Low-consumption high-energy vortex type incinerator process

Abstract

The invention provides a low-consumption and high-energy vortex type incinerator process, and relates to the technical field of waste incineration disposal. The bottom of a feeding channel is connected with an incinerator body, a slag discharging door is rotationally installed on the outer surface of the incinerator body, a conical top frame is fixed to the top of the incinerator body, and the conical top frame is connected with the feeding channel; the conical plate is installed at a connecting opening of the feeding channel and the conical top frame, a bottom box is fixed to the bottom of the furnace body, and the bottom of the turbulent flow pipe is fixed to the circle center of the bottom of the bottom box. The mixing sufficiency of flue gas, oxygen and the like in the furnace body is improved, through cooperation of a semicircular frame and a conical plate in the feeding channel, garbage is intermittently fed to be mixed and preheated with flue gas in the channel, the follow-up combustion efficiency is improved, the garbage is evenly distributed through the conical plate, and the efficiency of the flue gas entering the feeding channel can be improved.

Description

Technical Field

[0001] The present invention relates to the technical field of waste incineration treatment, and specifically to a low-consumption and high-energy vortex incinerator process. Background Art

[0002] An incinerator is a harmless treatment device commonly used in medical and domestic waste, and animal harmless treatment. Its principle is to use the combustion of fuels such as coal, fuel oil, and gas to incinerate and carbonize the objects to be treated at high temperatures to achieve the purpose of disinfection. Small domestic waste incinerators are necessary waste treatment devices for industry, daily life, and remote areas.

[0003] Currently, there is no traditional production standard for small domestic waste incinerators. Most existing manufacturers incinerate in a fuel oil manner, which consumes resources severely, and it is difficult to solve the problems that some garbage cannot be fully burned or has a low combustion efficiency. Summary of the Invention

[0004] Aiming at the deficiencies of the existing technology, the purpose of the present invention is to provide a low-consumption and high-energy vortex incinerator process to solve the problems mentioned in the above background art. The structure of the present invention is novel. Through the cooperation of the air inlet at 360 degrees inside the furnace body by the spoiler tube and the air inlet at the bottom of the furnace body, the degree of mixing of flue gas and oxygen inside the furnace body is improved. Through the cooperation of the semi-circular frame and the conical plate in the feeding channel, the garbage is intermittently fed and mixed and preheated with the flue gas in the channel, improving the subsequent combustion efficiency. And through the conical plate, the garbage is evenly distributed, which can improve the efficiency of the flue gas entering the inside of the feeding channel.

[0005] In order to achieve the above purpose, the present invention is realized through the following technical solutions: A low-consumption and high-energy vortex incinerator process, the process includes the following steps:

[0006] (1) Feed the garbage to be incinerated in batches into the semi-circular frame at the top of the feeding channel for standby;

[0007] (2) Drive the semi-circular frame to make reciprocating left and right flips, and the opening of the conical plate sends the high-temperature flue gas in the furnace body into the channel to be mixed and preheated with the garbage;

[0008] (3) Supply the primary air for waste heat recovery at the bottom of the bottom box by a blower to dry the garbage;

[0009] (4) Supply air by a high-pressure blower into the spoiler tube to increase the mixing degree of combustion flue gas and oxygen;

[0010] (5) Send out the ashes after combustion from the slag discharge door for the next group of combustion.

[0011] According to the feeding channel mentioned in step (1) of the above process, the bottom of the feeding channel is connected to a furnace body. A slag discharge door is rotatably installed on the outer surface of the furnace body, and a conical top frame is fixed at the top of the furnace body. The conical top frame is connected to the feeding channel. The conical plate is installed at the connection port of the feeding channel and the conical top frame. The bottom of the furnace body is fixed with a bottom box. The bottom of the turbulence pipe is fixed at the center of the bottom of the bottom box. A connection layer is fixed around the bottom box outside the turbulence pipe. The bottom of the furnace body is fixed with a bearing plate, and the connection layer wraps around the bottom of the furnace body. A vertical rod is arranged inside the feeding channel. The top of the vertical rod is rotatably connected to the bottom of the semi-circular frame, and the bottom of the vertical rod is fixed on the top of the conical plate. Connection rings are equidistantly fixed on the surface of the vertical rod, and horizontal plates are fixed on both sides of the connection ring. The horizontal plates slide along the inner wall of the feeding channel. Both sides of the semi-circular frame are rotatably installed on the inner wall of the feeding channel through shaft rods, and there is a space at the top of the feeding channel for the semi-circular frame to flip. Multiple groups of horizontal air outlets are equidistantly arranged around the surface of the turbulence pipe.

