JP2005201466A - Heat exchanger - Google Patents

Heat exchanger Download PDF

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Publication number
JP2005201466A
JP2005201466A JP2004005255A JP2004005255A JP2005201466A JP 2005201466 A JP2005201466 A JP 2005201466A JP 2004005255 A JP2004005255 A JP 2004005255A JP 2004005255 A JP2004005255 A JP 2004005255A JP 2005201466 A JP2005201466 A JP 2005201466A
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Japan
Prior art keywords
fins
heat exchanger
fin
air
amount
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Pending
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JP2004005255A
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Japanese (ja)
Inventor
Masatoshi Takahashi
正敏 高橋
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Panasonic Holdings Corp
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Matsushita Electric Industrial Co Ltd
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Priority to JP2004005255A priority Critical patent/JP2005201466A/en
Publication of JP2005201466A publication Critical patent/JP2005201466A/en
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  • Devices For Blowing Cold Air, Devices For Blowing Warm Air, And Means For Preventing Water Condensation In Air Conditioning Units (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To solve a problem wherein evaporating capacity is reduced because condensed water tends to stay between fins at the bottom part of a heat exchanger to reduce the amount of heat exchange between the fins and air as compared with the other part. <P>SOLUTION: This heat exchanger is provided with upper side fins 12a and lower side fins 12b divided in the flow direction of air, and heat exchanger tubes 13 passing through orthogonally to the respective fins. The fin spacing and fin width of the fins 12b are made larger than those of the fins 12a. The amount of condensed water held in the fin 12b part can thereby be reduced to improve the amount of heat exchange between the fins 12b and air. As a result, evaporating capacity can be improved. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

本発明は空気調和機等にもちいられ、冷媒と空気のような流体間で熱交換を行わせるフィン&チューブ型等の熱交換器に関するものである。   The present invention relates to a fin-and-tube type heat exchanger that is used in an air conditioner or the like and performs heat exchange between a refrigerant and a fluid such as air.

従来、この種の熱交換器は1枚のフィンに伝熱管を貫通させることで、伝熱管内を通過する冷媒の熱エネルギーをフィンを介してフィン近傍の空気に供給している。   Conventionally, this type of heat exchanger supplies heat energy of the refrigerant passing through the heat transfer tube to the air in the vicinity of the fin by passing the heat transfer tube through one fin.

図3は、従来の熱交換器を示すもので、熱交換器11はフィン12と伝熱管13から構成されている。
特開平1−28494号公報
FIG. 3 shows a conventional heat exchanger, and the heat exchanger 11 is composed of fins 12 and heat transfer tubes 13.
JP-A-1-28494

しかしながら、前記従来の構成では熱交換器を蒸発器として使用した場合、空気が熱交換器を通過する際に凝縮された凝縮水が熱交換器底部のフィンとフィンの間に溜まり易くなるために、フィンと空気との熱交換量が他の箇所に比べて少なくなり、蒸発能力が減少するという課題を有していた。   However, in the conventional configuration, when the heat exchanger is used as an evaporator, the condensed water condensed when air passes through the heat exchanger is likely to accumulate between the fins at the bottom of the heat exchanger. The amount of heat exchange between the fins and air is smaller than that in other locations, and there is a problem that the evaporation capacity is reduced.

本発明は、前記従来の課題を解決するもので、熱交換器底部での凝縮水の保有量を低減する熱交換器を提供することを目的とする。   This invention solves the said conventional subject, and it aims at providing the heat exchanger which reduces the holding | maintenance amount of the condensed water in a heat exchanger bottom part.

