JP2014013130A - Surface treatment method for heat exchanger - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a surface treatment method for a heat exchanger, capable of, at a step of cutting a stock solution of a surface treatment film, securely removing an excess stock solution to form the surface treatment film having a uniform thickness.SOLUTION: A surface treatment method for a heat exchanger 1 includes the steps of: applying hydrophilic paint to a surface of the heat exchanger 1 (applying step); removing the hydrophilic paint by using centrifugal force acting on the heat exchanger 1 attached to a tip end of a pendulum swung around a support shaft 103 to adjust an adhesion amount of the hydrophilic paint to be applied to the heat exchanger 1 (liquid cutting step); and then forming a film of the hydrophilic paint (film forming step).

Description

  The present invention relates to a surface treatment method for a heat exchanger.

  Conventionally, in a heat exchanger such as an evaporator of an air conditioner, water vapor adheres to the surface of the fins of the heat exchanger due to condensation of water vapor in the air, so-called condensation occurs, or the water droplets become frost and so-called landing. There is concern about frosting. As a result, the water droplets and frost hinder heat exchange on the surface of the fin, and the gap between the fins of the heat exchanger becomes narrow, and the resistance of the air passing through the gap (ventilation resistance) increases. As a result, there has been a problem that the amount of air passing between the fins decreases and the heat exchange efficiency of the heat exchanger decreases. A measure of performing a defrosting operation to remove frost and ice generated in the heat exchanger is also taken, but there is also a problem that extra energy is consumed for the defrosting operation.

  Therefore, a surface treatment has been proposed in which a highly hydrophilic coating is applied to the fin surface of the heat exchanger. Thereby, the effect | action which a water droplet flows down on the surface of a fin is heightened, or the time until frost adheres is extended.

  Here, in recent years, development of a heat exchanger having a complicated structure, such as a narrow fin pitch, has been advanced in order to improve heat exchange efficiency. For example, heat in which a pair of shunt tubes arranged opposite to each other are connected by a plurality of heat transfer tubes arranged along the longitudinal direction of the flow shunt tube, and fins (for example, corrugated fins) are arranged and joined between adjacent heat transfer tubes An exchanger is known. In addition, heat exchangers in which all components are made of aluminum are being developed with the aim of improving heat exchange efficiency, reducing refrigerant, and high recyclability. As a surface treatment method for a heat exchanger in which all such components are made of aluminum, a dip coating method is known in which a heat exchanger that has been assembled is immersed in a stock solution of a surface treatment film.

  In addition, as a surface treatment method of a general heat exchanger, a precoat method for performing a surface treatment before assembly such as a roll coat method or a curtain coat method is used. Since a general heat exchanger composed of a copper member and an aluminum member is assembled by tube expansion processing (non-heat treatment or local heat treatment), surface treatment by a precoat method is suitable. On the other hand, all the structural members made of aluminum are assembled by batch brazing (heating process). When surface treatment is performed before assembly and heat treatment is performed by batch brazing, the surface treatment agent is altered or sublimated. Therefore, as a surface treatment method for a heat exchanger in which all the constituent members are made of aluminum, an after coating method such as a dip coating method in which the surface treatment is performed after the assembly is completed is preferable.

  In the surface treatment process of the heat exchanger by the dip coating method, the heat exchanger after washing with water is immersed in a container containing the stock solution of the surface treatment film. And after pulling up a heat exchanger from a container, the liquid draining process and film-forming process (for example, drying process, baking process) are performed, and the method of keeping the thickness of a surface treatment film within a standard value is employ | adopted. Such a conventional heat exchanger surface treatment method is disclosed in Patent Document 1.

  The surface treatment method of the conventional heat exchanger described in Patent Document 1 is a method of performing a liquid draining process using centrifugal force, and the heat exchanger is applied to a basket-like processing container whose side plate is a perforated plate. And the processing container is rotated at a predetermined speed. As a result, the excess stock solution of the surface treatment film adhering to the surface of the heat exchanger is centrifuged, and the thickness of the surface treatment film is made uniform and the quality is stabilized.

JP-A-6-10150

  Here, the heat exchanger used for an air conditioner for general households is relatively large in size and relatively heavy in weight. When the surface treatment method of the conventional heat exchanger described in Patent Document 1 is applied to such a heat exchanger, an excessive load may be applied to the rotating shaft of the centrifugal separator in the liquid draining process. There was a problem that it was necessary to prepare a very large centrifuge. Furthermore, there is also a problem that it is highly likely that it is difficult to obtain a sufficient centrifugal force for removing excess stock solution of the surface treatment film from the surface of the heat exchanger.

