JPH0735496A - Heat exchanger - Google Patents
Heat exchangerInfo
- Publication number
- JPH0735496A JPH0735496A JP18011093A JP18011093A JPH0735496A JP H0735496 A JPH0735496 A JP H0735496A JP 18011093 A JP18011093 A JP 18011093A JP 18011093 A JP18011093 A JP 18011093A JP H0735496 A JPH0735496 A JP H0735496A
- Authority
- JP
- Japan
- Prior art keywords
- room
- evaporator
- blower
- height
- partition
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn
Links
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は空気調和機に適用される
熱交換装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heat exchange device applied to an air conditioner.
【0002】[0002]
【従来の技術】従来の熱交換器システムの側断面図を図
3に示す。2. Description of the Related Art A side sectional view of a conventional heat exchanger system is shown in FIG.
【0003】図において、1は蒸発器,2は送風機で各
々空気通路3の内部に組み込まれている。なお、4は蒸
発器1を収納する部屋,6は送風機2を配設する部屋,
12は部屋4,6間にあって、蒸発器1からの凝縮水
(露滴)が送風機2に到達しないよう落下空間として設
けた部屋である。In the figure, reference numeral 1 is an evaporator, and 2 is a blower, which are incorporated in an air passage 3. In addition, 4 is a room for storing the evaporator 1, 6 is a room for installing the blower 2,
Reference numeral 12 denotes a room that is provided between the rooms 4 and 6 and is provided as a falling space so that condensed water (dew drops) from the evaporator 1 does not reach the blower 2.
【0004】[0004]
【発明が解決しようとする課題】上記従来の熱交換器シ
ステムには解決すべき次の不具合があった。The above conventional heat exchanger system has the following problems to be solved.
【0005】即ち、蒸発器1から送風機2へ飛散流入す
る凝縮水の絶無を期すため、部屋12の横(図の左右)
方向の長さを十分に長くし勝ちであったため、熱交換器
システムが大きくなり、設置スペースが大きく,コスト
アップ,重量アップの要因となっていた。That is, in order to ensure the absence of condensed water that flows from the evaporator 1 to the blower 2, the side of the room 12 (right and left in the figure)
Since it was easy to make the length of the direction sufficiently long, the heat exchanger system became large, the installation space was large, and the cost and weight were increased.
【0006】本発明は上記不具合解決のため、蒸発器の
大きさ,送風機を収納する部屋への距離,通風開口面積
に関係する部屋間の仕切り高さ等の間に定性的な関係を
見出し、それに基づいて蒸発器と送風機との距離を必要
最小限にした熱交換装置を提供することを目的とする。In order to solve the above problems, the present invention finds a qualitative relationship among the size of the evaporator, the distance to the room accommodating the blower, and the partition height between the rooms related to the ventilation opening area. Based on this, it is an object to provide a heat exchange device in which the distance between the evaporator and the blower is minimized.
【0007】[0007]
【課題を解決するための手段】本発明は上記課題の解決
手段として、空気流通路中に蒸発器,送風機を順次配設
してなる熱交換装置において、前記蒸発器の高さを
H01,厚さをH02,蒸発器を配設する部屋の入口及び出
口に設けた仕切りの高さをH3 とすると共に、前記送風
機を配設する部屋と蒸発器との間の距離をH1 ,送風機
を配設する部屋の入口の仕切りの高さをH2 としたと
き、以下の条件を満足する熱交換装置。Means for Solving the Problems As a means for solving the above problems, the present invention relates to a heat exchange device in which an evaporator and a blower are sequentially arranged in an air flow passage, and the height of the evaporator is H 01 , The thickness is H 02 , the height of the partition provided at the entrance and the exit of the room where the evaporator is installed is H 3, and the distance between the room where the blower is installed and the evaporator is H 1 , A heat exchange device that satisfies the following conditions when the height of the partition at the entrance of the room in which the blower is installed is H 2 .
【0008】0.05H01≦H3 ≦0.1H01 H2 >H3 H1 ≦0.5H02 を提供しようとするものである。[0008] is intended to provide a 0.05H 01 ≦ H 3 ≦ 0.1H 01 H 2> H 3 H 1 ≦ 0.5H 02.
