High-temperature and high-pressure reaction system

Abstract

The invention relates to a high-temperature and high-pressure reaction system which mainly comprises a reactor, a storage tank, a high-pressure separator and waste gas treatment equipment, the storage tank is connected with a first feeder and a second feeder, the first feeder and the second feeder are connected with the reactor, the reactor is connected with a heat regenerator, and the heat regenerator is connected with the high-pressure separator. The heat regenerator is respectively connected with the preheater and the cooler, the preheater is provided with a plurality of electric heating belts and is connected with the reactor, the cooler is connected with the high-pressure separator, and the high-pressure separator is respectively connected with the gas-liquid separator and the waste gas treatment equipment. The reaction reaches a high-temperature and high-pressure state by adjusting the temperature and the pressure, so that the reaction rate and the selectivity are improved. In the aspect of preparing the energy-saving gas, the system can convert organic matters, mineral substances and chemical substances into the energy-saving gas by utilizing the characteristics of high-temperature and high-pressure reaction, so that efficient energy preparation is realized.

Description

Technical Field

[0001] This invention belongs to the technical field of energy-saving gas reaction system preparation, and specifically relates to a high-temperature and high-pressure reaction system. Background Technology

[0002] Methods for preparing energy-saving gases typically require reactions under high temperature and high pressure conditions. Traditional methods often fail to adequately treat, recover, or convert waste gases and solvents generated during the reaction process, resulting in low reaction efficiency, high energy consumption, and severe environmental pollution. Therefore, a highly efficient, economical, and environmentally friendly reaction system is needed to address these issues. Summary of the Invention

[0003] The purpose of this invention is to solve the above-mentioned problems. This application proposes a high-temperature and high-pressure reaction system that utilizes high-temperature and high-pressure conditions to process organic matter, minerals and chemical substances, thereby achieving efficient, energy-saving and environmentally friendly preparation of energy-saving gases.

[0004] To achieve the above objectives, the present invention provides the following technical solution: a high-temperature and high-pressure reaction system, comprising several accumulators, a high-pressure water pump, a high-pressure flushing pump, a high-pressure feed pump, a reactor, a storage tank, a high-pressure separator, and waste gas treatment equipment; the high-pressure water pump is connected to the accumulator, and the accumulator is connected to a regenerator; a pressure controller, a flow meter, a check valve, and a pneumatic ball valve are provided between the accumulator and the regenerator; the high-pressure flushing pump is connected to the accumulator, and the accumulator is connected to the regenerator and a first feeder and a second feeder respectively; a pressure controller, a check valve, and a pneumatic ball valve are provided between the accumulator and the regenerator and the first and second feeders; the high-pressure feed pump is connected to the accumulator, and the accumulator is connected to the first and second feeders; a pressure controller, a flow meter, a check valve, and a pneumatic ball valve are provided between the accumulator and the first and second feeders. The storage tank is connected to the first feeder and the second feeder. The first feeder and the second feeder are connected to the reactor. The reactor is connected to the regenerator. The regenerator is connected to the preheater and the cooler respectively. The preheater is equipped with several electric heating belts and is connected to the reactor. The cooler is connected to the high-pressure separator. The high-pressure separator is connected to the gas-liquid separator and the waste gas treatment equipment respectively.

[0005] Furthermore: an air compressor is provided outside the storage tank, a discharge pipe is provided at the bottom of the storage tank, and a ball valve is provided on the discharge pipe. A pneumatic ball valve is provided on the connecting pipe between the storage tank and the first feeder and the second feeder, and a pneumatic ball valve is provided on the connecting pipe between the first feeder, the second feeder and the reactor.

[0006] Furthermore: the high-pressure separator is provided with a drain port, a cleaning port and a connecting pipe connected to the gas-liquid separator. Ball valves are provided at the ports of the drain port and the cleaning port, and ball valves and back pressure valves are provided on the connecting pipes connected to the gas-liquid separator.

