Branched feeding structure
By adopting a branched feeding structure and a pressure expansion tube design in the evaporator, the problem of heat exchanger blockage in high-salt wastewater treatment was solved, achieving smooth liquid flow and improved heat exchange efficiency, while reducing scaling and resource consumption.
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- WUXI LANGPAN ENVIRONMENTAL TECH CO LTD
- Filing Date
- 2025-04-30
- Publication Date
- 2026-04-10
AI Technical Summary
When treating high-salt wastewater, existing evaporators have high evaporation temperatures, which easily lead to scaling and blockage of the heat exchanger inlet, affecting heat exchange efficiency and increasing energy consumption.
The system adopts a branched feeding structure. By setting up a feeding chamber and a discharge vertical pipe in the top tank and installing a pressure telescopic pipe, the liquid material is directly sprayed into the heat exchange tube. The inlet end of the heat exchange tube is cleaned by the telescopic movement of the pressure telescopic pipe, and the inner wall of the heat exchange tube is cleaned by the aeration pipe and the gas collecting spray.
It effectively reduces scaling at the inlet of heat exchange tubes, ensures smooth feeding, reduces the possibility of blockage, improves heat exchange efficiency, and saves resources.
Smart Images
Figure CN224100014U_ABST
Abstract
Description
TECHNICAL FIELD
[0001] The utility model relates to evaporator technical field, concretely relates to a branchy feed structure. BACKGROUND
[0002] The evaporating tank for wastewater treatment is a device for treating wastewater, and its main principle is to evaporate water in the wastewater by heating to separate impurities, thereby realizing the separation of water and impurities.
[0003] The existing evaporating tank has high evaporation temperature for high-salinity wastewater with high difficulty, and the crystalline substance is prone to scaling, which blocks the heat exchange pipeline in the heat exchanger, especially the inlet end of the heat exchanger. When the crystalline substance scales, it will first block part of the inlet of the heat exchanger, so that the liquid material cannot flow smoothly, affecting the heat exchange efficiency and increasing energy consumption. Then, the scaling will occur on the inner wall of the heat exchanger pipeline, increasing the wall thickness and reducing the heat exchange efficiency.
[0004] Therefore, the utility model provides a branchy feed structure. UTILITY MODEL CONTENT
[0005] The utility model discloses a branchy feed structure.
[0006] The utility model discloses a branchy feed structure to realize the above-mentioned purpose specifically adopts the following technical scheme:
[0007] A branchy feed structure comprises:
[0008] The tank body comprises a bottom tank, an intermediate tank and a top tank, the bottom tank, the intermediate tank and the top tank are connected to each other through flanges, a discharge pipe is formed on the bottom tank, a feeding pipe is formed on the top tank, and an aeration pipe is installed through the bottom tank.
[0009] The heat exchange part comprises a top plate and a bottom plate installed in the intermediate tank, a heating cavity is formed between the top plate and the bottom plate, a plurality of heat exchange pipes located in the heating cavity are arrayed and communicated between the top plate and the bottom plate, and two water passing pipes are formed on the outer side of the intermediate tank and communicated with the heating cavity.
[0010] The feeding mechanism comprises a partition plate formed in the top tank, a feeding cavity is formed between the partition plate and the top tank, a plurality of discharge vertical pipes are arrayed and formed on the bottom of the partition plate and communicated with the feeding cavity, a pressure expansion pipe is installed on each discharge vertical pipe and used for spraying liquid material into the heat exchange pipe.
[0011] Further, an upper ring plate and a lower ring plate are formed on the inner wall of the intermediate tank, the inner diameter of the upper ring plate is larger than that of the lower ring plate, the outer diameter of the top plate is larger than that of the bottom plate, and the top plate and the bottom plate abut on the upper ring plate and the lower ring plate respectively.
[0012] Further, the aeration pipe comprises a main flow pipe installed through the bottom tank, and a plurality of branch flow pipes are arranged on both sides of the main flow pipe, and a plurality of air injection holes are arranged on the upper side of the branch flow pipes.
