A dual high gravity reactor and its use method

Abstract

The invention discloses a dual hypergravity reactor and a method for using the same, which relates to the field of hypergravity engineering technology. The reactor comprises an outer shell, a liquid feed pipe and a gas feed pipe. A first transmission shaft, a moving disk, parabolic blades and a fixed disk are arranged in the outer shell, and the moving disk is provided with jet holes and parabolic blades. A driving assembly for driving the first transmission shaft to drive the moving disk to rotate is provided on the outer shell. In the reactor of the present invention, liquid and gas form mist-like gas-liquid bubbles after passing through a nozzle. The gas-liquid bubbles are deflected at high speed by the moving disk blades, parabolic blades and fixed disk blades, and are broken through the jet holes to form a large and continuously updated micro-gas-liquid bubble surface area. The tortuous and high-kinetic energy flow channel intensifies the extremely thin gas-liquid bubble body and the surface renewal, forming an ultra-thin gas-liquid film bubble. At the same time, after the ultra-thin gas-liquid film bubble passes through multiple layers of moving disk blades and fixed disk blades, the hypergravity gas-liquid bubble grows and explodes rapidly, thereby generating a high-temperature and high-pressure hypergravity field, so that two-phase or multi-phase substances react rapidly.

Description

Technical Field

[0001] The present invention relates to the technical field of supergravity engineering, and in particular to a double supergravity reactor. Background Art

[0002] The basic principle of high-gravity engineering technology is to utilize the unique flow behavior of multiphase flow systems under high-gravity conditions to enhance the relative velocity and mutual contact between phases, thereby achieving efficient mass transfer, heat transfer, and chemical reaction processes. The main way to obtain high gravity is to rotate the entire device or its components to form a centrifugal field. The multiphase flow systems involved mainly include gas-solid systems and gas-liquid systems. Centrifugal fields (high-gravity fields) are used for phase separation and have a long history both in daily life and in industrial applications.

[0003] The reactor in the prior art has only one gravity field condition, and the reaction rate of its two-phase or multi-phase reactants is limited, which makes the packing bed easily clogged by the reactants, resulting in an inability to operate for a long time, increasing maintenance time, reducing the production efficiency of the reactor, and increasing production costs. Summary of the Invention

[0004] The main purpose of the present invention is to provide a dual high-gravity reactor to solve the problem that the existing high-gravity reactor has limited reaction speed, easily causes packing bed blockage and reduces production efficiency.

[0005] To achieve the above object, the present invention provides a dual high-gravity reactor, comprising an outer shell, a liquid feed pipe, a gas feed pipe, and a nozzle; the nozzles are respectively arranged on the liquid feed pipe and the gas feed pipe; and further comprising:

[0006] The drive assembly includes a first drive member and a first transmission shaft disposed in the outer shell;

[0007] The fixed disc body comprises a plurality of fixed disc blades arranged in a concentric circle at intervals within the outer shell, with fixed disc spaces formed between adjacent fixed disc blades;

[0008] A moving disc body, comprising a moving disc base plate, a plurality of groups of moving disc blades arranged concentrically and spaced apart on the moving disc base plate, and a moving disc space formed between adjacent moving disc blades;

[0009] The fixed disk blades and the movable disk blades are respectively inserted into the movable disk space and the fixed disk space, so that a flow gap is formed between the fixed disk blades and the movable disk blades; the movable disk bottom plate is connected to the first transmission shaft;

[0010] The nozzles on the liquid feed pipe and the gas feed pipe are located above the fixed disk blades and are arranged near the first transmission shaft, so as to allow the external gas-liquid microbubbles transported in the liquid feed pipe and the gas feed pipe to enter the flow gap respectively;

[0011] The moving disk blades are provided with jet holes; parabolic blades are provided at the connection between the moving disk bottom plate and the moving disk blades; the parabolic blades are provided with parabolic surfaces; the first driving member drives the first transmission shaft to rotate under the action of external force, so that the moving disk drives the parabolic blades to rotate, thereby allowing the parabolic surfaces to provide supergravity kinetic energy to the external gas-liquid microbubbles, thereby allowing the external gas-liquid microbubbles to pass through the jet holes on the moving disk blades from the inside to the outside in sequence and be in a double gravity field.

[0012] As a further improvement of the present invention, connecting strips are provided between the multiple groups of fixed disk blades; and the connecting strips are connected to the outer shell.