【0009】[0009]
【作用】本発明は上記のように構成されるので次の作用
を有する。Since the present invention is constructed as described above, it has the following actions.
【0010】即ち、送風機の部屋に蒸発器から到達する
凝縮水の飛散量は蒸発器の高さと流路方向の厚さ,蒸発
器の部屋の出口側仕切りの高さ,蒸発器から送風機の部
屋までの距離,送風機の部屋の入口側仕切りの高さ等に
関係するが、諸テストの結果,蒸発器から送風機の部屋
までの距離と蒸発器の部屋の出口側仕切りの高さに対す
る送風機の部屋の入口側仕切りの高さの割合が強く関わ
り、一定容量の蒸発器,一定風速,風量の送風機につい
ては、蒸発器下流端から送風機の部屋入口側仕切り迄の
距離をH1 ,送風機収納箱(部屋と同義)への流入凝縮
水量(飛散流入する露滴水量)をQ,上記距離H1 を蒸
発器の流路方向の厚さH02の関数とするとき,図2のよ
うな関係のあることが分った。なお、H2 は送風機の部
屋の入口側仕切りの高さ,H3 は蒸発器の部屋の出口側
仕切りの高さである。That is, the amount of condensed water that reaches the room of the blower from the evaporator depends on the height of the evaporator and the thickness in the direction of the flow path, the height of the partition on the outlet side of the evaporator room, the room from the evaporator to the room of the blower. It depends on the distance to the room, the height of the partition on the inlet side of the fan room, etc., but as a result of various tests, the room of the fan for the distance from the evaporator to the room of the fan and the height of the partition on the outlet side of the evaporator room The ratio of the height of the partition on the inlet side is strongly related. For a constant capacity evaporator, a constant wind speed, and a blower with a fixed air volume, the distance from the downstream end of the evaporator to the partition on the inlet side of the blower room is H 1 , the blower storage box ( When the amount of condensed water flowing in (synonymous with the room) (the amount of dewdrop water that flows in and out) is Q and the distance H 1 is a function of the thickness H 02 in the flow path direction of the evaporator, there is a relationship as shown in FIG. I found out. H 2 is the height of the partition on the inlet side of the blower room, and H 3 is the height of the partition on the outlet side of the evaporator room.
【0011】即ち、H1 が小さくなればQは増し,H2
が大きくなればQは減る。That is, when H 1 becomes smaller, Q increases and H 2
Becomes larger, Q decreases.
【0012】他方、H3 は上記の通り、蒸発器の部屋の
出口側仕切りの高さであるが、これを余りの高くするこ
とは空気流路の断面積を狭めて効率を低下させ、低くし
すぎると蒸発器の下方へ集中し勝ちとなる凝縮水を溢流
させ、下流側への飛散の原因の一つとなりやすいのでH
3 は自と高低に限界を有することとなり、その範囲は概
ね蒸発器の高さH01の5〜10%が望ましいことが分っ
た。H2 は送風機に有効に、かつ、大きな流路抵抗とな
らない程度に空気流を絞って送り込む点からも、また、
H3 の頂部近傍を通過した液滴(凝縮水)が、確実にH
2 の高さに阻まれてその上流側に落下することを期する
点からもH3 より高いことが望ましい。そこでH2 の下
限をH3 の高さに置けば、即ち、H2 =H3 と置けばH
1 の上限は図2より0.5H02となる。On the other hand, H 3 is the height of the partition on the outlet side of the chamber of the evaporator as described above, but making it too high narrows the cross-sectional area of the air flow passage, lowering the efficiency and lowering it. If too much, it concentrates below the evaporator and overflows the condensate that tends to overflow, which tends to be one of the causes of scattering to the downstream side.
It was found that 3 has its own height limit and its range is preferably about 5 to 10% of the height H 01 of the evaporator. H 2 is also effective in the blower, and from the point of narrowing the air flow to the extent that it does not cause a large flow path resistance,
Make sure that the droplets (condensed water) that have passed near the top of H 3 are H
It is preferably higher than H 3 from the standpoint of being blocked by the height of 2 and falling to the upstream side. Therefore, if the lower limit of H 2 is set to the height of H 3 , that is, H 2 = H 3 , then H
The upper limit of 1 is 0.5H 02 from FIG.
