CN210801699U - Evaporator with dryness regulating and controlling function - Google Patents

Abstract

The utility model relates to an evaporator with a dryness control function, comprising a header, the header is provided with a side plate A and a side plate B arranged oppositely, a pipeline is arranged between the side plate A and the side plate B, and the side plate A and the side plate B are arranged The side plate B is provided with a partition, which partitions the side plate A and the side plate B into a plurality of mutually independent working medium stroke sections, the side plate A is connected to the working medium inlet section, and the side plate B is connected to the working medium outlet. The working medium enters the side plate A from the working medium inlet section, and circulates in the working medium stroke section, side plate A, side plate B, pipeline, and working medium outlet section, and a gas-liquid separator is arranged in the working medium outlet section, among which, A first branch is arranged between the working medium stroke section of the side plate B and the working medium inlet section, and a second branch is arranged between the working medium stroke section of the side plate A and the outlet end of the gas-liquid separator. The utility model can adjust the dryness of the working medium during the use of the evaporator, and has the advantage of maintaining a stable heat exchange coefficient.

Description

An evaporator with dryness control function

technical field

The utility model relates to an evaporator with a dryness control function.

Background technique

Relevant studies have shown that in the process of evaporative heat transfer, the dryness of the working medium has a high heat transfer coefficient when the dryness is 0.6-0.8. When the working fluid exchanges heat in the evaporator, the dryness of the working fluid will gradually increase along the process, so it cannot be guaranteed that the dryness of the working fluid in each tube pass is within the optimal range of 0.6-0.8. Therefore, the evaporation in the prior art During use, the heat transfer coefficient will change due to the change in the dryness of the working medium, and the best heat transfer effect cannot be achieved.

Utility model content

In order to overcome the problem of unstable dryness of the working medium during the use of the evaporator in the prior art, the utility model provides an evaporator with a dryness control function, which can adjust the dryness of the working medium during the use of the evaporator, and has the advantages of The advantage of maintaining a stable heat transfer coefficient.

In order to solve the above-mentioned technical problems, the technical scheme adopted by the present utility model is: an evaporator with a dryness control function, which includes a header, and the header is provided with a side plate A and a side plate B oppositely arranged, and the side plate A and the side plate B are arranged oppositely. Pipes are arranged between the side plates B, and partition plates are arranged in the side plates A and B. The partition plates partition the side plates A and B into a plurality of independent working medium stroke sections, and the side plates A are connected to the working medium. The side plate B is connected to the outlet section of the working medium, and the working medium enters the side plate A from the inlet section of the working medium, and circulates in the stroke section of the working medium, the side plate A, the side plate B, the pipeline and the outlet section of the working medium. The outlet section of the working medium is provided with a gas-liquid separator, wherein a first branch is provided between the working medium stroke section of the side plate B and the working medium inlet section, and the working medium stroke section of the side plate A is connected to the outlet of the gas-liquid separator. A second branch is provided between the ends.

In the solution of the present application, a second branch is provided between the working medium stroke section of the side plate A of the evaporator and the outlet end of the gas-liquid separator, and the saturated gas phase working medium in the side plate A is split through the second branch. It is mixed with the saturated gas-phase working medium separated by the gas-liquid separator, and the saturated gas-phase working medium is split through the second branch to adjust the dryness of the working medium. A first branch is provided between the working medium stroke section of the side plate B and the working medium inlet section, and the first branch splits a part of the saturated liquid-phase working medium at the working medium inlet into the working medium stroke section of the side plate B, to adjust the dryness of the working medium. There is a first branch between the working medium stroke section of the side plate B and the working medium inlet section, and a second branch is arranged between the working medium stroke section of the side plate A and the outlet end of the gas-liquid separator to cooperate with each other. Adjust the dryness of the working fluid in the evaporator to stabilize the dryness of the working fluid in a suitable range and improve the heat exchange efficiency of the evaporator.

In one embodiment, the first branch is provided with a flow regulating valve.

In one embodiment, the second branch is provided with a flow regulating valve.

In one embodiment, a third branch with a suction pump is provided between the working medium inlet section and the working medium stroke section of the side plate A.

Preferably, a fourth branch with a liquid suction pump is provided between the working medium stroke section of the side plate B and the gas-liquid separator.

Compared with the prior art, the utility model has the following characteristics:

Compared with the existing ordinary evaporator, the utility model achieves the purpose of separating or transporting the corresponding working medium by reasonably adding each branch branch, and separates or transports the saturated gas-phase working medium or the saturated liquid-phase working medium, so as to achieve the adjustment of each working medium. The purpose of the dryness of the working fluid in the pipe project is to stabilize the heat transfer coefficient of the working fluid, and finally achieve high-efficiency heat exchange.