[0013] Further, the pressure telescopic pipe comprises an extension pipe slidingly inserted into the discharge vertical pipe, a supporting spring sleeved on the extension pipe is connected between the upper end of the extension pipe and the bottom end of the discharge vertical pipe, a piston ring is connected to the upper end of the extension pipe, and a pressure valve plate is arranged in the piston ring.
[0014] Further, the pressure valve plate comprises four fan-shaped plates arranged on the inner wall of the piston ring, and a cross-shaped gap is arranged between the four fan-shaped plates.
[0015] Further, the bottom end of the extension pipe is arranged with an outwardly expanding conical ring, and the diameter of the outwardly expanding conical ring is smaller than the inner diameter of the heat exchange pipe.
[0016] Further, the air collection and injection member comprises a hollow circular frame arranged on the top plate, a plurality of insertion pipes are arranged on the bottom side of the hollow circular frame and inserted into the heat exchange pipe, an air injection cavity is arranged in the inner wall of the insertion pipe and connected to the hollow circular frame, and a plurality of air injection pipes are arranged at the bottom end of the insertion pipe and located in the heat exchange pipe.
[0017] Further, the bottom side of the hollow circular frame is arranged with an air inlet pipe penetrating through the top plate and the bottom plate, and the diameter of the air inlet pipe is much larger than the diameter of the heat exchange pipe.
[0018] The beneficial effects of the utility model are as follows: the utility model sets a feeding cavity in the top tank, installs a pressure telescopic pipe on the discharge vertical pipe, extends by the pressure of feeding, inserts the port into the heat exchange pipe, directly injects the liquid material into the heat exchange pipe, directly enters the bottom tank through the port of the heat exchange pipe to heat, can effectively reduce the scaling phenomenon of the inlet end of the heat exchange pipe, guarantees the smooth feeding, and the pressure telescopic pipe can perform the extraction and insertion friction on the port of the heat exchange pipe every time, so that the edge crystallization is cleaned, and the possibility of blockage is reduced. BRIEF DESCRIPTION OF DRAWINGS
[0019] Figure 1 is the utility model three-dimensional structure diagram;
[0020] Figure 2 is the utility model three-dimensional structure half cut diagram;
[0021] Figure 3 is the utility model three-dimensional structure half cut plane view;
[0022] Figure 4 is the utility model Figure 4 is the utility model enlarged view of A;
[0023] Figure 5It is the three-dimensional structure diagram of the aeration pipe of the utility model;
[0024] Figure 6 It is the three-dimensional structure half sectional view of the pressure telescopic pipe of the utility model;
[0025] Reference signs: 1, tank body; 101, bottom tank; 102, intermediate tank; 1021, upper ring plate; 1022, lower ring plate; 103, top tank; 104, lower feeding pipe; 105, upper feeding pipe; 2, aeration pipe; 201, main flow pipe; 202, branch flow pipe; 203, air injection hole; 3, heat exchange part; 301, top plate; 302, bottom plate; 303, heating cavity; 304, heat exchange pipe; 305, water passing pipe; 4, feeding mechanism; 401, partition plate; 402, feeding cavity; 403, discharging vertical pipe; 404, pressure telescopic pipe; 4041, extension pipe; 40411, outward expanding cone ring; 4042, supporting spring; 4043, piston ring; 4044, pressure valve piece; 40441, fan-shaped piece; 40442, cross gap; 5, gas collecting and spraying member; 501, hollow circular frame; 502, cannula; 503, air injection cavity; 504, air injection pipe; 505, air inlet pipe. DETAILED DESCRIPTION
[0026] To make the purpose, technical scheme and advantages of the embodiments of the utility model clearer, the technical scheme in the embodiments of the utility model will be clearly and completely described below in combination with the drawings in the embodiments of the utility model.
