Chemical condensing tower capable of simultaneously treating multiple pipelines

Abstract

The utility model provides a chemical condensing tower capable of simultaneously treating multiple pipelines, which belongs to the technical field of condensing towers and comprises a distilled water accommodating tower body, a condensing tower supporting tower body fixedly connected to the top end of the distilled water accommodating tower body, and a condensing tower sealing cover fixedly connected to the top end of the condensing tower supporting tower body. The outer side of the condensing tower sealing cover body is fixedly connected with a plurality of heat exchange assemblies which are uniformly distributed, each heat exchange assembly comprises a heat exchange gas inlet pipe, a rapid ventilation pipe and a strong heat exchange pipe, and the top end of the heat exchange gas inlet pipe and the bottom end of the heat exchange gas inlet pipe are fixedly connected with the rapid ventilation pipe and the strong heat exchange pipe respectively; according to the utility model, water vapor enters the heat exchange gas inlet pipe from the condensing tower sealing cover body and then enters the rapid ventilation pipe from the heat exchange gas inlet pipe, so that the water vapor is divided into two flow channels by the triangular guide block and the square guide block in the steam guide assembly when passing through the steam guide assembly, and the flow rate of the water vapor in the rapid ventilation pipe is improved.

Description

Technical Field

[0001] The utility model belongs to the technical field of condensation towers, in particular to a chemical condensation tower capable of processing multiple pipelines at the same time. Background Art

[0002] A condensing tower is a device that uses water as a circulating coolant to absorb heat from a system and discharge it into the atmosphere to lower the water temperature. The cooling process is to generate steam by exchanging heat between water and air flow. The steam evaporates and takes away the heat to achieve evaporative heat dissipation.

[0003] After searching, for example, a Chinese patent document discloses a natural cooling ventilation tower based on condensation heat exchange and efficient recovery of cooling water (publication number: CN113237357A). Although the above patent sets multiple heat exchange pipes on the surface of the ventilation tower to achieve the recovery of evaporated water, there are still the following problems:

[0004] Although the above patent realizes the recycling of evaporated water, in real life, due to the high height of the condensation tower and the relatively long length of the heat exchange pipe, it takes too long for the steam to enter the bottom end of the heat exchange pipe from the top end of the heat exchange pipe, which greatly affects the use efficiency of the heat exchange pipe. Utility Model Content

[0005] The purpose of the utility model is to address the above-mentioned problems in the existing technology and to propose a chemical condensation tower that can process multiple pipelines simultaneously. The technical problem to be solved by the utility model is that it takes too long for steam to enter the bottom end of the heat exchange pipeline from the top end of the heat exchange pipeline, which greatly affects the use efficiency of the heat exchange pipeline.

[0006] To solve the above technical problems, the utility model provides the following technical solutions: a chemical condensation tower capable of processing multiple pipelines at the same time, comprising a distilled water containing tower body, the top of the distilled water containing tower body is fixedly connected to a condensation tower supporting tower body, the top of the condensation tower supporting tower body is fixedly connected to a condensation tower covering body, and the outer side of the condensation tower covering body is fixedly connected to multiple evenly distributed heat exchange components, the heat exchange components comprise a heat exchange air inlet pipe, a quick ventilation pipe and a strong heat exchange pipe, the top of the heat exchange air inlet pipe and the bottom of the heat exchange air inlet pipe are respectively fixedly connected to the quick ventilation pipe and the strong heat exchange pipe, one side of the quick ventilation pipe is fixedly connected to one side of the condensation tower covering body, one end of the strong heat exchange pipe is fixedly connected to one side of the distilled water containing tower body, the inside of the heat exchange air inlet pipe is fixedly connected to multiple steam guide components, the steam guide components comprise a main frame, a triangular guide block and a square guide block, both sides of the inner wall of the main frame are fixedly connected to the triangular guide blocks, and the bottom end of the inner wall of the main frame is fixedly connected to the square guide block.

[0007] As a preferred solution of the chemical condensation tower capable of processing multiple pipelines simultaneously according to the utility model, a protective cover is provided on the top of the condensation tower sealing body.

[0008] As an optimal solution of the chemical condensation tower that can process multiple pipes simultaneously as described in the utility model, wherein: a plurality of heat pipes are fixedly connected to one side of the strong heat exchange pipe, the heat pipe is a shaped pipe, one side of the shaped pipe is located inside the strong heat exchange pipe, and a ventilation fan is fixedly arranged inside the heat pipe.

[0009] As an optimal solution of the chemical condensation tower that can process multiple pipes simultaneously as described in the utility model, a plurality of heat pipes are fixedly connected to one side of the strong heat exchange pipe, and the heat pipe is a straight cylindrical pipe, one end of the straight cylindrical pipe extends to the interior of the strong heat exchange pipe and is fixedly connected to the side wall of the strong heat exchange pipe.