  The present invention has been made in view of the above points, and when forming a surface treatment film that promotes drainage of condensed water on the surface of the heat exchanger, an extra stock solution is removed in the step of draining the stock solution of the surface treatment film. It is an object of the present invention to provide a surface treatment method for a heat exchanger that can be reliably removed and can form a surface treatment film having a uniform thickness.

  In order to solve the above problems, the present invention provides a surface treatment method for a heat exchanger that forms a surface treatment film for promoting drainage of condensed water on the surface of the heat exchanger, the surface of the heat exchanger being Applying the undiluted solution of the surface treatment film and removing the undiluted solution by centrifugal force acting on the heat exchanger attached to the tip of a pendulum swinging around a fulcrum, and attaching the undiluted solution to the heat exchanger It is characterized by having a liquid draining step for adjusting the amount and a film forming step for forming the stock solution into a film.

  According to this structure, the excess stock solution of the surface treatment film | membrane of a heat exchanger is removed using the centrifugal force of a pendulum. Therefore, it is prevented that an excessive load is applied to the fulcrum supporting the heat exchanger.

  In the heat exchanger surface treatment method having the above-described configuration, the liquid draining step starts swinging by the pendulum after holding the heat exchanger at an initial position for a predetermined time.

  According to this configuration, before starting swinging by the pendulum, excess stock solution of the surface treatment film of the heat exchanger moves downward and collects due to the action of gravity. When swinging by the pendulum is started, excess stock solution collected by the centrifugal force of the pendulum is efficiently removed.

  Note that the “predetermined time” described here is an arbitrary time set in advance with respect to the timing of starting swinging by the pendulum, and may be, for example, about several seconds to five seconds. In the embodiment described later, this “predetermined time” is set to “3 seconds”, but it is not limited to such a time.

  In the heat exchanger surface treatment method having the above-described configuration, the liquid draining step is characterized in that a predetermined initial speed is applied to the pendulum.

  According to this configuration, when starting swinging by the pendulum, excess stock solution of the surface treatment film of the heat exchanger moves vigorously. Therefore, even if the number of reciprocations of the pendulum is relatively small, excess stock solution is easily removed by the action of the centrifugal force of the pendulum.

  The “predetermined initial speed” described here is an arbitrary speed set in advance with respect to the moving speed of the pendulum, and may be a speed of about 1 to 4 m / sec, for example. In the embodiment described later, the “predetermined initial speed” is set to “1 m / sec”, but is not limited to such a speed.

  In the heat exchanger surface treatment method configured as described above, the liquid draining step sets a predetermined number of reciprocations for swinging the pendulum.

  According to this configuration, for example, by setting the number of reciprocations of the pendulum to be relatively large, it becomes easy to remove excess stock solution of the surface treatment film of the heat exchanger. Therefore, even if the movement speed of the pendulum is relatively low, excess stock solution is easily removed by the action of the centrifugal force of the pendulum.

  The “predetermined number of reciprocations” described here is an arbitrary number of reciprocations set in advance regarding the swing of the pendulum, and may be, for example, about 3 to 10 reciprocations. In the embodiment described later, this “predetermined number of reciprocations” is set to “10 times”, but is not limited to such a number.

  Moreover, in the surface treatment method of the heat exchanger having the above-described configuration, the liquid draining step includes a suspension member that suspends the heat exchanger and a grip portion provided on the heat exchanger that connects the suspension member. It is characterized by being shared with the coating step.

  According to this configuration, the liquid draining process is executed immediately after the coating process. Therefore, the surface treatment of the heat exchanger is performed quickly, and the trouble of attaching / detaching the heat exchanger to / from the suspension member is also saved.

  Moreover, in the surface treatment method for a heat exchanger having the above-described configuration, the heat exchanger connects a pair of opposing shunt tubes with a plurality of heat transfer tubes, and arranges and joins fins between the adjacent heat transfer tubes. In the heat exchanger, the liquid draining step is characterized in that the pendulum swings so that a ventilation direction of the heat exchanger with respect to the fin and a swinging direction of the pendulum are always parallel to each other.

  According to this configuration, the air flow generated by the swing of the pendulum circulates along the ventilation direction with respect to the fins. Therefore, the excess stock solution of the surface treatment film is easily removed by the action of the centrifugal force of the pendulum, and a ventilation path is preferably ensured without storing the excess stock solution in the gaps between the fins.