[0012] Further, a high-pressure blower is arranged outside the bottom box, and the high-pressure blower penetrates into the bottom box through a pipeline and is communicated with the bottom of the turbulence pipe.

[0013] Further, a waste heat recovery layer is sleeved on the outer surface of the furnace body. The bottom of the waste heat recovery layer is connected to an air supply pipe, and the other end of the air supply pipe penetrates into the bottom box and is communicated with the connection layer. Ventilation grooves are arranged on the surface of the bearing plate.

[0014] Further, inclined air outlets are annularly and equidistantly arranged at the top of the turbulence pipe, and the inclined air outlets are inclined downward at an angle of 45° with the turbulence pipe.

[0015] Further, a top cover is rotatably and sealingly installed at the top of the feeding channel, and a smoke exhaust pipe is arranged on one side of the top of the feeding channel.

[0016] Further, a motor is fixed on the outer wall of the feeding channel, and the output end of the motor is fixed to the shaft rod of the semi-circular frame. The motor drives the semi-circular frame to make a reciprocating flip of no more than ninety degrees.

[0017] Further, a slide rail is fixed at the bottom of the semi-circular frame, and a sliding seat is slidably connected inside the slide rail. A connecting shaft is installed at the bottom of the sliding seat, and the top of the vertical rod is installed on the connecting shaft.

[0018] Further, the connecting shaft is composed of two groups of rotating shafts, and the rotation directions of the connecting shaft are respectively parallel to the slide rail and perpendicular to the axis of the vertical rod.

[0019] Further, inclined slots are opened at the positions of the feeding channel corresponding to each group of horizontal plates, and the inclined slots are symmetrically arranged with respect to the axis of the feeding channel. One end of the horizontal plate is rotatably installed with a slider, and the slider slides along the inside of the inclined slot.

[0020] Furthermore, the surface of the cross plate is inclined, and the inclination directions of the cross plates on both sides of the connecting ring are opposite.

[0021] Advantages of the present invention:

[0022] 1. When the semi-circular frame of the present invention is in a horizontal state, through the connection of the vertical rod, the conical plate blocks the bottom outlet end of the feeding channel. At this time, the flue gas cannot enter the interior of the feeding channel, avoiding the direct entry of the flue gas from the top of the feeding channel into the air.

[0023] 2. The present invention drives the semi-circular frame to reciprocally rotate around the shaft rod by a motor. The rotation angle is not too large, satisfying the descending height of the vertical rod and the moving path of the cross plate along the inclined groove. When the semi-circular frame rotates towards one side, since the vertical rod always remains at the axis position of the feeding channel, the connecting shaft and the sliding seat connecting the vertical rod slide along the sliding rail. At this time, the vertical rod will be pressed down. Because the vertical rod is restricted by the cross plate, during the pressing-down process, the cross plate slides along the inclined groove, and the inclined groove is a chute from high to low, surrounding the inner wall of the feeding channel. At this time, as the vertical rod descends, the cross plate slides along the inclined groove and rotates itself, driving the vertical rod and the conical plate to rotate together through the connecting ring. On the one hand, as the semi-circular frame rotates, part of the garbage will fall from the lower side of the semi-circular frame. During this process, the rotation of the vertical rod and the cross plate scatters the garbage, so as to better mix and preheat with the high-temperature flue gas. Then, when it falls on the conical plate, the inclined surface of the conical plate and its own rotation can evenly spread the garbage on the bearing plate, avoiding the problems of incomplete combustion and low efficiency caused by garbage accumulation.

[0024] 3. During the process of the semi-circular frame rotating to the other side, the slider of the cross plate will return from the lowest point to the highest point of the inclined groove and slide towards the inclined groove on the other side. The conical plate returns to the bottom outlet end of the feeding channel again. During this process, the rising of the conical plate drives the air flow to move upward, thereby sending the flue gas into the interior of the feeding channel to preheat the garbage. Until the semi-circular frame rotates to the other side, the conical plate continues to descend, repeating this process until all the garbage inside the conical plate is emptied. The flue gas inside the feeding channel is extracted through the exhaust pipe for waste gas treatment.

