Industrial waste salt and fly ash water washing liquid synergistic purification device
Patent Information
- Application Number
- CN202521263883.5
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2025-06-19
- Publication Date
- 2026-10-09
- Estimated Expiration
- 2035-06-19
AI Technical Summary
目前常见的净化流程是先将工业废盐与飞灰水洗液搅拌混合,使其中的物质充分反应,然后进行固液分离,分离后的溶液再经过加热、电解等程序进一步提纯净化,然而,现有的用于分离的装置在运行时,难以及时将拦截的固态废物清理掉,随着时间推移,固态废物会不断堆积,不仅容易造成装置内部管道和过滤部件的堵塞,影响分离效率,还会降低整个协同净化装置的运行稳定性,增加维护成本与停机时间,严重阻碍了工业废盐与飞灰水洗液协同净化工作的高效开展
1、通过设置分离机构,具体是废盐溶液与飞灰水洗液混合搅拌之后从反应罐落到分离箱内的分离板上之后,电机一驱动往复丝杆转动,往复丝杆转动时带动内螺纹块移动、内螺纹块移动时带动齿条移动,再经过齿条和齿轮传动,带动刮板沿弧形分离板往复刮动,从而及时清除分离板上的固态废物,防止其堆积堵塞分离孔隙,使得液态净化产物可以快速稳定地经分离板孔隙流入分离箱底部排出,确保固液分离的高效性与彻底性,为后续处理提供纯净液体原料,保障整体净化流程的稳定运行。
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Figure CN224832321U_ABST
Abstract
Description
Technical Field
[0001] This utility model belongs to the field of synergistic purification technology of industrial waste salt and fly ash washing liquid, and in particular relates to a synergistic purification device for industrial waste salt and fly ash washing liquid. Background Technology
[0002] Industrial waste salt is a solid waste mainly composed of inorganic salts, generated during industrial production and high-salt wastewater treatment. It contains a large amount of inorganic salts and organic pollutants. Fly ash washing liquid is generated during the fly ash washing process of waste incineration. It is a typical high-concentration inorganic high-salt wastewater, characterized by high salt, high calcium, high pH value, heavy metals, and suspended solids. Synergistic purification of both can effectively achieve resource recycling and environmental protection. The current common purification process involves first mixing industrial waste salt with fly ash washing liquid to allow the substances to react fully, followed by solid-liquid separation. The separated solution is then further purified through heating, electrolysis, and other processes. However, existing separation devices struggle to remove the intercepted solid waste in a timely manner during operation. Over time, the solid waste accumulates, easily clogging internal pipes and filter components, affecting separation efficiency, reducing the operational stability of the entire co-purification device, increasing maintenance costs and downtime, and severely hindering the efficient implementation of co-purification of industrial waste salt and fly ash washing liquid. Utility Model Content
[0003] The purpose of this invention is to provide a co-purification device for industrial waste salt and fly ash washing liquid. This device features a separation mechanism. Specifically, after the waste salt solution and fly ash washing liquid are mixed and stirred, they fall from the reaction tank onto a separation plate in a separation tank. A motor drives a reciprocating screw to rotate. The rotation of the reciprocating screw moves an internal threaded block, which in turn moves a rack. Through rack and gear transmission, a scraper reciprocates along the arc-shaped separation plate, thus promptly removing solid waste from the separation plate and preventing its accumulation and blockage of the separation pores. This allows the liquid purification product to flow quickly and stably through the pores of the separation plate into the bottom of the separation tank for discharge, ensuring efficient and thorough solid-liquid separation. This provides pure liquid raw materials for subsequent processing, guarantees the stable operation of the overall purification process, and solves the problem that existing separation devices struggle to promptly remove intercepted solid waste during operation.
[0004] To solve the above-mentioned technical problems, this utility model is achieved through the following technical solution: This utility model relates to a co-purification device for industrial waste salt and fly ash washing liquid, comprising a support frame, a reaction tank fixedly connected to the inner wall of the support frame, a separation box fixedly connected to the support frame, a feed inlet fixedly connected to the top of the reaction tank, a connecting pipe fixedly connected to the bottom of the reaction tank, the bottom end of the connecting pipe fixedly connected to the separation box, and a valve fixedly connected to the outer wall of the connecting pipe, and further comprising: A separation mechanism, mounted on a separation tank, is used to separate the purified solid and liquid phases; and A reaction mechanism is installed on a reaction tank, and the reaction mechanism is used to cause a reaction between the waste salt solution and the fly ash washing liquid to remove residual pollutants; In this process, a certain proportion of waste salt solution and fly ash washing liquid are fed into the reaction tank through the inlet. The reaction mechanism allows the two products to interact and work together to purify the waste salt solution and fly ash washing liquid, further removing pollutants from them. Finally, the solid and liquid are separated by the separation mechanism.