[0027] As Figures 1-3 shown, one embodiment of the utility model proposes a branch-like feeding structure, which comprises:
[0028] The tank body 1 comprises the bottom tank 101, the intermediate tank 102 and the top tank 103, the bottom tank 101, the intermediate tank 102 and the top tank 103 are connected with each other through flanges, the lower feeding pipe 104 is constructed on the bottom tank 101, the upper feeding pipe 105 is constructed on the top tank 103, the aeration pipe 2 is installed through the bottom tank 101, the bottom tank 101, the intermediate tank 102 and the top tank 103 are connected through the flange plate and the bolt, which can conveniently split the tank body 1 into three parts, so that the interior of the equipment can be cleaned regularly, and the convenience of the device is increased;
[0029] The heat exchange part 3 comprises a top plate 301 and a bottom plate 302 installed in the intermediate tank 102, a heating cavity 303 is arranged between the top plate 301 and the bottom plate 302, a plurality of heat exchange pipes 304 located in the heating cavity 303 are arranged in array between the top plate 301 and the bottom plate 302, and two water passing pipes 305 are arranged outside the intermediate tank 102 and communicated with the heating cavity 303. The heat exchange part 3 is arranged in the intermediate tank 102, and the heat exchange pipes 304 are vertically arranged, so that the liquid material flows from the top tank 103 into the bottom tank 101 through the heat exchange pipes 304. The liquid material can be preliminarily heated in this process, and then heated and evaporated by the temperature in the bottom tank 101, so as to realize evaporation and separation of impurities. The liquid level of the liquid material is always in the middle part of the heat exchange pipes 304, so as to be heated better.
[0030] The feeding mechanism 4 comprises a partition plate 401 arranged in the top tank 103, a feeding cavity 402 is arranged between the partition plate 401 and the top tank 103, a plurality of discharge vertical pipes 403 are arranged in array at the bottom of the partition plate 401 and communicated with the feeding cavity 402, and a pressure telescopic pipe 404 is arranged on each discharge vertical pipe 403 and used for spraying the liquid material into the heat exchange pipe 304. It should be noted that the pressure telescopic pipe 404 can move up and down on the discharge vertical pipe 403, and can also store and release pressure. The pressure telescopic pipe 404 is inserted into the heat exchange pipe 304 by telescopic movement, and then the pressure is released, so that the liquid material directly passes through the inlet end of the heat exchange pipe 304 without contacting the heat exchange pipe 304, thereby avoiding the scaling phenomenon of the inlet end of the heat exchange pipe 304 and preventing the heat exchange pipe 304 from being blocked. The telescopic movement of the pressure telescopic pipe 404 can also move the inlet end of the heat exchange pipe 304 in and out, so as to remove the accidentally scaled part of the inlet end of the heat exchange pipe 304 and further avoid the blockage. The regular feeding of the feeding mechanism 4 can effectively automatically clean the scaling of the inlet end of the heat exchange pipe 304, ensure the smooth flow of the liquid material, and increase the safety.
[0031] As shown in Figures 1-3 some embodiments, an upper ring plate 1021 and a lower ring plate 1022 are arranged on the inner wall of the intermediate tank 102, the inner diameter of the upper ring plate 1021 is greater than the inner diameter of the lower ring plate 1022, the outer diameter of the top plate 301 is greater than the outer diameter of the bottom plate 302, and the top plate 301 and the bottom plate 302 abut on the upper ring plate 1021 and the lower ring plate 1022, respectively. When it is necessary to clean the inner wall of the tank body 1, the bottom tank 101, the intermediate tank 102 and the top tank 103 need to be separated, and the top plate 301 and the bottom plate 302 are sequentially installed on the upper ring plate 1021 and the lower ring plate 1022. The top plate 301, the bottom plate 302 and the heat exchange pipes 304 can be pulled out from the upper side of the upper ring plate 1021, so as to clean the heat exchange pipes 304 and the top plate 301 and the bottom plate 302. The disassembly is more scattered, the personnel operation is facilitated, and the convenience of the device is increased.