【0013】従って、上記構成によれば、熱交換装置の
大きさに最も寄与するH1 の上限をQが零という条件を
与えて知ることができる。Therefore, according to the above configuration, the upper limit of H 1 that most contributes to the size of the heat exchange device can be known by giving the condition that Q is zero.
【0014】なお、H1 の下限は、上記の通りQがH2
にも大きく依存するところから、H 2 の決定と整合させ
て決める。因みに図2によれば、H2 =H3 のとき、H
1 は格別の下限幅を有せず、従ってH1 ≒0.5H02と
ほぼ一義的に決まるが、たとえばH2 =2H3 の場合は
下限は0.3H02が適値となる。従ってH1 は0.3H
02〜0.5H02内で選べばよい。この場合、0.3H02
でも図2よりQは零近傍となるが、かつ、その方が熱交
換装置の大きさのみの観点からは望ましい訳であるが、
Qを零ならしめるための全きを期する上から、〜0.5
H02は安全幅となる。即ち、熱交換装置の大きさの制限
に重きを置く場合は0.3H02に近い側を採用し、送風
機の防湿に重きを置く場合は0.5H02に近い側を採用
するといった選択の仕方をする。H1The lower limit of Q is H2
H depends on 2Aligned with the decision of
Decide. Incidentally, according to FIG. 2, H2= H3When H
1Has no particular lower bound, so H1≒ 0.5H02When
Almost uniquely determined, but for example H2= 2H3In the case of
The lower limit is 0.3H02Is an appropriate value. Therefore H1Is 0.3H
02~ 0.5H02You can choose from within. In this case, 0.3H02
However, as shown in Fig. 2, Q is near zero, and that is more heat exchange.
Although it is desirable only from the viewpoint of the size of the replacement device,
From the top of the line to make Q zero, ~ 0.5
H02Is a safety margin. That is, the size of the heat exchange device is limited.
0.3H when placing a weight on02The side closer to the
0.5H when placing emphasis on moisture protection of the machine02Adopt the side closer to
Make a choice such as doing.
【0015】[0015]
【実施例】本発明の一実施例を図1,図2により説明す
る。なお、従来例と同様の構成部材には同符号を付し、
必要ある場合を除き、説明を省略する。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described with reference to FIGS. The same components as those in the conventional example are designated by the same reference numerals,
The description is omitted unless necessary.
【0016】図1は本実施例に係る熱交換装置の側断面
図、図2は送風機収納箱(部屋と同義)への流入凝縮水
量と熱交換装置の主要仕切り部寸法との関係図である。FIG. 1 is a side sectional view of a heat exchange device according to the present embodiment, and FIG. 2 is a relational diagram between the amount of condensed water flowing into a fan storage box (synonymous with a room) and the size of a main partition of the heat exchange device. .
【0017】図1において、5は部屋4の入口側の仕切
り、7は送風機2を収納した部屋6の入口(上流)側の
仕切り、8は蒸発器1で発生した凝縮水(露滴)、9は
空気流を模式的に示した矢印(空気流)、10は部屋4
の底部に穿設された下部排水孔、11は部屋4の出口側
の仕切り、13は部屋12の底部に穿設されたドレン排
出口である。In FIG. 1, 5 is a partition on the inlet side of the room 4, 7 is a partition on the inlet (upstream) side of the room 6 in which the blower 2 is housed, 8 is condensed water (dew drop) generated in the evaporator 1, 9 is an arrow schematically showing the air flow (air flow), 10 is the room 4
Is a lower drainage hole formed in the bottom of the room 4, 11 is a partition on the outlet side of the room 4, and 13 is a drain discharge hole formed in the bottom of the room 12.
【0018】なお、記号は作用の項で説明した通り、H
1 は蒸発器1の下流端から送風機2の部屋6の入口側仕
切り7迄の距離、即ち、部屋12の空気流路方向の幅、
H2は仕切り7の高さ、H3 は仕切り11の高さ、H01
は蒸発器1の高さ(部屋4の高さに相当)、H02は蒸発
器1の空気流路方向の厚さである。The symbols are H as described in the section of action.
