Organic waste sulfuric acid carbonization treatment device

Abstract

The invention discloses an organic waste sulfuric acid carbonization treatment device, and relates to the technical field of organic waste sulfuric acid carbonization treatment. Comprising a supporting seat, the supporting seat is fixedly connected with a reaction tank, the reaction tank is provided with a control panel, the side, close to the supporting seat, of the reaction tank is fixedly connected and communicated with a discharging part, and the side, close to the discharging part, of the reaction tank is provided with an electromagnetic valve electrically connected with the control panel. A cover plate is fixedly connected to the side, away from the discharging piece, of the reaction tank, the cover plate is fixedly connected with a feeding pipe communicated with the reaction tank, the cover plate is fixedly connected with a fixing frame, the fixing frame is provided with a motor electrically connected with the control panel, and a driving shaft of the motor is provided with a transmission shaft. In the process of carbonizing the organic waste sulfuric acid, the magnetic particles in the organic waste sulfuric acid are pretreated, so that the later-stage separation time is shortened, and the later-stage separation pressure is reduced.

Description

Technical Field

[0001] The invention relates to the technical field of carbonization treatment of organic waste sulfuric acid, and in particular to a carbonization treatment device for organic waste sulfuric acid. Background Art

[0002] Organic waste sulfuric acid refers to sulfuric acid waste liquid containing organic matter, which includes acidic compounds, magnetic particles and organic compounds. It is a corrosive and toxic industrial wastewater. In the process of treating organic waste sulfuric acid, the methods commonly used are: membrane separation, neutralization treatment and carbonization treatment.

[0003] Among them, carbonization treatment refers to the process of heating the waste liquid to high temperature conditions to make it carbonized. It can also be understood as separating the solution into gas and liquid to remove the water in the solution and convert the carbonized solution into sulfur-containing compounds.

[0004] Since organic waste sulfuric acid contains a large number of different types of impurities, after the organic waste sulfuric acid is treated, the sulfur-containing compounds, impurities and magnetic particles need to be screened to recycle the sulfur-containing compounds. This treatment method takes too long, puts a heavy burden on subsequent sorting equipment, and the process is too cumbersome. Summary of the invention

[0005] In order to solve the problems mentioned in the above background technology, the present invention provides a carbonization treatment device for organic waste sulfuric acid.

[0006] The technical solution of the present invention is: a carbonization treatment device for organic waste sulfuric acid, comprising a support base, the support base is fixedly connected to a reaction tank, the reaction tank is provided with a control panel, the side of the reaction tank close to the support base is fixedly connected and connected with a discharge piece, the side of the reaction tank close to the discharge piece is provided with an electromagnetic valve electrically connected to the control panel, the side of the reaction tank away from the discharge piece is fixedly connected to a cover plate, the cover plate is fixedly connected to a feed pipe connected to the reaction tank, the cover plate is fixedly connected to a fixing frame, the fixing frame is provided with a motor electrically connected to the control panel, the driving shaft of the motor is provided with a transmission shaft, the transmission shaft is fixedly connected to a rotating part located in the reaction tank, the rotating part is fixedly connected to a fixing part symmetrically distributed at the center, the fixing part is fixedly connected to a spiral plate fixedly connected to the rotating part, an electromagnet electrically connected to the control panel is provided in the spiral plate, the fixing frame is provided with the air extraction component, and the reaction tank is provided with an air intake component.

[0007] Preferably, the exhaust assembly includes a first gas outlet shell, which is fixedly connected to a side of the fixing frame away from the cover plate, and a side of the first gas outlet shell close to the fixing frame is fixedly connected and connected to a first gas supply pipe distributed in a ring array, and a side of the first gas supply pipe away from the first gas outlet shell is fixedly connected and connected to the cover plate, an exhaust member electrically connected to the control panel is provided in the first gas outlet shell, and a connecting groove distributed in a ring array is provided on a side of the reaction tank close to the cover plate for connecting the reaction tank with the cover plate, and a filter member is provided in the first gas outlet shell, and the filter member is located below the exhaust member, and the filter member is used for filtering gas discharged from the first gas outlet shell.

[0008] Preferably, the air intake assembly includes an air guide ring, which is fixedly connected to a side of the reaction tank close to the cover plate, the air guide ring is fixedly connected and connected to an air intake pipe that runs through the reaction tank, the air guide ring is fixedly connected and connected to a second air supply pipe distributed in an annular array on a side close to the center of the circle, the rotating member is rotatably connected to a fixing ring that rotatably cooperates with the transmission shaft on a side close to the motor, the second air supply pipe distributed in an annular array on a side away from the air guide ring is fixedly connected to the fixing ring, the second air supply pipe is connected to the rotating member through the fixing ring, the rotating member is fixedly connected and connected to an air outlet member distributed in a mirror image and in a linear array, a one-way valve is arranged in the air outlet member, a second air outlet shell distributed in an annular array is fixedly connected to the reaction tank, air outlet holes are arranged on opposite sides of the second air outlet shell distributed in an annular array, the second air outlet shell is fixedly connected to the air guide ring and connected to each other, and the fixing ring is provided with a conductive component.

[0009] Preferably, an air guide member connected to the side of the rotating member away from the fixed ring is fixed inside the fixed member, the air guide member is provided with air outlets in a linear array and in an inclined state, and a liquid guide member distributed in a linear array is fixed to the side of the fixed member away from the fixed ring.

[0010] Preferably, the conductive component includes a first conductive part, the first conductive part is fixed to the fixed ring, the first conductive part is rotatably connected to the second conductive part, the electromagnets in the spiral plate symmetrically distributed centrally are all fixed to the second conductive part, the first conductive part is electrically connected to a connecting line that runs through the reaction tank, and the side of the connecting line away from the first conductive part is electrically connected to the control panel.