[0025] 4. The present invention sucks air into the waste heat recovery layer through a blower, uses the temperature outside the furnace body to recover waste heat into primary air, and sends it into the interior of the connection layer through the air supply pipe, and then dries the garbage through the ventilation grooves on the bearing plate, improving the subsequent combustion efficiency and enabling the garbage to burn stably.

[0026] 5. The air supply of the present invention enters the spoiler tube through a high-pressure blower. The spoiler tube plays a crucial role in the combustion of the incinerator. The spoiler tube can increase the mixing degree of combustion flue gas and oxygen, making the combustion more complete. The structure of the spoiler tube is a 45° micro-hole surrounding type, and the furnace chamber is a vertical circle, making the mixing effect more sufficient. In addition, the upper end of the spoiler tube is a high-pressure air supply area, and an inclined air outlet is inclined downward at a 45° angle to form a downward pressing air curtain, allowing the flue gas to stay in the furnace for a longer time. The upper and lower air duct structures plus the bottom waste heat recovery air distribution structure enable the garbage to burn fully without using oil.

[0027] 6. Compared with the prior art, the present invention improves the sufficiency of the mixing of flue gas, oxygen, etc. inside the furnace body through the cooperation of the 360° air inlet inside the furnace body and the air inlet at the bottom of the furnace body by the spoiler tube. Through the cooperation of the semi-circular frame and the conical plate in the feeding channel, the garbage is intermittently fed and mixed and preheated with the flue gas in the channel, improving the subsequent combustion efficiency. And through the conical plate, the garbage is evenly distributed, which can improve the efficiency of the flue gas entering the inside of the feeding channel. BRIEF DESCRIPTION OF THE DRAWINGS

[0028] Figure 1 It is a schematic diagram of the overall front structure of a low-consumption and high-energy vortex incineration furnace process of the present invention;

[0029] Figure 2 It is a schematic diagram of the overall back structure of a low-consumption and high-energy vortex incineration furnace process of the present invention;

[0030] Figure 3 It is a schematic diagram of the separation of the furnace body bottom and the bottom box of a low-consumption and high-energy vortex incineration furnace process of the present invention;

[0031] Figure 4 It is a schematic diagram of the internal structure of the furnace body of a low-consumption and high-energy vortex incineration furnace process of the present invention;

[0032] Figure 5 It is a schematic diagram of the top structure of the furnace body of a low-consumption and high-energy vortex incineration furnace process of the present invention;

[0033] Figure 6 It is a schematic diagram of the top structure of the feeding channel of a low-consumption and high-energy vortex incineration furnace process of the present invention;

[0034] Figure 7 It is a schematic diagram of the bottom structure of the feeding channel of a low-consumption and high-energy vortex incineration furnace process of the present invention;

[0035] Figure 8 It is a schematic diagram of the connection between the vertical rod and the semi-circular frame of a low-consumption and high-energy vortex incineration furnace process of the present invention.

[0036] In the figure: 1. Furnace body; 11. Slag discharge door; 12. Bearing plate; 13. Turbulence tube; 14. Horizontal air outlet; 15. Inclined air outlet; 16. Conical top frame; 17. Conical plate; 2. Bottom box; 21. High-pressure blower; 3. Waste heat recovery layer; 31. Air supply pipe; 32. Connection layer; 4. Feeding channel; 41. Top cover; 42. Smoke exhaust pipe; 43. Semi-circular frame; 44. Motor; 45. Inclined chute; 46. Vertical rod; 47. Connecting ring; 48. Cross plate; 49. Slide block; 410. Slide rail; 411. Connecting shaft; 412. Slide seat. Detailed implementation manners

[0037] In order to make the technical means, creative features, achieved purposes and functions of the present invention easy to understand, the present invention will be further described below in conjunction with specific implementation manners.

[0038] Please refer to Figures 1 to 8 , the present invention provides a technical solution: a low-consumption and high-energy vortex incinerator process, and the process includes the following steps:

[0039] (1) Feed the waste to be incinerated into the semi-circular frame at the top of the feeding channel in batches for standby;

[0040] (2) Drive the semi-circular frame to make reciprocating left and right flips, and the opening of the conical plate sends the high-temperature flue gas in the furnace body into the channel to be mixed and preheated with the waste;

[0041] (3) Supply the primary air for waste heat recovery into the bottom box by the blower to dry the waste;

[0042] (4) Supply air by the high-pressure blower into the turbulence tube to increase the mixing degree of combustion flue gas and oxygen;

[0043] (5) Send out the ashes after combustion from the slag discharge door for the next group of combustion.

