A wastewater desulfurization device
By designing a wastewater desulfurization device including a desulfurization cylinder, a division device and a first storage chamber, and using a concentration detection device and a liquid discharge supplementary device to achieve efficient desulfurization of wastewater, the problems of energy consumption and volatile sulfide generation in the prior art are solved.
Patent Information
- Application Number
- CN202420866868.9
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2024-04-24
- Publication Date
- 2025-04-11
- Estimated Expiration
- 2034-04-24
AI Technical Summary
The existing wastewater desulfurization method consumes a large amount of energy and produces volatile sulfides.
A wastewater desulfurization device is designed, including a desulfurization cylinder, a division device and a first storage chamber. The concentration detection device drives the division device to control the communication between the first storage chamber and the precipitate storage chamber, and the mixture of the precipitate and liquid is discharged by the first discharge device to purify the sulfide, and the replacement of the liquid is controlled by the liquid discharge replenishment device.
It effectively reduces energy consumption, reduces the production of volatile sulfides, and achieves efficient desulfurization of wastewater.
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Figure CN222744132U_ABST
Abstract
Description
Technical Field
[0001] The utility model belongs to the technical field of wastewater desulfurization, and particularly relates to a wastewater desulfurization device. Background Art
[0002] Wastewater is generated in daily life and industrial production. Wastewater in daily life contains relatively few harmful chemicals, while industrial wastewater contains a large amount of harmful substances. If it is not properly treated, it will cause environmental pollution, among which sulfur is the main culprit.
[0003] The existing desulfurization method is to extract sulfur through evaporation, which not only consumes a lot of energy but also produces volatile sulfides. Utility Model Content
[0004] The utility model aims to provide a wastewater desulfurization device to solve the energy consumption and generated volatile sulfides during desulfurization.
[0005] In order to achieve the above-mentioned purpose, the specific technical scheme of a wastewater desulfurization device of the utility model is as follows:
[0006] A wastewater desulfurization device comprises a desulfurization cylinder, a dividing device and a first storage chamber, wherein the dividing device is provided inside the desulfurization cylinder, and above the dividing device is a first storage chamber for mixing sewage and desulfurization materials. The device is characterized in that a sediment storage chamber inside the purification cylinder is placed below the dividing device, and a concentration detection device is provided in the first storage chamber to drive the dividing device to divide the first storage chamber and the sediment storage chamber, and the dividing device drives a first discharge device to discharge a mixture of sediment and liquid from the sediment storage chamber for sulfide purification, and a liquid discharge replenishing device is provided inside the first storage chamber to control a liquid outlet and a liquid inlet to replace the liquid inside the first storage chamber.
[0007] Furthermore, the segmentation device includes a fixed disk, a first through hole, a rotating disk and a second through hole, the fixed disk is arranged inside the desulfurization cylinder, the rotating disk is arranged inside the fixed disk, the first through hole is arranged on the fixed disk, and the second through hole is arranged on the rotating disk. The concentration detection device drives the rotating disk to rotate to control whether the first storage chamber and the sediment storage chamber are connected, and the rotating disk drives the first discharge device to discharge the sediment inside the sediment storage chamber.
[0008] Furthermore, the concentration detection device includes a mounting seat, a first float, a movable rack, a gear, a pulley group, a first bevel gear and a second bevel gear. The mounting seat is arranged on a fixed disk, the movable rack slides on the mounting seat, the first float is arranged on the movable rack, the movable rack and the gear are meshed, the gear is connected to the first bevel gear through the pulley group, and the first bevel gear is connected to the rotating disk through the second bevel gear.
[0009] Furthermore, the liquid discharge replenishing device includes an installation sliding cylinder, a movable disk, a limiting ball, a spring, a limiting groove, a connecting rod, a movable arc plate, a discharge hole, a baffle, a first connecting rod, a second float, a second connecting rod, a movable float and a sealing plug. The installation sliding cylinder is arranged on a fixed disk, and the movable disk slides inside the installation sliding cylinder. A limiting groove is provided inside the installation sliding cylinder. Two limiting balls are arranged inside the movable disk. A spring is provided between the two limiting balls. The limiting groove limits the movement of the movable disk through the limiting balls. The movable arc plate with the discharge hole is connected to the movable float through the connecting rod. The movable float is arranged on the movable disk through the first connecting rod. The movable arc plate baffle with the discharge hole is arranged on the rotating disk. The second connecting rod is arranged on the second float. The movable float slides on the second connecting rod. The sealing plug is arranged on the movable float. The sealing plug controls the opening and closing of the liquid inlet hole.