[0011] Preferably, it also includes a material feeding component, which is arranged in the reaction tank, and the material feeding component includes material feeding parts distributed in an annular array, the material feeding parts distributed in the annular array are all fixedly connected in the reaction tank, the second air outlet shell is fixedly connected to the adjacent material feeding parts, the material feeding parts distributed in the annular array are all located below the air guide ring, the material feeding parts are fixedly connected toward the bottom of the reaction tank and are connected with a material extraction pipe, a limit rod is fixedly connected in the material feeding part, a sliding plate is slidably connected in the material feeding part and slidably cooperates with the adjacent limit rod, the sliding plate is provided with through holes distributed in a mirror image, the limit rod sleeve is provided with a spring located between the adjacent sliding plates and the adjacent material feeding parts, the sliding plate is fixedly connected to an elastic telescopic rod, the telescopic end of the elastic telescopic rod is fixedly connected to a blocking part, the blocking part cooperates with the through holes distributed in a mirror image of the adjacent sliding plates, and the sliding plate is rotatably connected to a sliding rod that slidably cooperates with the adjacent material feeding parts.

[0012] Preferably, mirror-distributed L-shaped rods are fixedly connected in the material conveying member, and the mirror-distributed L-shaped rods are matched with the adjacent blocking members.

[0013] Preferably, a driving assembly is also included, which is arranged in the reaction tank, and the driving assembly includes first rotating parts distributed in a ring array, the first rotating parts distributed in the ring array are respectively rotatably connected to the feeding parts distributed in the ring array, the sliding rod is provided with an inclined sliding groove that cooperates with the adjacent first rotating parts and is distributed in a ring array, the first rotating part is fixedly connected with a gear, and a limiting shell is fixedly connected between the feeding parts distributed in the ring array, the limiting shell is rotatably connected with a second rotating part fixed to the rotating part, and the second rotating part is provided with a rack that meshes with the adjacent gear and is distributed in a mirror image.

[0014] Preferably, the material conveying member is slidably connected with a baffle, a floating member is fixed between the baffles distributed in a ring array, and a side of the material conveying member away from the adjacent material drawing pipe is provided with air outlet holes distributed in a linear array, and the baffle cooperates with the air outlet holes distributed in the linear array of the adjacent material conveying member.

[0015] Preferably, it also includes a stirring component distributed in a circular array, the stirring component is arranged on the adjacent feeding piece, the stirring component includes a transmission rod, the transmission rod is rotatably connected to the side of the adjacent feeding piece away from the air outlet thereon, the transmission rod is limitedly slidably matched with the adjacent sliding rod, and the side of the transmission rod away from the adjacent feeding piece is fixedly connected with a blade fan.

[0016] The beneficial effects of the present invention are: 1. The present invention pre-treats the magnetic particles in the organic waste sulfuric acid during the carbonization treatment of the organic waste sulfuric acid, thereby saving the time and pressure of the later sorting.

[0017] 2. The magnetic particles in the organic waste sulfuric acid are adsorbed by the magnetic force released by the electromagnet in the spiral plate to realize the pretreatment of the organic waste sulfuric acid. The organic waste sulfuric acid in the reaction tank is preheated by the gas ejected by the gas outlet, thereby improving the carbonization efficiency of the reaction tank for the organic waste sulfuric acid. The organic waste sulfuric acid near the center of the reaction tank is blown toward the inner wall of the reaction tank by the gas ejected by the gas outlet, thereby achieving the effect of exchanging the organic waste sulfuric acid inside and outside the reaction tank.

[0018] 3. Through the cooperation of the feeding component and the driving component, the organic waste sulfuric acid at the bottom of the reaction tank is transferred upward and sprayed out by the feeding component. The organic waste sulfuric acid sprayed out by the feeding component contacts the gas sprayed out by the adjacent second gas outlet shell, and the organic waste sulfuric acid is directly blown to enhance the treatment effect of the organic waste sulfuric acid. BRIEF DESCRIPTION OF THE DRAWINGS

[0019] Figure 1 It is a front view of the three-dimensional structure of the present invention; Figure 2 It is a rear view of the three-dimensional structure of the present invention; Figure 3 It is a three-dimensional structural cross-sectional view of the cover plate of the present invention; Figure 4 It is a three-dimensional structural cross-sectional view of the reaction tank of the present invention; Figure 5 It is a schematic diagram of the three-dimensional structure of the air intake assembly of the present invention; Figure 6 is a schematic diagram of the three-dimensional structure of the conductive component of the present invention; Figure 7 It is a three-dimensional structural cross-sectional view of the rotating member of the present invention; Figure 8 It is a three-dimensional structural exploded diagram of the conductive component of the present invention; Fig. 9 It is a three-dimensional structure explosion diagram of the air guide member and the liquid guide member of the present invention; Fig.10 It is a three-dimensional structure explosion diagram of the second rotating member and the baffle of the present invention; Fig.11 It is a three-dimensional structural cross-sectional view of the material feeding assembly of the present invention; Fig.12 It is a three-dimensional structural exploded diagram of the first rotating member and the gear of the present invention; Fig.13 It is a three-dimensional structural cross-sectional view of the material feeding member of the present invention.