Description of drawings

FIG. 1 is a schematic structural diagram of an evaporator with three partition plates provided on the side plate A and the side plate B in the embodiment of the present invention.

FIG. 2 is a schematic structural diagram of an evaporator with four partitions on the side plate A and the side plate B in the embodiment of the present invention.

FIG. 3 is a schematic structural diagram of the evaporator with two partition plates on the side plate A and the side plate B in the embodiment of the present invention.

Detailed ways

The accompanying drawings are for illustrative purposes only, and should not be construed as limitations on the present invention; in order to better illustrate the present embodiment, some parts of the accompanying drawings may be omitted, enlarged or reduced, and do not represent the size of the actual product; For those skilled in the art, it is understandable that some well-known structures and their descriptions may be omitted from the drawings. The positional relationships described in the accompanying drawings are only for exemplary illustration and should not be construed as limiting the present invention.

The same or similar symbols in the drawings of the embodiments of the present invention correspond to the same or similar components; in the description of the present invention, it should be understood that if there are terms "upper", "lower", "left", " The orientation or positional relationship indicated by "right" and the like is based on the orientation or positional relationship shown in the accompanying drawings, and is only for the convenience of describing the present invention and simplifying the description, rather than indicating or implying that the indicated device or element must have a specific orientation, It is constructed and operated in a specific orientation, so the terms describing the positional relationship in the accompanying drawings are only used for exemplary illustration, and should not be construed as a limitation on this patent. specific meaning.

Example 1:

The utility model provides an evaporator with a dryness control function. The evaporator is provided with a header 103. The header 103 is provided with a side plate A and a side plate B that are oppositely arranged, and channels are provided in the side plate A and the side plate B. A plurality of pipes are arranged between the side plate A and the side plate B, and the openings at both ends of the pipes are respectively connected with the channels in the side plate A and the side plate B.

The side plate A is connected with the working medium inlet section, and the side plate B is connected with the working medium outlet section. The working medium enters the side plate A through the working medium inlet section, then enters the pipeline, and enters the side plate B through the pipeline.

A plurality of partition plates are arranged in the side plate A and the side plate B. The partition plate divides the passages of the side plate A and the side plate B into a plurality of mutually independent working fluid stroke sections. The partition plates in the side plate A and the side plate B The plate, in cooperation with the side plate A and the side plate B and the pipeline between the side plate A and the side plate B, restricts the flow direction of the working medium to the form of a repeatedly circuitous path.

A gas-liquid separator is provided in the outlet section of the working medium, and the gas-liquid separator separates the working medium in the outlet section of the working medium from gas and liquid, extracts the gas phase and the liquid phase, and the gas phase enters the next working equipment.

In this embodiment, a first branch is provided between the working medium stroke section of the side plate B and the working medium inlet section, and the saturated liquid phase working medium in the working medium inlet section enters the working medium inlet section and the first branch, and the saturated liquid phase working medium enters the working medium inlet section and the first branch. The liquid phase working medium is split. The saturated liquid phase working medium entering the inlet section of the working medium flows in the evaporator. As the work progresses, the dryness of the saturated liquid phase working medium increases gradually after heat absorption, and the heat transfer coefficient decreases. The first branch will divert the saturated liquid phase. The working medium is fed into the working medium stroke section of the side plate B, and the saturated liquid phase working medium is mixed with the working medium with increased dryness in the working medium stroke section of the side plate B to reduce the dryness of the working medium and improve the heat transfer coefficient.

A second branch is provided between the working medium stroke section of the side plate A and the outlet end of the gas-liquid separator, and the second branch splits the working medium in the working medium stroke section of the side plate A and flows out of the saturated gas phase working medium. quality, reduce the dryness of the working medium, the saturated gas-phase working medium that flows out follows the second branch and enters the outlet end of the gas-liquid separator, and combines with the saturated gas-phase working medium separated by the gas-liquid separator to enter the next work together equipment.

In this embodiment, the number of the first branches can be changed according to the number of partitions provided on the side plate B. When the number of partitions on the side plate B is n (n is not less than 2), the first branch The number of can be n-1.

In this embodiment, the number of the second branches can be changed according to the number of partitions provided on the side plate A. When the number of partitions on the side plate A is m (m is not less than 2), the second branch The number of can be m-1.

In this embodiment, a third branch with an air pump is provided between the working medium inlet section and the working medium stroke section of the side plate A. The pressure of this part of the working medium is increased, the saturated gas phase working medium drawn by the air pump is mixed with the saturated liquid working medium in the working medium inlet section, and the dryness of the working medium in the working medium inlet section is adjusted.

There is a fourth branch with a pump between the working fluid stroke section of the side plate B and the gas-liquid separator. The pressure of the working medium mixes the extracted saturated liquid working medium with the working medium in the working medium stroke section to adjust the dryness of the working medium.

