CN219244322U

CN219244322U - Pipeline module cooling tower

Info

Publication number: CN219244322U
Application number: CN202223402864.5U
Authority: CN
Inventors: 张强; 刘元鹏; 宋建功; 苏京杰; 肖瑞玮; 刘凯
Original assignee: Shandong Lanxiang Environmental Technology Co ltd
Current assignee: Shandong Lanxiang Environmental Technology Co ltd
Priority date: 2022-12-19
Filing date: 2022-12-19
Publication date: 2023-06-23
Anticipated expiration: 2032-12-19

Abstract

Pipeline module cooling tower relates to cooling tower apparatus technical field, including the cooling tower, the region that the cooling tower is in the water receiver top is equipped with the pipeline heat exchanger, and the pipeline heat exchanger includes a plurality of pipeline heat transfer module that is the matrix setting along the horizontal direction, and every pipeline heat transfer module includes the dry cold passageway that communicates with external dry cold air to and the damp and hot passageway that communicates with the interior damp and hot air of tower, independently set up between dry cold passageway and the damp and hot passageway. The utility model solves the problems that the cooling tower in the prior art has extremely large fog in winter, seriously affects the air quality of the surrounding environment, corrodes the surrounding equipment and causes the loss of a large amount of circulating water; and current defogging module all is the design number preparation when the assembly, this just makes unable different volumetric cooling towers use, the narrow problem of application range.

Description

Pipeline module cooling tower

Technical Field

The utility model relates to the technical field of cooling tower tools, in particular to a pipeline module cooling tower.

Background

In the operation process of the existing cooling tower, when the hot and humid saturated air exhausted by the cooling tower encounters external cold air, water vapor is quickly condensed to generate plume, so that visual pollution and influence on the environment on the periphery of the cooling tower are caused.

The existing defogging cooling tower is characterized in that an air cooler is added on the side edge of the upper part of a spraying water distribution system of the existing cooling tower or a condensing module is added on the upper part of the spraying water distribution system, so that the moisture content of hot and humid air is reduced, and the 'plume' generated by air discharged from the tower is reduced. The existing defogging cooling tower is single in structure, the former dry and wet defogging cooling tower is higher in manufacturing cost and lower in water saving effect compared with the latter condensation module defogging cooling tower, but the latter condensation module defogging cooling tower is increased in air resistance and affects thermal performance.

The utility model discloses a CN 214747356U's patent among the prior art, this scheme includes the tower body, the tower body includes from the lower water collector that sets gradually, the air inlet chamber, cooling tower wet heat exchanger, spray water distribution system, the second water receiver, new trend condensing equipment, first water receiver, mixing wind device and hybrid chamber, the hybrid chamber is linked together with the fan that the tower body top set up, the air inlet chamber is linked together with the outside air of tower body through the fresh air inlet window, the both sides of new trend condensing equipment are linked together with the outside air of tower body through well air intake, the both sides of hybrid chamber are linked together with the outside air of tower body through air cooler and last air intake respectively, thereby moisture content and temperature in the wet hot air of play water conservation defogging's effect, reduce the "feather fog" that goes out the tower air and produce.

The prior devices, including the above patents, have also gradually exposed the disadvantages of this technology with use, mainly in the following respects:

first, current cooling towers are particularly in winter, and mist is particularly large, which seriously affects the air quality of the surrounding environment, corrodes peripheral equipment and causes a great amount of circulating water loss.

Second, current defogging module all is the design number preparation when the assembly, and this just makes unable different volumetric cooling towers use, and application range is narrow.

In summary, it is clear that the prior art has inconvenience and defects in practical use, so that improvement is needed.

Disclosure of Invention

Aiming at the defects in the prior art, the utility model solves the problems that the cooling tower in the traditional technology is particularly in winter, mist is particularly large, the air quality of the surrounding environment is seriously influenced, peripheral equipment is corroded, and a large amount of circulating water is lost; and current defogging module all is the design number preparation when the assembly, this just makes unable different volumetric cooling towers use, the narrow problem of application range.

In order to solve the problems, the utility model provides the following technical scheme:

the pipeline module cooling tower comprises a cooling tower, a pipeline heat exchanger is arranged in the region of the cooling tower above the water receiver,

the pipeline heat exchanger comprises a plurality of pipeline heat exchange modules which are arranged in a matrix along the horizontal direction,

each pipeline heat exchange module comprises a dry-cold channel communicated with external dry-cold air and a wet-heat channel communicated with wet-heat air in the tower, and the dry-cold channel and the wet-heat channel are independently arranged.