[0010] Furthermore, the first discharge device includes a second rotating disk, a third through hole and a fourth through hole. The second rotating disk is arranged on the rotating disk through a connecting rod, the third through hole is arranged on the second rotating disk, and the fourth through hole is arranged on the desulfurization cylinder so that the outside world and the sediment storage chamber are connected. The first through hole and the fourth through hole correspond to each other up and down, and the third through hole and the second through hole are arranged at 90 degrees.
[0011] The advantages of the utility model are:
[0012] The utility model produces precipitated sulfide by feeding wastewater and reactant into the first storage chamber of the desulfurization cylinder in equal proportion through a conveying device. The precipitated sulfide enters the sediment storage chamber through a dividing device. As the sulfur in the wastewater is extracted, the concentration of the liquid decreases. As the concentration of the liquid decreases, the buoyancy detected by the concentration detection device decreases, and the concentration detection device drives the dividing device to close the connection between the first storage chamber and the sediment storage chamber. At the same time, the first discharge device is opened to discharge the precipitated sulfide and a certain amount of liquid in the sediment storage chamber for purification. The reduction of liquid reduces the energy used. At the same time, the dividing device and the liquid discharge supplement device cooperate to discharge the desulfurized wastewater from the liquid outlet. When the amount of wastewater in the first storage chamber is less than a value, the liquid discharge supplement device closes the liquid outlet and releases the closure of the liquid inlet, so that the wastewater and reactant are added to the first storage chamber. When the wastewater in the first storage chamber comes to the previous position again, all devices that have changed their states are restored to their original states for the next desulfurization discharge. BRIEF DESCRIPTION OF THE DRAWINGS
[0013] Figure 1 It is a schematic diagram of the overall structure of the utility model;
[0014] Figure 2 The utility model is an overall cutaway view Figure 1 ;
[0015] Figure 3 The utility model is an overall cutaway view Figure 2 ;
[0016] Figure 4 This is a schematic diagram of the concentration detection device of the utility model;
[0017] Figure 5 This is a schematic diagram of the structure of the liquid discharge and replenishment device of the utility model;
[0018] Figure 6 for Figure 5 A partial enlarged schematic diagram;
[0019] Description of the markings in the figure:
[0020] Desulfurization cylinder 1; dividing device 2; fixed disk 2-1; first through hole 2-2; rotating disk 2-3; second through hole 2-4; first storage chamber 3; sediment storage chamber 4; liquid outlet 5; concentration detection device 6; mounting seat 6-1; first float 6-2; moving rack 6-3; gear 6-4; pulley group 6-5; first bevel gear 6-6; second bevel gear 6-7; liquid discharge replenishing device 7; installation sliding cylinder 7-1; moving disk 7-2; limiting ball 7-3; spring 7-4; limiting groove 7-5; connecting rod 7-6; moving arc plate 7-7; discharge hole 7-8; baffle 7-9; first connecting rod 7-10; second float 7-11; second connecting rod 7-12; moving float 7-13; sealing plug 7-14; first discharge device 8; second rotating disk 8-1; third through hole 8-2; fourth through hole 8-3; liquid inlet 9. DETAILED DESCRIPTION
[0021] The technical solution of the utility model will be described clearly and completely below in conjunction with the accompanying drawings. Obviously, the described embodiments are part of the embodiments of the utility model, not all of the embodiments. Based on the embodiments of the utility model, all other embodiments obtained by ordinary technicians in this field without creative work are within the scope of protection of the utility model.
[0022] In the description of the present invention, it should be noted that the terms "center", "upper", "lower", "left", "right", "vertical", "horizontal", "inner", "outer", etc., indicating the orientation or positional relationship, are based on the orientation or positional relationship shown in the drawings, and are only for the convenience of describing the present invention and simplifying the description, rather than indicating or implying that the device or element referred to must have a specific orientation, be constructed and operated in a specific orientation, and therefore cannot be understood as a limitation on the present invention. In addition, the terms "first", "second", and "third" are used for descriptive purposes only, and cannot be understood as indicating or implying relative importance.
