JP2000320927A - Refrigerant coil - Google Patents

Refrigerant coil

Info

Publication number
JP2000320927A
JP2000320927A JP11130810A JP13081099A JP2000320927A JP 2000320927 A JP2000320927 A JP 2000320927A JP 11130810 A JP11130810 A JP 11130810A JP 13081099 A JP13081099 A JP 13081099A JP 2000320927 A JP2000320927 A JP 2000320927A
Authority
JP
Japan
Prior art keywords
refrigerant
tube
heat transfer
air
flow
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.)
Pending
Application number
JP11130810A
Other languages
Japanese (ja)
Inventor
Tamon Kiyotaki
多門 清滝
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kimura Kohki Co Ltd
Original Assignee
Kimura Kohki Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Kimura Kohki Co Ltd filed Critical Kimura Kohki Co Ltd
Priority to JP11130810A priority Critical patent/JP2000320927A/en
Publication of JP2000320927A publication Critical patent/JP2000320927A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00Tubular elements; Assemblies of tubular elements
    • F28F1/10Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F28F1/12Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element
    • F28F1/24Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending transversely
    • F28F1/32Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending transversely the means having portions engaging further tubular elements
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D1/00Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
    • F28D1/02Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
    • F28D1/04Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits
    • F28D1/047Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being bent, e.g. in a serpentine or zig-zag
    • F28D1/0477Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being bent, e.g. in a serpentine or zig-zag the conduits being bent in a serpentine or zig-zag

Abstract

PROBLEM TO BE SOLVED: To facilitate a complete evaporation and a complete condensation of a refrigerant by constituting a refrigerant circuit to allow a gas-like refrigerant to flow in a heat transfer tube from windward when the air is heated and to allow a liquid-like refrigerant to flow in a heat transfer tube from leeward when the air is cooled and constituting the tube to be spirally formed. SOLUTION: The refrigerant coil is constituted to insert a straight portion of a heat transfer tube 2 to a fin group 1, which is constituted so that the many plate fins 4 are aligned in parallel at a predetermined pitch. A plurality of stags of the tubes 2 are provided so that the group 1 fall from a windward side to a leeward side toward a ventilating direction A while passing through its normal direction (a direction perpendicular to a plane of the fins 4), and a refrigerant circuit B is constituted so that a gas-like refrigerant flows in the tube 2 from the windward side when the air is heated and a liquid-like refrigerant flow in the tube 2 from the leeward side when the air is cooled. The tube 2 is partly or entirely spirally formed, and a straight portion of the tube 2 is formed in an elliptical tube so that its radial cut section becomes an elliptical shape.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、冷媒コイルに関するも
のである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a refrigerant coil.

【0002】[0002]

【従来の技術】図4に示すように、従来の冷媒コイル
は、フィン群に挿着される伝熱管の直管部が円形管で、
通風方向に対して直交流となるように伝熱管を複数列設
けていた。
2. Description of the Related Art As shown in FIG. 4, in a conventional refrigerant coil, a straight tube portion of a heat transfer tube inserted into a fin group is a circular tube.
A plurality of rows of heat transfer tubes were provided so as to have a cross flow in the ventilation direction.

【0003】[0003]

【発明が解決しようとする課題】しかし、このような構
造の冷媒コイルでは伝熱が悪く冷媒の完全蒸発・完全凝
縮が困難で、冷媒を送るポンプの負荷が大きくなる問題
があった。そこで、本発明は前記課題を解決する冷媒コ
イルを提供する事を目的とする。
However, in the refrigerant coil having such a structure, there is a problem that heat transfer is poor and it is difficult to completely evaporate and condense the refrigerant, so that a load of a pump for sending the refrigerant increases. Then, this invention aims at providing the refrigerant coil which solves the said subject.

【0004】[0004]

【課題を解決するための手段】前記課題を解決するため
に本発明は、フィン群に挿着される伝熱管を、通風方向
に向かいかつ風上側から風下側へ下降するように複数段
設け、空気加熱時にガス状冷媒が風上側から伝熱管に流
入しかつ空気冷却時に液状冷媒が風下側から伝熱管に流
入するように冷媒回路を構成したものである。さらに、
伝熱管を楕円管に形成する。
In order to solve the above-mentioned problems, the present invention provides a plurality of heat transfer tubes inserted in a fin group so as to face in the ventilation direction and descend from the windward side to the leeward side, The refrigerant circuit is configured such that the gaseous refrigerant flows into the heat transfer tube from the windward side during air heating, and the liquid refrigerant flows into the heat transfer tube from the leeward side during air cooling. further,
The heat transfer tube is formed into an elliptical tube.