[0013] As a further improvement of the present invention, the jet holes are evenly arranged in a honeycomb shape on the moving disk blades, the axis of the jet holes is perpendicular to the moving disk blades, the jet holes are conical with one end large and the other end small, and the large mouth of the jet holes faces the first rotating shaft.

[0014] As a further improvement of the present invention, a multiphase material downstream channel is formed between the parabolic blades and the adjacent moving disk blades located on the inner circle.

[0015] As a further improvement of the present invention, a guide plate is obliquely provided inside the outer shell, and a product outlet pipe and a product exhaust gas outlet pipe are respectively provided on the outer wall of the outer shell; a demister is provided on the guide plate; the product outlet pipe is located at the lowest end of the guide plate; and the product exhaust gas outlet pipe is located at the highest end of the guide plate.

[0016] As a further improvement of the present invention, the first driving member includes a variable frequency motor, a main transmission wheel connected to the output end of the variable frequency motor, and an auxiliary transmission wheel arranged on the first transmission shaft; a transmission belt is provided between the main transmission wheel and the auxiliary transmission wheel.

[0017] As a further improvement of the present invention, the nozzles on the liquid feed pipe and the gas feed pipe are provided in multiple groups and respectively correspond to the flow gaps between the moving disk blades and the fixed disk blades; the outlet directions on the nozzles are respectively perpendicular to the axes of the liquid feed pipe and the gas feed pipe.

[0018] As a further improvement of the present invention, the fixed plate body and the movable plate body are provided in multiple groups from top to bottom in the outer shell; the liquid feed pipe and the gas feed pipe are provided in multiple groups corresponding to the fixed plate body.

[0019] As a further improvement of the present invention, the parabolic blades are arranged at intervals along the circumferential direction at the connection between the moving disk bottom plate and the moving disk blades.

[0020] The beneficial effects of the present invention are embodied in:

[0021] The liquid and gas in the reactor of this scheme are jetted from the jet holes on the passive disk blades, fixed disk blades, parabolic blades, and multi-layer dynamic disk blades, which are broken to form a huge and constantly updated surface area of the gas-liquid film bubble. The tortuous flow path intensifies the extreme thinness of the gas-liquid film bubble and the renewal of the surface, forming an ultra-thin gas-liquid film bubble. At the same time, after the ultra-thin gas-liquid film bubble passes through the jet holes on the dynamic disk blades, the large gas-liquid film bubble explodes and generates a high-energy supergravity shock wave and reacts rapidly. The small bubble grows rapidly and explodes and reacts in the next jet. After the gas-liquid film bubble passes through the jet holes on each layer of dynamic disk blades, the reaction speed and efficiency are accelerated due to the existence of the double force field.

[0022] The driving assembly can drive the moving disc to rotate centrifugally at different speeds. At the same time, a vortex-shaped gas-liquid microbubble fluid is formed behind the jet holes on the moving disc blades. Therefore, after passing through multiple layers of moving disc blades and fixed disc blades, the moving reaction substances form a supergravity field due to the high-speed rotation. At the same time, after passing through the multiple layers of jet holes, the extremely small gas-liquid microbubbles quickly grow and explode and generate a high-energy shock wave supergravity field, so that the entire reaction is in a double force field, so that the two-phase or multi-phase reactants react quickly, which increases the reaction speed, reduces maintenance time, improves production efficiency and reduces production costs. BRIEF DESCRIPTION OF THE DRAWINGS

[0023] Figure 1 This is a schematic diagram of the overall structure of a dual high-gravity reactor of the present invention;

[0024] Figure 2 This is a schematic diagram of the connection structure between the moving plate and the fixed plate of a dual high gravity reactor of the present invention;

[0025] Figure 3 This is a front view of a fixed plate body of a dual high gravity reactor of the present invention;

[0026] Figure 4 This is a top view of a fixed plate body of a dual high gravity reactor of the present invention;

[0027] Figure 5 This is a front view of a moving disk of a dual high gravity reactor of the present invention;

[0028] Figure 6 This is a top view of a moving disk of a dual high gravity reactor of the present invention;

[0029] Figure 7 This is a schematic diagram of the jet hole structure of a dual high gravity reactor of the present invention;

[0030] Description of reference numerals:

[0031] 1. Outer shell; 2. Liquid feed pipe; 3. Gas feed pipe; 4. Nozzle; 5. First drive member; 501. Frequency conversion motor; 502. Main drive wheel; 503. Auxiliary drive wheel; 504. Drive belt; 505. Support base; 6. First drive shaft; 7. Fixed disk blade; 8. Fixed disk space; 9. Moving disk bottom plate; 10. Moving disk blade; 11. Moving disk space; 12. Jet hole; 13. Parabolic blade; 14. Parabolic surface; 15. Shell top cover; 16. Shell flange; 17. Main bearing; 18. Auxiliary bearing; 19. Pressure transmitter interface; 20. Connecting strip; 21. Support frame; 22. Connecting plate; 23. Downstream channel; 24. Guide plate; 25. Product outlet pipe; 26. Product exhaust gas outlet pipe; 27. Demister; 28. Exhaust gas temperature measuring element interface; 29. Flow gap; 30. Temperature measuring element interface. DETAILED DESCRIPTION

[0032] In order to make the purpose, technical solutions and advantages of the present invention more clear, the present invention is further described in detail below with reference to the accompanying drawings and examples. It should be understood that the described embodiments are only part of the embodiments of the present invention, rather than all of the embodiments. In the absence of conflict, the embodiments in this application and the features in the embodiments can be combined with each other. Based on the embodiments in the present invention, all other embodiments obtained by ordinary technicians in this field without making creative work are within the scope of protection of the present invention.

[0033] In one embodiment, see Figure 1 A dual high-gravity reactor of the present invention includes an outer shell 1, a liquid feed pipe 2, a gas feed pipe 3, a nozzle 4, a drive assembly, a fixed plate assembly, and a moving plate assembly.

[0034] Among them, the nozzles 4 are respectively arranged on the liquid feed pipe 2 and the gas feed pipe 3; the driving assembly includes a first driving member 5 and a first transmission shaft 6 arranged in the outer shell 1; the fixed disk body includes a plurality of groups of fixed disk blades 7 arranged in a concentric circle in the outer shell 1, and a fixed disk space 8 is formed between adjacent fixed disk blades 7; the moving disk body includes a moving disk base plate 9 and a plurality of groups of moving disk blades 10 arranged in a concentric circle on the moving disk base plate 9, and a moving disk space 11 is formed between adjacent moving disk blades 10; the fixed disk blades 7 and the moving disk blades 10 are respectively inserted into the moving disk space 11 and the fixed disk space 8, so that a flow gap 29 is formed between the fixed disk blades 7 and the moving disk blades 10; the moving disk base plate 9 is connected to the first transmission shaft 6; the nozzles 4 on the liquid feed pipe 2 and the gas feed pipe 3 are located above the fixed disk blades 7 and are arranged near the first transmission shaft 6, so that the external gas-liquid microbubbles transported in the liquid feed pipe 2 and the gas feed pipe 3 enter the flow gap 29 respectively;

[0035] The moving disc blades 10 are provided with jet holes 12; a parabolic blade 13 is provided at the connection between the moving disc bottom plate 9 and the moving disc blades 10, and a parabolic surface 14 is provided on the parabolic blade 13; the first driving member 5 drives the first transmission shaft 6 to rotate under the action of an external force, so that the moving disc drives the parabolic blade 13 to rotate, thereby allowing the parabolic surface 14 to provide supergravity kinetic energy to the external gas-liquid microbubbles, thereby allowing the external gas-liquid microbubbles to pass through the jet holes 12 on the moving disc blades 10 from the inside to the outside in sequence and be in a double gravity field.

[0036] Preferably, the outer shell 1 is a hollow cylinder, and a first rotary hole is provided at the bottom end of the outer shell 1 . A temperature measuring element interface 30 is provided on the outer wall of the outer shell 1 .

[0037] Preferably, a shell top cover 15 is provided on the top of the outer shell 1, and a shell flange 16 is provided on the outer wall of the shell top cover 15 and the outer shell 1, and the shell top cover 15 and the outer shell 1 are connected by bolts passing through the shell flange 16; a second rotary hole is provided on the shell top cover 15; the first transmission shaft 6 passes through the first rotary hole, the inside of the outer shell 1, and the second rotary hole outside the shell top cover 15 in sequence from the bottom end of the outer shell 1.

[0038] Preferably, a main bearing 17 located at the second rotating hole is provided on the shell top cover 15, and a secondary bearing 18 located at the first rotating hole is provided on the outer shell 1, and the first transmission shaft 6 is connected to the main bearing 17 and the secondary bearing 18 respectively; a pressure transmitter interface 19 is also provided on the bearing top cover; the main bearing 17 and the secondary bearing 18 both use sealed bearings.

