JPS595835B2 - Counterflow type total heat exchanger - Google Patents

Counterflow type total heat exchanger

Info

Publication number
JPS595835B2
JPS595835B2 JP8093880A JP8093880A JPS595835B2 JP S595835 B2 JPS595835 B2 JP S595835B2 JP 8093880 A JP8093880 A JP 8093880A JP 8093880 A JP8093880 A JP 8093880A JP S595835 B2 JPS595835 B2 JP S595835B2
Authority
JP
Japan
Prior art keywords
heat exchanger
pipe
sheet
pipes
heat exchange
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.)
Expired
Application number
JP8093880A
Other languages
Japanese (ja)
Other versions
JPS5710082A (en
Inventor
豊 五十嵐
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.)
Toyo Netsu Kogyo Kaisha Ltd
Original Assignee
Toyo Netsu Kogyo Kaisha 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 Toyo Netsu Kogyo Kaisha Ltd filed Critical Toyo Netsu Kogyo Kaisha Ltd
Priority to JP8093880A priority Critical patent/JPS595835B2/en
Publication of JPS5710082A publication Critical patent/JPS5710082A/en
Publication of JPS595835B2 publication Critical patent/JPS595835B2/en
Expired legal-status Critical Current

Links

Classifications

    • 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
    • F28D1/053Heat-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 straight

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Description

【発明の詳細な説明】 この発明は対向流型全熱交換器に関する。[Detailed description of the invention] This invention relates to a counterflow type total heat exchanger.

最近は多数人の集まるホールとか、或いは住宅等におい
て、環境を一層快適にするために、熱交換器を備えた換
気装置が開発されている。
Recently, ventilation systems equipped with heat exchangers have been developed in order to make the environment more comfortable in halls where a large number of people gather, or in houses.

その際熱交換材料として、湿気を吸収、発散、透過させ
るような材料(プラスチックフィルム、紙、布類等)を
使用すれば、顕熱のみならず、潜熱交換をも行なわせる
ことができる。
In this case, if a material that absorbs, releases, or transmits moisture (plastic film, paper, cloth, etc.) is used as the heat exchange material, not only sensible heat but also latent heat exchange can be performed.

この種の熱交換器の欠点は対向流型の熱交換器を作るこ
とが難しいことで、熱交換材料を介して上下の交叉する
通路を二種の流体が流通するため全熱交換効率を高める
ためには大容量の熱交換器を作らねばならなかった。
The disadvantage of this type of heat exchanger is that it is difficult to create a counterflow type heat exchanger, and the two fluids flow through the upper and lower intersecting passages through the heat exchange material, increasing the total heat exchange efficiency. In order to do this, we had to create a large-capacity heat exchanger.

この発明はこの欠点を除くために、熱交換部材としてパ
イプを用うる対向流型全熱交換器において、必要に応じ
て吸湿処理した。
In order to eliminate this drawback, the present invention performs moisture absorption treatment as necessary in a counterflow type total heat exchanger that uses pipes as heat exchange members.

湿気を吸収、発散、透過させるような材料でできたパイ
プを横にならべたものを、上下に間隔を設けて、たてに
積層し、パイプ中に一方の流体を通し、上下のパイプ列
の間に他方の流体を対向的に流すようにし、パイプの両
端は上下をシートではさんでシールし、双方の流体の入
口、出口が交互に、熱交換要素の左右半分づつに、上下
にならんでいるようにしたもので、双方の流体の入口出
口が熱交換器の前後で互いに隣接するため熱交換器に接
続される流路の接続を簡単に行なうことができ、しかも
簡単な構成で効率のよい対向流型全熱交換器を得たもの
である。
Horizontal rows of pipes made of materials that absorb, wick, and permeate moisture are stacked vertically, with gaps between the top and bottom. The other fluid is made to flow in the opposite direction between them, and the upper and lower ends of the pipe are sealed with sheets sandwiched between them, and the inlets and outlets of both fluids are arranged vertically in the left and right halves of the heat exchange element alternately. Since the inlets and outlets of both fluids are adjacent to each other before and after the heat exchanger, the flow paths connected to the heat exchanger can be easily connected, and the simple configuration also improves efficiency. A good counterflow type total heat exchanger was obtained.

図について説明すれば、第1図は従来の構造の対向流型
の熱交換器を示すもので、熱交換器HCはシリンダーC
を有し、その上下に流体の入口部A、出口部Bを有し、
又シリンダーの側面の上下に他の流体の人口部D、出口
部Eを有している。
To explain the diagrams, Fig. 1 shows a counterflow type heat exchanger with a conventional structure, and the heat exchanger HC is a cylinder C.
It has a fluid inlet part A and an outlet part B above and below it,
Also, there are an intake section D and an outlet section E for other fluids on the upper and lower sides of the cylinder.

