in a lithium battery pack or near a single battery cell, gas drainage is configured, gas released in the battery operation process is sampled, and gas sample data is obtained; according to the method, a multi-stage gas spectral analysis process is constructed, multi-dimensional spectral characteristics such as spectral peak intensity, spectral position offset and full width at half maximum are extracted from trace release gas collected in the running process of the lithium battery, a thermal runaway risk vector is constructed, and the thermal runaway risk vector is input into a thermal runaway recognition model MOD for real-time risk judgment. The early thermal chemical reaction process in the battery is effectively identified, the pre-judgment of the thermal runaway trend is completed in advance, the early warning of the thermal runaway state of the lithium battery is realized, the preposition of the system response and the safety protection level are improved, and the overall safety performance and reliability of the battery pack are improved.

The application discloses a high-flux heat exchange device based on a thermo-chemical reaction auxiliary, which comprises a heat exchange chamber and a chemical phase change working medium. The chemical phase change working medium comprises a liquid cooling base fluid and a reversible thermal decomposition solute. The thermal decomposition temperature threshold of the reversible thermal decomposition solute is lower than the physical boiling point of the liquid cooling base fluid under the current environment. When the temperature or pressure of the heat exchange surface reaches the thermal decomposition temperature threshold, the reversible thermal decomposition solute undergoes an endothermic decomposition reaction on the heat exchange surface, rapidly generates a large number of non-condensable bubbles and high-frequency separates, thereby triggering strong local micro-convection disturbance of the fluid and absorbing a large amount of chemical decomposition heat, and finally achieving heat dissipation of the heating element. The application accelerates the transfer of wall heat by using a thermo-chemical reaction, and improves the separation rate of bubbles at the solid-liquid interface, breaks the engineering resistance that bubbles are difficult to nucleate and efficiently separate in traditional boiling heat transfer, and realizes rapid and large absorption and transfer of the combined chemical reaction heat of the solute and the latent heat of vaporization of the base fluid.

The invention provides a light energy-electric energy-chemical energy coupling coal-fired unit system and an operation system. The system comprises a coal-fired power generation subsystem, a photovoltaic-thermochemistry subsystem and a Kalina circulation subsystem. The coal-fired power generation subsystem is connected with the photovoltaic-thermochemistry subsystem, and the photovoltaic-thermochemistry subsystem is connected with the Kalina circulation subsystem; the coal-fired power generation subsystem is used for basic power generation and peak regulation of the whole system; the photovoltaic-thermochemistry subsystem is used for converting solar energy into electric energy through a photovoltaic device and driving a reversible thermochemistry device based on a calcium-based compound by using the electric energy, so that conversion and storage of electric energy-heat energy-chemical energy are realized; the Kalina circulation subsystem is used for waste heat utilization of thermal chemical reaction products. The heat storage / release temperature is matched with the coal-fired system through thermochemical reaction pressure regulation and control, dynamic regulation of the Kalina cycle working medium concentration is combined, the irreversible loss of heat transfer is remarkably reduced, and the comprehensive energy utilization efficiency is improved.

The invention discloses an electricity-heat-hydrogen comprehensive energy system based on thermochemical energy storage, which is characterized in that an outlet of a thermodynamic cycle system is communicated with an inlet of a steam turbine, a steam extraction opening of the steam turbine is communicated with a shell side inlet of a thermochemical reactor, a shell side outlet of the thermochemical reactor is communicated with an inlet of a solid oxide electrolytic tank, and a shell side outlet of the solid oxide electrolytic tank is communicated with a shell side outlet of the steam turbine; a hydrogen outlet of the solid oxide electrolytic tank is communicated with an inlet of the hydrogen storage tank, an oxygen outlet of the solid oxide electrolytic tank is communicated with an inlet of the oxygen storage tank, an outlet of the hydrogen storage tank is communicated with an inlet of the combustion chamber, an outlet of the oxygen storage tank is communicated with an inlet of the combustion chamber, and an outlet of the combustion chamber is communicated with an inlet of the steam turbine. By means of the system, a unit can better absorb new energy for power generation, and stable operation of a power grid is kept.