[0039] Specifically, connecting bars 20 are provided between the multiple groups of fixed disk blades 7 , and the connecting bars 20 are connected to the outer shell 1 .

[0040] Preferably, a support frame 21 is further provided at the bottom end of the outer shell 1 ; a connecting plate 22 is provided on the inner wall of the outer shell 1 , and the connecting plate 22 is connected to the connecting bar 20 by bolts, so that the fixed plate body is fixedly arranged in the outer shell 1 .

[0041] Preferably, the stator blades and the rotor blades 10 are both annular structures.

[0042] Furthermore, the jet holes 12 are evenly arranged on the moving disk blades 10 in a honeycomb shape, the axis of the jet holes 12 is perpendicular to the moving disk blades 10, the jet holes 12 are conical with one end large and the other end small, and the large end of the jet holes 12 faces the first rotating shaft.

[0043] In the above arrangement, the gas-liquid mixture flows through the jet hole 12 to the next-level jet hole 12 after being refracted by the moving disk blades 10 and the fixed disk blades 7, so that the fluid passes through the jet hole 12 at a speed of 9.8m / s to 11.5m / s, and at the same time, high-energy microbubbles are generated after passing through the jet hole 12.

[0044] Furthermore, a multiphase material downstream channel 23 is formed between the parabolic blade 13 and the adjacent rotor blade 10 located on the inner circle.

[0045] Furthermore, a guide plate 24 is obliquely provided inside the outer shell 1, and a product outlet pipe 25 and a product exhaust gas outlet pipe 26 are respectively provided on the outer wall of the outer shell 1; a demister 27 is provided on the guide plate 24; the product outlet pipe 25 is located at the lowest end of the guide plate 24; and the product exhaust gas outlet pipe 26 is located at the highest end of the guide plate 24.

[0046] Preferably, the product tail gas outlet pipe 26 is further provided with a tail gas temperature measuring element interface 3028; and the demister 27 facilitates the discharge of the tail gas.

[0047] Furthermore, the first driving member 5 includes a variable frequency motor 501, a main transmission wheel 502 connected to the output end of the variable frequency motor 501, and an auxiliary transmission wheel 503 arranged on the first transmission shaft 6. A transmission belt 504 is provided between the main transmission wheel 502 and the auxiliary transmission wheel 503.

[0048] Preferably, a support base 505 located on the support frame 21 is provided at the lower end of the variable frequency motor 501 .

[0049] In the above arrangement, the first transmission shaft 6 is driven to rotate by the variable frequency motor 501, thereby driving the moving disk blades 10 to rotate centrifugally at high speed; the speed of the variable frequency motor 501 is adjustable in the range of 0 rpm to 1000 rpm, thereby achieving the speed between the mass transfer objects generated after the gas-liquid phase passes through the first layer of moving disk blades 10 and the fixed disk blades 7, which can be controlled between 7 m / s and 12 m / s, and also makes the particle size of the reaction product controllable.

[0050] Furthermore, multiple groups of nozzles 4 are provided on the liquid feed pipe 2 and the gas feed pipe 3 and respectively correspond to the flow gaps 29 between the moving disk blades 10 and the fixed disk blades 7; the outlet directions on the nozzles 4 are respectively perpendicular to the axes of the liquid feed pipe 2 and the gas feed pipe 3.

[0051] Preferably, the nozzle 4 is a vortex or swirl nozzle 4 .

[0052] In the above arrangement, when the liquid is ejected from the nozzle 4 on the liquid feed pipe 2, a narrow tube effect is generated, which increases the initial velocity of the liquid outflow, making it easier to form ultra-thin gas-liquid film bubbles, accelerating the rapid growth and explosion of the gas-liquid bubble body, forming a high-energy explosion supergravity shock wave, and improving the reaction efficiency; when the gas is ejected from the nozzle 4 on the gas feed pipe 3, due to the narrow tube effect, the initial velocity of the gas is large, and when passing through the jet holes 12 on the first layer of the moving disk blades 10, the gas is accelerated again and forms nanometer to micrometer-level gas-liquid bubbles, thereby the jet holes on the first layer of the moving disk blades 10 12 forms a fast-flowing limit gas-liquid film bubble and explodes to produce a second shock wave gravity field; thus, a limit gas-liquid film bubble is formed after mixing with liquid mist; when the gas and liquid pass through the nozzle 4 on the gas feed pipe 3 and the liquid feed pipe 2, some gas-liquid microbubbles are formed, and then the kinetic energy is further increased after passing through the parabolic blades of the moving disk, and after the bubbles further pass through the jet hole 12, the large bubbles explode to produce an explosion supergravity field, and under the dual action of the high-speed supergravity field and the explosion supergravity, the small bubbles grow rapidly and explode, thereby making the two-phase or multi-phase reaction in a high-kinetic energy gravity field.