[0023] like Figure 1-6As shown, a wastewater desulfurization device includes a desulfurization cylinder 1, a dividing device 2 and a first storage chamber 3, wherein the dividing device 2 is provided inside the desulfurization cylinder 1, and above the dividing device 2 is a first storage chamber 3 where sewage and desulfurization materials are mixed. It is characterized in that a sediment storage chamber 4 inside the purification cylinder 1 is placed below the dividing device 2, and the first storage chamber 3 is provided with a concentration detection device 6 to drive the dividing device 2 to divide the first storage chamber 3 and the sediment storage chamber 4, and the dividing device 2 drives the first discharge device 8 to discharge the mixture of sediment and liquid in the sediment storage chamber 4 to purify sulfide, and a liquid discharge replenishing device 7 is provided inside the first storage chamber 3 to control the liquid outlet 5 and the liquid inlet 9 to replace the liquid inside the first storage chamber 3.
[0024] Precipitated sulfide is produced by feeding wastewater and reactant into the first storage chamber 3 of the desulfurization cylinder 1 in equal proportion through a conveying device. The precipitated sulfide will enter the sediment storage chamber 4 through the dividing device 2. As the sulfur in the wastewater is extracted, the concentration of the liquid decreases. As the concentration of the liquid decreases, the buoyancy detected by the concentration detection device 6 decreases. The concentration detection device 6 will drive the dividing device 2 to close the connection between the first storage chamber 3 and the sediment storage chamber 4. At the same time, the first discharge device 8 is opened to discharge the precipitated sulfide and a certain amount of liquid in the sediment storage chamber 4 for purification. The reduction of liquid will reduce the energy used. At the same time, the dividing device 2 and the liquid discharge supplement device 7 cooperate to discharge the desulfurized wastewater from the liquid outlet 5. When the amount of wastewater in the first storage chamber 3 is less than a value, the liquid discharge supplement device 7 will close the liquid outlet 5 and release the closure of the liquid inlet 9, so that the wastewater and reactant are added to the first storage chamber 3. When the wastewater in the first storage chamber 3 comes to the previous position again, all devices that have changed their states are restored to their original states for the next desulfurization discharge.
[0025] Among them, Figure 1-6 As shown, the dividing device 2 includes a fixed disk 2-1, a first through hole 2-2, a rotating disk 2-3 and a second through hole 2-4. The fixed disk 2-1 is arranged inside the desulfurization cylinder 1, and the rotating disk 2-3 is arranged inside the fixed disk 2-1. The first through hole 2-2 is arranged on the fixed disk 2-1, and the second through hole 2-4 is arranged on the rotating disk 2-3. The concentration detection device 6 drives the rotating disk 2-3 to rotate to control whether the first storage chamber 3 and the sediment storage chamber 4 are connected. The rotating disk 2-3 drives the first discharge device 8 to discharge the sediment inside the sediment storage chamber 4.
[0026] Among them, Figure 1-6As shown, the concentration detection device 6 includes a mounting seat 6-1, a first float 6-2, a movable rack 6-3, a gear 6-4, a pulley group 6-5, a first bevel gear 6-6 and a second bevel gear 6-7. The mounting seat 6-1 is arranged on the fixed disk 2-1, the movable rack 6-3 slides on the mounting seat 6-1, the first float 6-2 is arranged on the movable rack 6-3, the movable rack 6-3 is meshed with the gear 6-4, the gear 6-4 is connected to the first bevel gear 6-6 through the pulley group 6-5, and the first bevel gear 6-6 is connected to the rotating disk 2-3 through the second bevel gear 6-7.
[0027] When the liquid concentration decreases, the density will also decrease, and then the buoyancy of the first float 6-2 will also weaken, and the first float 6-2 will move downward. The first float 6-2 drives the gear 6-4 to rotate through the moving rack 6-3, and the gear 6-4 drives the first bevel gear 6-6 and the second bevel gear 6-7 to rotate through the pulley group 6-5. The rotating second bevel gear 6-7 drives the rotating disk 2-3 to rotate.