そしてシリンダー内部には出口部Eの上方に管板S1、
及び入口部りの下方に他の管板S2が取りつけられ、管
板S1,82間には多数のパイプPが貫通している。
Inside the cylinder, there is a tube plate S1 above the outlet E.
Another tube sheet S2 is attached below the inlet portion, and a large number of pipes P pass through between the tube sheets S1 and 82.

このような熱交換器では一方の流体F1 は入口部Aか
ら流入し、パイプPを通って出口部Bから流出する。
In such a heat exchanger, one fluid F1 enters from the inlet A, passes through the pipe P, and exits from the outlet B.

他方の流体F2は下方の入口部りから流入し、パイプの
周りを流体F1 とは対向的に上方に流れ、出口部Eか
ら流出するものである。
The other fluid F2 flows in from the lower inlet, flows upward around the pipe in opposition to the fluid F1, and flows out from the outlet E.

このような従来の構成では管板の取付も面倒であり管板
にパイプを取りつけるにしても、多数のパイプを精密に
取りつけねばならぬという手間がかかる。
In such a conventional structure, it is troublesome to attach the tube sheet, and even if the pipes are to be attached to the tube sheet, it takes time and effort to precisely attach a large number of pipes.

この発明はこれらの欠点を除去し、簡単な構成で効率も
高い対向流型全熱交換器を得たものである。
The present invention eliminates these drawbacks and provides a counterflow type total heat exchanger with a simple configuration and high efficiency.

第2図はこの発明の熱交換器の外観を示し、1はケーシ
ング、11は上方枠、12は側枠、13は底枠であり、
14は中央分離枠を示す。
FIG. 2 shows the appearance of the heat exchanger of the present invention, where 1 is a casing, 11 is an upper frame, 12 is a side frame, and 13 is a bottom frame.
14 indicates a central separation frame.

2はケーシング1中に収められた熱交換要素である。2 is a heat exchange element housed in the casing 1.

第3図に−F方からみたところを図式的に示す如く、熱
交換要素2はパイプ21を横にならべてその前後端部に
上下からシー)22,23を接着したものを、上下に複
数段ならべて積層したものである。
As shown diagrammatically in FIG. 3 when viewed from the -F direction, the heat exchange element 2 is made up of a plurality of pipes 21 arranged horizontally and sheets 22, 23 glued to the front and rear ends of the pipes from above and below. It is stacked in rows.

そして中央のパイプ群でパイプ部を、又パイプ群の両端
の各々とシート22−・・・・・・・・、及び23・・
・・・・・・・によって、シール部4,5を夫々形成す
る。
Then, the pipe section is formed by the central pipe group, and the sheets 22-, 23, and 23 are formed at each end of the pipe group.
The seal portions 4 and 5 are formed by . . . .

第4図はパイプ21・・・・・・・・・、とシート22
・・・・・・・・・との関係を第2図の矢印Rの方向か
らみたところ、第5図は第4図の■−V線に?6う断面
を示したものであって、シート22はその端縁を中央か
ら右半分と左半分を交互に上方及び下方に折り曲げて上
方折曲部22a、及び下方折曲部22bとする。
Figure 4 shows the pipe 21... and the sheet 22.
When looking at the relationship between ・・・・・・・・・ from the direction of arrow R in Fig. 2, Fig. 5 corresponds to the ■-V line in Fig. 4? The sheet 22 has its edges bent upward and downward alternately from the center to the right half and the left half to form an upper folded part 22a and a lower folded part 22b.

(即ち一つのシート22の右半分を上方折曲部22a、
左半分を下方折曲部22bとすれば、その一つ下方のシ
ートの右半分を下方折曲部22b、左半分を上方折曲部
22aとする。
(That is, the right half of one sheet 22 is
If the left half is defined as the lower folded part 22b, the right half of the sheet one sheet below it is defined as the lower folded part 22b, and the left half is defined as the upper folded part 22a.

以下同様である。The same applies below.

)そして上方のシート22の下方折曲部22 と、下方
のシートの上方折曲部22aとを接合する。
) Then, the lower bent portion 22 of the upper sheet 22 and the upper bent portion 22a of the lower sheet are joined.

