CN203811002U - Efficient heat exchange tube and evaporative condenser thereof - Google Patents

Abstract

The utility model discloses a high-efficiency heat exchange tube, which comprises a gas collection pipe and a liquid collection pipe. Several heat exchange pipe units are connected between the gas collection pipe and the liquid collection pipe. The heat exchange pipe unit includes a first The heat pipe, the second heat exchange pipe and the corner elbow, the inlet of the first heat exchange pipe communicates with the gas collector, the outlet of the second heat exchange pipe communicates with the liquid collector, and the first The two heat exchange tubes are arranged in layers and staggered up and down relative to the first heat exchange tube, the corner elbow is arranged between the first heat exchange tube and the second heat exchange tube, and the first heat exchange tube The outlet of the heat exchange tube is communicated with the inlet of the second heat exchange tube. This device solves the problem of low heat transfer coefficient inside the tube and excessive wind resistance outside the tube of the evaporative condenser heat exchange tube in the prior art. Provided are a high-efficiency heat exchange tube with good thermal conductivity and small diameter, and an evaporative condenser with good heat transfer performance, strong pressure resistance, compact structure and small floor space.

Description

A high-efficiency heat exchange tube and its evaporative condenser

technical field

The utility model relates to a high-efficiency heat exchanger, in particular to an evaporative condenser.

Background technique

The evaporative condenser is the main heat exchange equipment in the refrigeration system. Its working principle is: the superheated high-pressure refrigerant gas discharged from the compressor in the refrigeration system passes through the condensing exhaust pipe in the evaporative condenser, and the high-temperature gaseous refrigerant and The spray water and air outside the exhaust pipe perform heat exchange. When the evaporative condenser is working, the spray water is transported by the pump to the water in the sump to the spray pipe at the top of the evaporative condenser, and sprayed to the outer surface of the condensing pipe through the nozzle to form a thin water film. The middle part of the water evaporates into water vapor after absorbing heat, and the rest falls into the sump for circulation by the water pump. At the same time, the axial flow fan forces the air to be sucked from the top and the lower part of the side wall to flow through the coil, and the filler and saturated hot and humid air are sucked into the coil. Exhausted into the surrounding atmosphere, part of the water droplets entrained in the hot and humid air is intercepted by the water eliminator, effectively controlling the loss of water droplets drifting, and the loss of water vapor in the atmosphere is controlled by the float valve in the system to replenish cooling water.

The evaporative condenser has the characteristics of water saving, energy saving, compact structure, and small footprint. It is an energy-saving product and has been widely used in cold storage, sewage source heat pump water heater, sewage source heat pump, heat pump seawater desalination devices etc. At present, the evaporative condensers used in the refrigeration field mainly use φ16, φ19, φ25 stainless steel straight tubes with relatively thick tube diameters, resulting in low heat transfer coefficient inside the tubes, excessive wind resistance outside the tubes, and large heat exchanger footprints. . Chinese patent document CN202420262U discloses a heat exchange tube unit, a finned tube air-cooled condenser and a cooling air evaporator. The heat exchange tube unit includes a plurality of heat exchange tube monomers arranged in parallel. The heat exchange tubes are connected end to end through elbows to form a heat exchange medium channel, and the diameters of heat exchange tubes arranged adjacently in the direction of increasing gas specific volume gradually increase. The diameter of the heat exchange tubes arranged adjacently in the direction from the gas inlet pipe to the liquid collection pipe decreases gradually, and the elbow is a tapered pipe, and the heat exchange tubes arranged adjacently in the direction from the liquid distribution pipe to the gas collection pipe The diameter gradually increases, and the elbow is a gradually expanding diameter elbow. This structure can reduce metal consumption for the condenser and reduce flow loss for the evaporator, but the structural shape of the lower heat exchange body unit and the upper heat exchange body unit of the device are the same , and arranged in alignment, therefore, the surface of the lower heat exchange body unit is easily blocked by the upper heat exchange body unit and is not wetted by the spray water, so that the flow distribution of the spray water is uneven, and there is likely to be a flow dead zone, and the structure of the device is complex , The installation is cumbersome, and the overall footprint is large.