[0005] Furthermore, the separation mechanism includes a waste scraping assembly disposed on the separation tank, the waste scraping assembly being used to scrape off solid waste generated from the waste salt solution and fly ash washing liquid; and A drive assembly, which is mounted on a support frame, is used to provide power for the scraping action of the scraping assembly; A transmission assembly is mounted on a support frame and is used to transmit power from the drive assembly to the scraping assembly.
[0006] Furthermore, the reaction mechanism includes a mixing component disposed on the reaction tank, the mixing component being used to mix and stir the waste salt solution and fly ash washing liquid; and A flow disturbance component is installed inside the reaction tank and is used to turbulent the waste salt solution and fly ash washing liquid.
[0007] Further, the waste scraping assembly includes a separation plate fixedly connected to the inner wall of the separation box, a rotating shaft passing through the separation box and rotatably connected to the separation box, and a scraper fixedly connected to the outer wall of the rotating shaft and slidably connected to the separation plate; and The left and right sides of the separation box are respectively provided with through slots, the left and right sides of the separation box are respectively fixedly connected with guide plates, and the bottom of the separation box is fixedly connected with a drain pipe. Among them, the rotating shaft is rotatably connected to the separation box through a sealed bearing.
[0008] Furthermore, the drive assembly includes a motor mounted on a support frame, the output shaft of the motor being fixedly connected to a reciprocating lead screw via a coupling, an internal thread block being slidably connected to the outer wall of the reciprocating lead screw, a limit rod being fixedly connected to the support frame, and the internal thread block being slidably connected to the limit rod. The internal thread block is limited by a limiting rod.
[0009] Furthermore, the transmission assembly includes a rack fixedly connected to the bottom of the internal thread block, and a gear fixedly connected to the outer wall of the rotating shaft, wherein the rack meshes with the gear; When the internal threaded block moves, it drives the rack to move, and when the rack moves, it drives the gear to rotate. This, in turn, drives the rotating shaft to rotate, which in turn drives the scraper to scrape off the solid waste on the surface of the separation plate.
[0010] Furthermore, the mixing assembly includes a second motor mounted on the top of the reaction vessel, the output shaft of the second motor being fixedly connected to a second rotating shaft via a coupling, and a plurality of stirring blades being fixedly connected to the outer wall of the second rotating shaft; Among them, motor 2 is connected to the reaction vessel by bolts.
[0011] Furthermore, the turbulence-disrupting assembly includes several turbulence-disrupting plates fixedly connected to the inner wall of the reaction vessel, and several turbulence-disrupting columns are fixedly connected to the side of each turbulence-disrupting plate away from the inner wall of the reaction vessel.
[0012] This utility model has the following beneficial effects: 1. By setting up a separation mechanism, specifically after the waste salt solution and fly ash washing liquid are mixed and stirred, they fall from the reaction tank onto the separation plate in the separation box. The motor drives the reciprocating screw to rotate. When the reciprocating screw rotates, it drives the internal thread block to move. When the internal thread block moves, it drives the rack to move. Then, through the rack and gear transmission, it drives the scraper to scrape back and forth along the arc-shaped separation plate, thereby timely removing the solid waste on the separation plate and preventing it from accumulating and clogging the separation pores. This allows the liquid purification product to flow quickly and stably through the pores of the separation plate into the bottom of the separation box and be discharged, ensuring the high efficiency and thoroughness of solid-liquid separation. This provides pure liquid raw materials for subsequent processing and ensures the stable operation of the overall purification process.
[0013] 2. By setting up a reaction mechanism, specifically when mixing and stirring the waste salt solution and fly ash washing liquid, after starting motor two, the rotating shaft two drives the stirring blades to stir the waste salt solution and fly ash washing liquid at high speed. Combined with the baffle and baffle column to form a turbulent vortex, it significantly increases the contact area and reaction probability between pollutants and with auxiliary agents, prolongs the liquid residence time to ensure thorough reaction, thereby greatly improving the removal efficiency of pollutants in waste salt solution and fly ash washing liquid, and achieving efficient synergistic purification.
[0014] Of course, any product implementing this utility model does not necessarily need to achieve all of the advantages described above at the same time. Attached Figure Description
[0015] To more clearly illustrate the technical solutions of the embodiments of this utility model, the accompanying drawings used in the description of the embodiments will be briefly introduced below. Obviously, the drawings described below are only some embodiments of this utility model. For those skilled in the art, other drawings can be obtained based on these drawings without creative effort.