[0028] Among them, Figure 1-6 As shown, the liquid discharge replenishing device 7 includes a mounting sliding cylinder 7-1, a movable disk 7-2, a limiting ball 7-3, a spring 7-4, a limiting groove 7-5, a connecting rod 7-6, a movable arc plate 7-7, a discharge hole 7-8, a baffle 7-9, a first connecting rod 7-10, a second float 7-11, a second connecting rod 7-12, a movable float 7-13 and a sealing plug 7-14, the mounting sliding cylinder 7-1 is arranged on the fixed disk 2-1, the movable disk 7-2 slides inside the mounting sliding cylinder 7-1, the mounting sliding cylinder 7-1 is provided with a limiting groove 7-5, two limiting balls 7-3 are arranged inside the movable disk 7-2, and two limiting balls 7-3 A spring 7-4 is provided in between, and the limiting groove 7-5 limits the movement of the movable disk 7-2 through the limiting ball 7-3. The movable arc plate 7-7 with the discharge hole 7-8 is connected to the movable float 7-13 through the connecting rod 7-6. The movable float 7-13 is arranged on the movable disk 7-2 through the first connecting rod 7-10. The movable arc plate 7-7 with the discharge hole 7-8 and the baffle 7-9 are arranged on the rotating disk 2-3. The second connecting rod 7-12 is arranged on the second float 7-11. The movable float 7-13 slides on the second connecting rod 7-12. The sealing plug 7-14 is arranged on the movable float 7-13. The sealing plug 7-14 controls the opening and closing of the liquid inlet hole 9.
[0029] The rotating rotating disk 2-3 drives the baffle 7-9 to rotate, so that the first storage chamber 3 is connected with the liquid outlet 5 through the discharge hole 7-8, and then the desulfurized liquid will be discharged outward through the liquid outlet 5. As the liquid level drops, the moving float 7-13 is no longer subject to buoyancy, and the moving float 7-13 will drive the sealing plug 7-14 to move downward a distance but will not detach from the liquid inlet 9 until the liquid level drops to the position of the second float 7-11. The second float 7-11 moves downward without the action of the float, and the second float 7-11 drives the moving float 7-13 and the sealing plug 7-14 to move again through the first connecting rod 7-10 until the second float 7-11 moves to the discharge hole 7-8 and the liquid outlet 5 and stops moving. At this time, the sealing plug 7-14 just detaches from the inside of the liquid inlet 9, and at the same time the limiting ball 7-3 enters the limiting groove 7-5 to limit the position of the movable disk 7-2 and the second float 7-11, and then the wastewater and the reactant are injected into the first storage chamber 3 through the liquid inlet hole 9. As the liquid level rises to the position of the movable float 7-13, the movable float 7-13 is acted upon by the buoyancy, and then the pressure on the second float 7-11 is reduced. The buoyancy of the second float 7-11 breaks through the force of the limiting ball 7-3 applied by the spring 7-4 on the limiting groove 7-5, and then the liquid discharge replenishing device 7 is reset. At the same time, the high-concentration liquid will also reset the concentration detection device 6 and reset the dividing device 2 to connect the first storage chamber 3 and the sediment storage chamber 4 again. At the same time, the reset first discharge device 8 of the rotating disk 2-3 disconnects the sediment storage chamber 4 from the outside again.
[0030] Among them, Figure 1-6 As shown, the first discharge device 8 includes a second rotating disk 8-1, a third through hole 8-2 and a fourth through hole 8-3. The second rotating disk 8-1 is arranged on the rotating disk 2-3 through a connecting rod, the third through hole 8-2 is arranged on the second rotating disk 8-1, and the fourth through hole 8-3 is arranged on the desulfurization cylinder 1 so that the outside and the sediment storage chamber 4 are connected. The first through hole 2-2 and the fourth through hole 8-3 correspond to each other up and down, and the third through hole 8-2 and the second through hole 2-4 are arranged at 90 degrees.
[0031] It is understood that the present invention is described by some embodiments, and those skilled in the art are aware that various changes or equivalent substitutions may be made to these features and embodiments without departing from the spirit and scope of the present invention. In addition, under the teachings of the present invention, these features and embodiments may be modified to adapt to specific circumstances and powders without departing from the spirit and scope of the present invention. Therefore, the present invention is not limited to the specific embodiments disclosed herein, and all embodiments falling within the scope of the claims of this application belong to the scope protected by the present invention.