[0020] In the accompanying drawings: 101: support base, 102: reaction tank, 103: control panel, 104: discharge member, 1041: solenoid valve, 105: cover plate, 106: feed pipe, 107: fixing frame, 108: motor, 1081: transmission shaft, 109: rotating member, 1091: fixing member, 1092: spiral plate, 1093: air outlet member, 2: air extraction component, 201: first air outlet shell, 202: first air supply pipe, 203: air extraction member, 204: filter member, 3: air intake component, 301: air guide ring, 302: air intake pipe, 303: second air supply pipe, 304: fixing ring, 305: air intake assembly : Second air outlet shell, 306: Air guide part, 307: Liquid guide part, 4: Conductive component, 401: First conductive part, 402: Second conductive part, 403: Connecting line, 5: Feeding component, 501: Feeding part, 5011: Extraction pipe, 502: Limit rod, 503: Sliding plate, 504: Elastic telescopic rod, 505: Blocking part, 506: L-shaped rod, 507: Sliding rod, 6: Driving component, 601: First rotating part, 602: Gear, 603: Limiting shell, 604: Second rotating part, 605: Baffle, 606: Floating part, 7: Stirring component, 701: Transmission rod, 702: Fan. DETAILED DESCRIPTION

[0021] The present invention will be further described below in conjunction with specific embodiments. The illustrative embodiments and descriptions of the present invention are used to explain the present invention but are not intended to limit the present invention.

[0022] Embodiment 1: A device for treating organic waste sulfuric acid by carbonization, such as Figure 1-Figure 5As shown, it includes a support base 101, a reaction tank 102 is fixedly connected to the upper side of the support base 101, a control panel 103 is arranged on the upper side of the right part of the reaction tank 102, the outer wall of the reaction tank 102 is connected to the external heating device during use, and the lower side of the reaction tank 102 is fixedly connected and connected to a discharge piece 104, the discharge piece 104 has an inverted T-shaped material guide channel, the left side of the discharge piece 104 is connected to an external magnetic particle collection device for extracting magnetic particles in organic waste sulfuric acid in the reaction tank 102, and the right side of the discharge piece 104 is connected to The external sulfur-containing compound treatment equipment is connected, and a solenoid valve 1041 is arranged on the lower side of the reaction tank 102, and the solenoid valve 1041 is electrically connected to the control panel 103, and the solenoid valve 1041 is used to block the part where the discharge piece 104 and the reaction tank 102 are connected, and a cover plate 105 is fixedly connected to the upper side of the reaction tank 102, and a feed pipe 106 is fixedly connected to the right part of the cover plate 105. During use, the upper side of the feed pipe 106 will be connected to the external feed equipment, and the feed pipe 106 is connected to the reaction tank 102 through the cover plate 105, and the upper side of the cover plate 105 A fixing frame 107 is fixedly connected to the middle of the reaction tank 102, and the fixing frame 107 is provided with a motor 108, and the motor 108 is electrically connected to the control panel 103. The driving shaft of the motor 108 is provided with a transmission shaft 1081, and the transmission shaft 1081 is fixedly connected to a rotating member 109, and the rotating member 109 is located in the reaction tank 102. The rotating member 109 is fixedly connected to a fixing member 1091 symmetrically distributed at the center of the reaction tank 102, and the fixing member 1091 is fixedly connected to a spiral plate 1092, and the two spiral plates 1092 are symmetrically distributed on the center of the transmission shaft 1081. The facing sides of the plate 1092 are fixedly connected to the rotating part 109, and an electromagnet electrically connected to the control panel 103 is arranged in the spiral plate 1092. The fixed frame 107 is provided with a vacuum assembly 2, and the vacuum assembly 2 is used to extract the gas in the reaction tank 102. The reaction tank 102 is provided with an air intake assembly 3, and the air intake assembly 3 is used to transport hot air into the reaction tank 102. The organic waste sulfuric acid in the reaction tank 102 is heated by an external heating device of the reaction tank 102, so that after the organic waste sulfuric acid is heated, the moisture in the organic waste sulfuric acid remains in the reaction tank 102 in a gaseous state.

[0023] like Figure 3As shown, the exhaust assembly 2 includes a first gas outlet shell 201 fixedly connected to the upper side of the fixing frame 107, and a side of the cover plate 105 close to its outer periphery is fixedly connected and connected with a first gas supply pipe 202 distributed in a ring array, and the upper sides of the first gas supply pipes 202 distributed in the ring array are fixedly connected and connected with the lower side of the first gas outlet shell 201, and a connecting groove distributed in a ring array is provided on the upper side of the reaction tank 102 for connecting the reaction tank 102 with the cover plate 105, and the first gas outlet shell 201 is connected with the reaction tank 102 through the first gas supply pipe 202 distributed in a ring array, and an exhaust member 203 is provided in the first gas outlet shell 201, and the exhaust member 203 is a fan, and the exhaust member 203 is electrically connected to the control panel 103, and a filter member 204 is provided in the first gas outlet shell 201 and is located below the exhaust member 203, and the filter member 204 is activated carbon, and the filter member 204 is used to filter the gas discharged from the first gas outlet shell 201.