【0005】[0005]

【実施例】図1と図2は、本発明の冷媒コイルを例示
し、この冷媒コイルは、フィン群1と伝熱管2を備え、
フィン群1に伝熱管2の直管部3、3…を挿着して構成
される。フィン群1は、多数のプレートフィン4,4…
を所定ピッチで平行に並設して成る。符号Aで示す矢印
は図示省略の送風機による通風方向を示している。
1 and 2 illustrate a refrigerant coil according to the present invention. The refrigerant coil includes a fin group 1 and a heat transfer tube 2, and FIG.
The straight tube portions 3, 3,... Of the heat transfer tubes 2 are inserted and attached to the fin group 1. The fin group 1 includes a large number of plate fins 4, 4,.
Are arranged in parallel at a predetermined pitch. The arrow indicated by the symbol A indicates the direction of ventilation by a fan (not shown).

【0006】伝熱管2は、フィン群1をその法線方向
(プレートフィン4の平面に直交する方向)に貫きつつ
通風方向Aに向かいかつ風上側から風下側へ下降するよ
うに複数段設け、空気加熱時にガス状冷媒が風上側から
伝熱管2に流入しかつ空気冷却時に液状冷媒が風下側か
ら伝熱管2に流入するように冷媒回路Bを構成する。
The heat transfer tubes 2 are provided in a plurality of stages so as to penetrate the fin group 1 in the normal direction thereof (the direction perpendicular to the plane of the plate fins 4) and to descend in the ventilation direction A from the windward side to the leeward side. The refrigerant circuit B is configured so that the gaseous refrigerant flows into the heat transfer tube 2 from the windward side during air heating, and the liquid refrigerant flows into the heat transfer tube 2 from the leeward side during air cooling.

【0007】複数段の伝熱管2、2…の風上側端部(図
1の黒丸で示す)はヘッダ5に連通連結し、風下側端部
(図1の白丸で示す)は分流器6に連通連結する。冷媒
回路Bは、冷媒が流通する管路7と、管路7内の冷媒を
循環方向切変え自在に流通させるポンプPと、冷凍機な
どの熱交換機能などを有し液状冷媒からガス状冷媒・ガ
ス状冷媒から液状冷媒に任意に変換自在な熱交換部C
と、を備えている。図のごとく一部乃至全体が螺旋を描
くように伝熱管2を形成すれば、伝熱管有効長を長くと
ることができ、少ない冷媒流量で空気との交換熱量を多
くとれてポンプPの動力(負荷)が少なくてすむ。
The leeward ends (indicated by black circles in FIG. 1) of the plurality of stages of heat transfer tubes 2, 2,... Are connected to the header 5 and the leeward ends (indicated by white circles in FIG. Connect and connect. The refrigerant circuit B has a pipe 7 through which the refrigerant flows, a pump P through which the refrigerant in the pipe 7 can be freely circulated, and a heat exchange function such as a refrigerator.・ Heat exchange section C that can freely convert gaseous refrigerant to liquid refrigerant
And If the heat transfer tube 2 is formed so that a part or the whole draws a spiral as shown in the drawing, the effective length of the heat transfer tube can be increased, and the amount of heat exchanged with air can be increased with a small refrigerant flow rate, and the power of the pump P ( Load).

【0008】冷媒コイルの暖房運転時(コイル通風空気
加熱時)には、高温のガス状冷媒がヘッダ5から伝熱管
2、2…に分流入して内部を通り、伝熱管2、2…及び
フィン群1を介して、低温のコイル通風空気が冷媒と熱
交換されて、空気は暖風となり、かつガス状冷媒は凝縮
して液化され分流器6から流出する。このとき上から下
に冷媒が流れながら液化して比重が大きく(重く)なる
ので流下速度が増し、冷媒を送るポンプPの動力(負
荷)が少なくてすむ。
During the heating operation of the refrigerant coil (at the time of coil ventilation air heating), a high-temperature gaseous refrigerant flows from the header 5 into the heat transfer tubes 2, 2,. Through the fin group 1, the low-temperature coil ventilation air exchanges heat with the refrigerant, the air becomes warm air, and the gaseous refrigerant is condensed and liquefied and flows out of the flow divider 6. At this time, the refrigerant is liquefied while flowing from top to bottom, and the specific gravity is increased (heavy), so that the flow speed is increased, and the power (load) of the pump P for sending the refrigerant can be reduced.

