Utilization and treatment device for high-concentration organic wastewater in preserved fruit processing

Abstract

The invention discloses a utilization and treatment device for high-concentration organic wastewater in preserved fruit processing, and relates to the field of utilization and treatment devices for organic wastewater in preserved fruit processing, the utilization and treatment device comprises a base, a distillation retort and a cooling retort, a fixed plate is slidably connected in the distillation retort, and conical air outlets are formed in the two ends in the fixed plate; a baffle is rotationally connected to the interior of the conical air outlet, rotating plates are fixed to the two sides of the baffle, a crank is rotationally connected to one side of each rotating plate, a ball is arranged at the tail end of each crank, a first fixing block is rotationally connected to the bottom of each ball, and a second rotating shaft is rotationally connected to the middle of each first fixing block; through left-right swing and rotation of an arc-shaped ring and rotation of a spiral blade, irregular stirring is carried out, and heat transfer can be accelerated through stirring due to the fact that when substances are stirred, movement between molecules becomes more violent, heat can be rapidly transferred, and hot air emission is increased.

Description

Technical Field

[0001] The invention relates to the field of utilization and treatment devices for organic wastewater in preserved fruit processing, in particular to a utilization and treatment device for high-concentration organic wastewater in preserved fruit processing. Background Art

[0002] Preserved fruit is a kind of dried fruit formed by drying fruits. It has the functions of relieving hunger, providing nutrition, improving digestion, controlling blood sugar and improving taste. The utilization and treatment device of organic wastewater from preserved fruit processing is mainly used to treat the organic wastewater generated in the process of preserved fruit processing. These wastewaters contain a large amount of suspended matter, fructose, pectin substances, and high concentration of organic matter, which pollute the environment.

[0003] The existing pretreatment step of the preserved fruit wastewater is to remove macromolecular impurities and solid particles in the wastewater through pretreatment. If macromolecular particles such as peel and pulp are added to the preserved fruit processing wastewater for coagulation and precipitation, the formed floccules are separated by precipitation. The organic matter in the water is degraded by the anaerobic sludge bed through biochemical treatment to form methanogenic bioenergy. The digested liquid enters the intermediate sedimentation tank. The supernatant after precipitation enters the contact oxidation tank. Through aeration and oxygenation, the biofilm attached to the filler contacts with the preserved fruit processing wastewater to achieve the purpose of removing pollutants. The wastewater after the above treatment can be further concentrated and treated by evaporation technology. The evaporation technology can evaporate the water in the wastewater, thereby concentrating the organic matter. These concentrated organic matter can be further recycled, such as as fertilizer, energy or other industrial raw materials.

[0004] During distillation, the mist generated in the wastewater will come into contact with the top plate and the inner wall of the main body, causing part of the distilled mist liquid to fall into the wastewater liquid again, requiring multiple distillations. In addition, the upward discharge of the distilled gas during the distillation process is slow, resulting in reduced efficiency. Summary of the invention

[0005] The purpose of the present invention is to provide a device for utilizing and treating high-concentration organic wastewater in preserved fruit processing in order to solve the problem that the mist generated in the wastewater during distillation will contact the top plate and the inner wall of the main body, causing part of the distilled mist liquid to fall into the wastewater liquid again, requiring multiple distillations, and the process of discharging the distilled gas upward during the distillation process is slow, resulting in reduced efficiency.