The application provides a parallel solar photo-thermal chemical coupling lunar surface resource utilization system and method, which mainly comprises a solar light condensing and heat collecting system, a solar light splitter, a thermal chemical reactor, a photochemical reactor, a lunar soil-based thermal chemical circulation oxygen carrier material, a lunar soil-based photochemical catalyst, a heat recovery regulation unit and a vacuum collector. The solar light condensing and heat collecting system and the solar light splitter converge the sunlight irradiated on the lunar surface and supply the sunlight to the thermal chemical reaction and the photochemical reaction, respectively. The high-temperature waste heat of the thermal chemical part is distributed by the heat recovery regulation unit, water decomposition for hydrogen and oxygen production and metal material acquisition are realized by using the lunar soil material, and lunar resource acquisition and efficient utilization are realized.

This invention discloses a method for controlling the energy flux density distribution of a concentrating solar furnace device. The method includes: constructing an optical system model of the concentrating solar furnace device; determining an energy flux density distribution control model based on the optical system model, according to the cross-offset parameter within the light focusing point of the reactor, the position parameter of the heat-absorbing platform where the reactor is located, and the curvature parameter of the concentrating mirror; determining control parameters of the concentrating solar furnace device based on the energy flux density distribution control model, according to the set target region size, the peak energy flux control range within the target region, and the range of non-uniformity factors of the energy flux distribution within the target region, combined with the direct normal irradiance (DNI) parameter; the target region is the preset area to be focused by the reflected light; and controlling the operating state of the corresponding components of the concentrating solar furnace device according to the control parameters. This invention solves the problem that existing control methods are insufficient to achieve the desired control of thermochemical reaction products.

A solar concentrator reactor system and method of use for high temperature thermochemical processes. In one embodiment, the solar concentrator reactor system produces a thermochemical reaction of irradiated particles within an enclosed vessel volume of a solar concentrator reactor. In one aspect, the solar concentrator reactor system uses a solar concentrator to irradiate particles of a particle stream within an enclosed vessel volume of a solar concentrator reactor. The thermochemical reaction yields a chemical change of the feedstock and / or phase transition of the feedstock such as the production of a molten reacted material from a solid particulate feed. In one embodiment, the particles are a lunar regolith and the thermochemical reaction yields oxygen.

An outlet of a first feed pump is divided into two paths after passing through a heat exchange tube in a thermochemical reactor, one path is communicated with a steam inlet of a reversible solid oxide fuel cell, and the other path is communicated with an inlet of the heat exchange tube in the reversible solid oxide fuel cell; an outlet of a heat exchange pipe in the reversible solid oxide fuel cell is communicated with a water tank through a second water feeding pump, an oxygen outlet of the reversible solid oxide fuel cell is communicated with an oxygen storage tank, and a hydrogen outlet of the reversible solid oxide fuel cell is communicated with a hydrogen storage tank; an outlet of the first water feeding pump is communicated with a shell side opening of the thermochemical reactor, the steam storage tank is communicated with the shell side opening of the thermochemical reactor, the steam storage tank is communicated with a heat exchange pipe in the reversible solid oxide fuel cell, and the power grid is communicated with a power interface of the reversible solid oxide fuel cell. The system can realize waste heat utilization of the reversible solid oxide fuel cell, and meanwhile, the peak regulation capability of the power grid is improved.