[0007] Furthermore: the gas-liquid separator is provided with a sewage discharge pipe at the bottom and a ball valve at the port of the sewage discharge pipe; a sampling pipe is provided on one side of the top of the gas-liquid separator and connected to the waste gas treatment equipment through a pipe on the other side; a ball valve is provided at the port of the sampling pipe and at the port of the gas-liquid separator; and a ball valve and a wet flow meter are provided on the connecting pipe between the gas-liquid separator and the waste gas treatment equipment.

[0008] Furthermore, the reactor is made of high-temperature and high-pressure resistant materials.

[0009] Furthermore, the waste gas treatment device employs an adsorbent or a catalyst.

[0010] Furthermore, the preheater is an electric heater or a gas heater.

[0011] Furthermore: the cooler and high-pressure separator are solvent recovery devices for high-temperature and high-pressure reaction systems.

[0012] Compared with the prior art, the beneficial effects of the present invention are as follows: This invention discloses a high-temperature, high-pressure reaction system. In processing organic matter, minerals, and chemical substances, the system adjusts temperature and pressure to achieve a high-temperature, high-pressure state, thereby increasing the reaction rate and selectivity. In the preparation of energy-saving gases, this system utilizes the characteristics of high-temperature, high-pressure reactions to convert organic matter, minerals, and chemical substances into energy-saving gases, achieving efficient energy production. Attached Figure Description

[0013] To more clearly illustrate the technical solutions of the embodiments of the present invention, the accompanying drawings used in the description of the embodiments will be briefly introduced below. Obviously, the accompanying drawings described below are only for more clearly illustrating the technical solutions in the embodiments of the present invention or the prior art. For those skilled in the art, other drawings can be obtained based on these drawings without creative effort.

[0014] Figure 1 This is a schematic diagram of the overall structure of the present invention; In the diagram: 1-Accumulator, 2-Regenerator, 3-Preheater, 4-Cooler, 5-High-pressure separator, 51-Drain outlet, 52-Cleaning outlet, 6-Waste gas treatment equipment, 61-Wet flow meter, 7-Gas-liquid separator, 71-Back pressure valve, 72-Sewage discharge pipe, 73-Sampling pipe, 8-Reactor, 9-Air compressor, 10-Storage tank, 101-Discharge pipe, 11-Second feeder, 12-First feeder, 13-Pressure device, 14-Flow meter, 15-Check valve, 16-Pneumatic ball valve, 17-Ball valve. Detailed Implementation

[0015] To enable those skilled in the art to better understand and implement the technical solutions of the present invention, the present invention will be further described below with reference to specific embodiments. However, the embodiments are only for illustration and are not intended to limit the present invention.

[0016] like Figure 1 The high-temperature and high-pressure reaction system shown includes several accumulators 1, a high-pressure water pump, a high-pressure flushing pump, a high-pressure feed pump, a reactor 8, a storage tank 10, a high-pressure separator 5, and a waste gas treatment device 6. The storage tank 10 is connected to a first feeder 12 and a second feeder 11. The first feeder 12 and the second feeder 11 are connected to the reactor 8. The reactor 8 is connected to a regenerator 2. The regenerator 2 is connected to a preheater 3 and a cooler 4, respectively. The preheater 3 is equipped with several electric heating belts and is connected to the reactor 8. The cooler 4 is connected to the high-pressure separator 5. The high-pressure separator 5 is connected to a gas-liquid separator 7 and the waste gas treatment device 6, respectively.

[0017] The high-pressure water pump is connected to the accumulator 1, which is connected to the regenerator 2. A pressure controller 13, a flow meter 14, a check valve 15, and a pneumatic ball valve 16 are provided between the accumulator 1 and the regenerator 2. The high-pressure flushing pump is connected to the accumulator 1, which is also connected to the regenerator 3 and the first feeder 12 and the second feeder 11. A pressure controller 13, a check valve 14, and a pneumatic ball valve 16 are provided between the accumulator 1 and the regenerator 2 and the first feeder 12 and the second feeder 11. The high-pressure feed pump is connected to the accumulator 1, which is connected to the first feeder 12 and the second feeder 11. A pressure controller 13, a flow meter 14, a check valve 15, and a pneumatic ball valve 16 are provided between the accumulator 1 and the first feeder 12 and the second feeder 11.