[0044] According to the feeding channel 4 mentioned in step (1) of the above process, the bottom of the feeding channel 4 is connected to the furnace body 1. A slag discharge door 11 is rotatably installed on the outer surface of the furnace body 1, and a conical top frame 16 is fixed to the top of the furnace body 1. The conical top frame 16 is connected to the feeding channel 4. The conical plate 17 is installed at the connection port of the feeding channel 4 and the conical top frame 16. The bottom of the furnace body 1 is fixed with a bottom box 2. The bottom of the turbulence tube 13 is fixed at the center of the bottom of the bottom box 2. A connection layer 32 is fixed around the periphery of the bottom box 2 where the turbulence tube 13 is located. The bottom of the furnace body 1 is fixed with a bearing plate 12, and the connection layer 32 wraps around the bottom of the furnace body 1. Inside the feeding channel 4, there is a vertical rod 46. The top of the vertical rod 46 is rotatably connected to the bottom of the semi-circular frame 43, and the bottom of the vertical rod 46 is fixed to the top of the conical plate 17. Equally spaced connection rings 47 are fixed on the surface of the vertical rod 46, and cross plates 48 are fixed on both sides of the connection ring 47. The cross plates 48 slide along the inner wall of the feeding channel 4. Both sides of the semi-circular frame 43 are rotatably installed on the inner wall of the feeding channel 4 through shaft rods, and there is a space at the top of the feeding channel 4 for the semi-circular frame 43 to flip. On the surface of the turbulence tube 13, multiple groups of horizontal air outlets 14 are equally spaced and surrounded. When using the device, the garbage is put into the semi-circular frame 43 and sent into the furnace body 1 for burning through the flipping of the semi-circular frame 43. Under the action of blowing air from the top and bottom of the furnace body 1 through the turbulence tube 13 and the connection layer 32, a vortex air distribution is formed, so as to facilitate the more complete burning of the garbage and reduce energy consumption.

[0045] In this embodiment, a high-pressure blower 21 is arranged outside the bottom box 2, and the high-pressure blower 21 penetrates into the bottom box 2 through a pipeline and is communicated with the bottom of the turbulence tube 13. The top of the turbulence tube 13 is annularly and equally spaced with inclined air outlets 15, and the inclined air outlets 15 are inclined downward at an angle of 45° with the turbulence tube 13. The high-pressure blower 21 supplies air into the turbulence tube 13. The turbulence tube 13 plays a key role in the burning of the incinerator. The turbulence tube 13 can increase the mixing degree of the combustion flue gas and oxygen, making the combustion more complete. The structure of the turbulence tube 13 is a 360° micro-hole surrounding type, and the furnace chamber is a vertical circle, making the mixing effect more sufficient. In addition, the upper end of the turbulence tube 13 is a high-pressure air supply area. The 45° downward inclination of the inclined air outlets 15 forms a downward pressing air curtain, allowing the flue gas to stay in the furnace for a longer time. The upper and lower air duct structures plus the bottom waste heat recovery air distribution structure make the garbage burn fully without using oil.

[0046] In this embodiment, a waste heat recovery layer 3 is sleeved on the outer surface of the furnace body 1. The bottom of the waste heat recovery layer 3 is connected with an air supply pipe 31. The other end of the air supply pipe 31 penetrates into the inner part of the bottom box 2 and communicates with a connection layer 32. Ventilation grooves are arranged on the surface of the bearing plate 12. The waste heat recovery layer 3 is a common device for recovering waste heat. Air is sucked into the waste heat recovery layer 3 by a fan, and the temperature outside the furnace body 1 is used to recover waste heat into primary air, which is then sent into the connection layer 32 through the air supply pipe 31. Then, the waste is dried through the ventilation grooves on the bearing plate 12, improving the subsequent combustion efficiency and enabling the waste to burn stably.