【0009】冷媒コイルの冷房運転時(コイル通風空気
冷却時)には、低温の液状冷媒が分流器6から伝熱管
2、2…に分流入して内部を通り、伝熱管2、2…及び
フィン群1を介して、高温のコイル通風空気が冷媒と熱
交換されて、空気は冷風となり、かつ液状冷媒は蒸発し
て気化されヘッダ5から流出する。このとき下から上に
冷媒が流れながら気化して比重が小さく(軽く)なるの
で昇流速度が増し、冷媒を送るポンプPの動力(負荷)
が少なくてすむ。しかも、通風方向Aと冷媒の流れがカ
ウンターフロー(向流)となるので、無駄のない最も効
率の良い熱交換を行えて伝熱量・交換熱量が増大する。
これらの作用を効果的に発揮させるには伝熱管2を3段
・3列以上にするのがよいが、冷媒コイルの大きさや熱
交換能力に応じて、伝熱管2の段数を増減させるも自由
である。
During the cooling operation of the refrigerant coil (at the time of coil ventilation air cooling), a low-temperature liquid refrigerant flows from the flow divider 6 into the heat transfer tubes 2, 2,. Through the fin group 1, the high-temperature coil ventilation air exchanges heat with the refrigerant, the air becomes cold air, and the liquid refrigerant evaporates and vaporizes and flows out of the header 5. At this time, the refrigerant evaporates while flowing from bottom to top and the specific gravity becomes small (light), so that the ascending speed increases, and the power (load) of the pump P that sends the refrigerant
Need less. In addition, since the flow direction of the refrigerant and the flow direction of the refrigerant are counterflow (countercurrent), the most efficient heat exchange without waste can be performed, and the amount of heat transfer and exchange heat increases.
In order to effectively exert these effects, the heat transfer tubes 2 are preferably provided in three stages and three rows or more. However, the number of stages of the heat transfer tubes 2 may be increased or decreased according to the size of the refrigerant coil and the heat exchange capacity. It is.

【0010】図3に示すように、伝熱管2の直管部3
は、径方向切断面が楕円形の楕円管に形成し、直管部3
の中心軸方向(直管部3の長手方向)から見てこの直管
部3の楕円長軸を通風方向Aと略平行にする。なお本発
明において、楕円長軸とは楕円の長径の両端点(頂点)
を通る直線をいう。このように、直管部3の断面は形状
抗力の小さい楕円形にしてあるので、円形伝熱管の場合
よりも、通風抵抗が小さくて圧力損失が減少し、死水域
が狭小となって直管部3における空気流との接触面積
(伝熱面積)が増加し、一層熱交換効率が向上して、少
流量冷媒コイルに最適なものとなる。
As shown in FIG. 3, the straight tube portion 3 of the heat transfer tube 2
Is formed into an elliptical tube having a radially cut surface having an elliptical shape,
When viewed from the central axis direction (longitudinal direction of the straight pipe portion 3), the elliptical long axis of the straight pipe portion 3 is made substantially parallel to the ventilation direction A. In the present invention, the major axis of the ellipse is the both ends (vertex) of the major axis of the ellipse.
Means a straight line passing through. As described above, since the cross section of the straight pipe portion 3 is an elliptical shape having a small shape drag, the ventilation resistance is smaller and the pressure loss is reduced, and the dead water area becomes narrower than in the case of a circular heat transfer tube. The contact area (heat transfer area) with the air flow in the part 3 is increased, and the heat exchange efficiency is further improved, which is optimal for a low flow rate refrigerant coil.

【0011】なお、伝熱管2は円形管とするも自由であ
る。また、冷媒回路Bにおいて、ポンプPを省略して、
冷媒を循環方向切変え自在として自然循環させてもよ
い。
Note that the heat transfer tube 2 may be a circular tube or any shape. In the refrigerant circuit B, the pump P is omitted,
The refrigerant may be naturally circulated by freely changing the circulation direction.

【0012】[0012]

【発明の効果】請求項1の発明では、伝熱が良く、冷媒
の完全蒸発・完全凝縮が可能で冷媒流量が少なくて済
み、伝熱量・交換熱量が大きく、特に冷房時の熱交換効
率が向上し、冷媒コイルと冷媒を送るポンプの小型化を
図れる。請求項2では、一層熱交換効率が良好となる。
According to the first aspect of the present invention, the heat transfer is good, the refrigerant can be completely evaporated and completely condensed, the flow rate of the refrigerant is small, the amount of heat transfer and exchange heat is large, and the heat exchange efficiency in cooling is particularly high. The size of the pump for sending the refrigerant coil and the refrigerant can be reduced. According to the second aspect, the heat exchange efficiency is further improved.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明の冷媒コイルの一実施例を示す簡略側面
図である。
FIG. 1 is a simplified side view showing one embodiment of a refrigerant coil of the present invention.