The invention relates to the technical field of thermochemical reaction testing equipment, and provides a microreactor device capable of realizing high temperature and high pressure and a manufacturing method thereof. The microreactor device capable of realizing high temperature and high pressure comprises a corundum microreactor, the corundum microreactor is a corundum tube, a porous ceramic air distribution plate and aluminum oxide particles for preheating are arranged in the corundum tube, two ends of the corundum tube are hermetically connected through flanges and sealing rings, and the aluminum oxide content of the corundum tube is greater than 99%; the heating assembly is arranged outside the alundum tube in a sleeving mode, and the heating assembly comprises heating elements attached to the periphery of the outer wall of the alundum tube, a heat preservation layer wrapping the outer sides of the heating elements and a shell; the top explosion-proof cover covers the top of the heating assembly; the bottom explosion-proof cover covers the bottom of the heating assembly; and a plurality of heat dissipation holes are formed in the top explosion-proof cover and the bottom explosion-proof cover. The device disclosed by the invention has the advantages of good temperature-pressure cooperation performance, compact structure, high safety, low cost and the like.

One or more reactants are flowed into thermal contact with a heating element in a reactor for a first time period. During a first part of a heating cycle, the one or more reactants are provided with a first temperature by heating with the heating element, such that one or more thermochemical reactions is initiated. The one or more thermochemical reactions includes pyrolysis, thermolysis, synthesis, hydrogenation, dehydrogenation, hydrogenolysis, or any combination thereof. The first heating element operates by Joule heating and has a porous construction that allows gas to flow therethrough. During a second part of the heating cycle, the one or more reactants are provided with a second temperature less than the first temperature, for example, by de-energizing the heating element. A duration of the first time period is equal to or greater than a duration of the heating cycle, which is less than five seconds.

The invention discloses a method for treating coffee beans through combination of freezing and dipping and flavor coffee beans produced through the method. The method comprises the following steps: grading and screening coffee beans, mixing the coffee beans with exogenous additives (such as coconut milk, pure milk and the like) according to a ratio of (1-1.11): 1, freezing at-20 DEG C for 20-30 hours, unfreezing and soaking at 25 DEG C for 16 hours, then drying until the water content is 10-12%, and finally baking at 190-210 DEG C until the Eilkstrong value is 35. According to the working principle, the structure of coffee beans is destroyed through low temperature, exogenous additives enter the coffee beans, the content of flavor precursors is changed, the baking thermal chemical reaction is affected, and meanwhile the exogenous additives give unique fragrance. Coconut milk treatment is taken as an example, the content of sugar and protein can be increased, fragrance and sweetness can be improved, bitter and sour feeling can be reduced, and coffee with mellow and balanced coconut fragrance can be obtained. The method can effectively improve coffee quality and produce coffee beans with brand new flavor.

In accordance with the purpose(s) of the present disclosure, as embodied and broadly described herein, the disclosure, in one aspect, relates to methods, compositions, and systems for conducting efficient thermochemical reactions to produce a product, e.g., the production of ethylene and NH3 from CH4 / N2. The disclosed methods comprise a non-equilibrium, continuous synthesis method that uses microwave pulsed heating to drive a thermochemical process. The disclosed methods allow for switching between endothermic and exothermic reactions in one continuous process or within a single system. Also disclosed are compositions, i.e., catalysts, useful in the disclosed methods, and devices or systems for carrying out the disclosed methods.

The application discloses a landfill leachate treatment method based on coal water slurry gasification, which comprises the following steps: landfill leachate pretreatment, mixed coal powder preparation, composite coal water slurry preparation and gasification. The application has the beneficial effects that the viscosity, concentration, stability and heat value of the coal water slurry prepared under certain conditions reach the requirements of industrial coal water slurry. The composite coal water slurry is subjected to gasification reaction, the organic pollutants in the landfill leachate are subjected to thermochemical reaction, carbon and gas are formed and are high-valued, and the heavy metals in the landfill leachate are effectively solidified by chelation with the carbon. Compared with the original landfill leachate, the COD, ammonia nitrogen, total phosphorus, total nitrogen and turbidity in the obtained liquid phase product are greatly reduced, and the pH is reduced to below 9.0. The toxic and harmful components in the landfill leachate are stably and safely disposed, and a large amount of water resources is saved, and the obtained liquid phase product can be recycled to a coal water slurry preparation unit for secondary utilization.