[0047] In this embodiment, a top cover 41 is rotatably and sealingly installed at the top of the feeding channel 4, and a smoke exhaust pipe 42 is provided on one side of the top of the feeding channel 4. A motor 44 is fixed on the outer wall of the feeding channel 4, and the output end of the motor 44 is fixedly connected to the shaft of the semi-circular frame 43. The motor 44 drives the semi-circular frame 43 to reciprocally flip by no more than ninety degrees. A slide rail 410 is fixed at the bottom of the semi-circular frame 43, and a slide seat 412 is slidably connected inside the slide rail 410. A connecting shaft 411 is installed at the bottom of the slide seat 412, and the top of the vertical rod 46 is installed on the connecting shaft 411. The connecting shaft 411 is composed of two groups of rotating shafts, and the rotation directions of the connecting shaft 411 are respectively parallel to the slide rail 410 and perpendicular to the axis of the vertical rod 46. Oblique slots 45 are provided at the positions of the feeding channel 4 corresponding to each group of cross plates 48, and the oblique slots 45 are symmetrically arranged with respect to the axis of the feeding channel 4. One end of the cross plate 48 is rotatably installed with a slider 49, and the slider 49 slides along the inside of the oblique slot 45. The surface of the cross plate 48 is inclined, and the inclination directions of the cross plates 48 on both sides of the connecting ring 47 are opposite. When the semi-circular frame 43 is in a horizontal state, through the connection of the vertical rod 46, the conical plate 17 blocks the bottom outlet end of the feeding channel 4. At this time, flue gas cannot enter the inside of the feeding channel 4, avoiding the direct entry of flue gas from the top of the feeding channel 4 into the air. Open the top cover 41 and send a certain amount of garbage into the semi-circular frame 43. Close the top cover 41, and the motor 44 drives the semi-circular frame 43 to reciprocally flip around the shaft. The flipping angle is not too large, meeting the descending height of the vertical rod 46 and the moving path of the cross plate 48 along the oblique slot 45. When the semi-circular frame 43 flips to one side, because the vertical rod 46 always remains at the axis position of the feeding channel 4, the connecting shaft 411 and the slide seat 412 connecting the vertical rod 46 slide along the slide rail 410. At this time, the vertical rod 46 will be pressed down. Because the vertical rod 46 is restricted by the cross plate 48, during the pressing-down process, the cross plate 48 slides along the oblique slot 45, and the oblique slot 45 is a chute from high to low, surrounding the inner wall of the feeding channel 4. At this time, as the vertical rod 46 descends, the cross plate 48 slides along the oblique slot 45 and rotates itself, driving the vertical rod 46 and the conical plate 17 to rotate together through the connecting ring 47. The function of this rotation is that, on the one hand, as the semi-circular frame 43 flips, some garbage will fall from the lower side of the semi-circular frame 43. During this process, the rotation of the vertical rod 46 and the cross plate 48 breaks up the garbage, so as to better mix with the high-temperature flue gas for preheating. Then, when it falls on the conical plate 17, the inclined surface of the conical plate 17 and its own rotation can evenly spread the garbage on the bearing plate 12, avoiding problems such as incomplete combustion and low efficiency caused by garbage accumulation. Similarly, during the process of the semi-circular frame 43 rotating to the other side, the slider 49 of the cross plate 48 will return from the lowest point to the highest point of the oblique slot 45 and slide towards the oblique slot 45 on the other side. The conical plate 17 returns to the bottom outlet end of the feeding channel 4 again. During this process, the rising of the conical plate 17 will drive the air flow to move upward, thereby sending the flue gas into the inside of the feeding channel 4 to preheat the garbage.When the semi-circular frame 43 is flipped to the other side, the conical plate 17 continues to descend. During the repetition of this process, until all the garbage inside the conical disc is emptied, the flue gas inside the feeding channel 4 is extracted through the exhaust pipe 42 for waste gas treatment.