Utility model content

For this reason, the technical problem to be solved by the utility model is that the evaporative condensers in the prior art mostly use stainless steel straight tubes with relatively thick tube diameters, the heat transfer coefficient inside the tubes is not high, and the wind resistance outside the tubes is too large, providing a heat-conducting High-efficiency heat exchange tubes with good performance and small diameter.

Another object of the present invention is to provide an evaporative condenser with strong heat transfer performance and pressure resistance, compact structure and small footprint.

In order to solve the above technical problems, the utility model provides a high-efficiency heat exchange tube, which includes a gas collector and a liquid collector. There are several heat exchange tube units connected between the gas collector and the liquid collector. The heat exchange tube unit includes

The first heat exchange tube, the inlet of the first heat exchange tube communicates with the gas collecting tube,

The second heat exchange tube, the outlet of the second heat exchange tube communicates with the liquid collection pipe, and the second heat exchange tube is arranged in a staggered arrangement up and down relative to the first heat exchange tube;

A corner elbow is arranged between the first heat exchange tube and the second heat exchange tube, and connects the outlet of the first heat exchange tube with the inlet of the second heat exchange tube.

Both the first heat exchange tube and the second heat exchange tube are in a wave shape, and the crests or troughs of the first heat exchange tube are staggered from the crests or troughs of the second heat exchange tube.

The waves of the first heat exchange tube and the second heat exchange tube are formed by a plurality of "Ω" protruding upwards and downwards.

The diameters of the first heat exchange tube and the second heat exchange tube are not greater than 15mm.

The outer diameters of the first heat exchange tube and the second heat exchange tube are both D, the horizontal distance between the first heat exchange tube and the second heat exchange tube is L, the relationship between the two Need to meet: 1.5D≤L≤3D.

The heights of the first heat exchange tube and the second heat exchange tube are the same and both are S2, and the vertical height difference between the first heat exchange tube and the second heat exchange tube is S1. The relationship between them needs to satisfy: 0.5S2≤S1≤2S2.

The vertical height difference between the first heat exchange tube and the second heat exchange tube is staggered up and down: the center of the "Ω" protruding upward of the first heat exchange tube coincides with the center of the "Ω" protruding downward of the second heat exchange tube .

The first heat exchange tube and the second heat exchange tube are inner threaded tubes.

An inlet connecting pipe is arranged on the gas collecting pipe, and an outlet connecting pipe is arranged on the liquid collecting pipe.

The inlet connecting pipe and the outlet connecting pipe communicate with the nozzle of the gas collecting pipe and the nozzle of the liquid collecting pipe respectively.

The inlet connecting pipe and the outlet connecting pipe communicate with the side wall of the gas collecting pipe and the side wall of the liquid collecting pipe respectively.

An evaporative condenser, including a box body, a heat exchange coil, a fan, a water collecting pan, a circulating water pump and a spraying device, and the evaporative condenser includes the high-efficiency heat exchange tube described in any one of the above.

Compared with the prior art, the above-mentioned technical solution of the utility model has the following advantages:

(1) The high-efficiency heat exchange tube of the present utility model includes a gas collection pipe and a liquid collection pipe. There are several heat exchange tube units connected between the gas collection pipe and the liquid collection pipe. The heat exchange tube unit includes a first heat exchanger The heat pipe, the second heat exchange tube and the corner elbow, the inlet of the first heat exchange tube communicates with the gas collector, the outlet of the second heat exchange tube communicates with the liquid collector, and the first The two heat exchange tubes are arranged in layers and staggered up and down relative to the first heat exchange tube, the corner elbow is arranged between the first heat exchange tube and the second heat exchange tube, and the first heat exchange tube The outlet of the heat exchange tube communicates with the inlet of the second heat exchange tube, the first heat exchange tube and the second heat exchange tube are both wave-shaped, and the crest or trough of the first heat exchange tube is in line with the The crests or troughs of the second heat exchange tubes are arranged in a staggered manner, and the setting of the corner elbow can make two adjacent rows of heat exchange tubes arranged in a staggered arrangement, so as to prevent the surface of the lower heat exchange tube from being blocked by the upper heat exchange tube. It is not wetted by spray water, so that the flow of spray water is distributed more evenly, and there is no flow dead zone. At the same time, the arrangement of staggered rows and upper and lower layers makes the pressure drop on the air side of the heat exchange tube smaller and the air circulation The resistance is small, which is beneficial to reduce the power consumption of the fan, and helps the gas flow to take away the water vapor.