又一つのシートの上方折曲部22aと、その一つ下のシ
ートの下方折曲部22bとの間には互いちがいに開口2
4・・・・・・・・・、開口25・・・・・・・・・が
形成される。
Further, there are openings 2 at different intervals between the upper bent portion 22a of one sheet and the lower bent portion 22b of the sheet one below.
4......, opening 25...... is formed.

そしてシート22・・・・・・・・・の他端の間には一
段おきに横にならべたパイプ列21・−・・・・・・・
を挿入して接着する。
And between the other ends of the sheets 22, there are rows of pipes 21 arranged horizontally every other row.
Insert and glue.

シート22・・・・・・・・・の上下の間隔はパイプ2
1の径より少し小さくして第4図の左半分にみえるよう
に偏平部21′となし、シートの間ではパイプ間の隙間
がなくなるようにする。
The distance between the top and bottom of sheet 22 is the same as pipe 2.
The diameter of the pipe is slightly smaller than that of the pipe 1, and the flat part 21' is formed as shown in the left half of FIG. 4, so that there is no gap between the pipes between the sheets.

そしてパイプとシートとの間の隙間は後述する如く溶融
接着等でシールしてしまい、パイプとシートとでシール
部4を形成する。
Then, the gap between the pipe and the sheet is sealed by melt adhesion or the like as described later, and the pipe and the sheet form a sealed portion 4.

パイプの他端部にも同様にシート23・・・・−・・・
・を用いてシール部5を形成し、パイプ部3、シール部
4,5によって熱交換要素2を構成する。
Similarly, the sheet 23 is attached to the other end of the pipe.
The pipe portion 3 and the seal portions 4 and 5 constitute the heat exchange element 2.

そしてこの熱交換要素2をケーシング1中に収納する。This heat exchange element 2 is then housed in the casing 1.

すると中央分離枠14の左右の開口24・・・−・・−
・・、25・・・・・・・・・が分離され、流体の出入
がスムーズに行なわれる。
Then, the left and right openings 24 of the central separation frame 14...--
. . , 25 . . . are separated, and the fluid can enter and exit smoothly.

図では開口24はパイプ21・・・・・・・・・と通じ
、開口25はパイプ列とパイプ列の間の空間に通じてい
るので、開口24.250一方を入口、他方を出口とす
ることにより、二種の流体を対向流で流すと、対向流型
の全熱交換を行なうことができる。
In the figure, the openings 24 communicate with the pipes 21, and the openings 25 communicate with the space between the pipe rows, so one of the openings 24 and 250 is used as an inlet and the other as an outlet. By this, when two types of fluids flow in countercurrents, countercurrent type total heat exchange can be performed.

第6図はシール部4のみを取り出して示す説明図であっ
て、シート22の左半分を上方折曲部を上方折曲部22
a、右半分を下方折曲部22bとし、その一つ下のシー
ト22では逆に右半分を上方折曲部22aとし、左半分
を下方折曲部22bとする。
FIG. 6 is an explanatory diagram showing only the seal portion 4, in which the left half of the sheet 22 is folded upward and the upper folded portion 22 is shown.
a, the right half is the lower bent part 22b, and in the sheet 22 one below, the right half is the upper bent part 22a, and the left half is the lower bent part 22b.

そして右側の下方折曲部22bと、一つ下のシートの上
方折曲部22aとを接着する。
Then, the lower bent portion 22b on the right side and the upper bent portion 22a of the sheet one below are adhered.

左半分の上方折曲部22aと一つ下のシートの下方折曲
部22bとの間に開口24が形成される。
An opening 24 is formed between the upper bent portion 22a of the left half and the lower bent portion 22b of the sheet immediately below.

今開口24を入口とすれば、その左半分の開口から入っ
た流体は上下のシート22内に入ってシール部−ばいに
ひろがり、パイプ21に入って流れる。
If the opening 24 is now used as an inlet, the fluid entering from the left half opening enters the upper and lower sheets 22, spreads to the seal portion, enters the pipe 21, and flows.

(前述の如くパイプとシートの間はシールされているの
で、流体は完全に分離される。
(As mentioned above, the pipe and seat are sealed, so the fluid is completely separated.

)第7図はパイプ21とシート22の関係を示す平面図
であって、パイプ21の先端は偏平部21′となって、
シート22に接着部27のところで接着され、溶融接着
部26でシールされている。
) FIG. 7 is a plan view showing the relationship between the pipe 21 and the sheet 22, and the tip of the pipe 21 becomes a flat part 21',
It is adhered to the sheet 22 at an adhesive section 27 and sealed at a melt adhesive section 26.