[0024] like Figure 2 and Figure 4-Figure 9As shown, the air intake assembly 3 includes an air guide ring 301 fixedly connected to the reaction tank 102, the rear side of the air guide ring 301 is fixedly connected and connected to an air intake pipe 302, the air intake pipe 302 runs through the reaction tank 102, the air guide ring 301 is fixedly connected to and connected to a second air delivery pipe 303 distributed in a circular array on one side toward the center of the circle, the second air delivery pipe 303 is L-shaped, the upper side of the rotating member 109 is rotatably connected to a fixed ring 304, the fixed ring 304 is rotatably matched with the transmission shaft 1081, the lower sides of the second air delivery pipes 303 distributed in the circular array are all fixedly connected to the upper side of the fixed ring 304, the second air delivery pipe 303 is connected to the rotating member 109 through the fixed ring 304, and part of the gas in the second air delivery pipe 303 is The four second gas pipes 303 are transported to the rotating member 109 through the fixed ring 304. The second gas pipes 303 are connected with the rotating member 109 through the fixed ring 304 to complete the process of transporting gas to the rotating member 109. The rotating member 109 is fixedly connected and connected with the gas outlet member 1093 which is mirror image and distributed in a linear array. A one-way valve is arranged in the gas outlet member 1093. When the gas flows into the gas outlet member 1093 from the rotating member 109, the one-way valve in the gas outlet member 1093 is in an open state. On the contrary, when the gas no longer flows into the gas outlet member 1093 from the rotating member 109, the one-way valve in the gas outlet member 1093 is in a closed state. The gas ejected from the gas outlet member 1093 affects the gas in the reaction tank 102. The organic waste sulfuric acid is preheated to improve the efficiency of the reaction tank 102 in carbonizing the organic waste sulfuric acid, and the gas ejected by the gas outlet 1093 blows the organic waste sulfuric acid near the center of the reaction tank 102 toward the inner wall of the reaction tank 102, so as to achieve the effect of exchanging the organic waste sulfuric acid inside and outside the reaction tank 102. The reaction tank 102 is fixedly connected with a second gas outlet shell 305 distributed in an annular array, and the opposite sides of the second gas outlet shell 305 distributed in an annular array are provided with rectangular gas outlet holes. The second gas outlet shell 305 is fixedly connected to the air guide ring 301 and is interconnected. The fixed ring 304 is provided with a conductive component 4, and the conductive component 4 is used to make the electromagnet in the spiral plate 1092 generate magnetic force. The gas ejected from the four side air outlets of the second air outlet shells 305 creates a hot air environment for the organic waste sulfuric acid above the liquid level in the reaction tank 102, so as to dry and carbonize the organic waste sulfuric acid from top to bottom. The fixed part 1091 is fixedly connected with an air guide part 306 connected to the lower side of the rotating part 109. The air guide part 306 is provided with a linear array of inclined air outlets. All the air outlets on the air guide part 306 face the opposite direction of rotation of the rotating part 109. The fixed part 1091 is fixedly connected with a liquid guide part 307 distributed in a linear array on the side away from the fixed ring 304. The liquid guide part 307 is used to guide the organic waste sulfuric acid near the center of the circle in the reaction tank 102 to the inner wall of the reaction tank 102.

[0025] like Figure 2 and Figure 5-Figure 8As shown, the conductive component 4 includes a first conductive member 401 fixedly connected to the upper side of the fixed ring 304, the first conductive member 401 is rotatably connected to the second conductive member 402 and a passage is formed between the two, the lower side of the second conductive member 402 is fixedly connected to the electromagnets in the two spiral plates 1092, the first conductive member 401 is electrically connected to a connecting wire 403, the rear side of the connecting wire 403 passes through the reaction tank 102 and is electrically connected to the control panel 103.

[0026] Before treating the organic waste sulfuric acid, the user first connects the upper side of the feed pipe 106 to the external feed device, and then connects the left and right sides of the discharge piece 104 to the magnetic particle collection device and the sulfur-containing compound collection device respectively, and then connects the air intake pipe 302 to the external air intake device, and finally connects the outer wall of the reaction tank 102 to the external heating device, thereby completing the preparation work before treating the organic waste sulfuric acid.

[0027] After the above preparations are completed, the user starts the external feeding device of the feeding pipe 106 and transports the organic waste sulfuric acid into the reaction tank 102. After the organic waste sulfuric acid in the reaction tank 102 submerges the upper side of the rotating part 109, the user closes the external feeding device of the feeding pipe 106 to complete the feeding of the organic waste sulfuric acid in the reaction tank 102.

[0028] When the liquid level of the organic waste sulfuric acid in the reaction tank 102 reaches the required height for work, the user heats it through the external heating equipment of the reaction tank 102. The temperature generated when the reaction tank 102 is heated heats the organic waste sulfuric acid in the reaction tank 102, and the water in the organic waste sulfuric acid is evaporated, thereby realizing the carbonization treatment of the organic waste sulfuric acid. After the organic waste sulfuric acid is heated, the water in it will be evaporated to form a gas.

[0029] During the treatment of the organic waste sulfuric acid in the reaction tank 102, the user starts the exhaust member 203 through the control panel 103. After the exhaust member 203 starts to operate, the gas generated by the evaporation of water in the reaction tank 102 is sucked into the first gas outlet shell 201 through the four first gas pipes 202. When the gas entering the first gas outlet shell 201 flows through the filter element 204, the filter element 204 filters and purifies the gas to achieve the effect of purifying the gas. Through the above description, the organic waste sulfuric acid in the reaction tank 102 is basically carbonized.

[0030] During the treatment of the organic waste sulfuric acid in the reaction tank 102, the user starts the air intake device outside the air intake pipe 302 through the control panel 103, and the air intake device outside the air intake pipe 302 transports the high-temperature gas from the air intake pipe 302 to the air guide ring 301, and part of the gas entering the air guide ring 301 then enters the four second air outlet shells 305 distributed in a circular array, and is ejected from the air outlet holes on the opposite sides of the four second air outlet shells 305, creating a hot air environment above the liquid level of the organic waste sulfuric acid in the reaction tank 102, so as to dry and carbonize the organic waste sulfuric acid from top to bottom, and another part of the gas entering the air guide ring 301 is transported to the fixed ring 304 through the four second air delivery pipes 303 on the center side of the circle, and the fixed ring 304 transports the gas to the rotating member 109, and part of the gas in the rotating member 109 enters the two air guide members 306 respectively. , and is ejected from all the gas outlets in the gas guide member 306. When the gas flows through the gas guide member 306, the adjacent fixed member 1091 is heated, and another part of the gas entering the rotating member 109 is ejected from all the gas outlet members 1093 thereon (when the gas flows through the gas outlet member 1093, the one-way valve in the gas outlet member 1093 is in an open state, and conversely when the gas no longer flows through the one-way valve in the gas outlet member 1093, the one-way valve in the gas outlet member 1093 is in a closed state). The gas ejected from the gas outlet member 1093 preheats the organic waste sulfuric acid in the reaction tank 102, thereby improving the efficiency of the reaction tank 102 in carbonizing the organic waste sulfuric acid, and the organic waste sulfuric acid in the reaction tank 102 close to the center side thereof is blown toward the inner wall of the reaction tank 102 through the gas ejected from the gas outlet member 1093, thereby achieving the effect of exchanging the organic waste sulfuric acid in the reaction tank 102 inside and outside.