[0048] When using the device, when the semi-circular frame 43 is in a horizontal state, through the connection of the vertical rod 46, the conical plate 17 blocks the bottom outlet end of the feeding channel 4. At this time, the flue gas cannot enter the inside of the feeding channel 4, avoiding the direct entry of the flue gas from the top of the feeding channel 4 into the air. Open the top cover 41 and send a certain amount of garbage into the semi-circular frame 43, then close the top cover 41. The motor 44 drives the semi-circular frame 43 to reciprocally rotate around the shaft rod. The rotation angle is not too large, satisfying the descending height of the vertical rod 46 and the moving path of the cross plate 48 along the inclined groove 45. When the semi-circular frame 43 rotates towards one side, because the vertical rod 46 always remains at the axis position of the feeding channel 4, the connecting shaft 411 and the sliding seat 412 connecting the vertical rod 46 slide along the slide rail 410. At this time, the vertical rod 46 will be pressed down. Because the vertical rod 46 is restricted by the cross plate 48, during the pressing-down process, the cross plate 48 slides along the inclined groove 45, and the inclined groove 45 is a chute from high to low, surrounding the inner wall of the feeding channel 4. At this time, as the vertical rod 46 descends, the cross plate 48 slides along the inclined groove 45 and rotates itself, driving the vertical rod 46 and the conical plate 17 to rotate together through the connecting ring 47. The function of this rotation is that, on the one hand, as the semi-circular frame 43 rotates, part of the garbage will fall from the lower side of the semi-circular frame 43. During this process, the rotation of the vertical rod 46 and the cross plate 48 breaks up the garbage, so as to better mix and preheat with the high-temperature flue gas. Then when it falls on the conical plate 17, the inclined surface of the conical plate 17 and its own rotation can evenly spread the garbage on the bearing plate 12, avoiding problems such as incomplete combustion and low efficiency caused by garbage accumulation. Similarly, during the process of the semi-circular frame 43 rotating to the other side, the slider 49 of the cross plate 48 will return from the lowest point to the highest point of the inclined groove 45 and slide towards the inclined groove 45 on the other side. The conical plate 17 returns to the bottom outlet end of the feeding channel 4 again. During this process, the rising of the conical plate 17 will drive the air flow to move upward, and then send the flue gas into the inside of the feeding channel 4 to preheat the garbage. Until the semi-circular frame 43 rotates to the other side, the conical plate 17 continues to descend. Repeat this process until all the garbage inside the conical plate is emptied. The flue gas inside the feeding channel 4 is extracted through the exhaust pipe 42 for waste gas treatment. The air is inhaled into the waste heat recovery layer 3 by the fan, and the temperature outside the furnace body 1 is used to recover the waste heat into primary air, and then sent into the inside of the connection layer 32 through the air supply pipe 31, and the garbage is dried through the ventilation slots on the bearing plate 12 to improve the subsequent combustion efficiency and make the garbage burn stably. The high-pressure fan 21 supplies air into the turbulence pipe 13. The turbulence pipe 13 plays a key role in the combustion of the incinerator. The turbulence pipe 13 can increase the mixing degree of the combustion flue gas and oxygen, making the combustion more complete. The structure of the turbulence pipe 13 is a 360° micro-hole surrounding type, and the furnace chamber is a vertical circle, making the mixing effect more sufficient. In addition, the upper end of the turbulence pipe 13 is a high-pressure air supply area, and the 45° angle of the inclined air outlet 15 is inclined downward to form a downward pressing air curtain, making the flue gas stay in the furnace for a longer time. The upper and lower air pipe structures plus the bottom waste heat recovery air distribution structure make the garbage burn fully without using oil.

[0049] The foregoing has shown and described the basic principles, main features and advantages of the present invention. For a person skilled in the art, it is obvious that the present invention is not limited to the details of the above-described exemplary embodiments, and without departing from the spirit or essential characteristics of the present invention, the present invention can be implemented in other specific forms.

[0050] In addition, it should be understood that although this specification is described in terms of embodiments, not every embodiment contains only one independent technical solution. This narrative manner of the specification is only for clarity. Those skilled in the art should regard the specification as a whole, and the technical solutions in each embodiment can also be appropriately combined to form other embodiments that can be understood by those skilled in the art.