[0006] To achieve the above-mentioned purpose, the present invention provides the following technical solutions: a device for utilizing and treating high-concentration organic wastewater in preserved fruit processing, comprising a base, a distillation tank, and a cooling tank. A fixed plate is slidably connected to the interior of the distillation tank, and the fixed plate squeezes the gas in the distillation tank to increase the gas pressure in the distillation tank, thereby increasing the temperature and accelerating the distillation speed. Conical air outlets are arranged at both ends of the interior of the fixed plate. A baffle is rotatably connected to the interior of the conical air outlet. Rotating plates are fixed on both sides of the baffle. When the gas pressure inside the distillation tank reaches a certain level, steam will push one side of the baffle inside the conical air outlet to rotate the baffle. The rotation of the baffle drives the rotating plate to rotate, and one side of the two groups of rotating plates are respectively rotatably connected to cranks, and a round ball is arranged at the end of the crank. The bottom of the round ball is rotatably connected to a fixed block No. 1, and the middle of the fixed block No. 1 The first and second fixing blocks are fixed to the wheels of the present invention, and the bottom of the fixing block is provided with a fixing ring, and an annular groove is arranged at the bottom of the fixing ring. The inner rotation of the annular groove is connected with an arc ring. The rotating plate drives the cranks on both sides to move up and down respectively, and the crank drives the balls to move up and down respectively to push the first fixing block to swing left and right. The first fixing block drives the fixing ring and the arc ring to swing left and right. A stopper is fixed on one side of the arc ring. When the spiral blade rotates, it drives the stopper to move in a circle, and the stopper drives the arc ring to rotate. The arc ring is irregularly stirred through the left and right swinging and rotation of the arc ring and the rotation of the spiral blade. The stirring can accelerate the heat transfer because when the substance is stirred, the movement between the molecules becomes more violent, which helps to transfer heat quickly and increase the discharge of hot gas.

[0007] As a further solution of the present invention: the cranks are respectively arranged at positions where the center of one group of rotating plates is upward, and the other group of cranks are respectively arranged at positions where the center of another group of rotating plates is downward, and the tops of the No. 2 and No. 1 fixed blocks are fixedly connected to the bottoms of the fixed plates.

[0008] As a further solution of the present invention: a motor is installed on the outside of the distillation tank, a gear is fixed to the output end of the motor, a gear ring is rotatably connected to the inner cavity of the distillation tank, a rotating ring is fixed to the top and bottom of the gear ring, and the rotating ring is arranged in the inner cavity of the distillation tank.

[0009] As a further solution of the present invention: a No. 1 threaded ring is fixed to the inner wall of the gear ring, the motor drives the gear to rotate, the gear drives the gear ring to rotate, the gear ring drives the No. 1 threaded ring to rotate, the No. 2 threaded ring is internally rotatably connected to the No. 1 threaded ring, the bottom of the No. 2 threaded ring is fixedly connected to the top of the fixed plate, the No. 1 threaded ring drives the No. 2 threaded ring to move downward, the No. 2 threaded ring drives the fixed plate to move downward, and a conical column is provided at the bottom of the fixed plate.

[0010] As a further solution of the present invention: the middle part of the fixed plate is rotatably connected to a first rotating shaft, the top of the first rotating shaft is fixed with a fan blade, and the bottom of the first rotating shaft is fixed with a spiral blade.

[0011] As a further solution of the present invention: the bottom of the spiral blade is set to a groove shape, and the bottom of the spiral blade is set to a groove shape. When the spiral blade rotates, it can better push the wastewater downward, so that the top wastewater is pushed by the spiral blade to the bottom wastewater to move back and forth. The top of the spiral blade is in contact with the baffle, and when the baffle rotates, the steam is quickly ejected through the conical air outlet. The quickly ejected steam pushes the fan blade to rotate, and the fan blade drives the No. 1 rotating shaft to rotate, and the No. 1 rotating shaft drives the spiral blade to rotate. The fan blade is set at the air outlet of the conical air outlet.

[0012] As a further solution of the present invention: the inner cavity of the distillation tank is provided with a heat conduction pipe, the inner cavity of the cooling tank is provided with a cooling conduction pipe, the gas enters the cooling tank through the pipe, the steam is liquefied through the refrigerator and the cooling conduction pipe, and the organic matter after distillation is further recovered, the bottom of the distillation tank is provided with a heater funnel entering the pipe to prevent the distilled gas from remaining in the distillation tank, the bottom of the cooling tank is provided with a refrigerator, the middle of the bottom of the distillation tank is provided with a No. 1 discharge port, and the bottom of the cooling tank is provided with a No. 2 discharge port.

[0013] As a further solution of the present invention: a feed inlet arc ring is provided on one side of the distillation tank. When the arc ring swings and rotates left and right and the spiral blades rotate, the distilled objects will also be stirred to prevent them from condensing into blocks or accumulating at the bottom of the distillation tank. A pipeline is provided on the top of the distillation tank, a one-way valve is provided inside the pipeline, a pressure gauge is provided on the outside of the pipeline, a funnel is provided on the top of the distillation tank, and the end of the pipeline is connected to the top of the cooling tank.