[0016] Figure 1 This is a schematic diagram of the overall structure of this utility model; Figure 2 This is a schematic diagram of the rear view structure of this utility model; Figure 3 This is a cross-sectional structural diagram of the separation box of this utility model; Figure 4 This is a cross-sectional structural diagram of the reaction vessel of this utility model; Figure 5 This utility model Figure 1 A magnified structural diagram of A in the diagram.
[0017] The attached diagram lists the components represented by each number as follows: 1. Support frame; 11. Reaction tank; 111. Feed inlet; 112. Connecting pipe; 113. Valve; 12. Separation box; 2. Separation mechanism; 21. Waste scraping assembly; 211. Separation plate; 212. Rotating shaft one; 213. Scraper; 214. Through groove; 215. Guide plate; 216. Drain pipe; 22. Drive assembly; 221. Motor one; 222. Reciprocating screw; 223. Internal threaded block; 224. Limiting rod; 23. Transmission assembly; 231. Rack; 232. Gear; 3. Reaction mechanism; 31. Mixing assembly; 311. Motor two; 312. Rotating shaft two; 313. Stirring blade; 32. Baffle assembly; 321. Baffle plate; 322. Baffle column. Detailed Implementation
[0018] The technical solutions of the present utility model will be clearly and completely described below with reference to the accompanying drawings of the embodiments. Obviously, the described embodiments are only some embodiments of the present utility model, and not all embodiments. Based on the embodiments of the present utility model, all other embodiments obtained by those skilled in the art without creative effort are within the protection scope of the present utility model.
[0019] Please see Figure 1-5As shown, this utility model is a co-purification device for industrial waste salt and fly ash washing liquid, including a support frame 1, a reaction tank 11 fixedly connected to the inner wall of the support frame 1, a separation box 12 fixedly connected to the support frame 1, a feed inlet 111 fixedly connected to the top of the reaction tank 11, a connecting pipe 112 fixedly connected to the bottom of the reaction tank 11, the bottom end of the connecting pipe 112 fixedly connected to the separation box 12, and a valve 113 fixedly connected to the outer wall of the connecting pipe 112. It also includes: Separation mechanism 2, installed on separation tank 12, is used to separate the purified solid and liquid; and The reaction mechanism 3 is installed on the reaction tank 11. The reaction mechanism 3 is used to make the waste salt solution and fly ash washing liquid react to remove residual pollutants. In this process, a certain proportion of waste salt solution and fly ash washing liquid are fed into the reaction tank 11 through the feed inlet 111. The two products interact and work together to purify the waste salt solution and fly ash washing liquid, further removing pollutants from them. Finally, solid-liquid separation is performed through the separation mechanism 2.
[0020] The separation mechanism 2 includes a waste scraping assembly 21, which is mounted on the separation tank 12. The waste scraping assembly 21 is used to scrape off solid waste generated from the waste salt solution and fly ash washing liquid; and Drive component 22 is mounted on support frame 1 and is used to provide power for the scraping action of scraping component 21; The transmission component 23 is mounted on the support frame 1 and is used to transmit the power of the drive component 22 to the scraping component 21.
[0021] The reaction mechanism 3 includes a mixing component 31, which is mounted on the reaction tank 11. The mixing component 31 is used to mix and stir the waste salt solution and the fly ash washing liquid; and The turbulence-disrupting component 32 is installed inside the reaction tank 11 and is used to turbulent the waste salt solution and fly ash washing liquid.
[0022] The waste scraping assembly 21 includes a separation plate 211 fixedly connected to the inner wall of the separation box 12, a rotating shaft 212 passing through the separation box 12 and rotatably connected to the separation box 12, and a scraper 213 fixedly connected to the outer wall of the rotating shaft 212 and slidably connected to the separation plate 211; and The left and right sides of the separation box 12 are respectively provided with through slots 214, the left and right sides of the separation box 12 are respectively fixedly connected with guide plates 215, and the bottom of the separation box 12 is fixedly connected with a drain pipe 216. The distance from the center of the rotating shaft 212 to the side that contacts the scraper 213 is the same as the radius of the separating plate 211.
[0023] The drive assembly 22 includes a motor 221 mounted on the support frame 1. The output shaft of the motor 221 is fixedly connected to a reciprocating lead screw 222 via a coupling. An internal thread block 223 is slidably connected to the outer wall of the reciprocating lead screw 222. A limit rod 224 is fixedly connected to the support frame 1. The internal thread block 223 is slidably connected to the limit rod 224. Among them, motor 221 is connected to support frame 1 by bolts.