  In the heat exchanger surface treatment method having the above-described configuration, the liquid draining step may be performed on the heat exchanger in a direction parallel to the swinging direction of the pendulum at an initial position and / or a stop position of the pendulum. It is characterized by blowing air flow.

  According to this structure, the airflow which arises by blowing is added to the airflow which distribute | circulates along the ventilation direction with respect to a fin which generate | occur | produces with the swing of a pendulum. Therefore, the effect | action which removes the excess undiluted | stock solution of a surface treatment film | membrane, and the effect | action which ensures the ventilation path | route with respect to a fin improve further.

  According to the configuration of the present invention, when forming a surface treatment film that promotes drainage of condensed water on the surface of the heat exchanger, it is possible to reliably remove excess stock solution in the step of draining the stock solution of the surface treatment film. It is possible to provide a surface treatment method for a heat exchanger that can form a surface treatment film having a uniform thickness.

BRIEF DESCRIPTION OF THE DRAWINGS It is an external appearance schematic diagram which shows the heat exchanger for demonstrating the surface treatment method of the heat exchanger of 1st Embodiment of this invention. It is the vertical cross-section part enlarged view in the II-II line of the heat exchanger shown in FIG. It is the external appearance partial enlarged view of the heat exchanger for demonstrating the surface treatment method of the heat exchanger of 1st Embodiment of this invention. It is a flowchart which shows the procedure of the surface treatment method of the heat exchanger of 1st Embodiment of this invention. It is a schematic explanatory drawing which shows the immersion to the chemical | medical solution of the heat exchanger in the surface treatment method of the heat exchanger of 1st Embodiment of this invention. It is a schematic explanatory drawing which shows the liquid removal process of the surface treatment method of the heat exchanger of 1st Embodiment of this invention. It is a schematic explanatory drawing which shows the liquid removal process of the surface treatment method of the heat exchanger of 2nd Embodiment of this invention.

  Hereinafter, embodiments of the present invention will be described with reference to FIGS.

<First Embodiment>
First, prior to describing the surface treatment method for a heat exchanger according to the first embodiment of the present invention, a schematic structure of the heat exchanger to which the surface treatment method is applied will be described with reference to FIGS. Will be explained. FIG. 1 is a schematic external view of a heat exchanger, FIG. 2 is a partially enlarged view of a vertical section taken along line II-II of the heat exchanger shown in FIG. 1, and FIG. In the following description, the left-right direction in FIG. 1 is defined as the X direction, the up-down direction is defined as the Y direction, and the depth direction on the paper is defined as the Z direction. The X direction, Y direction, and Z direction in FIGS. 2 and 3 indicate the same directions as those in FIG.

  As shown in FIGS. 1 to 3, the heat exchanger 1 includes two branch pipes 2, a plurality of heat transfer pipes 3, fins 4, and a drainage unit 5.

  The diverter tube 2, the heat transfer tube 3, the fins 4 and the drainage part 5 are formed of, for example, aluminum or aluminum alloy having advantages such as relatively high thermal conductivity, low cost, and good workability. . Note that the material of these constituent elements is not limited to aluminum or aluminum alloy, and other metals having a relatively high thermal conductivity such as gold and copper may be arbitrarily used. You may change.

  Two, that is, a pair of opposing shunt pipes 2 extend in the Y direction in FIG. 1 and are arranged in parallel at a predetermined interval in the X direction. The two shunt pipes 2 are connected to different pipes (not shown) via pipe sections 6 respectively. The flow dividing pipe 2 is formed with a flow path through which the refrigerant can flow and communicates with the pipe section 6.

  The plurality of heat transfer tubes 3 extend in the X direction in FIG. 1 and are arranged in parallel at a predetermined interval in the Y direction. Each heat transfer tube 3 is connected to two shunt tubes 2 at both ends in the X direction in FIG. As shown in FIG. 2, the heat transfer tube 3 is formed with a flow passage 3 a through which a refrigerant can flow and communicates with the flow dividing tube 2.

  Each heat transfer tube 3 has a flat shape with a width in the Z direction wider than the thickness in the Y direction in FIG. 1 (see FIG. 2). As shown in FIG. 2, the heat transfer tube 3 has a plurality of flow paths 3a having the same cross-sectional shape and cross-sectional area along the Z direction, and the plurality of flow paths 3a are arranged in the Z direction.