[0014] As a further scheme of the present invention: first, the wastewater needs to be pretreated to remove macromolecular impurities and solid particles in the wastewater. Macromolecular particles such as peel and pulp are intercepted by a grid pool, and then simply separated by a primary sedimentation tank. The supernatant is taken into an adjusting tank for homogenization and equalization. After adjusting the pH, it flows into a coagulation sedimentation tank. A coagulant is added to the preserved fruit processing wastewater for reaction. The formed floccules are separated by precipitation. This step helps to remove floating matter and some soluble organic matter in the wastewater. The organic matter in the water is degraded by an anaerobic sludge bed to form methanogenic bioenergy. The digestate enters a medium sedimentation tank. The supernatant after precipitation enters a contact oxidation tank. Through air blowing and oxygenation, the biofilm adhered to the filler contacts with the preserved fruit processing wastewater to achieve the purpose of removing pollutants. The wastewater after the above treatment can be further concentrated and treated by evaporation technology. The evaporation technology can evaporate the water in the wastewater, thereby concentrating the organic matter. These concentrated organic matter can be further recycled, such as as fertilizer, energy or other industrial raw materials.

[0015] Compared with the prior art, the present invention has the following beneficial effects:

[0016] 1. The motor is set to drive the gear to rotate, the gear drives the gear ring to rotate, the gear ring drives the No. 1 thread ring to rotate, the No. 1 thread ring drives the No. 2 thread ring to move downward, and the No. 2 thread ring drives the fixed plate to move downward, so that the fixed plate squeezes the gas in the distillation tank, increases the gas pressure in the distillation tank, thereby increasing the temperature and speeding up the distillation;

[0017] 2. Through the baffle, when the air pressure inside the distillation tank reaches a certain level, the steam will push one side of the baffle inside the conical air outlet to make the baffle rotate. The rotation of the baffle drives the rotating plate to rotate. The rotating plate drives the cranks on both sides to move up and down respectively. The crank drives the balls to move up and down respectively to push the No. 1 fixed block to swing left and right. The No. 1 fixed block drives the fixed ring and the arc ring to swing left and right to prevent the residue of the waste water in the distillation tank from settling at the bottom.

[0018] 3. When the baffle rotates, steam is quickly ejected through the conical air outlet. The quickly ejected steam pushes the fan blades to rotate, and the fan blades drive the No. 1 rotating shaft to rotate, and the No. 1 rotating shaft drives the spiral blades to rotate. The bottom of the spiral blades is set in a groove shape. When the spiral blades rotate, the wastewater can be better pushed downward, so that the top wastewater is pushed by the spiral blades to the bottom wastewater to move back and forth. When the spiral blades rotate, they drive the push block to move in a circle, and the block drives the arc ring to rotate. The arc ring is swung left and right and rotated with the rotation of the spiral blades, so that it is irregularly stirred. The reason why stirring can accelerate heat transfer is that when the substance is stirred, the movement between molecules becomes more violent, which helps to quickly transfer heat and increase the discharge of hot air.

[0019] 4. The conical air outlet can be set to quickly discharge the gas and enter the pipeline through the funnel to prevent the distilled gas from remaining inside the distillation tank. The gas enters the cooling tank through the pipeline, and the steam is liquefied through the refrigerator and the cooling pipe. The organic matter after distillation is recovered in one step. The swing and rotation of the arc ring and the rotation of the spiral blades will also stir the distilled objects to prevent them from condensing into blocks or accumulating at the bottom of the distillation tank. BRIEF DESCRIPTION OF THE DRAWINGS

[0020] Figure 1 It is a schematic diagram of the overall structure of the present invention;

[0021] Figure 2 It is a schematic diagram of the overall internal structure of the present invention;

[0022] Figure 3 It is a schematic diagram of the internal structure of the distillation tank of the present invention;

[0023] Figure 4 It is a schematic diagram of the structure of the No. 1 and No. 2 threaded rings of the present invention;

[0024] Figure 5 It is a schematic diagram of the bottom structure of the fixing plate of the present invention;

[0025] Figure 6 It is a schematic diagram of the spiral leaf structure of the present invention;

[0026] Figure 7 It is a schematic diagram of the fixing ring structure of the present invention;

[0027] Figure 8 It is a schematic diagram of the bottom structure of the fixing ring of the present invention.