[0031] During the evaporation of water in the organic waste sulfuric acid, the user starts the motor 108 through the control panel 103, and the motor 108 drives the transmission shaft 1081 and the parts thereon to rotate. During the rotation of the rotating member 109 driven by the transmission shaft 1081, the gas ejected from all the gas outlet parts 1093 on the periphery of the rotating member 109 makes the organic waste sulfuric acid in the reaction tank 102 evenly contact with the gas, thereby enhancing the effect of evaporating water in the organic waste sulfuric acid. The rotating member 109 and the two fixed members 1091 rotate clockwise, and the side of the fixed member 1091 away from the adjacent spiral plate 1092 is the liquid-facing side (to determine the rotation direction of the rotating member 109 and the fixed member 1091). During the rotation of the two fixed members 1091, the surrounding organic waste sulfuric acid is evenly heated. When 1091 contacts with the surrounding organic waste sulfuric acid, when part of the organic waste sulfuric acid flows through the two fixed parts 1091, taking one of the fixed parts 1091 as an example, the gas ejected through all the gas outlets on the air guide part 306 evaporates the water in the organic waste sulfuric acid and blows the organic waste sulfuric acid to the inner wall of the adjacent fixed part 1091, guides the organic waste sulfuric acid in contact with the inner wall of the fixed part 1091, and enhances the evaporation effect of the water in the organic waste sulfuric acid. The organic waste sulfuric acid in contact with the lower side of the fixed part 1091 is guided by the adjacent four liquid guide parts 307 (taking one of the liquid guide parts 307 as an example, in the process of the organic waste sulfuric acid entering the liquid guide part 307, it enters from the liquid-facing side of the adjacent fixed part 1091 and flows out from the outside of the fixed part 1091), thereby realizing the internal and external exchange of the organic waste sulfuric acid.

[0032] In the process of evaporating the water in the organic waste sulfuric acid in the above manner, the user operates the control panel 103 and the connecting line 403 to form a path, the connecting line 403 transmits the electrical signal to the first conductive member 401 and the second conductive member 402, and the second conductive member 402 transmits the electrical signal to the electromagnets in the two spiral plates 1092. The magnetic force released by the electromagnets in the two spiral plates 1092 causes the spiral plates 1092 to adsorb the magnetic particles in the organic waste sulfuric acid while the rotating member 109 rotates, thereby reducing the pressure during subsequent sorting. After the water in the organic waste sulfuric acid is removed, the organic waste sulfuric acid will form sulfur-containing compounds (powder).

[0033] When all the moisture in the organic waste sulfuric acid is removed, sulfur-containing compounds, impurities and magnetic particles adsorbed by the electromagnet in the spiral plate 1092 will exist in the reaction tank 102, and then the user controls the exhaust part 203, the air intake device external to the air intake pipe 302 and the solenoid valve 1041 through the control panel 103, and finally the user opens the sulfur-containing compound treatment equipment on the right side of the discharge part 104, and the sulfur-containing compound treatment equipment extracts the sulfur-containing compounds and impurities in the reaction tank 102. After the sulfur-containing compounds and impurities in the reaction tank 102 are emptied, the user closes the sulfur-containing compound treatment equipment on the right side of the discharge part 104, thereby completing the treatment process of the sulfur-containing compounds and impurities.

[0034] When the sulfur-containing compounds and impurities in the reaction tank 102 are extracted, the user disconnects the control panel 103 from the connecting line 403. After the power is cut off, the electromagnets in the two spiral plates 1092 lose their magnetic force, and the magnetic particles fall into the reaction tank 102. Then the user opens the magnetic particle collection device on the left side of the discharge piece 104, and the magnetic particle collection device extracts the magnetic particles in the reaction tank 102. After the magnetic particles in the reaction tank 102 are emptied, the user closes the magnetic particle collection device on the left side of the discharge piece 104 to complete the magnetic particle processing process.

[0035] After finishing processing the magnetic particles in the reaction tank 102 , the user can simply turn off the motor 108 .