[0032] AsFigure 5 As shown, in some embodiments, the aeration pipe 2 includes a main flow pipe 201 that penetrates and is installed inside the bottom tank 101. Multiple branch pipes 202 are arrayed on both sides of the main flow pipe 201, and multiple jet holes 203 are arrayed on the upper side of the branch pipes 202. By installing the aeration pipe 2 inside the bottom tank 101 and configuring it as a main flow pipe 201 and multiple branch pipes 202, gas can be dispersed and sprayed into the liquid, thereby ensuring the crystal precipitation efficiency in the liquid. Figure 6 As shown, in some embodiments, the pressure telescopic tube 404 includes an extension tube 4041 slidably inserted into the discharge vertical tube 403. A support spring 4042 sleeved on the extension tube 4041 is connected between the upper end of the extension tube 4041 and the bottom end of the discharge vertical tube 403. A piston ring 4043 is connected to the upper end of the extension tube 4041, and a pressure valve plate 4044 is constructed inside the piston ring 4043. It should be noted that the pressure valve plate 4044 is used as a valve body. When the pressure in the feed chamber 402 does not reach the critical point, the pressure valve plate 4044 closes. At this time, the pressure of the liquid will push the piston ring 4043 downward, thereby pushing the extension tube 4041 to extend inside the discharge vertical pipe 403, so that the extension tube 4041 is gradually inserted into the heat exchange tube 304, cleaning the inlet end of the heat exchange tube 304 to avoid blockage. When the pressure is greater than the critical point, the pressure valve plate 4044 opens, and the liquid will quickly rush into the heat exchange tube 304, preventing the liquid from being in contact with the inlet end of the heat exchange tube 304 for a long time, reducing the possibility of scaling, further reducing the possibility of blockage, and increasing safety.
[0033] like Figure 6 As shown, in some embodiments, the pressure valve plate 4044 includes four sector-shaped plates 40441 constructed on the inner wall of the piston ring 4043, and a cross gap 40442 is constructed between the four sector-shaped plates 40441. When the pressure in the feed chamber 402 is insufficient, the cross gap 40442 is closed, and the four sector-shaped plates 40441 abut against each other to form a blockage. When the pressure is sufficient, the cross gap 40442 opens, and the four sector-shaped plates 40441 flip over, thereby allowing the liquid to flow out.
[0034] like Figure 6 As shown, in some embodiments, the bottom end of the extension tube 4041 is constructed with an expanding conical ring 40411. The diameter of the expanding conical ring 40411 is smaller than the inner diameter of the heat exchange tube 304. The lower end of the expanding conical ring 40411 is constructed with an angled surface, which allows it to be better inserted into the heat exchange tube 304. This allows for impact cleaning of scale at the port of the heat exchange tube 304. At the same time, when the extension tube 4041 contracts, the conical surface can be used to rub and clean the inner wall of the heat exchange tube 304, thereby improving the cleaning effect.
[0035] like Figures 3-4As shown in the drawings, in some embodiments, the gas collection jet 5 is also included, which comprises a hollow circular frame 501 mounted on the top plate 301, and a plurality of insertion pipes 502 inserted into the heat exchange pipe 304 are arranged at the bottom side of the hollow circular frame 501, and a jet cavity 503 in communication with the hollow circular frame 501 is arranged in the inner wall of the insertion pipe 502, and a plurality of jet pipes 504 located in the heat exchange pipe 304 are arranged at the bottom end of the insertion pipe 502. By injecting gas into the hollow circular frame 501, the insertion pipe 502 can be used to jet the inner wall of the heat exchange pipe 304, and in cooperation with the high temperature of the heat exchange pipe 304 itself, the scale on the inner wall of the heat exchange pipe 304 can be softened and cleaned to some extent, thereby reducing the wall thickness of the heat exchange pipe 304 and ensuring the heat exchange efficiency.
[0036] As shown in the drawings, Figure 3 In some embodiments, the bottom side of the hollow circular frame 501 is provided with an air inlet pipe 505 penetrating through the top plate 301 and the bottom plate 302, and the diameter of the air inlet pipe 505 is much larger than the diameter of the heat exchange pipe 304. The air inlet pipe 505 is connected in the bottom tank 101, so that the gas can be collected when the aeration pipe 2 is working, and the gas is re-pressurized into the heat exchange pipe 304 by pressure, thereby realizing the cleaning of the inner wall of the heat exchange pipe 304, without the need for additional air pressure supplement, thereby saving resources.