  The fins 4 are disposed between the heat transfer tubes 3 adjacent in the Y direction in FIG. 1 and are joined to the heat transfer tubes 3. The fin 4 is a member obtained by forming a flat plate into a wave shape (corrugated shape). The corrugated fin 4 is provided such that the top of the mountain in FIG. 1 is in contact with the upper heat transfer tube 3 and the bottom of the valley is in contact with the lower heat transfer tube 3. The fin 4 has a corrugated shape, thereby increasing the contact area with the external air. In addition, the ventilation direction with respect to the heat exchanger 1 is the Z direction in FIG.1 and FIG.2 (the direction which a solid line arrow points in FIG. 2). In addition to corrugated fins having a wave shape, the fins 4 may be configured in other shapes such as plate fins and louver fins.

  The drainage part 5 is formed in the outer surface of the upstream and downstream of the ventilation direction of the heat exchanger tube 3, as shown in FIG.2 and FIG.3. The drainage part 5 is comprised by the some plate 5a which makes the rectangular shape attached so that it might protrude toward the ventilation direction outer side from the outer surface of the heat exchanger tube 3. As shown in FIG. The plurality of plates 5 a are arranged along the refrigerant flow direction of the heat transfer tube 3. Further, as shown in FIG. 3, each plate 5 a is attached to the heat transfer tube 3 with a predetermined angle, for example, 21 °, with respect to the refrigerant flow direction (X direction) of the heat transfer tube 3 when viewed from the ventilation direction. ing. Condensed water generated on the surface of the fin 4 and transmitted through the surface of the fin 4 is guided to the drainage unit 5 and dripped outside the heat exchanger 1.

  The flow dividing pipe 2, the heat transfer pipe 3, the fin 4 and the drainage part 5 are connected by brazing. Thereby, the leakage of the refrigerant | coolant which distribute | circulates the inside of the heat exchanger 1 can be prevented, the efficiency of the heat conduction between the heat exchanger tube 3 and the fin 4 can be improved, and the fin 4 to the drainage part 5 can be improved. The efficiency of drainage can be increased. In addition, it may replace with each brazing process and may connect each component using connection processing methods, such as a thermal spraying process, thermal expansion, and welding.

  When the refrigerant is injected into the heat exchanger 1 having the above-described configuration from one of the pipe portions 6, the refrigerant flows through the shunt pipe 2 connected to the pipe portion 6. The refrigerant flowing through the inside of the branch pipe 2 is then divided and flows into the plurality of flow paths 3a of the plurality of heat transfer pipes 3 respectively. The refrigerant flowing through the flow path 3 a inside the heat transfer tube 3 exchanges heat with the air outside the heat exchanger 1 through the heat transfer tube 3 and the fins 4. For example, when the heat exchanger 1 is used as an evaporator, the refrigerant takes heat from outside air. On the other hand, when the heat exchanger 1 is used as a condenser, the refrigerant releases heat to the outside air.

  The heat exchanger 1 is used as, for example, a heat exchanger (evaporator) of an outdoor unit of a heat cycle used for an air conditioner or an evaporator of a cooling device of a refrigerator. At this time, if the temperature of the surface of the heat exchanger 1 becomes lower than the dew point of the external air, condensation occurs on the surface of the heat exchanger 1. When the temperature of the surface of the heat exchanger 1 is further lowered, the condensed moisture is frozen and frost is generated (frosting). When such frost formation occurs, the gaps between the fins 4 are filled with frost and become narrower, and the possibility that the air flow is hindered increases. As a result, the heat exchange efficiency of the heat exchanger 1 may be reduced.

  In order to solve such problems, the heat exchanger 1, that is, the diverter tube 2, the heat transfer tube 3, the fin 4 and the drainage portion 5 are formed with a surface treatment film for promoting drainage of condensed water generated on the surface thereof. Yes. As the surface treatment film, for example, a hydrophilic coating film is employed.

  When heat exchange is performed by the heat exchanger 1 provided in the outdoor unit, condensed water adheres to the surface of the heat exchanger 1, that is, the surfaces of the branch pipe 2, the heat transfer pipe 3, the fins 4, and the drainage section 5. A hydrophilic coating film is formed on the surfaces of the branch pipe 2, the heat transfer pipe 3, the fins 4 and the drainage part 5, and the attached condensed water flows as a water film. Water on the hydrophilic coating film has a small contact angle and a thin film thickness. As a result, even when the gap is narrow like the gap between the fins 4, the water adhering to the surface of the adjacent fin 4 is difficult to contact, and a bridge is not easily formed between the adjacent fins 4. Thus, the formation of the hydrophilic coating film on the heat exchanger 1 makes it difficult for dew condensation water to remain on the surface of the heat exchanger 1.