[0010] As a preferred solution of the chemical condensation tower capable of simultaneously processing multiple pipelines as described in the utility model, the tower base includes a trapezoidal chassis and support columns, the top of the trapezoidal chassis is fixedly connected to the bottom of the distilled water containing tower body, and the bottom of the trapezoidal chassis is fixedly connected to multiple support columns.

[0011] As a preferred solution of the chemical condensation tower capable of processing multiple pipelines simultaneously according to the utility model, a stable frame is fixedly connected to the inside of the condensation tower cover body, and the stable frame is in the shape of a cross.

[0012] As a preferred solution of the chemical condensation tower capable of processing multiple pipelines simultaneously according to the utility model, the bottom end of the strong heat exchange tube is fixedly connected with an inclined pipeline, and one end of the inclined pipeline is fixedly connected with one side of the distilled water containing tower body.

[0013] Compared with the prior art, the utility model has the following advantages:

[0014] In the utility model, water vapor enters into the heat exchange air inlet pipe from the condensation tower cover body, and then enters into the quick ventilation pipe from the heat exchange air inlet pipe. Then, when the water vapor passes through the steam guide component, it will be divided into two flow channels by the triangular guide block and the square guide block in the steam guide component, thereby increasing the flow rate of the water vapor in the quick ventilation pipe. BRIEF DESCRIPTION OF THE DRAWINGS

[0015] Figure 1 It is a structural schematic diagram of the utility model.

[0016] Figure 2 It is a schematic diagram of the internal structure of a heat exchange component in one embodiment.

[0017] Figure 3 It is a structural schematic diagram of the steam guide component in the utility model.

[0018] Figure 4is a side view of a U-shaped tube.

[0019] Figure 5 It is a schematic diagram of the internal structure of a heat exchange component in another embodiment.

[0020] Figure 6 It is a front view of the utility model.

[0021] Figure 7 It is a structural schematic diagram of the condensation tower cover body in the utility model.

[0022] In the figure, 100, distilled water containing tower body; 200, condensation tower supporting tower body; 300, condensation tower covering body; 301, stable frame; 400, heat exchange component; 401, heat exchange air inlet pipe; 401a, steam guide component; 402, quick ventilation pipe; 403, strong heat exchange pipe; 403a, heat pipe; 500, tower base. DETAILED DESCRIPTION

[0023] The following are specific embodiments of the present invention and the accompanying drawings to further describe the technical solution of the present invention, but the present invention is not limited to these embodiments.

[0024] like Figure 1-Figure 3 As shown, the present embodiment provides a chemical condensation tower capable of processing multiple pipelines simultaneously, including a distilled water containing tower body 100, the top of which is fixedly connected to a condensation tower supporting tower body 200, the top of a condensation tower cover body 300 is provided with a protective cover, the outer side of the condensation tower cover body 300 is fixedly connected to a plurality of evenly distributed heat exchange components 400, the heat exchange components 400 include a heat exchange air inlet pipe 401, a quick ventilation pipe 402 and a strong heat exchange pipe 403, the top of the heat exchange air inlet pipe 401 and the bottom of the heat exchange air inlet pipe 401 are fixedly connected to the top of the condensation tower cover body 300, and the heat exchange components 400 are evenly distributed. A quick ventilation pipe 402 and a strong heat exchange pipe 403 are fixedly connected respectively, one side of the quick ventilation pipe 402 is fixedly connected to one side of the condensation tower cover body 300, one end of the strong heat exchange pipe 403 is fixedly connected to one side of the distilled water containing tower body 100, and a plurality of steam guide components 401a are fixedly connected inside the heat exchange air inlet pipe 401. The steam guide component 401a includes a main frame, a triangular guide block and a square guide block. Both sides of the inner wall of the main frame are fixedly connected with the triangular guide blocks, and the bottom end of the inner wall of the main frame is fixedly connected with the square guide block;

[0025] In this embodiment, water vapor enters the heat exchange air inlet pipe 401 from the condensation tower cover body 300, and then enters the quick ventilation pipe 402 from the heat exchange air inlet pipe 401. When the water vapor passes through the steam guide component 401a, it will be divided into two flow channels by the triangular guide blocks and square guide blocks in the steam guide component 401a, thereby increasing the flow rate of the water vapor in the quick ventilation pipe 402.

[0026] A plurality of heat pipes 403a are fixedly connected to one side of the strong heat exchange pipe 403. The heat pipe 403a is a U-shaped pipe. One side of the U-shaped pipe is located inside the strong heat exchange pipe 403. A ventilation fan is fixedly arranged inside the heat pipe 403a. In this embodiment, the U-shaped pipe extends to the middle part of the strong heat exchange pipe 403, so that the water vapor located in the middle part of the strong heat exchange pipe 403 can quickly contact the surface of the U-shaped pipe and condense into water droplets. At the same time, the ventilation fan inside the heat pipe 403a can accelerate the flow of air inside the heat pipe 403a.