[0053] Furthermore, multiple groups of fixed plate bodies and movable plate bodies are provided from top to bottom in the outer shell 1, and multiple groups of liquid feed pipes 2 and gas feed pipes 3 are provided corresponding to the fixed plate bodies.

[0054] Furthermore, the parabolic blades 13 are arranged at intervals along the circumferential direction at the connection between the moving disk bottom plate 9 and the moving disk blades 10 .

[0055] Preferably, the cross section of the parabola 14 is parabolic.

[0056] Preferably, the bottom surface of the parabolic blade 13 is fixedly connected to the lower end surface of the moving disk bottom plate 9 , and the vertical surface of the parabolic blade 13 is fixedly connected to the circumferential surface of the moving disk blade 10 .

[0057] In this embodiment, the variable frequency motor 501 drives the first transmission shaft 6 and the moving disk blades 10 to rotate centrifugally. At the same time, the gas reactant passes through the nozzle 4 on the gas feed pipe 3 into the fixed disk space 8 and the moving disk space 11, and the liquid reactant enters the nozzle 4 fixed disk space 8 and the moving disk space 11 through the nozzle 4 on the liquid feed pipe 2. Under the action of high-speed centrifugation and gas pressure, the gas-liquid microbubbles are sequentially ejected from the jet holes 12 on the inner layer of the moving disk blades 10 adjacent to the first transmission shaft 6 to the second layer of the moving disk space 11 and the fixed disk space 8. Under the conditions of high centrifugal force and high gravity field of microbubble explosion, the gas-liquid microbubbles pass through the second to Nth layers of the moving disk blades 10 and the fixed disk blades 7 at high speed, so that the entire reaction is completed. The entire process is in a high-energy gravity field of shock waves of high centrifugal force and microbubble explosion, that is, the reaction is under the action of two gravity fields, and the two-phase microbubbles are further accelerated by energy. Under the conditions of two gravity fields, the gas and liquid phase bubbles react rapidly with explosion; under the action of high-speed centrifugation and liquid pressure, the liquid flows through the moving disk blades 10 and the fixed disk blades 7 and the jet holes 12 on the side walls of the moving disk blades 10, and forms ultra-thin gas-liquid film bubbles under the conditions of double supergravity fields; in this process, the liquid and gas are dispersed and broken by the first to Nth layers of moving disk blades 10 and fixed disk blades 7 to form a huge and constantly renewed surface area, and the tortuous flow channel intensifies the renewal of the extremely thin gas-liquid bubbles and the surface of the liquid and explodes rapidly. This creates excellent mass transfer and reaction conditions within the dual high-gravity reactor. Since both gas and liquid feed rates are automatically controlled based on the required reaction pressure, flow rate, and temperature, the velocity between the gas and liquid bubbles, after passing through the rotor blades 10, the fixed blades 7, and the jet holes 12, can be controlled between 7 and 12 m / s, creating controllable reaction conditions. Simultaneously, as the ultra-thin gas-liquid film bubbles pass through the first layer of rotor blades 10 and fixed blades 7 to the Nth layer of rotor blades 10 and fixed blades 7, a higher-energy microbubble vortex fluid is formed on the concave surfaces of the rotor blades 10, jet holes 12, and fixed blades 7. As a result, fine-particle products are ejected from the passages of the rotor blades 10 and fixed blades 7, achieving an unblocked state and controllable reaction product particle size. This makes the entire reactor less susceptible to clogging by reactants, preventing prolonged operation and enabling long-term operation. This reduces maintenance time, improves production efficiency, and reduces production costs.

[0058] The above description is only a preferred embodiment of the present invention and is not intended to limit the present invention. Any modifications, equivalent substitutions, improvements, etc. made within the spirit and principles of the present invention should be included in the scope of protection of the present invention.