[0024] The transmission assembly 23 includes a rack 231 fixedly connected to the bottom of the internal thread block 223, and a gear 232 fixedly connected to the outer wall of the rotating shaft 212, with the rack 231 meshing with the gear 232; Among them, gear 232 is fixedly connected to shaft 212 by welding.
[0025] The mixing assembly 31 includes a second motor 311 mounted on the top of the reaction vessel 11. The output shaft of the second motor 311 is fixedly connected to a second rotating shaft 312 via a coupling. Several stirring blades 313 are fixedly connected to the outer wall of the second rotating shaft 312. Among them, motor 2 311 is connected to reaction vessel 11 by bolts.
[0026] The turbulence assembly 32 includes several turbulence plates 321 fixedly connected to the inner wall of the reaction vessel 11, and several turbulence columns 322 are fixedly connected to the side of the several turbulence plates 321 away from the inner wall of the reaction vessel 11.
[0027] A specific application of this embodiment is as follows: When using this device, firstly, waste salt solution and fly ash washing liquid, along with auxiliary pharmaceutical solution, are added to the reaction tank 11 through the feed inlet 111. Then, motor 311 is started, driving shaft 312 to rotate, causing the two sets of stirring blades 313 distributed vertically to stir the liquid at high speed, promoting thorough mixing. At this time, the liquid forms a circulation under the action of the stirring blades 313, colliding with the baffles 321 and baffle columns 322 fixed on the inner wall of the reaction tank 11, disrupting the liquid streamlines and generating turbulent eddies. This turbulence... The effect further increases the probability of contact between pollutants such as heavy metal ions and organic matter in the waste salt solution and fly ash washing liquid, while accelerating the diffusion of auxiliary agents. For example, hydroxide ions in fly ash washing liquid and heavy metal ions in waste salt solution react rapidly under thorough mixing and turbulence to generate hydroxide precipitates; organic matter is degraded under the action of oxidant. The turbulence plate 321 and turbulence column 322 can also prolong the residence time of liquid in reaction tank 11 to ensure a more thorough reaction, and ultimately effectively remove pollutants such as organic matter and heavy metals from the solution, achieving synergistic purification.
[0028] After the waste salt solution and fly ash washing liquid in the reaction tank 11 have completed their synergistic reaction, the valve 113 is opened, and the solid-liquid mixture flows into the separation tank 12 through the connecting pipe 112 and falls onto the arc-shaped separation plate 211. At this time, the motor 221 is started, driving the reciprocating screw 222 to rotate, causing the internal thread block 223 to slide back and forth on the limit rod 224. The internal thread block 223 drives the rack 231 to move synchronously. The rack 231 meshes with the gear 232, driving the gear 232 to drive the rotating shaft 212 to rotate, causing the scraper 213 fixed on the rotating shaft 212 to scrape back and forth along the surface of the separation plate 211. The solid waste is scraped by the scraper 213 to the through grooves 214 on both sides of the separation tank 12 and discharged through the guide plate 215, while the liquid falls into the bottom of the separation tank 12 through the holes of the separation plate 211 and flows out through the drain pipe 216, realizing solid-liquid separation and ensuring that the purified liquid does not contain solid impurities, providing pure raw materials for subsequent processing.
[0029] In the description of this specification, references to terms such as "an embodiment," "example," "specific example," etc., indicate that a specific feature, structure, material, or characteristic described in connection with that embodiment or example is included in at least one embodiment or example of the present invention. In this specification, the illustrative expressions of the above terms do not necessarily refer to the same embodiment or example. Furthermore, the specific features, structures, materials, or characteristics described may be combined in any suitable manner in one or more embodiments or examples.
[0030] The preferred embodiments of this utility model disclosed above are merely illustrative of the present utility model. These preferred embodiments do not exhaustively describe all details, nor do they limit the utility model to the specific implementations described. Clearly, many modifications and variations can be made based on the content of this specification. This specification selects and specifically describes these embodiments to better explain the principles and practical applications of this utility model, thereby enabling those skilled in the art to better understand and utilize it. This utility model is limited only by the claims and their full scope and equivalents.