The invention discloses a thermochemical reactor and an integrated thermochemical reaction system and method.The thermochemical reactor comprises a shell, a plurality of reaction modules are arranged in the shell, a plurality of material channels are formed in the reaction modules, and the material channels are filled with thermochemical materials; according to the system and the method, the requirements of flexible configuration of energy storage capacity and power can be met, and meanwhile, the heat transfer and exchange efficiency is relatively high.

The invention discloses a closed multiphase thermochemical resource reconstruction platform and a treatment method thereof, and relates to the field of solid waste resource treatment. The solid waste receiving and treating unit pretreats solid waste and conveys the solid waste in a closed manner; the closed controlled thermochemical reaction unit applies set temperature, pressure and atmosphere conditions to the pretreated solid waste in a closed space, a multi-phase medium is introduced, the pretreated solid waste is subjected to thermochemical reconstruction, and the physical property difference between different components is amplified to obtain a resource product; the multiphase product flow separation unit performs one or more post-treatments on the recycling product to obtain at least two product flows with different phase states or different components; the monitoring and cooperative control unit is used for collecting one or more of temperature, pressure, atmosphere composition, flow and separation end indexes in the reaction and separation process, and regulating and controlling the closed controlled thermal chemical reaction unit and the multiphase product flow separation unit in a linkage manner, so that efficient, stable and resource recycling of various solid wastes is realized.

The present application belongs to the technical field of electric heating experimental analysis instrument, and discloses a high-temperature and high-pressure micro fluidized bed thermochemical reaction measuring device, which comprises a high-pressure gas distribution device, a high-pressure pulse sampling device, a high-temperature and high-pressure reactor and an analysis and detection device, one end of the high-pressure pulse sampling device is connected with the high-pressure gas distribution system, the other end is connected with the high-temperature and high-pressure reactor through a high-pressure sampling pipe, the high-pressure gas distribution device is connected with the high-temperature and high-pressure reactor through a high-pressure gas inlet pipe, and the analysis and detection device comprises a filter, a back pressure valve and a mass spectrum which are connected in sequence along the airflow direction. The present application can realize the separate control of temperature and pressure, the internal pressure can be real-time regulated through the back pressure valve and the gas inlet pressure relief valve, the temperature is controlled by a separate temperature control system, the two key reaction conditions of temperature and pressure are decoupled, and the thermochemical reaction analysis and measurement under various reaction conditions such as low temperature and high pressure, high temperature and low pressure and high temperature and high pressure can be realized.

The present invention relates to a method and device for producing hydrogen by dissociating the water molecule through thermochemical reactions, using a small amount of active material. The thermochemical reactions are induced by solar energy with a moderate concentration of up to 50 suns, which can be achieved through linear or parabolic concentrators.

This invention relates to the field of electrochemical material preparation technology, specifically disclosing an apparatus for large-scale manufacturing of high-performance water electrolysis electrodes using the Joule heating effect. The apparatus includes a frame body, an unwinding roller, a winding roller, and a conductive carrier conveyor belt transporting the materials. A spraying unit, a pre-drying unit, and a Joule heating unit are sequentially arranged along the conveyor belt's movement direction. The Joule heating unit includes a first conductive roller and a second conductive roller electrically connected to the positive and negative terminals of a DC power supply, respectively. When the second conductive roller contacts the moving conductive carrier conveyor belt, current flows through the conveyor belt, generating Joule heat and inducing a thermochemical reaction in the precursor loaded on its surface. This apparatus achieves integrated, streamlined operation from spraying and pre-drying to high-temperature reaction. Simultaneously, the direct, instantaneous, and localized heating method based on the Joule effect significantly reduces heat loss and promotes in-situ reaction and firm bonding of the catalyst precursor on the conductive carrier surface, effectively improving the electrode's catalytic activity and long-term stability.