[0028] In the figure: 1. base; 101. distillation tank; 102. cooling tank; 103. heat pipe; 104. cooling pipe; 105. discharge port No. 1; 106. discharge port No. 2; 107. heater; 108. refrigerator; 109. feed port; 110. pipeline; 111. check valve; 112. pressure gauge; 113. funnel; 2. motor; 201. gear; 202. gear ring; 203. threaded ring No. 1; 204. threaded ring No. 2 Threaded ring; 205, fixed plate; 206, rotating ring; 207, conical column; 208, conical air outlet; 3, rotating shaft No. 1; 301, fan blade; 302, spiral blade; 4, baffle; 401, rotating plate; 402, crank; 403, ball; 404, fixed block No. 1; 405, rotating shaft No. 2; 406, No. 2 and No. 1 fixed blocks; 407, fixed ring; 408, annular groove; 409, arc ring; 410, block. DETAILED DESCRIPTION

[0029] The following will be combined with the drawings in the embodiments of the present invention to clearly and completely describe the technical solutions in the embodiments of the present invention. Obviously, the described embodiments are only part of the embodiments of the present invention, not all of the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by ordinary technicians in this field without creative work are within the scope of protection of the present invention.

[0030] See also Figure 2 , 3 , 4, 5, 7, 8, in the embodiment of the present invention, a device for utilizing and treating high-concentration organic wastewater in preserved fruit processing comprises a base 1, a distillation tank 101, and a cooling tank 102. The interior of the distillation tank 101 is slidably connected with a fixed plate 205, the fixed plate 205 squeezes the gas in the distillation tank 101 to increase the gas pressure of the distillation tank 101, thereby increasing the temperature and accelerating the distillation speed. Both ends of the interior of the fixed plate 205 are provided with conical air outlets 208, and the interior of the conical air outlet 208 is rotatably connected to the cooling tank 102. The baffle 4 is connected to the distillation tank 101, and rotating plates 401 are fixed on both sides of the baffle 4. When the air pressure inside the distillation tank 101 reaches a certain level, the steam will push one side of the baffle 4 inside the conical air outlet 208 to rotate the baffle 4. The rotation of the baffle 4 drives the rotating plates 401 to rotate, and one side of the two sets of rotating plates 401 is respectively rotatably connected to a crank 402, and a ball 403 is arranged at the end of the crank 402. The bottom of the ball 403 is rotatably connected to a No. 1 fixed block 404, and the middle of the No. 1 fixed block 404 is rotatably connected to two The end of the No. 2 rotating shaft 405 is fixed with a No. 2 and No. 1 fixing block 406, a fixing ring 407 is fixed to the bottom of the No. 1 fixing block 404, a ring groove 408 is provided at the bottom of the fixing ring 407, an arc ring 409 is connected to the inner rotation of the ring groove 408, the rotating plate 401 drives the cranks 402 on both sides to move up and down respectively, the cranks 402 drive the balls 403 to move up and down respectively to push the No. 1 fixing block 404 to swing left and right, the No. 1 fixing block 404 drives the fixing ring 407 to move left and right, and the No. 1 fixing block 404 drives the fixing ring 407 to move left and right. 07. The arc ring 409 swings left and right, and a stopper 410 is fixed on one side of the arc ring 409. When the spiral blade 302 rotates, it drives the stopper 410 to perform circular motion, and the stopper 410 drives the arc ring 409 to rotate. The arc ring 409 swings left and right and rotates with the spiral blade 302, so that it is irregularly stirred. The reason why stirring can accelerate heat transfer is that when the material is stirred, the movement between molecules becomes more intense, which helps to quickly transfer heat and increase the discharge of hot gas;