  Since the condensed water adhering to the hydrophilic coating film is slow but keeps moving, the condensed water is difficult to freeze. And the dew condensation water which generate | occur | produced on the surface of the fin 4 and transmitted along the surface of the fin 4 is guide | induced to the waste_water | drain part 5, and is dripped outside the heat exchanger 1. As described above, in the heat exchanger 1 having a hydrophilic coating film formed on the surface, condensation occurs, but the drainage of condensed water is promoted and frost formation is difficult to occur.

  On the other hand, a water-repellent coating film may be formed on the surface of the heat exchanger 1 instead of the hydrophilic coating film. When the water-repellent coating film is formed, the contact area between the dew condensation water and the surface of the heat exchanger 1 is reduced, so that even a small amount of dew condensation water is released to the outside of the heat exchanger 1. Thereby, even when the gap is narrow like the gap of the fins 4, it is difficult to form a bridge and it is difficult for dew condensation water to remain. Thus, also when a water-repellent coating film is formed on the surface of the heat exchanger 1, drainage of condensed water is promoted and frost formation is less likely to occur as in the case where a hydrophilic coating film is formed.

  Next, the surface treatment method of the heat exchanger 1 will be described with reference to FIGS. 5 and 6 along the procedure shown in FIG. FIG. 4 is a flowchart showing the procedure of the surface treatment method of the heat exchanger 1. FIG. 5 is a schematic explanatory view showing immersion of the heat exchanger 1 in a chemical solution in the surface treatment method of the heat exchanger 1, and FIG. 6 is a schematic explanatory view showing a liquid draining step. In addition, the X direction, Y direction, and Z direction of FIG. 5 show the same directions as the respective directions of FIG. Moreover, when the heat exchanger 1 exists in the lowest part in FIG. 6, the X direction of FIG. 6, Y direction, and Z direction show the same direction as each direction of FIG.

  Moreover, FIG. 5 is a figure explaining the condition of the immersion to the chemical | medical solution M of the heat exchanger 1 in the degreasing | defatting process mentioned later, a base treatment process, and a hydrophilic coating application process, Comprising: The chemical | medical solution M stored by the container V is respectively In the process. When the heat exchanger 1 is immersed in the chemical solution M, as shown in FIG. 5, the clamp 102 of the suspending member 101 for suspending the heat exchanger 1 is provided at the end of the branch pipe 2 of the heat exchanger 1. Grip.

  Here, it is assumed that the assembly of the heat exchanger 1 is completed prior to the surface treatment of the heat exchanger 1. In the heat exchanger 1, the shunt pipe 2, the heat transfer pipe 3, the fins 4 and the drainage part 5 are assembled in a predetermined shape (see FIGS. 1 to 3), and the joining portion of each member is connected by a brazing method or the like. It is fixed with.

  When the assembly of the heat exchanger 1 is completed, the surface treatment of the heat exchanger 1 is performed. As a surface treatment of the heat exchanger 1, a dip coating method is adopted.

  When the surface treatment of the heat exchanger 1 is started (start of FIG. 4), a degreasing process for removing oil and the like on the surface of the heat exchanger 1 is executed (step # 101 of FIG. 4). The degreasing step is performed by immersing the heat exchanger 1 that has been assembled in a container V in which a strong alkaline degreasing agent is stored as the chemical solution M in FIG.

  In the degreasing step, the heat exchanger 1 is degreased by immersing it in a 2% solution of a commercially available strong alkaline degreasing agent (for example, a degreasing agent manufactured by Nippon Parkerizing Co., Ltd.) at a temperature of 60 ° C. for 2 minutes. By this degreasing treatment, dirt such as oil on the surface of the metal material of the heat exchanger 1 can be removed, and a hydrophilic coating film to be formed later can be formed as a smooth and uniform coating film.

  After the degreasing process, a cleaning process is executed (step # 102). In this washing step, the heat exchanger 1 is washed with clean water or pure water to wash away the degreasing agent.

  Subsequently, a ground treatment process for imparting corrosion resistance, rust resistance and the like to the surface of the heat exchanger 1 is executed (step # 103). The ground treatment step is performed by immersing the heat exchanger 1 subjected to the degreasing treatment in the container V in which the chemical conversion agent solution is stored as the chemical solution M in FIG.

  In the ground treatment step, the heat exchanger 1 is subjected to chemical conversion treatment by immersing it in a commercially available chemical conversion solution at a temperature of 70 ° C. (for example, a chemical conversion agent manufactured by Nihon Parkerizing Co., Ltd. adjusted to pH 4) for 2 minutes. A base film is formed by an oxide film. This base film imparts corrosion resistance, rust resistance, and the like to the heat exchanger 1. The formation method of the base film is not limited to such a chemical conversion treatment with an acid, and the base film may be formed using a method such as etching, oxidation, or metal vapor deposition.