[0037] The above description of the disclosed embodiments enables those skilled in the art to implement or use the present application. Various modifications to these embodiments will be apparent to those skilled in the art, and the general principles defined herein can be implemented in other embodiments without departing from the spirit or scope of the present application. Therefore, the present application will not be limited to the embodiments shown herein, but will conform to the widest scope consistent with the principles and novel features disclosed herein.
Claims
1. A branched feed structure, characterized by, Include: The tank body (1) includes bottom tank (101), intermediate tank (102) and top tank (103), the bottom tank (101), intermediate tank (102) and top tank (103) are connected by flange, the bottom tank (101) is configured with a discharge pipe (104), the top tank (103) is configured with a feeding pipe (105), the bottom tank (101) is installed with aeration pipe (2) through; Heat exchange part (3), including the top plate (301) and bottom plate (302) installed in the intermediate tank (102), the top plate (301) and bottom plate (302) are configured with heating cavity (303), the top plate (301) and bottom plate (302) are arrayed and communicated with a plurality of heat exchange pipes (304) in the heating cavity (303), the outer side of the intermediate tank (102) is configured with two water pipes (305) connected with the heating cavity (303); Feeding mechanism (4), including the partition (401) configured in the top tank (103), the partition (401) and the top tank (103) are configured with a feeding cavity (402), the partition (401) bottom is arrayed and configured with a plurality of discharge vertical pipe (403) communicated with the feeding cavity (402), the discharge vertical pipe (403) is installed with pressure expansion pipe (404) for inserting into the heat exchange pipe (304) to spray liquid material.
2. A branched feed structure according to claim 1, wherein, The intermediate tank (102) is configured with an upper ring plate (1021) and a lower ring plate (1022) on the inner wall, The inner diameter of the upper ring plate (1021) is greater than that of the lower ring plate (1022), the outer diameter of the top plate (301) The outer diameter of the bottom plate (302), the top plate (301) and the bottom plate (302) are respectively contacted on the upper ring plate (1021) and the lower ring plate (1022).
3. A branched feed structure according to claim 1, wherein, The aeration pipe (2) includes a main flow pipe (201) installed through the bottom tank (101), a plurality of branch flow pipes (202) are arrayed on both sides of the main flow pipe (201), a plurality of air injection holes (203) are arrayed on the upper side of the branch flow pipe (202).
4. A branched feed structure according to claim 1, wherein The pressure expansion pipe (404) includes an extension pipe (4041) slidingly inserted into the discharge vertical pipe (403), a support spring (4042) sleeved on the extension pipe (4041) is connected between the upper end of the extension pipe (4041) and the bottom end of the discharge vertical pipe (403), a piston ring (4043) is connected to the upper end of the extension pipe (4041), and a pressure valve plate (4044) is configured in the piston ring (4043).
5. A branched feed structure according to claim 4, wherein, The pressure valve plate (4044) includes four fan-shaped plates (40441) configured on the inner wall of the piston ring (4043), and a cross gap (40442) is configured between the four fan-shaped plates (40441).
6. A branched feed structure according to claim 4, wherein, The bottom end of the extension pipe (4041) is configured with an outwardly expanding cone ring (40411), and the diameter of the outwardly expanding cone ring (40411) is smaller than the inner diameter of the heat exchange pipe (304).
7. A branched feed structure according to claim 1, wherein Also included are gas collecting jet elements (5), which include a hollow circular frame (501) mounted on the top plate (301), and a plurality of spigots (502) inserted into the heat exchange pipes (304) are arranged in an array on the bottom side of the hollow circular frame (501), and a jet cavity (503) in communication with the hollow circular frame (501) is arranged in the inner wall of the spigot (502), and a plurality of jet pipes (504) located in the heat exchange pipes (304) are arranged at the bottom end of the spigot (502).
8. A branched feed structure according to claim 7, wherein, The bottom side of the hollow circular frame (501) is arranged with an air inlet pipe (505) penetrating through the top plate (301) and the bottom plate (302), and the diameter of the air inlet pipe (505) is much larger than the diameter of the heat exchange pipes (304).