前記従来の課題を解決するために、本発明の熱交換器は、フィンを空気の流れ方向に分割し、下部側の前記フィンの間隔と前記フィンの幅を上部側の前記フィンより大きくしたものである。これによって、前記熱交換器を蒸発器として使用した場合、前記フィンの間隔が大きくなったため、前記熱交換器底部での凝縮水保有量の低減ができるため蒸発能力向上が可能となる。さらに、前記フィン幅を大きくしたことで、前記フィンの総面積が前記フィンの間隔を大きくする以前と同等にできるため、前記熱交換器を凝縮器として使用した場合の凝縮能力を維持できる。   In order to solve the above-mentioned conventional problems, the heat exchanger according to the present invention is configured such that fins are divided in the air flow direction, and the interval between the fins on the lower side and the width of the fins are larger than those on the upper side. It is. As a result, when the heat exchanger is used as an evaporator, the gap between the fins is increased, so that the amount of condensed water retained at the bottom of the heat exchanger can be reduced, thereby improving the evaporation capacity. Furthermore, by increasing the fin width, the total area of the fins can be made the same as before the gap between the fins is increased, so that the condensing capacity when the heat exchanger is used as a condenser can be maintained.

また、本発明の熱交換器は、空気の流れ方向に分割した前記フィンの間に排水手段を設けたものである。これによって、分割した前記フィンの上部側で凝縮した凝縮水を前記熱交換器底部に流れ込まないために、前記熱交換器底部での凝縮水保有量の大幅な低減による蒸発能力向上ができるだけでなく、下部側の前記フィンの間隔や前記フィンの幅の設計自由度が広がる。   Moreover, the heat exchanger of this invention provides the drainage means between the said fins divided | segmented into the flow direction of air. As a result, the condensed water condensed on the upper side of the divided fins does not flow into the bottom of the heat exchanger, so that not only can the evaporation capacity be improved by significantly reducing the amount of condensed water held at the bottom of the heat exchanger. Further, the degree of freedom in designing the interval between the fins on the lower side and the width of the fins is widened.

本発明の熱交換器は凝縮水が熱交換器底部のフィンとフィンの間に溜まる量を低減できるために蒸発能力向上が可能となる。   The heat exchanger of the present invention can improve the evaporation capacity because the amount of condensed water accumulated between the fins at the bottom of the heat exchanger can be reduced.

第1の発明はフィンを外部流体の流れ方向に分割し、下部側のフィン間隔とフィン幅を上部より大きくしたことにより、熱交換器を蒸発器として使用した場合、フィン間隔が大きくなったため、熱交換器底部での凝縮水保有量が減少するため蒸発能力向上とフィン部の通過面積が増大し、送風機の消費電力の低減ができる。さらに、フィン幅を大きくしたことで、フィンの総面積がフィン間隔を大きくする以前と同等にできるため、熱交換器を
凝縮器として使用した場合の凝縮能力を維持できる。
In the first invention, the fins are divided in the flow direction of the external fluid, and the fin interval on the lower side and the fin width are made larger than the upper part, so that when the heat exchanger is used as an evaporator, the fin interval is increased. Since the amount of condensed water retained at the bottom of the heat exchanger is reduced, the evaporation capacity is improved, the passage area of the fins is increased, and the power consumption of the blower can be reduced. Furthermore, by increasing the fin width, the total area of the fins can be made the same as before increasing the fin interval, so that the condensing capacity when the heat exchanger is used as a condenser can be maintained.

第2の発明は、特に、第1の発明の熱交換器は空気の流れ方向に分割した前記フィンの間に排水手段を設けたことにより、分割した前記フィンの上部側で凝縮した凝縮水を熱交換器底部に流れ込まないために、熱交換器底部での凝縮水保有量の大幅な減少による蒸発能力向上ができるだけでなく、下部側の前記フィンの間隔や前記フィンの幅の設計自由度が広がる。さらに、排水手段の形状を変えることで、風向変更板としての働きも可能となるため、熱交換器での風切り音低減ができる。   In the second invention, in particular, the heat exchanger according to the first invention is provided with drainage means between the fins divided in the air flow direction, so that the condensed water condensed on the upper side of the divided fins can be obtained. Since it does not flow into the bottom of the heat exchanger, not only can the evaporation capacity be improved by significantly reducing the amount of condensed water retained at the bottom of the heat exchanger, but also the freedom in designing the gap between the fins and the width of the fins. spread. Furthermore, by changing the shape of the drainage means, it is possible to function as a wind direction changing plate, so that wind noise in the heat exchanger can be reduced.