Claims
1. A wastewater desulfurization device, comprising a desulfurization cylinder (1), a splitting device (2) and a first storage chamber (3), wherein the desulfurization cylinder (1) is provided with a splitting device (2), and above the splitting device (2) is a first storage chamber (3) for mixing sewage and desulfurization materials, characterized in that: The sediment storage chamber (4) inside the desulfurization cylinder (1) is placed below the dividing device (2); the first storage chamber (3) is provided with a concentration detection device (6) to drive the dividing device (2) to divide the first storage chamber (3) and the sediment storage chamber (4); the dividing device (2) drives the first discharge device (8) to discharge the mixture of sediment and liquid inside the sediment storage chamber (4) to purify sulfide; the first storage chamber (3) is provided with a liquid discharge supplement device (7) to control the liquid outlet (5) and the liquid inlet (9) to replace the liquid inside the first storage chamber (3).
2. A wastewater desulfurization device according to claim 1, characterized in that: The dividing device (2) comprises a fixed disk (2-1), a first through hole (2-2), a rotating disk (2-3) and a second through hole (2-4); the fixed disk (2-1) is arranged inside the desulfurization cylinder (1); the rotating disk (2-3) is arranged inside the fixed disk (2-1); the first through hole (2-2) is arranged on the fixed disk (2-1); the second through hole (2-4) is arranged on the rotating disk (2-3); the concentration detection device (6) drives the rotating disk (2-3) to rotate to control whether the first storage chamber (3) and the sediment storage chamber (4) are connected; the rotating disk (2-3) drives the first discharge device (8) to discharge the sediment inside the sediment storage chamber (4).
3. A wastewater desulfurization device according to claim 2, characterized in that: The concentration detection device (6) comprises a mounting seat (6-1), a first float (6-2), a movable rack (6-3), a gear (6-4), a pulley group (6-5), a first bevel gear (6-6) and a second bevel gear (6-7); the mounting seat (6-1) is arranged on a fixed disk (2-1); the movable rack (6-3) slides on the mounting seat (6-1); the first float (6-2) is arranged on the movable rack (6-3); the movable rack (6-3) and the gear (6-4) are meshed; the gear (6-4) is connected to the first bevel gear (6-6) via the pulley group (6-5); and the first bevel gear (6-6) is connected to the rotating disk (2-3) via the second bevel gear (6-7).
4. A wastewater desulfurization device according to claim 1, characterized in that: The liquid discharge replenishing device (7) comprises a mounting sliding cylinder (7-1), a movable disk (7-2), a limiting ball (7-3), a spring (7-4), a limiting groove (7-5), a connecting rod (7-6), a movable arc plate (7-7), a discharge hole (7-8), a baffle (7-9), a first connecting rod (7-10), a second float (7-11), a second connecting rod (7-12), a movable float (7-13) and a sealing plug (7-14); the mounting sliding cylinder (7-1) is arranged on the fixed disk (2-1); the movable disk (7-2) slides inside the mounting sliding cylinder (7-1); a limiting groove (7-5) is arranged inside the mounting sliding cylinder (7-1); two limiting balls (7-3) are arranged inside the movable disk (7-2); a space between the two limiting balls (7-3) is provided. A spring (7-4) is provided, a limiting groove (7-5) limits the movement of a movable disk (7-2) through a limiting ball (7-3), a movable arc plate (7-7) with a discharge hole (7-8) is connected to a movable float (7-13) through a connecting rod (7-6), the movable float (7-13) is arranged on the movable disk (7-2) through a first connecting rod (7-10), a baffle plate (7-9) of the movable arc plate (7-7) with a discharge hole (7-8) is arranged on a rotating disk (2-3), a second connecting rod (7-12) is arranged on a second float (7-11), the movable float (7-13) slides on the second connecting rod (7-12), a sealing plug (7-14) is arranged on the movable float (7-13), and the sealing plug (7-14) controls the opening and closing of the liquid inlet hole (9).
5. A wastewater desulfurization device according to claim 2, characterized in that: The first discharge device (8) comprises a second rotating disk (8-1), a third through hole (8-2) and a fourth through hole (8-3); the second rotating disk (8-1) is arranged on the rotating disk (2-3) through a connecting rod; the third through hole (8-2) is arranged on the second rotating disk (8-1); the fourth through hole (8-3) is arranged on the desulfurization cylinder (1) so that the outside and the sediment storage chamber (4) are connected; the first through hole (2-2) and the fourth through hole (8-3) correspond to each other up and down; the third through hole (8-2) and the second through hole (2-4) are arranged at 90 degrees.
Citation Information
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