(2) In the high-efficiency heat exchange tube of the present utility model, the wavy shape of the first heat exchange tube and the second heat exchange tube has a plurality of "Ω" protruding upward and downward, and the heat exchange tube adopts "Ω" The shape of the elbow design makes the shape of the pipe change, so that the fluid flow in the pipe is continuously disturbed to generate strong turbulence, and the heat transfer coefficient is high, which greatly enhances the heat transfer performance and pressure resistance of the heat exchanger.

(3) In the high-efficiency heat exchange tube of the present utility model, the outer diameters of the first heat exchange tube and the second heat exchange tube are both D, and the distance between the first heat exchange tube and the second heat exchange tube is The horizontal distance between them is L, and the relationship between the two needs to satisfy: 1.5D≤L≤3D. The setting of the horizontal distance between two adjacent rows of heat exchange tubes makes the high-efficiency heat exchange tubes of the present utility model not close to each other because the distance is too small While hindering the flow of wind, the wind flow will not be invalid due to excessive spacing.

(4) In the high-efficiency heat exchange tube of the present invention, the height of the first heat exchange tube is equal to that of the second heat exchange tube, and the vertical position of the first heat exchange tube and the second heat exchange tube is staggered up and down. The height difference is S1, the heat exchange tube "Ω" bend height is S2, and the relationship between the two needs to satisfy: 0.5S2≤S1≤2S2, the setting of the height difference makes the first heat exchange tube and the second heat exchange tube The staggered arrangement of the two heat exchange tubes is conducive to the installation of the corner elbow, and the process installation is more convenient.

(5) The evaporative condenser of the utility model has good thermal conductivity of the heat exchange tube and a small tube diameter, thereby greatly enhancing the heat transfer performance and pressure resistance of the heat exchanger, which is conducive to improving the cooling performance of the evaporative condenser. High performance, and simple structure, can be manufactured into a flat and compact type, occupying less space, thus helping to reduce the volume of the condenser product.

Description of drawings

In order to make the content of the utility model easier to understand clearly, the utility model will be described in further detail below according to specific embodiments of the utility model in conjunction with the accompanying drawings, wherein

Fig. 1 is a schematic diagram of the evaporative condenser structure 1 of the present utility model;

Fig. 2 is the schematic diagram of evaporative condenser structure 2 of the present utility model;

Figure 3 is a schematic diagram of the layout of heat exchange tubes in two adjacent rows;

Figure 4 is a schematic diagram of the spatial layout of two adjacent rows of heat exchange tubes;

The reference signs in the figure are expressed as: 1-inlet pipe interface, 2-gas collecting pipe, 3-first heat exchange tube, 4-corner elbow, 5-liquid collecting pipe, 6-outlet connection pipe, 7-second heat exchange tube .

Detailed ways

A high-efficiency heat exchange tube of the present invention and its evaporative condenser are described in detail below in conjunction with specific embodiments:

Embodiment one

As shown in Figure 1, a high-efficiency heat exchange tube includes a gas collection pipe 2 and a liquid collection pipe 5, and several heat exchange tube units are connected between the gas collection pipe 2 and the liquid collection pipe 5, and the heat exchange tube The unit includes a first heat exchange tube 3, a second heat exchange tube 7 and a corner elbow 4, the inlet of the first heat exchange tube 3 communicates with the collector 2, the outlet of the second heat exchange tube 7 communicates with the The liquid collection pipes 5 are connected, and the second heat exchange tubes 7 are arranged in layers and staggered up and down relative to the first heat exchange tubes 3 , and the corner elbows 4 are arranged on the first heat exchange tubes 3 Between the second heat exchange tube 7 , the outlet of the first heat exchange tube 3 is communicated with the inlet of the second heat exchange tube 7 . The setting of the corner elbow 4 can make the adjacent two rows of condensing pipes arranged in a staggered arrangement, avoiding that the surface of the lower condensing pipes is not wetted by the spray water due to the cover of the upper condensing pipes, and makes the spray water flow distribution more uniform , there is no flow dead zone, and the staggered insertion and arrangement of the upper and lower layers makes the pressure drop on the air side of the heat exchange tube smaller, and the air circulation resistance is smaller, which is beneficial to reduce the power consumption of the fan and facilitate the gas circulation Take away water vapor.

Both the first heat exchange tube 3 and the second heat exchange tube 7 are wave-shaped, and the crests or troughs of the first heat exchange tube 3 are staggered from the peaks or troughs of the second heat exchange tube 7 cloth. In this embodiment, the wave shape of the first heat exchange tube 3 and the second heat exchange tube 7 has a plurality of "Ω" protruding upward and downward, and the first heat exchange tube 3 and the second heat exchange tube The diameter of the second heat exchange tube 7 is not greater than 15mm, and the material of the high-efficiency heat exchange tube of the present invention can be copper or other metals with excellent thermal conductivity. The internal thread pipe with a pipe diameter of 15mm or less makes the diameter of the heat exchange pipe of the present invention smaller. The metal pipe is bent into an "Ω" shape through a process, and the change of the pipe shape can cause the fluid flow in the pipe to be continuously disturbed. The strong turbulent flow improves the heat transfer coefficient of the heat exchange tube, thereby greatly enhancing the heat transfer performance and pressure resistance of the heat exchanger.

In this embodiment, as shown in FIG. 4 , the shape and size of the first heat exchange tube 3 and the second heat exchange tube 7 are completely equal, and the first heat exchange tube 3 and the second heat exchange tube 7 The tubes 7 are bent tube structures formed by a plurality of "Ω" protruding upwards and downwards. At the same time, the heights of the "Ω" bends of the first heat exchange tube 3 and the second heat exchange tube 7 are equal, and The size and bending degree of the "Ω" bend are also consistent, so that the overall structure of the heat exchange tube is symmetrical up and down, that is, the peak or trough of the heat exchange tube completely corresponds to the position of the trough or peak of the adjacent row, as shown in As shown in Figure 3, in this embodiment, the outer diameters of the first heat exchange tube 3 and the second heat exchange tube 7 are both D, and the first heat exchange tube 3 and the second heat exchange tube 7 The horizontal distance between the tubes 7 is L, and the relationship between the two needs to satisfy: 1.5D≤L≤3D. The setting of the horizontal distance between two adjacent rows of heat exchange tubes of the present invention makes the high-efficiency heat exchange tubes of the present invention not It will hinder the flow of wind because the distance is too small, and it will not cause the wind flow to be invalid because the distance is too large. At the same time, as shown in Figure 4, the vertical height difference between the first heat exchange tube 3 and the second heat exchange tube 7 is S1, the "Ω" bend height of the heat exchange tube is S2, and the difference between the two The relationship between them needs to satisfy: 0.5S2≤S1≤2S2, the setting of the height difference makes the staggered arrangement of the first heat exchange tube and the second heat exchange tube at the same time conducive to the installation of the corner elbow, and the process installation is more convenient It is convenient, and in this embodiment, the first heat exchange tube 3 and the second heat exchange tube 7 are internally threaded tubes, which further improves the heat exchange performance of the heat exchange tubes. In particular, the vertical height difference between the first heat exchange tube and the second heat exchange tube staggered up and down satisfies: the "Ω" protruding upward of the first heat exchange tube and the "Ω" protruding downward of the second heat exchange tube When the centers are coincident, the installation is more convenient and the heat exchange efficiency is higher.