以下、本発明の実施の形態について、図面を参照しながら説明する。なお、この実施の形態によって本発明が限定されるものではない。   Hereinafter, embodiments of the present invention will be described with reference to the drawings. Note that the present invention is not limited to the embodiments.

(実施の形態1)
図1は、本発明の第1の実施の形態における熱交換器の斜視図を示すものである。図1において、熱交換器11は空気の流れ方向に流れ方向に分割した上部側のフィン12aと、フィン間隔とフィン幅を上部より大きくした下部側のフィン12bと、フィン12aとフィン12bに直交するように貫通させた伝熱管13から構成されている。
(Embodiment 1)
FIG. 1 is a perspective view of a heat exchanger according to the first embodiment of the present invention. In FIG. 1, the heat exchanger 11 is divided into an upper fin 12a divided in the flow direction in the air flow direction, a lower fin 12b having a fin interval and fin width larger than the upper portion, and orthogonal to the fin 12a and the fin 12b. It is comprised from the heat exchanger tube 13 penetrated so that it might do.

以上のように構成された熱交換器について、以下その動作、作用を説明する。まず、フィン12aとフィン12bに伝熱管を貫通させることで、伝熱管13内を通過する冷媒の熱エネルギーをフィン12aとフィン12b介してフィン12aとフィン12b近傍の空気に供給している。   About the heat exchanger comprised as mentioned above, the operation | movement and an effect | action are demonstrated below. First, by passing the heat transfer tubes through the fins 12a and 12b, the heat energy of the refrigerant passing through the heat transfer tubes 13 is supplied to the air near the fins 12a and 12b via the fins 12a and 12b.

以上のように、本実施の形態においては熱交換器11の底部のフィン12bをフィン12aよりフィン間隔を大きくし、かつ、フィン幅を大きくすることにより、熱交換器11を蒸発器として使用した場合、フィン12b底部での凝縮水保有量が減少し、フィン12bと空気との熱交換量がアップするため蒸発能力向上が可能となる。さらに、フィン12bの総面積がフィン間隔を大きくする以前と同等にできるため、熱交換器を凝縮器として使用した場合の凝縮能力を維持できる。   As described above, in the present embodiment, the heat exchanger 11 is used as an evaporator by making the fin 12b at the bottom of the heat exchanger 11 larger than the fin 12a and by increasing the fin width. In this case, the amount of condensed water retained at the bottom of the fin 12b is reduced, and the amount of heat exchange between the fin 12b and air is increased, so that the evaporation capability can be improved. Furthermore, since the total area of the fins 12b can be made the same as before the fin interval is increased, the condensing capacity when the heat exchanger is used as a condenser can be maintained.

(実施の形態2)
図2は、本発明の第2の実施の形態の熱交換器の斜視図である。図2において、熱交換器11は空気の流れ方向に流れ方向に分割した上部側のフィン12aと、フィン間隔とフィン幅を上部より大きくした下部側のフィン12bと、フィン12aとフィン12bに直交するように貫通させた伝熱管13と、フィン12aとフィン12bの間に設置された排水手段14から構成されている。
(Embodiment 2)
FIG. 2 is a perspective view of the heat exchanger according to the second embodiment of the present invention. In FIG. 2, the heat exchanger 11 is orthogonal to the fins 12a on the upper side divided in the flow direction in the air flow direction, the fins 12b on the lower side with the fin interval and fin width larger than the upper part, and the fins 12a and 12b. The heat transfer tube 13 is made to penetrate therethrough and the drainage means 14 installed between the fins 12a and 12b.