[0036] Embodiment 2: Based on embodiment 1, Figure 4 and Figure 11-13As shown, it also includes a feeding assembly 5 for transferring the material at the bottom of the reaction tank 102 upward. The feeding assembly 5 is arranged in the reaction tank 102. The feeding assembly 5 includes feeding members 501 fixedly connected to the reaction tank 102 and distributed in an annular array. The height of the upper side of the feeding member 501 is higher than the liquid level of the organic waste sulfuric acid in the reaction tank 102. The lower side of the second gas outlet shell 305 is fixedly connected to the adjacent feeding member 501. The feeding members 501 distributed in the annular array are all located below the air guide ring 301. The lower side of the feeding member 501 is fixedly connected and connected to a pumping pipe 5011. A limiting rod 502 is fixedly connected inside the material piece 501, and the limiting rod 502 is sealingly and slidingly connected with a sliding plate 503, and the sliding plate 503 is sealingly and slidingly connected with the adjacent material feeding piece 501, and the sliding plate 503 is provided with through holes distributed in a mirror image, and the limiting rod 502 is sleeved with a spring, and the spring on the limiting rod 502 is located between the adjacent sliding plate 503 and the adjacent material feeding piece 501, and the upper side of the sliding plate 503 is fixedly connected with an elastic telescopic rod 504 in a stretched state, and the telescopic end of the elastic telescopic rod 504 is fixedly connected with a blocking piece 505, and the blocking piece 505 is composed of a connecting frame and a mutually fixed connection. The blocking member 505 is composed of two truncated cone blocks, and the blocking member 505 cooperates with the through holes of the adjacent sliding plate 503 in a mirror-image distribution. When the blocking member 505 moves upward along with the sliding plate 503, the two truncated cone blocks on the blocking member 505 can be completely fitted with the two through holes on the adjacent blocking member 505. A mirror-image distribution L-shaped rod 506 is fixedly connected to the feeding member 501, and the mirror-image distribution L-shaped rod 506 is squeezed and matched with the adjacent blocking member 505. After the L-shaped rod 506 is separated from the squeezing of the adjacent blocking member 505, the blocking member 505 moves toward the direction of the adjacent sliding plate 503 and pushes the adjacent sliding plate 503. The two through holes of plate 503 are blocked, and the sliding plate 503 is rotatably connected to a sliding rod 507 that slides with the adjacent feeding member 501. When the sliding plate 503 is located in the middle of the adjacent feeding member 501, the organic waste sulfuric acid in the feeding member 501 flows through the through holes on the adjacent sliding plate 503 that are distributed in a mirror image. When the sliding plate 503 moves upward, the organic waste sulfuric acid in the adjacent feeding member 501 is pushed upward, so that the organic waste sulfuric acid is sprayed out from the upper side of the feeding member 501, so that the organic waste sulfuric acid is directly in contact with the hot air on the upper side of the reaction tank 102, so as to enhance the carbonization efficiency of the organic waste sulfuric acid.

[0037] like Figure 4 , Figure 5 and Figure 10-12As shown, it also includes a driving assembly 6 for four driving sliding plates 503, the driving assembly 6 is arranged in the reaction tank 102, the driving assembly 6 includes a first rotating member 601 distributed in an annular array, the first rotating members 601 distributed in an annular array are respectively limited and rotatably connected to the feeding member 501 distributed in an annular array, the first rotating member 601 is composed of a fixed ring fixedly connected to each other and four limiting pins distributed in an annular array, the slide bar 507 is provided with four inclined grooves distributed in an annular array, the rotating member 601 is limited and slidably matched with the inclined grooves on the adjacent slide bars 507, the four limiting pins distributed in an annular array of the slide bar 507 all slide along the adjacent inclined grooves on the adjacent slide bars 507, the middle part of the first rotating member 601 is fixed with a gear 602, the first rotating member 601 is distributed in an annular array, and the first rotating member 601 is connected to the feeding member 501 in an annular array. A limiting shell 603 is fixedly connected between the feeding member 501, and the limiting shell 603 is sealingly rotatably connected with a second rotating member 604. The side of the second rotating member 604 close to its center is fixedly connected to the side of the rotating member 109 close to its periphery. The second rotating member 604 is provided with a rack distributed in a mirror image. The rack on the second rotating member 604 is meshed with the adjacent gear 602. The feeding member 501 is slidably connected with a baffle 605. A floating member 606 is fixedly connected between the baffles 605 distributed in a ring array. A side of the upper part of the feeding member 501 close to the adjacent baffle 605 is provided with air outlet holes distributed in a linear array. The baffle 605 cooperates with the air outlet holes distributed in a linear array on the adjacent feeding member 501, and the baffle 605 is used to cover the air outlet holes distributed in a linear array on the adjacent feeding member 501.

[0038] like Fig.11 and Fig.13 As shown, it also includes a stirring assembly 7 distributed in a ring array for stirring the organic waste sulfuric acid at the bottom of the reaction tank 102. The stirring assembly 7 distributed in a ring array is arranged on the adjacent feeding member 501. The stirring assembly 7 includes a transmission rod 701. The transmission rod 701 is rotatably connected to the lower side of the adjacent feeding member 501. The transmission rod 701 and the adjacent sliding rod 507 are sealed and limited in sliding cooperation. A blade fan 702 is fixed to the lower side of the transmission rod 701. Through the rotation of the blade fan 702, the organic waste sulfuric acid at the bottom of the reaction tank 102 is disturbed to prevent the organic waste sulfuric acid from being deposited at the bottom of the reaction tank 102, resulting in the organic waste sulfuric acid at the bottom of the reaction tank 102 being unable to be evenly heated.

[0039] In the process of treating the organic waste sulfuric acid in the reaction tank 102, the organic waste sulfuric acid in the reaction tank 102 enters the adjacent feeding members 501 from the lower sides of the four extraction pipes 5011 respectively, and the second rotating member 604 is driven to rotate during the rotation of the rotating member 109. Taking one of the feeding members 501 as an example, during the rotation of the second rotating member 604, the gear 602 is meshed with the adjacent gear 602 through the engagement of the rack on the second rotating member 604, so that the gear 602 drives the adjacent first rotating member 601 to rotate. Under the cooperation of the inclined slide grooves distributed in a ring array on the first rotating member 601 and the adjacent slide bar 507, the slide bar 507 drives the parts on it to move upward, and the sliding plate 503 moves upward along the adjacent limit rod 502. The adjacent spring is squeezed in the middle, and the sliding plate 503 moves upward to make the adjacent blocking piece 505 break away from the contact with the two adjacent L-shaped rods 506. Under the action of the elastic pulling force provided by the adjacent elastic telescopic rod 504, the blocking piece 505 moves toward the adjacent sliding plate 503 and blocks the two through holes thereon. The sliding plate 503 squeezes the organic waste sulfuric acid in the adjacent feeding piece 501 upward, so that the organic waste sulfuric acid is sprayed from the upper side of the feeding piece 501, thereby realizing the transfer of the organic waste sulfuric acid at the bottom of the reaction tank 102. The gas sprayed from the second gas outlet shell 305 contacts the organic waste sulfuric acid sprayed from the upper side of the adjacent feeding piece 501, and directly blows the organic waste sulfuric acid to enhance the treatment effect of the organic waste sulfuric acid.