As an optimized scheme, the dry and cold channels on the adjacent pipeline heat exchange modules are communicated.

As an optimized scheme, the pipeline heat exchangers are vertically arranged in parallel and are communicated with the wet heat channels in the adjacent rows.

As an optimized scheme, a shutter is arranged on the outer wall of the cooling tower in a surrounding manner, and a cold air inlet channel is arranged between an air outlet of the shutter and the end part of the pipeline heat exchanger.

As an optimized scheme, the pipeline heat exchange module comprises a square box body, and the dry-cooling channels comprise air inlets respectively formed in the opposite side walls of the square box body in a matrix mode.

As an optimized scheme, a side plug-in cylinder positioned outside is fixedly connected in the air inlet at one side, and the caliber of the air inlet at the other side is the same as the outer diameter of the side plug-in cylinder.

As an optimized scheme, the wet and hot channels are arranged in a matrix, each wet and hot channel comprises a vertical pipeline vertically arranged in the square box body, and two ends of the vertical pipeline are communicated with the outside.

As an optimized scheme, the lower port of the vertical pipeline is fixedly connected with a lower plug-in cylinder positioned outside, and the caliber of the upper port of the vertical pipeline is the same as the outer diameter of the lower plug-in cylinder.

As an optimized scheme, a supporting frame is horizontally arranged in the cooling tower, and the pipeline heat exchanger is supported on the supporting frame.

Compared with the prior art, the utility model has the beneficial effects that:

the wet and hot channels and the dry and cold channels are mutually perpendicular, and the pipelines are mutually separated;

under the action of a fan, the hot and humid air rises through the water collector, enters the pipeline heat exchanger, enters the hot and humid channel, and enters and fills the square box body through the external louver, so that the hot and humid air exchanges heat with the outer wall of the hot and humid channel;

the condensing recovery tower has the functions of condensing the vapor in the damp and hot air in the recovery tower and enhancing the mixing of the cold fluid and the hot fluid of the device, and has the advantages of convenient installation, low energy consumption and low cost;

the pipeline heat exchanger is formed by a plurality of pipeline heat exchange modules which are arranged in a matrix mode, the transversely adjacent pipeline heat exchange modules are fixed by utilizing the side cartridge, the vertically adjacent pipeline heat exchange modules are fixed by utilizing the lower cartridge, the assembly is more convenient, and the use of cold area towers with different volumes and sizes is met.

Drawings

In order to more clearly illustrate the embodiments of the present utility model or the technical solutions in the prior art, the drawings used in the description of the embodiments or the prior art will be briefly described below. Like elements or portions are generally identified by like reference numerals throughout the several figures. In the drawings, elements or portions thereof are not necessarily drawn to scale.

FIG. 1 is a schematic diagram of the structure of the present utility model;

fig. 2 is a schematic structural view of the pipe heat exchanger of the present utility model.

In the figure: the cooling device comprises a cooling tower 1, a pipeline heat exchanger 2, a water collector 3, a shutter 4, a cold air inlet channel 5, a fan 6, a square box 7, a side plug-in cylinder 8 and a lower plug-in cylinder 9; 10-an air inlet; 11-vertical pipeline.

Detailed Description

Embodiments of the technical scheme of the present utility model will be described in detail below with reference to the accompanying drawings. The following examples are only for more clearly illustrating the technical aspects of the present utility model, and thus are merely examples, and are not intended to limit the scope of the present utility model.

As shown in fig. 1 and 2, the pipeline module cooling tower comprises a cooling tower 1, a pipeline heat exchanger 2 is arranged in the area of the cooling tower 1 above a water receiver 3,

the pipe heat exchanger 2 comprises a plurality of pipe heat exchange modules which are arranged in a matrix along the horizontal direction,

each pipeline heat exchange module comprises a dry-cold channel communicated with the outside dry-cold air and a wet-heat channel communicated with the wet-heat air in the tower, and the dry-cold channel and the wet-heat channel are independently arranged.

And the dry and cold channels on the adjacent pipeline heat exchange modules are communicated.

The pipeline heat exchangers 2 are vertically arranged in parallel and are communicated with the damp-heat channels in the adjacent rows.