Claims
1. A co-purification device for industrial waste salt and fly ash washing liquid, comprising a support frame (1), a reaction tank (11) fixedly connected to the inner wall of the support frame (1), a separation box (12) fixedly connected to the support frame (1), a feed inlet (111) fixedly connected to the top of the reaction tank (11), a connecting pipe (112) fixedly connected to the bottom of the reaction tank (11), the bottom end of the connecting pipe (112) fixedly connected to the separation box (12), and a valve (113) fixedly connected to the outer wall of the connecting pipe (112), characterized in that, Also includes: A separation mechanism (2), which is mounted on a separation tank (12), is used to separate the purified solid and liquid; and The reaction mechanism (3) is installed on the reaction tank (11) and is used to cause a reaction between the waste salt solution and the fly ash washing liquid to remove residual pollutants. In this process, a certain proportion of waste salt solution and fly ash washing liquid are fed into the reaction tank (11) through the feed inlet (111). The two products interact and work together to purify the waste salt solution and fly ash washing liquid, further removing organic matter and heavy metal pollutants from them. Finally, solid-liquid separation is carried out through the separation mechanism (2).
2. The industrial waste salt and fly ash washing liquid co-purification device according to claim 1, characterized in that, The separation mechanism (2) includes a waste scraping component (21), which is installed on the separation box (12) and is used to scrape off solid waste generated from waste salt solution and fly ash washing liquid. as well as A drive assembly (22) is mounted on a support frame (1) and is used to provide power for the scraping action of the scraping assembly (21); The transmission assembly (23) is mounted on the support frame (1) and is used to transmit the power of the drive assembly (22) to the scraper assembly (21).
3. The industrial waste salt and fly ash washing liquid co-purification device according to claim 2, characterized in that, The reaction mechanism (3) includes a mixing component (31), which is installed on the reaction tank (11) and is used to mix and stir the waste salt solution and fly ash washing liquid. as well as A turbulence-inducing component (32) is disposed inside the reaction tank (11) and is used to turbulent the waste salt solution and fly ash washing liquid.
4. The industrial waste salt and fly ash washing liquid co-purification device according to claim 3, characterized in that, The waste scraping assembly (21) includes a separation plate (211) fixedly connected to the inner wall of the separation box (12), a rotating shaft (212) passing through the separation box (12), the rotating shaft (212) being rotatably connected to the separation box (12), a scraper (213) fixedly connected to the outer wall of the rotating shaft (212), and the scraper (213) being slidably connected to the separation plate (211); and The separation box (12) has through slots (214) on its left and right sides respectively, and guide plates (215) are fixedly connected to the left and right sides respectively. A drain pipe (216) is fixedly connected to the bottom of the separation box (12). The separation plate (211) is fixedly connected to the separation box (12) by welding.
5. The industrial waste salt and fly ash washing liquid co-purification device according to claim 4, characterized in that, The drive assembly (22) includes a motor (221) mounted on a support frame (1). The output shaft of the motor (221) is fixedly connected to a reciprocating screw (222) via a coupling. An internal thread block (223) is slidably connected to the outer wall of the reciprocating screw (222). A limit rod (224) is fixedly connected to the support frame (1). The internal thread block (223) is slidably connected to the limit rod (224). Among them, the motor (221) starts and drives the reciprocating screw (222) to rotate. When the reciprocating screw (222) rotates, it drives the internal thread block (223) to slide on the limit rod (224).
6. The industrial waste salt and fly ash washing liquid co-purification device according to claim 5, characterized in that, The transmission assembly (23) includes a rack (231) fixedly connected to the bottom of the internal thread block (223), and a gear (232) fixedly connected to the outer wall of the rotating shaft (212), wherein the rack (231) meshes with the gear (232); When the internal thread block (223) moves, it drives the rack (231) to move. When the rack (231) moves, it drives the gear (232) to rotate. Thus, the gear (232) drives the rotating shaft (212) to rotate, which in turn drives the scraper (213) to scrape off the solid waste on the surface of the separation plate (211).
7. The industrial waste salt and fly ash washing liquid co-purification device according to claim 3, characterized in that, The mixing assembly (31) includes a second motor (311) installed on the top of the reaction vessel (11). The output shaft of the second motor (311) is fixedly connected to a second rotating shaft (312) via a coupling. Several stirring blades (313) are fixedly connected to the outer wall of the second rotating shaft (312). Among them, after the second motor (311) is started, it drives several stirring blades (313) to rotate through the second rotating shaft (312), thereby mixing and stirring the waste salt solution and fly ash washing liquid in the reaction tank (11).
8. The industrial waste salt and fly ash washing liquid co-purification device according to claim 3, characterized in that, The turbulence assembly (32) includes several turbulence plates (321) fixedly connected to the inner wall of the reaction vessel (11), and several turbulence columns (322) are fixedly connected to the side of the several turbulence plates (321) away from the inner wall of the reaction vessel (11).