In this implementation, as shown in Figures 1 and 2, the gas collecting pipe 2 and the liquid collecting pipe 5 are two cylindrical structures arranged side by side, and the gas collecting pipe 2 is arranged below the liquid collecting pipe 5 , the diameter of the gas collecting pipe 2 is greater than the diameter of the liquid collecting pipe 5 . The gas collecting pipe 2 is provided with an inlet connecting pipe 1 , and the liquid collecting pipe 5 is provided with an outlet connecting pipe 6 . As shown in Figure 1, the inlet connecting pipe 1 and the outlet connecting pipe 6 are correspondingly arranged on the bottom surface of the cylindrical structure of the gas collecting pipe 2 and the liquid collecting pipe 5, and the inlet connecting pipe 1 and the The outlet connecting pipe 6 is arranged on the same side of the heat exchange tube unit. However, as shown in FIG. 2 , the inlet connecting pipe 1 and the outlet connecting pipe 6 can also be correspondingly arranged on the cylindrical structure of the gas collecting pipe 2 and the liquid collecting pipe 5 along the height thereof according to actual needs. The middle position of the direction. It should be pointed out that the shape of the gas header 2 and the liquid header 5 of the high-efficiency heat exchange tube of the present invention is not limited to a cylindrical structure, and can be adjusted to other shapes according to installation requirements or space constraints. The shape is suitable for the space requirements, and the installation positions of the inlet connecting pipe 1 and the outlet connecting pipe 6 are not limited to one side or the middle of the gas collecting pipe 2 and the liquid collecting pipe 5, the operator can adjust the The positions of the inlet connecting pipe 1 and the outlet connecting pipe 6 are, for example, arranged on opposite sides of the cylindrical structure or at any position along the length of the cylindrical structure. the

Embodiment two

An evaporative condenser includes a box body, a heat exchange coil, a fan, a water collecting pan, a circulating water pump and a spraying device, and the evaporative condenser includes the high-efficiency heat exchange tubes described above. The evaporative condenser involved in the utility model mainly adopts the above-mentioned high-efficiency heat exchange tubes with better thermal conductivity and smaller tube diameters.

In the evaporative condenser of the present utility model, the refrigerant enters the gas collecting pipe 2 from the inlet connection pipe 1, and flows through the "Ω"-shaped twisted heat exchange tube, and the diameter of the heat exchange tube is φ≤15mm. In this embodiment, Among them, the heat exchange tubes include the first heat exchange tube 3 of upper and lower layers, the second heat exchange tube 7 and the corner elbow 4, the first heat exchange tube 3 and the second The shape, size and arrangement of the heat exchange tubes 7 are consistent with the description of the high-efficiency heat exchange tubes above, and will not be repeated here. The first heat exchange tubes 3 and the second heat exchange tubes 7 can be arranged in a row Or multiple rows, when multiple rows of heat exchange tubes are used, the first heat exchange tubes 3 and the second heat exchange tubes 7 of two adjacent rows are welded and connected by the corner elbow 4, and the refrigerant flows through several rows After the heat exchange tube, it is collected in the liquid collecting pipe 5 and flows out through the outlet connecting pipe 6 .

The evaporative condenser of the utility model has good thermal conductivity of the heat exchange tube and a small tube diameter, thereby greatly enhancing the heat transfer performance and pressure resistance of the heat exchanger, which is conducive to improving the refrigeration performance of the evaporative condenser, and The structure is simple, and it can be manufactured into a flat and compact type, occupying less space, thereby helping to reduce the volume of the condenser product.