1 is the distance from the downstream end of the evaporator 1 to the partition 7 on the inlet side of the room 6 of the blower 2, that is, the width of the room 12 in the air flow direction,
H 2 is the height of the partition 7, H 3 is the height of the partition 11, H 01
Is the height of the evaporator 1 (corresponding to the height of the room 4), and H 02 is the thickness of the evaporator 1 in the air flow path direction.
【0019】次に上記構成の作用について説明する。Next, the operation of the above configuration will be described.
【0020】図1において、H3 はH01の5〜10%の
範囲に形成され、H2 はH3 より稍大きく(高く)形成
されている。H1 は符号その他の記載の都合上、実際の
割合より大きく示されているが、H02の1/2以下程度
に形成されている。従って、図2に従えば、H1 に対す
るQの曲線は図のH2 =H3 の場合とH2 =2H3 の場
合との中間近傍に存することとなり、Qを零とした場合
でもH1 は0.5H02以下となり、きわめてコンパクト
な熱交換装置が得られる。In FIG. 1, H 3 is formed in the range of 5 to 10% of H 01 , and H 2 is formed to be slightly larger (higher) than H 3 . H 1 is shown to be larger than the actual ratio for the sake of convenience of reference numerals and the like, but it is formed to be about 1/2 or less of H 02 . Therefore, according to FIG. 2, the curve of Q with respect to H 1 exists near the middle of the case of H 2 = H 3 and the case of H 2 = 2H 3 in the figure, and even if Q is set to 0, H 1 Is 0.5H 02 or less, and an extremely compact heat exchange device can be obtained.
【0021】なお、凝縮水8等の挙動は次の通りであ
る。The behavior of the condensed water 8 and the like is as follows.
【0022】空気流9が蒸発器1を通過する際、凝縮水
8が下部排水孔10より系外に出てゆく。また空気流9
により蒸発器1の下部より凝縮水8の一部が運び出され
ても、蒸発器1の出口側と送風機2を収納している部屋
6との間の部屋12に落下し、この部屋12のドレン排
出口13より系外へ排出され、空気流9は凝縮水8を持
たずに送風機2の部屋6に流入してゆく。When the air stream 9 passes through the evaporator 1, the condensed water 8 flows out of the system through the lower drain hole 10. Also air flow 9
Even if a part of the condensed water 8 is carried out from the lower part of the evaporator 1 by the above, it falls into the room 12 between the outlet side of the evaporator 1 and the room 6 housing the blower 2, and the drain of this room 12 is drained. The air flow 9 is discharged from the discharge port 13 to the outside of the system, and flows into the room 6 of the blower 2 without having the condensed water 8.
【0023】以上の他送風機2を納める部屋6が、図示
しない加熱器を収納する場合も、単なる空気流9の出口
であっても任意の場合に広く実施可能である。Even if the room 6 for accommodating the other blower 2 accommodates a heater (not shown) or is simply the outlet of the air flow 9, it can be widely implemented in any case.
【0024】以上の通り、本実施例によれば凝縮水8を
部屋12等で落下排出し、送風機2の部屋6に流入させ
ることなく、しかも部屋12の幅H1 を最小にして最も
小型,軽量の熱交換装置が得られるという利点がある。As described above, according to the present embodiment, the condensed water 8 is not dropped into the room 12 or the like, and is not discharged into the room 6 of the blower 2, and the width H 1 of the room 12 is minimized. There is an advantage that a lightweight heat exchange device can be obtained.
【0025】また、この結果、製造コストも低減すると
いう利点がある。As a result, there is an advantage that the manufacturing cost can be reduced.
【0026】[0026]
【発明の効果】本発明は上記のように構成されるので次
の効果を有する。Since the present invention is constructed as described above, it has the following effects.