[0040] During the process of transferring the organic waste sulfuric acid at the bottom of the reaction tank 102, the parts in the feeding member 501 rotate and gradually move away from the adjacent blade fan 702 during the upward movement of the slide bar 507. The slide bar 507 drives the blade fan 702 to rotate. The rotation of the blade fan 702 disturbs the organic waste sulfuric acid at the bottom of the reaction tank 102, preventing the organic waste sulfuric acid from being deposited at the bottom of the reaction tank 102, resulting in the organic waste sulfuric acid at the bottom of the reaction tank 102 being unable to be evenly heated.

[0041] After the rack on the second rotating member 604 is no longer engaged with the adjacent gear 602, the sliding plate 503 moves downward under the action of the adjacent spring, and the sliding plate 503 drives the sliding rod 507 to move downward. Through the cooperation of the sliding rod 507 and the inclined sliding groove on the first rotating member 601, the first rotating member 601 and the gear 602 are self-rotated and reset. After the sliding plate 503 and the sliding rod 507 move downward to the limit position, the bottom of the sliding rod 507 contacts the adjacent feeding member 501. After the blocking member 505 is squeezed by the two adjacent L-shaped rods 506, the blocking member 505 is disengaged from the blockage of the two through holes on the adjacent feeding member 501, so that the organic waste sulfuric acid in the adjacent feeding member 501 enters the upper side of the sliding plate 503 in the feeding member 501 from the two through holes on the feeding member 501, preparing for the next transfer of organic waste sulfuric acid.

[0042] After the moisture in the organic waste sulfuric acid in the reaction tank 102 is gradually removed, the liquid level of the organic waste sulfuric acid in the reaction tank 102 gradually decreases, and the floating member 606 moves downward along with the decrease in the liquid level of the organic waste sulfuric acid. The floating member 606 drives four floating members 606 to move downward. Taking one of the floating members 606 as an example, the floating member 606 gradually breaks away from the obstruction of the adjacent air outlet on the upper side of the adjacent feed member 501 during the downward movement, so that the organic waste sulfuric acid in the feed member 501 is discharged from the air outlet on the upper side of the feed member 501, and the organic waste sulfuric acid discharged from the air outlet on the upper side of the feed member 501 is evenly contacted with the hot air in the reaction tank 102, thereby shortening the time for treating the organic waste sulfuric acid.

[0043] The above description is only an example of the present invention and is not intended to limit the present invention. Any equivalent substitutions made within the principles of the present invention should be included in the protection scope of the present invention. The contents not elaborated in detail in the present invention belong to the existing technologies known to those skilled in the art.

Claims

1. A carbonization treatment device for organic waste sulfuric acid, characterized in that: The invention comprises a support base (101), the support base (101) is fixedly connected to a reaction tank (102), the reaction tank (102) is provided with a control panel (103), a side of the reaction tank (102) close to the support base (101) is fixedly connected to and communicated with a discharge piece (104), a side of the reaction tank (102) close to the discharge piece (104) is provided with a solenoid valve (1041) electrically connected to the control panel (103), a side of the reaction tank (102) away from the discharge piece (104) is fixedly connected to a cover plate (105), the cover plate (105) is fixedly connected to a feed pipe (106) communicated with the reaction tank (102), the cover plate (105) is fixedly connected to a fixing frame (107), and the The fixing frame (107) is provided with a motor (108) electrically connected to the control panel (103); the driving shaft of the motor (108) is provided with a transmission shaft (1081); the transmission shaft (1081) is fixedly connected to a rotating member (109) located in the reaction tank (102); the rotating member (109) is fixedly connected to a centrally symmetrically distributed fixing member (1091); the fixing member (1091) is fixedly connected to a spiral plate (1092) fixedly connected to the rotating member (109); an electromagnet electrically connected to the control panel (103) is provided in the spiral plate (1092); the fixing frame (107) is provided with the air extraction component (2); and the reaction tank (102) is provided with an air intake component (3).

2. The device for carbonizing organic waste sulfuric acid as claimed in claim 1, characterized in that: The air extraction assembly (2) comprises a first air outlet shell (201), the first air outlet shell (201) being fixedly connected to a side of the fixing frame (107) away from the cover plate (105), the side of the first air outlet shell (201) close to the fixing frame (107) being fixedly connected to and connected to a first air supply pipe (202) distributed in a circular array, the side of the first air supply pipe (202) away from the first air outlet shell (201) being fixedly connected to and connected to the cover plate (105), and the first air outlet shell (201) being provided with An air suction member (203) electrically connected to the control panel (103) is provided; a side of the reaction tank (102) close to the cover plate (105) is provided with communicating grooves distributed in a ring array, for connecting the reaction tank (102) with the cover plate (105); a filter member (204) is provided in the first gas outlet shell (201); the filter member (204) is located below the air suction member (203); and the filter member (204) is used to filter gas discharged from the first gas outlet shell (201).