[0027] A plurality of heat pipes 403a are fixedly connected to one side of the strong heat exchange tube 403. The heat pipe 403a is a straight cylindrical pipe. One end of the straight cylindrical pipe extends to the interior of the strong heat exchange tube 403 and is fixedly connected to the side wall of the strong heat exchange tube 403. The surface of the straight cylindrical pipe can be in direct contact with the gas inside the strong heat exchange tube 403.

[0028] The tower base 500 includes a trapezoidal chassis and support columns. The top of the trapezoidal chassis is fixedly connected to the bottom of the distilled water containing tower body 100. The bottom of the trapezoidal chassis is fixedly connected to multiple support columns. The top of the condensation tower supporting tower body 200 is fixedly connected to the condensation tower cover body 300. The interior of the condensation tower cover body 300 is fixedly connected to a stable frame 301. The stable frame 301 is cross-shaped. In this embodiment, the stable frame 301 can enhance the strength of the interior of the condensation tower cover body 300. At the same time, the tower base 500 can enhance the stability of the condensation tower.

[0029] The bottom end of the strong heat exchange tube 403 is fixedly connected to an inclined pipe, one end of which is fixedly connected to one side of the distilled water containing tower body 100. The distilled water accumulated at the bottom end of the strong heat exchange tube 403 can quickly enter the interior of the distilled water containing tower body 100 through the inclined pipe, thereby avoiding excessive water accumulation at the bottom of the strong heat exchange tube 403, which may cause water vapor reflux.

[0030] The specific embodiments described herein are merely examples of the spirit of the present invention. Those skilled in the art may make various modifications or additions to the specific embodiments described or replace them in similar ways, but they will not deviate from the spirit of the present invention or exceed the scope defined by the appended claims.

Claims

1. A chemical condensation tower capable of processing multiple pipelines simultaneously, comprising a distilled water containing tower body (100), the top of the distilled water containing tower body (100) is fixedly connected to a condensation tower support tower body (200), the top of the condensation tower support tower body (200) is fixedly connected to a condensation tower cover body (300), and the outer side of the condensation tower cover body (300) is fixedly connected to a plurality of evenly distributed heat exchange components (400), characterized in that: The heat exchange component (400) includes a heat exchange air inlet pipe (401), a quick ventilation pipe (402) and a strong heat exchange pipe (403); the top end of the heat exchange air inlet pipe (401) and the bottom end of the heat exchange air inlet pipe (401) are respectively fixedly connected with the quick ventilation pipe (402) and the strong heat exchange pipe (403); one side of the quick ventilation pipe (402) is fixedly connected with one side of the condensation tower cover body (300); one end of the strong heat exchange pipe (403) is fixedly connected with one side of the distilled water containing tower body (100); a plurality of steam guide components (401a) are fixedly connected inside the heat exchange air inlet pipe (401); the steam guide components (401a) include a main frame, a triangular guide block and a square guide block; both sides of the inner wall of the main frame are fixedly connected with the triangular guide blocks; the bottom end of the inner wall of the main frame is fixedly connected with the square guide block.

2. The chemical condensation tower capable of processing multiple pipelines simultaneously according to claim 1, characterized in that: A protective cover is engaged with the top of the condensation tower cover body (300).

3. The chemical condensation tower capable of processing multiple pipelines simultaneously according to claim 1, characterized in that: A plurality of heat pipes (403a) are fixedly connected to one side of the strong heat exchange pipe (403), the heat pipe (403a) is a U-shaped pipe, one side of the U-shaped pipe is located inside the strong heat exchange pipe (403), and a ventilation fan is fixedly arranged inside the heat pipe (403a).

4. The chemical condensation tower capable of processing multiple pipelines simultaneously according to claim 1, characterized in that: A plurality of heat pipes (403a) are fixedly connected to one side of the strong heat exchange pipe (403). The heat pipe (403a) is a straight tube. One end of the straight tube extends to the inside of the strong heat exchange pipe (403) and is fixedly connected to the side wall of the strong heat exchange pipe (403).

5. The chemical condensation tower capable of processing multiple pipelines simultaneously according to claim 1, characterized in that: The tower base (500) comprises a trapezoidal chassis and support columns. The top of the trapezoidal chassis is fixedly connected to the bottom of the distilled water containing tower (100), and the bottom of the trapezoidal chassis is fixedly connected to a plurality of support columns.

6. The chemical condensation tower capable of processing multiple pipelines simultaneously according to claim 1, characterized in that: A stabilizing frame (301) is fixedly connected to the interior of the condensation tower cover body (300), and the stabilizing frame (301) is in a cross shape.

7. The chemical condensation tower capable of processing multiple pipelines simultaneously according to claim 1, characterized in that: The bottom end of the strong heat exchange tube (403) is fixedly connected to an inclined pipe, and one end of the inclined pipe is fixedly connected to one side of the distilled water containing tower body (100).

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