In this embodiment, both the first branch and the second branch are provided with a flow regulating valve, and the flow regulating valve adjusts the flow, so as to precisely adjust the dryness of the working medium, and the dryness of the working medium is adjusted to 0.6-0.8, Has a high heat transfer coefficient.

As shown in FIG. 1 , the side plate A and the side plate B are provided with three partitions 105 , the saturated liquid phase working medium is divided by the first branch 108 at the working medium inlet section 110 , part of it enters the first branch 108 , and the rest Continue to advance along the working medium inlet section 110, under the action of the working medium stroke section formed by the partition plate 105 of the side plate A, enter the side plate B through the pipeline 104, and the pipeline 104 is provided between the side plate A and the side plate B with several , under the action of the working medium stroke section formed by the partition plate 105 of the side plate B, it flows back to the side plate A through the pipeline 104, and then flows to the side plate A through the pipeline 104 under the action of the working medium stroke section formed by the partition plate 105 of the side plate A. Side plate B, the working medium flow path in the header 103 and so on, until the working medium flows into the working medium outlet section 111 . The straight line with the arrow in Fig. 1 indicates the flow direction of the working medium.

The first branch 108 diverts the saturated liquid-phase working medium to the working medium stroke section of the side plate B, mixes with the working medium in the working medium stroke section of the side plate B, adjusts the dryness of the working medium, and adjusts the working medium dryness. At 0.6-0.8, it has a higher heat transfer coefficient.

The second branch 109 divides the saturated gas-phase working medium in the working medium, which can adjust the dryness of the working medium. At the same time, the second branch 109 mixes the split saturated gas-phase working medium with the saturated gas-phase working medium separated by the gas-liquid separator. , enter the working medium outlet section 111, and the saturated gas-phase working medium enters the next working equipment together.

A flow regulating valve 107 is provided on the first branch 108 and the second branch 109 for the purpose of accurately adjusting the dryness of the working medium, and the dryness of the working medium is adjusted to 0.6-0.8, which has a high heat transfer coefficient.

A third branch 112 with a suction pump 101 is provided between the working medium inlet section 110 and the working medium stroke section of the side plate A. The suction pump pulls out the partially saturated gas phase working medium in the working medium stroke section, and raises the The pressure of this part of the working fluid.

A fourth branch 113 with a liquid pump 102 is provided between the working medium stroke section of the side plate B and the gas-liquid separator 106, and the liquid pump 102 pulls the partially saturated liquid-phase working medium of the gas-liquid separator 106 away. , and increase the pressure of this part of the working fluid.

Figure 2 shows the structure and branch design of the evaporator with four partitions on both the side plate A and the side plate B. The flow of working medium is the same as that of the evaporator with three partitions, and so on.

Figure 3 shows the structure and branch design of the evaporator with two partitions on both the side plate A and the side plate B. The flow of working medium is the same as that of the evaporator with three partitions, and so on.

Obviously, the above-mentioned embodiments of the present invention are only examples for clearly illustrating the present invention, rather than limiting the implementation of the present invention. For those of ordinary skill in the art, changes or modifications in other different forms can also be made on the basis of the above description. There is no need and cannot be exhaustive of all implementations here. Any modifications, equivalent replacements and improvements made within the spirit and principles of the present utility model shall be included within the protection scope of the claims of the present utility model.

Claims (5)

1. an evaporator with a dryness control function, comprising a header, the header is provided with a side plate A and a side plate B that are oppositely arranged, and a pipeline is provided between the side plate A and the side plate B, The side plate A and the side plate B are provided with a partition plate, and the partition plate partitions the side plate A and the side plate B into a plurality of mutually independent working medium stroke sections, and the side plate A is connected to the working medium inlet section. , the side plate B is connected to the outlet section of the working medium, and the working medium enters the side plate A from the inlet section of the working medium, circulates in the travel section of the working medium, the side plate A, the side plate B, the pipeline and the outlet section of the working medium, and flows at the outlet of the working medium. There is a gas-liquid separator in the side plate B, which is characterized in that a first branch is arranged between the working medium stroke section of the side plate B and the working medium inlet section, and the working medium stroke section of the side plate A is separated from gas and liquid A second branch is arranged between the outlet ends of the device. 2 . The evaporator with dryness control function according to claim 1 , wherein the first branch is provided with a flow control valve. 3 . 3 . The evaporator with dryness control function according to claim 1 , wherein the second branch is provided with a flow control valve. 4 . 4 . The evaporator with dryness control function according to claim 1 , wherein a third branch with an air pump is provided between the working medium inlet section and the working medium stroke section of the side plate A. 5 . . 5 . The evaporator with dryness control function according to claim 4 , wherein a fourth branch with a liquid pump is provided between the working medium stroke section of the side plate B and the gas-liquid separator. 6 . road.

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