Claims

1. A dual high gravity reactor, comprising an outer shell (1), a liquid feed pipe (2), a gas feed pipe (3), and a nozzle (4); the nozzle (4) is respectively arranged on the liquid feed pipe (2) and the gas feed pipe (3); characterized in that, Also includes: A drive assembly comprising a first drive member (5) and a first transmission shaft (6) disposed within an outer shell (1); A fixed disc body, the fixed disc body comprising a plurality of groups of fixed disc blades (7) arranged in a concentric circle at intervals within the outer shell (1), with fixed disc spaces (8) formed between adjacent fixed disc blades (7); A moving disc body, comprising a moving disc base plate (9), a plurality of moving disc blades (10) arranged concentrically and spaced apart on the moving disc base plate (9), and a moving disc space (11) formed between adjacent moving disc blades (10); The fixed disk blades (7) and the moving disk blades (10) are respectively inserted into the moving disk space (11) and the fixed disk space (8), so that a flow gap (29) is formed between the fixed disk blades (7) and the moving disk blades (10); the moving disk bottom plate (9) is connected to the first transmission shaft (6); The nozzles (4) on the liquid feed pipe (2) and the gas feed pipe (3) are located above the fixed disk blades (7) and are arranged adjacent to the first transmission shaft (6) so as to allow the external gas-liquid microbubbles transported in the liquid feed pipe (2) and the gas feed pipe (3) to enter the flow gap (29). The moving disc blade (10) is provided with a jet hole (12); a parabolic blade (13) is provided at the connection between the moving disc bottom plate (9) and the moving disc blade (10); a parabolic surface (14) is provided on the parabolic blade (13); the first driving member (5) drives the first transmission shaft (6) to rotate under the action of an external force, so that the moving disc drives the parabolic blade (13) to rotate, thereby allowing the parabolic surface (14) to provide supergravity kinetic energy for the external gas-liquid microbubble body, thereby allowing the external gas-liquid microbubble body to pass through the jet hole (12) on the moving disc blade (10) from the inside to the outside in sequence and be in a double gravity field.

2. A dual high gravity reactor according to claim 1, characterized in that: Connecting strips (20) are provided between the stator blades (7); the connecting strips (20) are connected to the outer shell (1).

3. A dual high gravity reactor according to claim 2, characterized in that: The jet holes (12) are evenly arranged on the moving disk blades (10) in a honeycomb shape, the axis of the jet holes (12) is perpendicular to the moving disk blades (10), the jet holes (12) are conical with one end large and the other end small, and the large end of the jet holes (12) faces the first rotating shaft.

4. A dual high gravity reactor according to claim 3, characterized in that: A multiphase material downstream channel (23) is formed between the parabolic blade (13) and the adjacent moving disk blade (10) located on the inner circle.

5. A dual high gravity reactor according to claim 4, characterized in that: A guide plate (24) is obliquely provided inside the outer shell (1), and a product outlet pipe (25) and a product exhaust gas outlet pipe (26) are respectively provided on the outer wall of the outer shell (1); a demister (27) is provided on the guide plate (24); the product outlet pipe (25) is located at the lowest end of the guide plate (24); and the product exhaust gas outlet pipe (26) is located at the highest end of the guide plate (24).

6. A dual high gravity reactor according to claim 5, characterized in that: The first driving member (5) comprises a variable frequency motor (501), a main transmission wheel (502) connected to the output end of the variable frequency motor (501), and a secondary transmission wheel (503) arranged on a first transmission shaft (6); a transmission belt (504) is provided between the main transmission wheel (502) and the secondary transmission wheel (503).

7. A dual high gravity reactor according to claim 6, characterized in that: The nozzles (4) on the liquid feed pipe (2) and the gas feed pipe (3) are provided in multiple groups and respectively correspond to the flow gaps (29) between the moving disk blades (10) and the fixed disk blades (7); the outlet directions on the nozzles (4) are respectively perpendicular to the axes of the liquid feed pipe (2) and the gas feed pipe (3).

8. A dual high gravity reactor according to claim 7, characterized in that: The fixed plate body and the movable plate body are provided in multiple groups from top to bottom in the outer shell (1); and the liquid feed pipe (2) and the gas feed pipe (3) are provided in multiple groups corresponding to the fixed plate body.

9. The dual high gravity reactor according to claim 7, characterized in that: The parabolic blades (13) are arranged at intervals along the circumferential direction at the connection between the moving disk base plate (9) and the moving disk blades (10).

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