  After the chemical conversion treatment, a cleaning process is executed (step # 104). In this washing step, the heat exchanger 1 is washed with pure water to wash away the chemical conversion treatment agent.

  Subsequently, a hydrophilic paint coating process is performed in which a paint that is a stock solution of the hydrophilic coating film is applied to the surface of the heat exchanger 1 (step # 105). The hydrophilic coating application step is executed by immersing the heat exchanger 1 subjected to the base treatment in a container V in which the hydrophilic coating is stored as the chemical solution M in FIG.

In the hydrophilic coating application step, the heat exchanger 1 is dipped in a hydrophilic coating (for example, SX-01 manufactured by Kansai Paint Co., Ltd.) and pulled up, and then the film thickness is controlled so that a predetermined film thickness is obtained. The management of the film thickness is controlled by the amount of change in weight of the heat exchanger 1 before and after the coating treatment with the hydrophilic paint. As a method for weight management, the wet coating weight is calculated from the solid content concentration and density of the hydrophilic coating and the surface area of the heat exchanger 1 (for example, 1.2 g / m ^{2 in} the case of SX-01), The weight is added as the weight increased from the initial weight.

  Subsequently, a liquid draining process for adjusting the film thickness of the hydrophilic paint applied to the surface of the heat exchanger 1 is executed (step # 106). In the liquid draining process, the centrifugal force of the pendulum is used to remove excess paint from the heat exchanger 1, particularly the fins 4 and the drainage unit 5, and the weight is measured to obtain a weight corresponding to a desired film thickness.

  In the liquid draining process, as shown in FIG. 6, a surface treatment apparatus 100 capable of realizing the movement of the pendulum that swings the suspension member 101 around the support shaft 103 that is a fulcrum is used. Then, excess paint is removed by centrifugal force acting on the heat exchanger 1 attached to the tip of the pendulum, that is, the tip of the hanging member 101. The arc-shaped arrow drawn in FIG. 6 indicates the swinging direction (circumferential direction) of the pendulum.

  Here, an example is described about the specifications of the heat exchanger 1 and the pendulum. The heat exchanger 1 has, for example, a core length (length in the X direction in FIG. 1) of 868.3 mm, a pitch (interval) between adjacent heat transfer tubes 3 of 21 mm, a number of stages of the heat transfer tubes 3 of 28 and a pitch of fins 4. 19 mm and the width of the fin 4 are 18.2 mm. Accordingly, the heat exchanger 1 has a length (width) in the X direction of 868.3 mm in FIG. 1, a length (height) in the Y direction of 588 mm (= 21 mm × 28 steps), and a length in the Z direction. The (thickness) is 18.2 mm (= the width of the fin 4). The length of the pendulum is, for example, 0.5 to 1 m. In FIG. 1, the configuration of the heat exchanger 1 such as the above dimensions and quantity is omitted.

  As an initial position for starting swinging by the pendulum, for example, a substantially horizontal position on the left side with respect to the support shaft 103 is set as an initial position as shown in FIG. The initial position of the pendulum is not limited to the horizontal position with respect to the support shaft 103, and may be set to another position (height).

  The heat exchanger 1 is attached to the tip of the suspension member 101 so that the ventilation direction with respect to the fins 4 and the swinging direction of the pendulum are always parallel. That is, the heat exchanger 1 is attached to the tip of the suspension member 101 so that the ventilation direction with respect to the fins 4 is parallel to the Y direction at the initial position of FIG. Further, the relative posture between the heat exchanger 1 and the suspension member 101 does not change during the swinging, but swings in the form depicted by a two-dot chain line in FIG.

  Here, the liquid draining step may start swinging by the pendulum after the heat exchanger 1 is held at the initial position for a predetermined time, for example, 3 seconds. The holding time of 3 seconds is preset in the surface treatment apparatus 100 and can be arbitrarily changed as appropriate.

  In the liquid draining step, a predetermined initial speed, for example, an initial speed of 1 m / sec, may be applied to the pendulum. Further, the liquid draining step may be set to reciprocate a predetermined number of times, for example, 10 times with respect to the swing of the pendulum. The initial speed of 1 m / sec and the number of reciprocations of 10 are preset in the surface treatment apparatus 100 and can be arbitrarily changed as appropriate.