A shutter 4 is arranged on the outer wall of the cooling tower 1, and a cold air inlet channel 5 is arranged between the air outlet of the shutter 4 and the end part of the pipeline heat exchanger 2.

The pipeline heat exchange module comprises a square box body 7, and the dry-cooling channel comprises air inlets 10 which are respectively arranged on opposite side walls of the square box body 7 in a matrix mode.

Wherein, the air inlet 10 at one side is fixedly connected with the side plug-in cylinder 8 positioned outside, and the caliber of the air inlet 10 at the other side is the same as the outer diameter of the side plug-in cylinder 8.

The damp-heat channel is a plurality of in matrix arrangement, each comprises a vertical pipeline 11 vertically arranged in the square box body 7, and two ends of the vertical pipeline 11 are communicated with the outside.

The lower port of the vertical pipeline 11 is fixedly connected with a lower plug-in cylinder 9 positioned outside, and the caliber of the upper port of the vertical pipeline 11 is the same as the outer diameter of the lower plug-in cylinder 9.

A supporting frame is horizontally arranged in the cooling tower 1, and the pipeline heat exchanger 2 is supported on the supporting frame.

The working principle of the device is as follows:

under the action of a fan 6, the hot and humid air rises through the water collector 3, enters the pipeline heat exchanger 2, enters the hot and humid channel, and enters and fills the square box body 7 through the external louver 4, so that the hot and humid air exchanges heat with the outer wall of the hot and humid channel;

the pipeline heat exchanger 2 comprises a plurality of pipeline heat exchange modules which are arranged in a matrix, the transversely adjacent pipeline heat exchange modules are fixed by utilizing the side cartridge 8, the vertically adjacent pipeline heat exchange modules are fixed by utilizing the lower cartridge 9, the assembly is more convenient, and the cold-zone towers with different volumes and sizes are satisfied for use.

Finally, it should be noted that: the above embodiments are only for illustrating the technical solution of the present utility model, and not for limiting the same; although the utility model has been described in detail with reference to the foregoing embodiments, it will be understood by those of ordinary skill in the art that: the technical scheme described in the foregoing embodiments can be modified or some or all of the technical features thereof can be replaced by equivalents; such modifications and substitutions do not depart from the spirit of the utility model, and are intended to be included within the scope of the appended claims and description.

Claims

1. Pipeline module cooling tower, its characterized in that: comprises a cooling tower (1), a pipeline heat exchanger (2) is arranged in the area of the cooling tower (1) above a water receiver (3),

the pipeline heat exchanger (2) comprises a plurality of pipeline heat exchange modules which are arranged in a matrix along the horizontal direction,

2. The pipe module cooling tower of claim 1, wherein: and the dry and cold channels on the adjacent pipeline heat exchange modules are communicated.

3. The pipe module cooling tower of claim 2, wherein: the pipeline heat exchangers (2) are vertically arranged in parallel and are communicated with the damp-heat channels in the adjacent rows.

4. A pipe module cooling tower according to claim 3, wherein: the cooling tower is characterized in that a shutter (4) is arranged on the outer wall of the cooling tower (1), and a cold air inlet channel (5) is arranged between an air outlet of the shutter (4) and the end part of the pipeline heat exchanger (2).

5. The pipe module cooling tower of claim 4, wherein: the pipeline heat exchange module comprises a square box body (7), and the dry-cold channel comprises air inlets (10) which are respectively arranged on the opposite side walls of the square box body (7) in a matrix mode.

6. The pipe module cooling tower of claim 5, wherein: wherein, a side plug-in cylinder (8) positioned outside is fixedly connected in the air inlet (10) at one side, and the caliber of the air inlet (10) at the other side is the same as the outer diameter of the side plug-in cylinder (8).

7. The pipe module cooling tower of claim 6, wherein: the wet and hot channels are arranged in a matrix, each wet and hot channel comprises a vertical pipeline (11) vertically arranged in the square box body (7), and two ends of the vertical pipeline (11) are communicated with the outside.

8. The pipe module cooling tower of claim 7, wherein: the lower port of the vertical pipeline (11) is fixedly connected with a lower plug-in cylinder (9) positioned outside, and the caliber of the upper port of the vertical pipeline (11) is the same as the outer diameter of the lower plug-in cylinder (9).

9. The pipe module cooling tower of claim 8, wherein: the cooling tower (1) is internally and horizontally provided with a supporting frame, and the pipeline heat exchanger (2) is supported on the supporting frame.