[0031] The cranks 402 are respectively arranged at the upward position of the center of one group of rotating plates 401, and the other group of cranks 402 are respectively arranged at the downward position of the center of the other group of rotating plates 401. The top of the No. 2 and No. 1 fixing blocks 406 is fixedly connected to the bottom of the fixing plate 205. The motor 2 is installed on the outside of the distillation tank 101, and the output end of the motor 2 is fixed with a gear 201. The inner cavity of the distillation tank 101 is rotatably connected with a gear ring 202. The top and bottom of the gear ring 202 are fixed with a rotating ring 206. The rotating ring 206 is arranged in the inner cavity of the distillation tank 101. The inner wall of the gear ring 202 is fixed with a No. 1 threaded ring 203. The motor 2 drives the gear 201 rotates, the gear 201 drives the gear ring 202 to rotate, the gear ring 202 drives the No. 1 threaded ring 203 to rotate, the No. 1 threaded ring 203 is internally rotatably connected with the No. 2 threaded ring 204, the bottom of the No. 2 threaded ring 204 is fixedly connected with the top of the fixed plate 205, the No. 1 threaded ring 203 drives the No. 2 threaded ring 204 to move downward, the No. 2 threaded ring 204 drives the fixed plate 205 to move downward, a conical column 207 is provided at the bottom of the fixed plate 205, the middle part of the fixed plate 205 is rotatably connected with the No. 1 rotating shaft 3, the top of the No. 1 rotating shaft 3 is fixed with a fan blade 301, and the bottom of the No. 1 rotating shaft 3 is fixed with a spiral blade 302.

[0032] In this embodiment: the motor 2 drives the gear 201 to rotate, the gear 201 drives the gear ring 202 to rotate, the gear ring 202 drives the first pattern ring 203 to rotate, the first pattern ring 203 drives the second threaded ring 204 to move downward, the second threaded ring 204 drives the fixed plate 205 to move downward, so that the fixed plate 205 squeezes the gas in the distillation tank 101, so that the air pressure of the distillation tank 101 increases, thereby increasing the temperature and accelerating the distillation speed. When the air pressure inside the distillation tank 101 reaches a certain level, the steam will push one side of the baffle 4 inside the conical air outlet 208 to rotate the baffle 4, and the rotation of the baffle 4 drives the rotating plate 401 to rotate, and the rotating plate 401 drives the cranks 402 on both sides to move up and down respectively, and the cranks 402 drive the balls 403 to move up and down respectively to push the first fixed block 404 to swing left and right, and the first fixed block 404 drives the fixed ring 407, the arc The ring 409 swings left and right, and when the baffle 4 rotates, steam is quickly ejected through the conical air outlet 208. The quickly ejected steam pushes the fan blade 301 to rotate, and the fan blade 301 drives the No. 1 rotating shaft 3 to rotate, and the No. 1 rotating shaft 3 drives the spiral blade 302 to rotate. The bottom of the spiral blade 302 is set in a groove shape. When the spiral blade 302 rotates, it can better push the wastewater downward, so that the top wastewater is pushed by the spiral blade 302 to the bottom wastewater to move back and forth. When the spiral blade 302 rotates, it drives the push block 410 to move in a circle, and the block 410 drives the arc ring 409 to rotate. Through the left and right swinging and rotation of the arc ring 409 and the rotation of the spiral blade 302, it is irregularly stirred. The reason why stirring can accelerate heat transfer is that when the substance is stirred, the movement between molecules becomes more violent, which helps to quickly transfer heat and increase the discharge of hot air.

[0033] Please refer to Figure 1 , 2, 3, 6, the bottom of the spiral blade 302 is set to a groove shape, and the bottom of the spiral blade 302 is set to a groove shape. When the spiral blade 302 rotates, it can better push the wastewater downward, so that the top wastewater is pushed by the spiral blade 302 to the wastewater at the bottom to move back and forth, and the top of the spiral blade 302 contacts the block 410. When the baffle 4 rotates, the steam is quickly ejected through the conical air outlet 208. The quickly ejected steam pushes the fan blade 301 to rotate, and the fan blade 301 drives the No. 1 rotating shaft 3 to rotate, and the No. 1 rotating shaft 3 drives the spiral blade 302 to rotate. The fan blade 301 is set at the outlet of the conical air outlet 208. The inner cavity of the distillation tank 101 is provided with a heat conduction pipe 103, and the inner cavity of the cooling tank 102 is provided with a cooling pipe 104. The gas enters the cooling tank 102 through the pipeline 110, and the steam is liquefied through the refrigerator 108 and the cooling pipe 104. After distillation The organic matter is further recovered. A heater 107 and a funnel 113 are provided at the bottom of the distillation tank 101 to enter the pipeline 110 to prevent the distilled gas from remaining in the distillation tank 101. A refrigerator 108 is provided at the bottom of the cooling tank 102. A No. 1 discharge port 105 is provided in the middle of the bottom of the distillation tank 101, and a No. 2 discharge port 106 is provided at the bottom of the cooling tank 102. A feed port 109 is provided on one side of the distillation tank 101. When the arc ring 409 swings and rotates left and right and the spiral blade 302 rotates, the distilled object will also be stirred to prevent it from condensing into blocks or accumulating at the bottom of the distillation tank 101. A pipeline 110 is provided at the top of the distillation tank 101, a one-way valve 111 is provided inside the pipeline 110, a pressure gauge 112 is provided on the outside of the pipeline 110, a funnel 113 is provided at the top of the distillation tank 101, and the end of the pipeline 110 is connected to the top of the cooling tank 102.