The embodiment of the invention provides a coal-fired unit system coupling a thermochemical reactor and Carnot battery energy storage and an operation method. The system comprises a coal-fired power generation subsystem, a thermochemical subsystem and a Carnot battery subsystem. The coal-fired power generation subsystem is connected with the thermochemical subsystem through a fixed bed reactor and a reaction water evaporator, and the coal-fired power generation subsystem is connected with the Carnot battery subsystem through a heat pump low-temperature heat exchanger and a heat engine low-temperature heat exchanger; the coal-fired power generation subsystem is used for heating feed water and generating power, the thermochemistry subsystem is used for storing heat and heating reheated steam, and the Carnot battery subsystem is used for storing heat and heating feed water. According to the system, the thermochemical heat storage subsystem and the Carnot battery subsystem cooperatively operate in different temperature zones, layered storage and release are conducted on main steam high-grade latent heat and reheat steam medium-temperature sensible heat, and gradient utilization of heat energy is achieved.

The invention relates to the technical field of nuclear energy-light energy coupling hydrogen production, and discloses a nuclear energy coupling photocatalytic water splitting hydrogen production system and a hydrogen production method. The nuclear energy coupling photocatalytic water splitting hydrogen production system comprises a photocatalytic reaction unit used for decomposing an aqueous solution containing a sacrificial agent under the action of a photocatalyst to produce hydrogen; the thermal chemical reaction unit is connected with the photocatalytic reaction unit and is used for receiving ammonium sulfate generated by the photocatalytic reaction and performing thermal chemical decomposition to generate oxygen; the gas absorption and regeneration unit is connected with the thermochemical reaction unit and is used for absorbing and regenerating gas generated by thermochemical decomposition into a sacrificial agent and returning the sacrificial agent to the photocatalytic reaction unit; and the nuclear energy heat supply unit is used for providing heat required by reaction for the thermal chemical reaction unit. Solar energy and nuclear energy are efficiently cooperated, the hydrogen purity is larger than or equal to 99.9%, the comprehensive energy efficiency of the system is larger than or equal to 85%, the problem of consumption of a traditional photocatalytic sacrificial agent is solved, and a new path is provided for large-scale production of green hydrogen.

The invention discloses a heat storage and release integrated calcium-based thermal chemical reaction system which comprises a reactor, and a heating assembly and a circulating water layer are arranged between the inner cylinder wall and the outer cylinder wall of the reactor; the steam structure comprises a steam generator and a water tank, the water tank is connected with the steam generator, and the steam generator is connected with the steam inlet in the reactor through a steam input valve and a pipeline; the heat recovery structure comprises a first heat recovery assembly and a second heat recovery assembly, and the first heat recovery assembly is used for recovering heat in the circulating water layer; the second heat recovery assembly is used for recovering heat in the reactor; the heat recovery structure is connected with the steam structure; the stirring structure comprises a rotating shaft, a bracket and a spiral square tube stirrer. According to the heat storage and release integrated rotary kiln type reactor structure, the integrated device design of heat storage and heat release circular reaction is integrated in the same rotary kiln body, and seamless switching between energy storage and energy release is achieved; a built-in stirring structure is used for forcibly dispersing particles, inhibiting sintering and strengthening reaction uniformity.

A process and a related plant for decomposing ammonia and synthesizing a hydrogen-rich process stream by a direct cooling performed downstream of the decomposition reactor with a stream consists of, or essentially consists of, nitrogen and / or ammonia, where the decomposition of ammonia takes place in a thermal or autothermal chemical reactor.