以上のように構成された熱交換器について、以下その動作、作用を説明する。まず、フィン12aとフィン12bに伝熱管を貫通させることで、伝熱管13内を通過する冷媒の熱エネルギーをフィン12aとフィン12b介してフィン12aとフィン12b近傍の空気に供給している。   About the heat exchanger comprised as mentioned above, the operation | movement and an effect | action are demonstrated below. First, by passing the heat transfer tubes through the fins 12a and 12b, the heat energy of the refrigerant passing through the heat transfer tubes 13 is supplied to the air near the fins 12a and 12b via the fins 12a and 12b.

以上のように、本実施の形態においては空気の流れ方向に分割したフィン12aと12bの間に排水手段14を設けたことにより、フィン12aで凝縮した凝縮水は排水手段14に導かれて排水されるため、フィン12aで凝縮した凝縮水がフィン12bに流れ込まないために、熱交換器底部での凝縮水保有量の大幅な減少による蒸発能力向上ができるだけでなく、フィン12bの間隔やフィン12bの幅の設計自由度が広がる。   As described above, in the present embodiment, by providing the drainage means 14 between the fins 12a and 12b divided in the air flow direction, the condensed water condensed by the fins 12a is guided to the drainage means 14 and drained. Therefore, since the condensed water condensed by the fin 12a does not flow into the fin 12b, not only can the evaporation capacity be improved by greatly reducing the amount of condensed water retained at the bottom of the heat exchanger, but also the spacing between the fins 12b and the fins 12b. The degree of freedom of design is widened.

以上のように、本発明にかかる熱交換器は、熱交換器底部での凝縮水の保有量が低減で
きるために蒸発能力の向上が可能となるので、空気調和機等の用途にも適用できる。
As described above, since the heat exchanger according to the present invention can reduce the amount of condensed water held at the bottom of the heat exchanger and thus can improve the evaporation capacity, it can be applied to uses such as an air conditioner. .

本発明の実施の形態1における熱交換器の斜視図The perspective view of the heat exchanger in Embodiment 1 of this invention 本発明の実施の形態2における熱交換器の斜視図The perspective view of the heat exchanger in Embodiment 2 of this invention 従来の熱交換器の斜視図A perspective view of a conventional heat exchanger

符号の説明Explanation of symbols

12、12a、12b フィン
13 伝熱管
14 排水手段
12, 12a, 12b Fin 13 Heat transfer tube 14 Drainage means

Claims (2)

互いに間隔を設けて積層し、外部流体の流れ方向に1列以上並べたフィンと、前記フィンを直交するように貫通させた伝熱管と、前記フィンを外部流体の流れ方向に分割し、下部側の前記フィン間隔と前記フィン幅を上部より大きくしたことを特徴とする熱交換器。 The fins are stacked at intervals and arranged in one or more rows in the flow direction of the external fluid, the heat transfer tubes passing through the fins so as to be orthogonal to each other, and the fins are divided in the flow direction of the external fluid. The heat exchanger according to claim 1, wherein the fin interval and the fin width are made larger than the upper part. 外部流体の流れ方向に分割した前記フィンの間に排水手段を設けたことを特徴とする請求項1記載の熱交換器。 The heat exchanger according to claim 1, wherein drainage means is provided between the fins divided in the flow direction of the external fluid.
JP2004005255A 2004-01-13 2004-01-13 Heat exchanger Pending JP2005201466A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2004005255A JP2005201466A (en) 2004-01-13 2004-01-13 Heat exchanger

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Application Number Priority Date Filing Date Title
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2020202560A1 (en) * 2019-04-05 2020-10-08 三菱電機株式会社 Air conditioning device

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2020202560A1 (en) * 2019-04-05 2020-10-08 三菱電機株式会社 Air conditioning device
JPWO2020202560A1 (en) * 2019-04-05 2021-10-21 三菱電機株式会社 Air conditioner
JP7130116B2 (en) 2019-04-05 2022-09-02 三菱電機株式会社 air conditioner

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