[0034] In this embodiment: the funnel 113 enters the pipeline 110 to prevent the distilled gas from remaining inside the distillation tank 101. The gas enters the cooling tank 102 through the pipeline 110, and the steam is liquefied through the refrigerator 108 and the cooling pipe 104. The distilled organic matter is further recovered. The swinging and rotation of the arc ring 409 and the rotation of the spiral blade 302 will also stir the distilled object to prevent it from condensing into blocks or accumulating at the bottom of the distillation tank 101.

[0035] Working principle: wastewater is transported to the distillation tank 101 through the feed port 109, and the wastewater inside the distillation tank 101 is heated by the heater 107 and the heat pipe 103. The control motor 2 drives the gear 201 to rotate, the gear 201 drives the gear ring 202 to rotate, the gear ring 202 drives the first threaded ring 203 to rotate, the first threaded ring 203 drives the second threaded ring 204 to move downward, and the second threaded ring 204 drives the fixed plate 205 to move downward, so that the fixed plate 205 is pressed against the distillation tank 101. The gas in the distillation tank 101 is squeezed to increase the gas pressure, thereby increasing the temperature and accelerating the distillation speed. When the gas pressure inside the distillation tank 101 reaches a certain level, the steam will push one side of the baffle 4 inside the conical outlet 208 to rotate the baffle 4. The rotation of the baffle 4 drives the rotating plate 401 to rotate. The rotating plate 401 drives the cranks 402 on both sides to move up and down respectively. The cranks 402 drive the balls 403 to move up and down respectively to push the No. 1 fixed block 404. Swing left and right, the No. 1 fixed block 404 drives the fixed ring 407 and the arc ring 409 to swing left and right, when the baffle 4 rotates, the steam is quickly ejected through the conical air outlet 208, and the quickly ejected steam drives the fan blade 301 to rotate, the fan blade 301 drives the No. 1 rotating shaft 3 to rotate, the No. 1 rotating shaft 3 drives the spiral blade 302 to rotate, the bottom of the spiral blade 302 is set in a groove shape, when the spiral blade 302 rotates, it can better push the wastewater downward, so that the top wastewater is pushed by the spiral blade 302 to the wastewater at the bottom to move back and forth, when the spiral blade 302 rotates, it drives the push block 410 to move in a circle, the block 410 drives the arc ring 409 to rotate, through the left and right swinging and rotation of the arc ring 409 and the rotation of the spiral blade 302, it is irregularly stirred, the reason why stirring can accelerate heat transfer is that when the material is stirred, the movement between molecules becomes more intense, which helps to quickly transfer heat and increase the discharge of hot air;

[0036] The conical gas outlet 208 can be set to quickly discharge the gas and enter the pipeline 110 through the funnel 113, so as to prevent the distilled gas from remaining in the distillation tank 101. The gas enters the cooling tank 102 through the pipeline 110, and the steam is liquefied through the refrigerator 108 and the cooling pipe 104. The organic matter after distillation is further recovered. The swinging and rotation of the arc ring 409 and the rotation of the spiral blade 302 will also stir the distilled object to prevent it from condensing into blocks or accumulating at the bottom of the distillation tank 101.