At the same time, it should be pointed out that the arrangement of the evaporative condensation heat exchange tubes of the present invention can be arranged in three layers, four layers or multiple layers as required, as long as the pipes of different layers are staggered, At the same time, the structure of the high-efficiency heat exchange tube of the present invention is not limited thereto, and the height difference between the adjacent first heat exchange tube 3 and the second heat exchange tube 7 can be adjusted as required. The heights of the first heat exchange tube 3 and the second heat exchange tube 7 can also be different, and the first heat exchange tube 3 and the second heat exchange tube 7 can be arranged as separate " Ω” protrudes upward or downward to form an elbow structure. For example, the first heat exchange tube 3 is composed of a downwardly bent “Ω” elbow structure, and the second heat exchange tube 7 is composed of an upwardly bent “Ω” The elbow structure is composed of adjacent "Ω" elbows connected by several short straight pipes.

Apparently, the above-mentioned embodiments are only examples for clearly explaining, rather than limiting the implementation. For those of ordinary skill in the art, other changes or changes in different forms can be made on the basis of the above description. It is not necessary and impossible to exhaustively list all the implementation manners here. And the obvious changes or variations derived therefrom are still within the scope of protection of the utility model.

Claims (12)

1. an efficient heat-exchanging pipe, comprises discharge and collector tube, it is characterized in that: between described discharge and described collector tube, be communicated with some heat exchange tube units, described heat exchange tube unit comprises

The first heat exchanger tube, the import of described the first heat exchanger tube is communicated with described discharge,

The second heat exchanger tube, the outlet of described the second heat exchanger tube is communicated with described collector tube, and on relatively described the first heat exchanger tube of described the second heat exchanger tube, lower leaf stagger arrangement is arranged;

Corner elbow, is arranged between described the first heat exchanger tube and described the second heat exchanger tube, and the outlet of described the first heat exchanger tube is communicated with the entrance of described the second heat exchanger tube.

2. efficient heat-exchanging pipe according to claim 1, is characterized in that: described the first heat exchanger tube, described the second heat exchanger tube are all wavy, and the crest of the crest of described the first heat exchanger tube or trough and described the second heat exchanger tube or trough stagger and arrange.

3. efficient heat-exchanging pipe according to claim 2, is characterized in that: the wavy of described the first heat exchanger tube, the second heat exchanger tube upwards given prominence to and formed downwards by a plurality of " Ω ".

4. efficient heat-exchanging pipe according to claim 3, is characterized in that: the caliber of described the first heat exchanger tube, described the second heat exchanger tube is not more than 15mm.

5. efficient heat-exchanging pipe according to claim 4, it is characterized in that: the external diameter of described the first heat exchanger tube and described the second heat exchanger tube is D, level interval between described the first heat exchanger tube and described the second heat exchanger tube is L, and between the two, relation need meet: 1.5D≤L≤3D.

6. efficient heat-exchanging pipe according to claim 5, it is characterized in that: the height of described the first heat exchanger tube and described the second heat exchanger tube is identical and be S2, the vertical drop that described the first heat exchanger tube and described the second heat exchanger tube stagger is up and down S1, and between the two, relation need meet: 0.5S2≤S1≤2S2.

7. efficient heat-exchanging pipe according to claim 6, is characterized in that: the vertical drop that the first heat exchanger tube, the second heat exchanger tube stagger up and down meets: " Ω " that described the first heat exchanger tube projects upwards and described the second heat exchanger tube be the center superposition of outstanding " Ω " downwards.

8. efficient heat-exchanging pipe according to claim 7, is characterized in that: described the first heat exchanger tube, described the second heat exchanger tube are riffled tube.

9. efficient heat-exchanging pipe according to claim 8, is characterized in that: on described discharge, be provided with inlet connection, on described collector tube, be provided with discharge connection.

10. efficient heat-exchanging pipe according to claim 9, is characterized in that: described inlet connection and described discharge connection are communicated with the mouth of pipe of described discharge and the mouth of pipe of described collector tube respectively.

11. efficient heat-exchanging pipes according to claim 9, is characterized in that: described inlet connection and described discharge connection are communicated with the sidewall of described discharge and the sidewall of described collector tube respectively.

12. 1 kinds of evaporative condensers, comprise casing, heat exchange coil, and blower fan, water-collecting tray, water circulating pump and spray equipment, is characterized in that: described evaporative condenser comprises the efficient heat-exchanging pipe described in any one in claim 1-11.