【図2】簡略斜視図である。FIG. 2 is a simplified perspective view.

【図3】要部側面断面図である。FIG. 3 is a side sectional view of a main part.

【図4】従来例を示す斜視図である。FIG. 4 is a perspective view showing a conventional example.

【符号の説明】[Explanation of symbols]

1 フィン群 2 伝熱管 A 通風方向 B 冷媒回路 DESCRIPTION OF SYMBOLS 1 Fin group 2 Heat transfer tube A Ventilation direction B Refrigerant circuit

─────────────────────────────────────────────────────
────────────────────────────────────────────────── ───

【手続補正書】[Procedure amendment]

【提出日】平成12年1月26日(2000.1.2
6)
[Submission Date] January 26, 2000 (2000.1.2
6)

【手続補正1】[Procedure amendment 1]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】請求項1[Correction target item name] Claim 1

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【手続補正2】[Procedure amendment 2]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0012[Correction target item name] 0012

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【0012】[0012]

【発明の効果】請求項1の発明では、伝熱が良く、冷媒
の完全蒸発・完全凝縮が可能で冷媒流量が少なくて済
み、伝熱量・交換熱量が大きく、特に冷房時の熱交換効
率が向上し、冷媒コイルと冷媒を送るポンプの小型化を
図れる。しかも、伝熱管有効長を長くとることができ、
少ない冷媒流量で空気との交換熱量を多くとれてポンプ
の動力(負荷)が少なくてすむ。請求項2では、一層熱
交換効率が良好となる。
According to the first aspect of the present invention, the heat transfer is good, the refrigerant can be completely evaporated and completely condensed, the flow rate of the refrigerant is small, the amount of heat transfer and exchange heat is large, and the heat exchange efficiency in cooling is particularly high. The size of the pump for sending the refrigerant coil and the refrigerant can be reduced. Moreover, the effective length of the heat transfer tube can be increased,
Pump that can exchange a large amount of heat with air with a small refrigerant flow rate
Power (load) is small. According to the second aspect, the heat exchange efficiency is further improved.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 フィン群1に挿着される伝熱管2を、通
風方向Aに向かいかつ風上側から風下側へ下降するよう
に複数段設け、空気加熱時にガス状冷媒が風上側から上
記伝熱管2に流入しかつ空気冷却時に液状冷媒が風下側
から上記伝熱管2に流入するように冷媒回路Bを構成し
たことを特徴とする冷媒コイル。
A plurality of heat transfer tubes inserted into a fin group are provided so as to face a ventilation direction and descend from a windward side to a leeward side. A refrigerant coil having a refrigerant circuit B configured to flow into the heat pipe 2 and to flow the liquid refrigerant from the leeward side into the heat transfer pipe 2 during air cooling.
【請求項2】 伝熱管2を楕円管に形成した請求項1記
載の冷媒コイル。
2. The refrigerant coil according to claim 1, wherein the heat transfer tube 2 is formed as an elliptic tube.
JP11130810A 1999-05-12 1999-05-12 Refrigerant coil Pending JP2000320927A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11130810A JP2000320927A (en) 1999-05-12 1999-05-12 Refrigerant coil

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11130810A JP2000320927A (en) 1999-05-12 1999-05-12 Refrigerant coil

Publications (1)

Publication Number Publication Date
JP2000320927A true JP2000320927A (en) 2000-11-24

Family

ID=15043248

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11130810A Pending JP2000320927A (en) 1999-05-12 1999-05-12 Refrigerant coil

Country Status (1)

Country Link
JP (1) JP2000320927A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2007080483A2 (en) * 2006-01-08 2007-07-19 Obrist Engineering Gmbh Heat exchanger and group of heat exchangers
JP2012107857A (en) * 2010-11-18 2012-06-07 Lg Electronics Inc Air conditioner
JP2018169078A (en) * 2017-03-29 2018-11-01 株式会社富士通ゼネラル Air conditioner

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2007080483A2 (en) * 2006-01-08 2007-07-19 Obrist Engineering Gmbh Heat exchanger and group of heat exchangers
WO2007080483A3 (en) * 2006-01-08 2008-05-08 Obrist Engineering Gmbh Heat exchanger and group of heat exchangers
JP2012107857A (en) * 2010-11-18 2012-06-07 Lg Electronics Inc Air conditioner
JP2015117936A (en) * 2010-11-18 2015-06-25 エルジー エレクトロニクス インコーポレイティド Air conditioner
US9140474B2 (en) 2010-11-18 2015-09-22 Lg Electronics Inc. Air conditioner
JP2018169078A (en) * 2017-03-29 2018-11-01 株式会社富士通ゼネラル Air conditioner

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