3. The device for carbonizing organic waste sulfuric acid as claimed in claim 2, characterized in that: The air intake assembly (3) comprises an air guide ring (301), the air guide ring (301) being fixedly connected to a side of the reaction tank (102) close to the cover plate (105), the air guide ring (301) being fixedly connected to and in communication with an air intake pipe (302) penetrating the reaction tank (102), the air guide ring (301) being fixedly connected to and in communication with a second air supply pipe (303) distributed in an annular array on a side close to the center of the circle thereof, the rotating member (109) being rotatably connected to a fixing ring (304) rotatably matched with the transmission shaft (1081) on a side close to the motor (108), the second air supply pipes (303) distributed in an annular array being away from the air guide ring (301). One side of each of the two reaction tanks (102) is fixedly connected to the fixing ring (304); the second gas delivery pipe (303) is connected to the rotating member (109) through the fixing ring (304); the rotating member (109) is fixedly connected to and connected to a gas outlet member (1093) that is distributed in a mirror image and in a linear array; a one-way valve is provided in the gas outlet member (1093); second gas outlet shells (305) that are distributed in a circular array are fixedly connected to the reaction tank (102); gas outlet holes are provided on opposite sides of the second gas outlet shells (305) that are distributed in a circular array; the second gas outlet shells (305) that are distributed in a circular array are fixedly connected to the gas guide ring (301) and are connected to each other; and the fixing ring (304) is provided with a conductive component (4).

4. The device for carbonizing organic waste sulfuric acid as claimed in claim 3, characterized in that: An air guide member (306) is fixedly connected inside the fixed member (1091) and is in communication with a side of the rotating member (109) away from the fixed ring (304); the air guide member (306) is provided with air outlets arranged in a linear array and in an inclined state; and a liquid guide member (307) is fixedly connected in a linear array to a side of the fixed member (1091) away from the fixed ring (304).

5. The device for carbonizing organic waste sulfuric acid as claimed in claim 3, characterized in that: The conductive component (4) comprises a first conductive member (401), the first conductive member (401) being fixedly connected to the fixing ring (304), the first conductive member (401) being rotatably connected to a second conductive member (402), the electromagnets in the spiral plate (1092) being centrally symmetrically distributed are all fixedly connected to the second conductive member (402), the first conductive member (401) is electrically connected to a connecting line (403) penetrating the reaction tank (102), and the connecting line (403) is electrically connected to the control panel (103) on a side away from the first conductive member (401).

6. The device for carbonizing organic waste sulfuric acid as claimed in claim 5, characterized in that: The invention also comprises a material feeding assembly (5), wherein the material feeding assembly (5) is arranged in the reaction tank (102), the material feeding assembly (5) comprises material feeding members (501) distributed in an annular array, the material feeding members (501) distributed in an annular array are all fixedly connected in the reaction tank (102), the second gas outlet shell (305) is fixedly connected to the adjacent material feeding members (501), the material feeding members (501) distributed in an annular array are all located below the gas guide ring (301), the material feeding members (501) are fixedly connected to the bottom of the reaction tank (102) and are connected to a material extraction pipe (5011), the limiting rod (502) is fixedly connected in the material feeding member (501), and the material feeding member (501) is fixedly connected to the bottom of the reaction tank (102). 1) A sliding plate (503) is internally slidably connected to the adjacent limiting rod (502), the sliding plate (503) is provided with through holes distributed in a mirror image, the limiting rod (502) is sleeved with a spring located between the adjacent sliding plate (503) and the adjacent feeding member (501), the sliding plate (503) is fixedly connected with an elastic telescopic rod (504), the telescopic end of the elastic telescopic rod (504) is fixedly connected with a blocking member (505), the blocking member (505) is matched with the through holes distributed in a mirror image of the adjacent sliding plate (503), and the sliding plate (503) is rotatably connected with a sliding rod (507) that is slidably matched with the adjacent feeding member (501).

7. The device for carbonizing organic waste sulfuric acid as claimed in claim 6, characterized in that: The material conveying member (501) is fixedly connected with L-shaped rods (506) distributed in a mirror image, and the L-shaped rods (506) distributed in a mirror image are matched with adjacent blocking members (505).

8. The device for carbonizing organic waste sulfuric acid as claimed in claim 6, characterized in that: The invention also comprises a driving assembly (6), wherein the driving assembly (6) is arranged in the reaction tank (102), and the driving assembly (6) comprises first rotating members (601) distributed in a ring array, wherein the first rotating members (601) distributed in the ring array are respectively rotatably connected to the feeding members (501) distributed in the ring array, and the sliding rod (507) is provided with an inclined sliding groove which cooperates with the adjacent first rotating members (601) and is distributed in a ring array, and the first rotating members (601) are fixedly connected with gears (602), and the feeding members (501) distributed in the ring array are fixedly connected with limiting shells (603), and the limiting shells (603) are rotatably connected with second rotating members (604) fixedly connected to the rotating member (109), and the second rotating members (604) are provided with racks which mesh with the adjacent gears (602) and are distributed in a mirror image.

9. The device for carbonizing organic waste sulfuric acid as claimed in claim 8, characterized in that: The material conveying member (501) is slidably connected to a baffle plate (605), and a floating member (606) is fixedly connected between the baffle plates (605) distributed in an annular array. A side of the material conveying member (501) away from the adjacent material extraction pipe (5011) is provided with air outlet holes distributed in a linear array, and the baffle plate (605) cooperates with the air outlet holes distributed in a linear array of the adjacent material conveying member (501).

10. The device for carbonizing organic waste sulfuric acid as claimed in claim 9, characterized in that: The invention also comprises stirring components (7) distributed in a circular array, wherein the stirring components (7) are arranged on the adjacent material feeding member (501), and the stirring components (7) comprise a transmission rod (701), wherein the transmission rod (701) is rotatably connected to a side of the adjacent material feeding member (501) away from the air outlet thereon, and the transmission rod (701) is in limited sliding cooperation with the adjacent sliding rod (507), and a blade fan (702) is fixedly connected to a side of the transmission rod (701) away from the adjacent material feeding member (501).

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