Claims

1. A low-consumption, high-energy vortex incinerator process, characterized in that: The process comprises the following steps: (1) Feed the garbage to be incinerated into the semicircular frame at the top of the feeding channel in batches as a backup; (2) The semicircular frame is driven to flip back and forth, and the conical plate is opened to send the high-temperature flue gas in the furnace body into the channel to mix with the garbage for preheating; (3) The fan supplies primary air for waste heat recovery in the bottom box to dry the garbage; (4) The high-pressure fan supplies air into the turbulence tube to increase the mixing degree of combustion flue gas and oxygen; (5) The ashes after combustion are sent out through the slag discharge door for the next group of combustion. According to the feeding channel (4) mentioned in step (1) of the above process, the bottom of the feeding channel (4) is connected to the furnace body (1), a slag discharge door (11) is rotatably installed on the outer surface of the furnace body (1), and a conical top frame (16) is fixed on the top of the furnace body (1), the conical top frame (16) is connected to the feeding channel (4), the conical plate (17) is installed at the connection between the feeding channel (4) and the conical top frame (16), the bottom of the furnace body (1) is fixed to the bottom of the bottom box (2), the bottom of the spoiler tube (13) is fixed at the bottom center of the bottom box (2), the bottom box (2) is located on the periphery of the spoiler tube (13) and is fixed with a connecting layer (32), the bottom of the furnace body (1) is fixed to the bottom of the bearing plate (12), and the connecting layer (3 2) wrapped around the bottom of the furnace body (1), a vertical rod (46) is provided inside the feeding channel (4), the top of the vertical rod (46) is rotatably connected to the bottom of the semicircular frame (43), and the bottom of the vertical rod (46) is fixed to the top of the conical plate (17), connecting rings (47) are fixed at equal intervals on the surface of the vertical rod (46), and horizontal plates (48) are fixed on both sides of the connecting ring (47), and the horizontal plates (48) slide along the inner wall of the feeding channel (4), the two sides of the semicircular frame (43) are rotatably mounted on the inner wall of the feeding channel (4) through an axial rod, and a space for the semicircular frame (43) to flip is provided at the top of the feeding channel (4), and a plurality of groups of horizontal air outlets (14) are equidistantly arranged on the surface of the spoiler pipe (13).

2. A low-consumption, high-energy vortex incinerator process according to claim 1, characterized in that: A high-pressure fan (21) is arranged on the outside of the bottom box (2), and the high-pressure fan (21) penetrates into the inside of the bottom box (2) through a pipeline and communicates with the bottom of the spoiler tube (13).

3. A low-consumption, high-energy vortex incinerator process according to claim 2, characterized in that: A waste heat recovery layer (3) is sleeved on the outer surface of the furnace body (1), an air supply pipe (31) is connected to the bottom of the waste heat recovery layer (3), and the other end of the air supply pipe (31) penetrates into the interior of the bottom box (2) and communicates with the connection layer (32). Ventilation grooves are arranged on the surface of the bearing plate (12).

4. A low-consumption, high-energy vortex incinerator process according to claim 3, characterized in that: The top of the spoiler tube (13) is provided with inclined air outlets (15) in an annular manner and at equal intervals, and the inclined air outlets (15) are inclined downward at an angle of 45° to the spoiler tube (13).

5. The low-consumption and high-energy vortex incinerator process according to claim 1 is characterized in that: A top cover (41) is rotatably sealed and installed on the top of the feeding channel (4), and a smoke exhaust pipe (42) is arranged on one side of the top of the feeding channel (4).

6. A low-consumption, high-energy vortex incinerator process according to claim 1, characterized in that: A motor (44) is fixed on the outer wall of the feeding channel (4), and the output end of the motor (44) is fixedly connected to the shaft rod of the semicircular frame (43). The motor (44) drives the semicircular frame (43) to perform reciprocating flipping within 90 degrees.

7. A low-consumption, high-energy vortex incinerator process according to claim 6, characterized in that: A slide rail (410) is fixed at the bottom of the semicircular frame (43), and a slide seat (412) is slidably connected inside the slide rail (410). A connecting shaft (411) is installed at the bottom of the slide seat (412), and the top of the vertical rod (46) is installed on the connecting shaft (411).

8. A low-consumption, high-energy vortex incinerator process according to claim 7, characterized in that: The connecting shaft (411) is composed of two groups of rotating shafts, and the rotation directions of the connecting shaft (411) are respectively parallel to the slide rail (410) and perpendicular to the axis of the vertical rod (46).

9. A low-consumption, high-energy vortex incinerator process according to claim 8, characterized in that: The feeding channel (4) is provided with an inclined groove (45) corresponding to the position of each group of transverse plates (48), and the inclined groove (45) is symmetrically arranged with respect to the axis of the feeding channel (4). A sliding block (49) is rotatably mounted on one end of the transverse plate (48), and the sliding block (49) slides inside the inclined groove (45).

10. A low-consumption, high-energy vortex incinerator process according to claim 9, characterized in that: The surface of the transverse plate (48) is arranged to be inclined, and the transverse plates (48) on both sides of the connecting ring (47) are inclined in opposite directions.

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