  Regarding the swinging by the pendulum, the moving speed differs between the radially inner portion and the radially outer portion of the heat exchanger 1 relative to the support shaft 103. However, it has been found that there is no change in the amount of excess paint removed using centrifugal force beyond a certain speed. Therefore, it is only necessary to set a suitable moving speed on the basis of the radially inner portion of the heat exchanger 1 with respect to the support shaft 103, and there is an adverse effect that the paint is removed more than necessary at the radially outer portion of the heat exchanger 1. Does not occur.

  Subsequently, a film forming process for forming a hydrophilic paint on the surface of the heat exchanger 1 is executed (step # 107). In the film forming step, the heat exchanger 1 is baked in a drying apparatus at 100 ° C. for 10 minutes to form a hydrophilic paint. In addition, as a hydrophilic coating material, it has thermosetting property, photocuring property, etc., You may use the coating material provided with any property. In the film forming process, when a thermosetting hydrophilic paint is used, a drying device that heats the heat exchanger 1 is used. When a photocurable hydrophilic paint is used, the hydrophilic paint is cured. A drying apparatus that irradiates light having a wavelength necessary for the above is used.

  When the film forming step is completed, the surface treatment of the heat exchanger 1 is finished (end in FIG. 4).

  As described above, the surface treatment method of the heat exchanger 1 for forming the surface treatment film that promotes drainage of the dew condensation water on the surface of the heat exchanger 1 is performed by applying a hydrophilic paint that is a stock solution of the surface treatment film. The paint is removed by the paint application process and the centrifugal force acting on the heat exchanger 1 attached to the tip of the pendulum swinging around the support shaft 103, which is a fulcrum, and the amount of paint applied to the heat exchanger 1 is adjusted. A liquid draining step, and a film forming step for forming the coating material into a film. Thereby, the excess paint of the hydrophilic coating film of the heat exchanger 1 is removed using the centrifugal force of the pendulum. Therefore, it is possible to prevent an excessive load from being applied to the support shaft 103 that supports the heat exchanger 1.

  In the liquid draining process, the swinging by the pendulum is started after the heat exchanger 1 is held at the initial position for a predetermined time. Thereby, before the rocking | fluctuation by a pendulum is started, the excess coating material of the hydrophilic coating film of the heat exchanger 1 moves below and gathers by the effect | action of gravity.

  For example, when the initial position at which swinging by the pendulum starts is a horizontal position with respect to the support shaft 103 as shown in FIG. 6, the Z direction in FIG. 2 is parallel to the Y direction (vertical direction) in FIG. As a result, excess paint adhering to the fins 4 and the like moves downward due to the action of gravity and collects in the drainage portion 5. When the swinging by the pendulum is started, excess paint collected in the drainage part 5 due to the centrifugal force of the pendulum can be efficiently removed.

  Further, the liquid draining process gives a predetermined initial speed to the pendulum, so that when the swinging by the pendulum is started, excess paint on the hydrophilic coating film of the heat exchanger 1 moves vigorously. Therefore, even when the number of reciprocations of the pendulum is relatively small, excess paint can be easily removed by the action of the centrifugal force of the pendulum.

  In the liquid draining process, for example, by setting the number of reciprocations of the pendulum to be relatively large with respect to the swinging of the pendulum, it becomes easy to remove excess paint on the hydrophilic coating film of the heat exchanger 1. Therefore, even if the movement speed of the pendulum is relatively low, excess paint can be easily removed by the action of the centrifugal force of the pendulum.

  In addition, the liquid draining process shares the suspension member 101 that suspends the heat exchanger 1 and the grip portion 7 provided on the heat exchanger 1 that connects the suspension member 101 with the application process. Thereby, a liquid draining process is performed immediately following the coating process. Therefore, the surface treatment of the heat exchanger 1 can be performed quickly, and the trouble of attaching / detaching the heat exchanger 1 to / from the suspension member 101 can be saved.

  Further, in the liquid draining process, the pendulum swings so that the ventilation direction with respect to the fins 4 of the heat exchanger 1 and the swinging direction of the pendulum are always parallel. Thereby, the air flow generated by the swing of the pendulum circulates along the ventilation direction with respect to the fins 4. Therefore, it is possible to easily remove the excess paint on the hydrophilic coating film by the action of the centrifugal force of the pendulum, and it is possible to favorably secure a ventilation path without storing excess paint in the gaps of the fins 4.