【0027】即ち、本発明によれば蒸発器を配設する部
屋と送風機を配設する部屋との距離を各部屋の仕切りの
高さ、蒸発器の高さ、厚さと関連づけて、送風機の部屋
に凝縮水の流入しない範囲の最小値に決めることができ
るので、コンパクトでかつ、凝縮水の露が再飛散しな
い、高性能,コンパクト,低コストの熱交換装置が得ら
れる。That is, according to the present invention, the distance between the room in which the evaporator is installed and the room in which the fan is installed is related to the height of the partition of each room, the height and thickness of the evaporator, and the room of the fan. Since it is possible to determine the minimum value of the range in which the condensed water does not flow in, it is possible to obtain a compact, high-performance, compact, low-cost heat exchange device in which the condensed water dew does not re-spray.
【図1】本発明の一実施例に係る熱交換装置の側断面
図,FIG. 1 is a side sectional view of a heat exchange device according to an embodiment of the present invention,
【図2】上記実施例に係る送風機収納箱への流入凝縮水
量と熱交換装置の主要仕切り部寸法との関係図,FIG. 2 is a diagram showing the relationship between the amount of condensed water flowing into the fan storage box and the size of the main partition of the heat exchange device according to the above embodiment,
【図3】従来の熱交換器システムの側断面図である。FIG. 3 is a side sectional view of a conventional heat exchanger system.
1 蒸発器 2 送風機 3 空気通路 4 部屋 5 仕切り 6 部屋 7 仕切り 8 凝縮水 9 空気流 10 下部排水孔 11 仕切り 12 部屋 13 ドレン排出孔 1 Evaporator 2 Blower 3 Air passage 4 Room 5 Partition 6 Room 7 Partition 8 Condensed water 9 Airflow 10 Lower drain hole 11 Partition 12 room 13 Drain discharge hole
───────────────────────────────────────────────────── フロントページの続き (72)発明者 三井 正俊 名古屋市中村区岩塚町字高道1番地 三菱 重工業株式会社名古屋研究所内 (72)発明者 沢田 正夫 愛知県西春日井郡西枇杷島町字旭町3丁目 1番地 三菱重工業株式会社エアコン製作 所内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Masatoshi Mitsui Masatoshi Mitsui, No. 1 Takamichi, Iwazuka-cho, Nakamura-ku, Nagoya City Mitsubishi Heavy Industries, Ltd. Nagoya Research Institute (72) Masao Sawada 3 Asahi-cho, Nishibiwajima-cho, Nishikasugai-gun, Aichi Prefecture 1-chome, Mitsubishi Heavy Industries, Ltd. Air Conditioning Factory
Claims (1)
設してなる熱交換装置において、前記蒸発器の高さをH
01,厚さをH02,蒸発器を配設する部屋の入口及び出口
に設けた仕切りの高さをH3 とすると共に、前記送風機
を配設する部屋と蒸発器との間の距離をH1 ,送風機を
配設する部屋の入口の仕切りの高さをH2 としたとき、
以下の条件を満足する熱交換装置。 0.05H01≦H3 ≦0.1H01 H2 >H3 H1 ≦0.5H02 1. In a heat exchange device in which an evaporator and a blower are sequentially arranged in an air flow passage, the height of the evaporator is H.
01 , the thickness is H 02 , the height of the partition provided at the entrance and the exit of the room where the evaporator is installed is H 3, and the distance between the room where the blower is installed and the evaporator is H 1, when the partition of the height of the entrance of the room to dispose the blower was H 2,
A heat exchange device that satisfies the following conditions. 0.05H 01 ≤H 3 ≤0.1H 01 H 2 > H 3 H 1 ≤0.5H 02
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP18011093A JPH0735496A (en) | 1993-07-21 | 1993-07-21 | Heat exchanger |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP18011093A JPH0735496A (en) | 1993-07-21 | 1993-07-21 | Heat exchanger |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0735496A true JPH0735496A (en) | 1995-02-07 |
Family
ID=16077601
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP18011093A Withdrawn JPH0735496A (en) | 1993-07-21 | 1993-07-21 | Heat exchanger |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0735496A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6796368B1 (en) * | 1997-08-11 | 2004-09-28 | Denso Corporation | Air conditioning apparatus for vehicle |
-
1993
- 1993-07-21 JP JP18011093A patent/JPH0735496A/en not_active Withdrawn
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6796368B1 (en) * | 1997-08-11 | 2004-09-28 | Denso Corporation | Air conditioning apparatus for vehicle |
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