[0018] An air compressor 9 is provided outside the storage tank 10. A discharge pipe 101 is provided at the bottom of the storage tank 10, and a ball valve 17 is provided on the discharge pipe 101. A pneumatic ball valve 16 is provided on the connecting pipe between the storage tank 10 and the first feeder 12 and the second feeder 11. A pneumatic ball valve 16 is also provided on the connecting pipe between the first feeder 12, the second feeder 11 and the reactor 8. The high-pressure separator 5 is provided with a drain port 51, a cleaning port 52 and a connecting pipe connected to the gas-liquid separator 7. A ball valve 17 is provided at the port of the drain port 51 and the cleaning port 52. A ball valve 17 and a back pressure valve 71 are respectively provided on the connecting pipe connected to the gas-liquid separator 7. The gas-liquid separator 7 is provided with a sewage discharge pipe 72 at the bottom, and a ball valve 17 is provided at the port of the sewage discharge pipe 72. A sampling pipe 73 is provided on one side of the top of the gas-liquid separator 7, and the other side is connected to the waste gas treatment equipment 6 through a pipe. A ball valve 17 is provided at the port of the sampling pipe 73, a ball valve 17 is provided at the port of the gas-liquid separator 7, and a ball valve 17 and a wet flow meter 61 are provided on the connecting pipe between the gas-liquid separator 7 and the waste gas treatment equipment 6.

[0019] Preferred feature: The reactor 8 is made of high temperature and high pressure resistant material, which has good sealing performance and corrosion resistance.

[0020] Preferred: The waste gas treatment equipment 6 uses adsorbents or catalysts to treat the waste gas during the reaction process, thereby reducing environmental pollution.

[0021] Priority: The cooler 7 and the high-pressure separator 5 are solvent recovery devices for the high-temperature and high-pressure reaction system, which can recover and utilize the solvent generated during the reaction process.

[0022] Working principle Organic matter, minerals, or chemicals in the storage tank are transported to the first and second feeders, and then to the reactor for reaction. During the reaction, the preheater is turned on to provide the reactor with the required high temperature conditions. The reactants in the reaction process flow through pipelines to the regenerator, cooler, and high-pressure separator. In the high-pressure separator, the solvent is separated and recycled. Other substances then enter the enterprise separator through pipelines to separate the gas and liquid. The liquid is discharged through the sewage pipe at the bottom, and the gas enters the waste gas treatment equipment through the pipe at the top for purification treatment to reduce environmental pollution.

[0023] This invention discloses a high-temperature, high-pressure reaction system. In processing organic matter, minerals, and chemical substances, the system adjusts temperature and pressure to achieve a high-temperature, high-pressure state, thereby increasing the reaction rate and selectivity. In the preparation of energy-saving gases, this system utilizes the characteristics of high-temperature, high-pressure reactions to convert organic matter, minerals, and chemical substances into energy-saving gases, achieving efficient energy production.

[0024] The following are the energy-saving gas masses obtained by this system for the reactions of different substances at different temperatures and the same pressure: Organic matter, under conditions of 650℃ and 25MPa, has a carbon gasification rate of 95%-98%. The minerals, under conditions of 750℃ and 25MPa pressure, exhibit a carbon gasification rate of 95%-100%. Chemical substances, under conditions of 700℃ and 25MPa, have a carbonization rate of 90%-99%.

[0025] All content not described in detail in this invention is prior art.

[0026] The above description is merely a preferred embodiment of the present invention and is not limited to the description in the specification and embodiments. Therefore, all equivalent changes or modifications made to the structure, features, and principles described in the claims of this invention should be included within the scope of this patent application.