The oxygen-control low-nitrogen air-cooled gas hot blast stove comprises a stove body and a combustor, the combustor is provided with a gas pipe and a combustion-supporting air pipe, the gas pipe is provided with an electric V-shaped ball valve and a turbine flowmeter, the combustion-supporting air pipe is provided with an electric V-shaped ball valve, an air flowmeter and a frequency conversion fan which are matched with a combustion-supporting air pipe, and the turbine flowmeter is provided with a turbine flowmeter. The furnace body is divided into an outer cylinder and an inner cylinder, a gas inlet pipe, a gas outlet pipe and a tail gas pipe are arranged on the furnace body, and the tail gas pipe is connected with the combustor. The electric V-shaped ball valves and the flow meters are arranged on the gas pipe and the combustion-supporting gas pipe on the combustor, so that the ratio of gas fuel to combustion-supporting air is strictly controlled according to the air amount needed by combustion, excessive air is reduced to the complete combustion limit, when gas is fully combusted, the gas and the supplied air generate a violent thermal chemical reaction, and the combustion effect is improved. O2 in the air is basically exhausted, so that low-oxygen and oxygen-controlled combustion in the whole process is realized.

The utility model discloses a partition reaction device for a calcium hydroxide solution in reversible thermal chemical reaction. The partition reaction device comprises a plurality of partition reaction tubes which are arranged in an array, one end of the partitioned reaction pipe is connected with a calcium hydroxide mixed solution conveying pipe, so that the calcium hydroxide mixed solution is conveyed into the partitioned reaction pipe for continuous exothermic reaction; the other end of the partition reaction pipe is connected with a calcium hydroxide mixed liquid recovery pipe; a cold water pipe and a hot water pipe are further arranged on the partition reaction pipe, cold water is guided into the partition reaction pipe through the cold water pipe for heat exchange, hot water is recycled from the hot water pipe, and continuous heat exchange is formed; compared with an integrated reaction tank, the reaction tank disclosed by the utility model has the advantages that the efficiency of partitioned exothermic reaction is higher, and heat energy can be supplied more quickly; and partial partition reaction pipes can be opened, so that a small amount of hot water is output, and waste is avoided.

The invention relates to a method for extracting unconventional oil and to a complex for the implementation thereof. The method comprises injecting oxygen into an oil-bearing formation through injection-production wells, igniting the oil in the vicinity of an injection well, and displacing the oil toward production wells in an injection-production well cluster. Water is injected into the injection wells along with the oxygen, creating within the formation a pressure of the medium which is higher than that supercritical for water. A movable cloud of water in a supercritical state is formed at the well bottom. The combustion zone and the supercritical water cloud are induced to move through the oil-bearing formation from a depleted well to the next well. As the supercritical water cloud moves, it carries out thermochemical reactions, extracting hydrocarbons into itself and directing these hydrocarbons into the production wells to be brought to the surface. Oil recovery and the movement of the cloud are effectuated from the deepest wells. Having a cluster of injection-production wells that are hydrodynamically connected to one another makes it possible to sweep oil-bearing formations that extend over a large area, since the supercritical water cloud can be made to move from one injection-production well to another by changing the ratio of the flow rates of the water and the oil products in individual injection-production wells.

The invention discloses a solid waste synergistic thermochemical conversion integrated control system and method, and relates to the technical field of solid waste energy utilization. Comprising a raw material gas loading module, a magnetic traction feeding and heating module, a magnetic traction discharging and cooling module, a liquid-phase product online collection module and a pyrolysis gas automatic storage and monitoring module. When the system runs, inert gas or reaction gas is introduced into the pyrolyzing furnace; the solid waste is fed into the pyrolyzing furnace for a thermal chemical reaction through the magnetic traction feeding heating module; gas generated in the initial stage of pyrolysis enters a pyrolysis gas automatic storage and monitoring module for online analysis; a liquid product generated in the reaction is subjected to online acquisition and analysis through a liquid-phase product online collection module; and after the reaction is finished, discharging and cooling are performed through a magnetic traction discharging and cooling module. The whole process is automatically controlled by a PLC, and collaborative acquisition and real-time analysis of gas, liquid and solid products in the solid waste pyrolysis process can be achieved.