  And according to the structure of the said embodiment of this invention, when forming the surface treatment film which promotes the drainage of condensed water on the surface of the heat exchanger 1, ie, a hydrophilic coating film, in the draining process of a hydrophilic coating material It is possible to provide a surface treatment method for the heat exchanger 1 that can reliably remove excess paint and can form a hydrophilic coating film having a uniform thickness.

Second Embodiment
Next, a surface treatment method for a heat exchanger according to a second embodiment of the present invention will be described with reference to FIG. FIG. 7 is a schematic explanatory view showing a liquid draining step of the surface treatment method of the heat exchanger. Since the basic configuration of this embodiment is the same as that of the first embodiment described with reference to FIGS. 1 to 6, the same reference numerals are assigned to the same components as those of the first embodiment. The description of the drawings and the description thereof will be omitted.

  In the surface treatment method of the heat exchanger 1 according to the second embodiment, an air flow is blown to the heat exchanger 1 at an initial position at which the swinging by the pendulum in the liquid draining process starts as shown in FIG. This air flow is blown against the heat exchanger 1 from the nozzle 105 provided in the blowing portion 104 as depicted by a white arrow in FIG. The air flow is blown in a direction parallel to the swinging direction of the pendulum at the initial position, that is, downward.

  According to this configuration, an air flow generated by blowing from the nozzle 105 is added to an air flow that flows along the ventilation direction with respect to the fins 4 that is generated by the swing of the pendulum. Therefore, it is possible to further improve the action of removing excess paint from the hydrophilic coating film and the action of securing the ventilation path for the fins 4.

  Although the embodiments of the present invention have been described above, the scope of the present invention is not limited to these embodiments, and various modifications can be made without departing from the spirit of the invention.

  For example, in the above embodiment, the description has been given by taking as an example the formation of a hydrophilic coating film as a surface treatment film on the surface of the heat exchanger 1, but a water-repellent coating film is formed instead of the hydrophilic coating film. Anyway.

  In the second embodiment, the air flow is blown against the heat exchanger 1 at the initial position of the pendulum. However, the heat is generated at the pendulum stop position on the opposite side of the initial position across the vertical line passing through the support shaft 103. An air flow may be blown against the exchanger 1. Even at the stop position, the air flow is blown in a direction parallel to the swinging direction of the pendulum, that is, substantially downward. Furthermore, you may spray an airflow with respect to the heat exchanger 1 in both the initial position and stop position of a pendulum.

  The present invention can be used in a surface treatment method for a heat exchanger.

DESCRIPTION OF SYMBOLS 1 Heat exchanger 2 Diverging pipe 3 Heat transfer pipe 4 Fin 5 Drainage part 7 Gripping part 101 Hanging member 102 Clamp 103 Support shaft (fulcrum)
105 nozzles

Claims (7)

A heat exchanger surface treatment method for forming a surface treatment film that promotes drainage of condensed water on the surface of the heat exchanger,
A coating step of coating the surface treatment film stock solution on the surface of the heat exchanger;
A liquid draining step of removing the stock solution by a centrifugal force acting on the heat exchanger attached to a tip of a pendulum swinging around a fulcrum, and adjusting an amount of the stock solution attached to the heat exchanger;
A film forming step of forming the stock solution into a film;
A surface treatment method for a heat exchanger, comprising:   The surface treatment method for a heat exchanger according to claim 1, wherein the liquid draining step starts swinging by the pendulum after holding the heat exchanger at an initial position for a predetermined time.   The surface treatment method for a heat exchanger according to claim 1 or 2, wherein the liquid draining step imparts a predetermined initial speed to the pendulum.   The surface treatment method for a heat exchanger according to any one of claims 1 to 3, wherein the liquid draining step sets a predetermined number of reciprocations for swinging the pendulum.   2. The liquid draining step shares a suspension member for suspending the heat exchanger and a grip portion provided on the heat exchanger for connecting the suspension member with the application step. The surface treatment method for a heat exchanger according to any one of claims 4 to 5. The heat exchanger is a heat exchanger in which a pair of opposing shunt tubes are connected by a plurality of heat transfer tubes, and fins are arranged and joined between the adjacent heat transfer tubes,
6. The liquid draining step according to claim 1, wherein the pendulum swings so that a ventilation direction of the heat exchanger with respect to the fin and a swinging direction of the pendulum are always parallel to each other. A surface treatment method for a heat exchanger according to claim 1.   The said liquid draining process blows an airflow with respect to the said heat exchanger in the direction which makes | forms the rocking | fluctuation direction of the pendulum in the initial position and / or stop position of the pendulum. Heat exchanger surface treatment method.

Images