Claims

1. A high temperature and high pressure reaction system comprising several accumulators (1), a high pressure water pump, a high pressure flushing pump, a high pressure material pump, a reactor (8), a material storage tank (10), a high pressure separator (5) and a waste gas treatment device (6), characterized in that: The high-pressure water pump is connected to the accumulator (1), and the accumulator (1) is connected to the regenerator (2). A pressure controller (13), a flow meter (14), a check valve (15), and a pneumatic ball valve (16) are provided between the accumulator (1) and the regenerator. The high-pressure flushing pump is connected to the accumulator (1), and the accumulator (1) is connected to the regenerator (2) and the first feeder (12) and the second feeder (11). The accumulator (1) is connected to the regenerator (2) and the first feeder (12) and the second feeder (11). A pressure controller (13), a check valve (15), and a pneumatic ball valve (16) are provided between the feeder (12) and the second feeder (11); the high-pressure feed pump is connected to the accumulator (1), the accumulator (1) is connected to the first feeder (12) and the second feeder (11), and a pressure controller (13), a flow meter (14), a check valve (15), and a pneumatic ball valve (16) are provided between the accumulator (1) and the first feeder (12) and the second feeder (11); The storage tank (10) is connected to the first feeder (12) and the second feeder (11). The first feeder (12) and the second feeder (11) are connected to the reactor (8). The reactor (8) is connected to the regenerator (2). The regenerator (2) is connected to the preheater (3) and the cooler (4) respectively. The preheater (3) is provided with several electric heating belts and is connected to the reactor (8). The cooler (4) is connected to the high-pressure separator (5). The high-pressure separator (5) is connected to the gas-liquid separator (7) and the waste gas treatment equipment (6) respectively.

2. The high temperature and high pressure reaction system according to claim 1, characterized in that: An air compressor (9) is provided outside the storage tank (10). A discharge pipe (101) is provided at the bottom of the storage tank (10), and a ball valve (17) is provided on the discharge pipe (101). A pneumatic ball valve (16) is provided on the connecting pipe between the storage tank (10) and the first feeder (12) and the second feeder (11). A pneumatic ball valve (16) is provided on the connecting pipe between the first feeder (12), the second feeder (11) and the reactor (8).

3. The high-temperature and high-pressure reaction system according to claim 1, characterized in that: The high-pressure separator (5) is provided with a drain port (51), a cleaning port (52) and a connecting pipe connected to the gas-liquid separator (7). A ball valve (17) is provided at the port of the drain port (51) and the cleaning port (52). A ball valve (17) and a back pressure valve (71) are respectively provided on the connecting pipe connecting the high-pressure separator (5) and the gas-liquid separator (7).

4. The high-temperature and high-pressure reaction system according to claim 1, characterized in that: The gas-liquid separator (7) is provided with a sewage pipe (72) at the bottom and a ball valve (17) at the port of the sewage pipe (72). A sampling pipe (73) is provided on one side of the top of the gas-liquid separator (7), and the other side is connected to the waste gas treatment equipment (6) through a pipe. A ball valve (17) is provided at the port of the sampling pipe (73). A ball valve (17) is provided at the port of the gas-liquid separator (7). A ball valve (17) and a wet flow meter (61) are provided on the connecting pipe between the gas-liquid separator (7) and the waste gas treatment equipment (6).

5. The high-temperature and high-pressure reaction system according to claim 1, characterized in that: The reactor (8) is made of high temperature and high pressure resistant materials.

6. The high-temperature and high-pressure reaction system according to claim 1, characterized in that: The waste gas treatment equipment (6) uses adsorbents or catalysts to treat waste gas.

7. The high-temperature and high-pressure reaction system according to claim 1, characterized in that: The preheater (3) is an electric heater or a gas heater.

8. A high-temperature and high-pressure reaction system according to any one of claims 1 to 7, characterized in that: The cooler (7) and the high-pressure separator (5) are solvent recovery devices for the high-temperature and high-pressure reaction system.

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