[0037] What is described above is only a preferred specific implementation manner of the present invention, but the protection scope of the present invention is not limited thereto. Any technician familiar with the technical field can make equivalent replacements or changes according to the technical scheme and inventive concept of the present invention within the technical scope disclosed by the present invention, which should be covered by the protection scope of the present invention.

Claims

1. A device for utilizing and treating high-concentration organic wastewater in preserved fruit processing, comprising a base (1), a distillation tank (101), and a cooling tank (102), characterized in that: The interior of the distillation tank (101) is slidably connected to a fixed plate (205), both ends of the interior of the fixed plate (205) are provided with conical air outlets (208), the interior of the conical air outlet (208) is rotatably connected to a baffle (4), both sides of the baffle (4) are fixed with rotating plates (401), and one side of the two sets of rotating plates (401) is rotatably connected to a crank (402), the end of the crank (402) is provided with a ball (403), and the bottom of the ball (403) is rotatably connected to A No. 1 fixed block (404), the middle part of which is rotatably connected to a No. 2 rotating shaft (405), the end of which is fixed to a No. 2 and No. 1 fixed blocks (406), a fixing ring (407) is fixed to the bottom of the No. 1 fixed block (404), an annular groove (408) is provided at the bottom of the fixing ring (407), an arcuate ring (409) is rotatably connected inside the annular groove (408), and a stopper (410) is fixed to one side of the arcuate ring (409).

2. The device for utilizing and treating high-concentration organic wastewater in preserved fruit processing according to claim 1, characterized in that: The cranks (402) are respectively arranged at the upward position of the center of one group of rotating plates (401), and the other group of cranks (402) are respectively arranged at the downward position of the center of another group of rotating plates (401), and the tops of the second and first fixing blocks (406) are fixedly connected to the bottom of the fixing plate (205).

3. The device for utilizing and treating high-concentration organic wastewater in preserved fruit processing according to claim 1, characterized in that: A motor (2) is installed on the outside of the distillation tank (101), a gear (201) is fixed to the output end of the motor (2), a gear ring (202) is rotatably connected to the inner cavity of the distillation tank (101), a rotating ring (206) is fixed to the top and bottom of the gear ring (202), and the rotating ring (206) is arranged in the inner cavity of the distillation tank (101).

4. The device for utilizing and treating high-concentration organic wastewater in preserved fruit processing according to claim 3, characterized in that: A first threaded ring (203) is fixed to the inner wall of the gear ring (202), a second threaded ring (204) is rotatably connected inside the first threaded ring (203), the bottom of the second threaded ring (204) is fixedly connected to the top of a fixed plate (205), and a conical column (207) is provided at the bottom of the fixed plate (205).

5. The device for utilizing and treating high-concentration organic wastewater in preserved fruit processing according to claim 1, characterized in that: The middle part of the fixed plate (205) is rotatably connected to a first rotating shaft (3), a fan blade (301) is fixed to the top of the first rotating shaft (3), and a spiral blade (302) is fixed to the bottom of the first rotating shaft (3).

6. The device for utilizing and treating high-concentration organic wastewater in preserved fruit processing according to claim 5, characterized in that: The bottom of the spiral blade (302) is arranged in the shape of a groove, the top of the spiral blade (302) is in contact with the stopper (410), and the fan blade (301) is arranged at the air outlet of the conical air outlet (208).

7. The device for utilizing and treating high-concentration organic wastewater in preserved fruit processing according to claim 1, characterized in that: The inner cavity of the distillation tank (101) is provided with a heat conduction pipe (103), the inner cavity of the cooling tank (102) is provided with a cooling pipe (104), the bottom of the distillation tank (101) is provided with a heater (107), the bottom of the cooling tank (102) is provided with a refrigerator (108), a first discharge port (105) is provided in the middle of the bottom of the distillation tank (101), and a second discharge port (106) is provided at the bottom of the cooling tank (102).

8. The device for utilizing and treating high-concentration organic wastewater in preserved fruit processing according to claim 7, characterized in that: A feed port (109) is provided on one side of the distillation tank (101), a pipeline (110) is provided on the top of the distillation tank (101), a one-way valve (111) is provided inside the pipeline (110), a pressure gauge (112) is provided on the outside of the pipeline (110), a funnel (113) is provided on the top of the distillation tank (101), and the end of the pipeline (110) is connected to the top of the cooling tank (102).

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