このシール部分を断面で示すと、第8図の如くなり、シ
ート220間にパイプ21の偏平部21’が入り、シー
トとパイプの間の隙間は凡て溶融接着部26でシールさ
れている。
When this sealed portion is shown in cross section, as shown in FIG. 8, the flat portion 21' of the pipe 21 is inserted between the sheets 220, and all gaps between the sheet and the pipe are sealed with the melted adhesive portion 26.

このシールに当っては例えばシートの内面に溶融接着材
を印刷しておき、パイプとシートの間に熱をかげながら
接着する。
For this seal, for example, a melt adhesive is printed on the inner surface of the sheet, and the pipe and the sheet are bonded together while being heated.

このときシートの溶融接着剤が溶けてシートとパイプの
隙間に入って、隙間をシールしてしまうものである。
At this time, the molten adhesive on the sheet melts and enters the gap between the sheet and the pipe, sealing the gap.

第9図は熱交換要素2におけるシール部4,5の関係を
図式的に示すもので、パイプ部3の一端には今まで説明
した如くシート22・・・・−・・・・を用いてシール
部4が形成され、又反対端にはシート23・・・・・・
・・・を用いて同様なシール部5が形成されている。
FIG. 9 schematically shows the relationship between the seal parts 4 and 5 in the heat exchange element 2, and one end of the pipe part 3 is provided with a sheet 22 as described above. A seal portion 4 is formed, and a sheet 23 is formed at the opposite end.
A similar seal portion 5 is formed using...

尚シール部4,5との開口の位置は図示の如く反対とな
っている。
Note that the positions of the openings and the seal portions 4 and 5 are opposite to each other as shown in the figure.

熱交換される流体の一方は開口部24から入り上下のシ
ートの間にひろがり、パイプ21・・・・・・・・・に
入り、その間を通って反対側の開口24’から出る。
One of the fluids to be heat exchanged enters through the opening 24, spreads between the upper and lower sheets, enters the pipe 21, passes therebetween and exits through the opposite opening 24'.

他方の流体は反対側の開口25′から入り、上下のパイ
プ列の間を通り開口25から出るようにすれば対向流型
の全熱交換を行なうものである。
The other fluid enters from the opening 25' on the opposite side, passes between the upper and lower pipe rows, and exits from the opening 25, thereby performing counterflow type total heat exchange.

(尚第9図では図示を簡単にするためにパイプは省略し
である。
(In FIG. 9, the pipes are omitted to simplify the illustration.

)パイプは円形のほか、だ円形、多面形、などの任意の
形状でよい。
) The pipe may be of any shape, such as circular, oval, polyhedral, etc.

又パイプの材料に潜熱の移動のないものを使用すれば顕
熱のみの熱交換器となる。
Furthermore, if the material of the pipe is one that does not transfer latent heat, it becomes a heat exchanger that uses only sensible heat.

この発明は以上のような構成であって、簡単な構成でし
かも効率のよい対向流型全熱交換器を得たものである。
The present invention has the above-described configuration, and provides a counterflow type total heat exchanger with a simple configuration and high efficiency.

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

第1図は従来の対向流型熱交換器の説明図、第2図はこ
の発明の熱交換器の外観図、第3図は熱交換要素の平面
図、第4図はパイプとシートとの関係を正面からみた図
、第5図は第4図のV−V線に沿う断面図、第6図はシ
ール部を取り出して示した斜面図、第7図はパイプとシ
ートとの関係の平面図、第8図は溶融接着部の断面図、
第9図は熱交換要素の図式的説明図を夫々示す。 符号の説明、1・・・・・・ケーシング、2・・・・・
・熱交換要素、21・・・・・・パイプ、22,23・
・・・・・シート、24.25・・・・・・開口、計・
・・・・パイプ部、4,5・・・・・・シール部。
Fig. 1 is an explanatory diagram of a conventional counterflow type heat exchanger, Fig. 2 is an external view of the heat exchanger of the present invention, Fig. 3 is a plan view of the heat exchange element, and Fig. 4 is an illustration of a pipe and a sheet. Figure 5 is a cross-sectional view taken along line V-V in Figure 4, Figure 6 is an oblique view showing the seal section, Figure 7 is a plane view of the relationship between the pipe and the sheet. Figure 8 is a cross-sectional view of the melted bonding part,
FIG. 9 shows a schematic illustration of the heat exchange elements, respectively. Explanation of symbols, 1...Casing, 2...
・Heat exchange element, 21...Pipe, 22, 23・
... Sheet, 24.25 ... Opening, total.
...Pipe part, 4,5... Seal part.

Claims (1)

【特許請求の範囲】 1 熱交換用パイプを所定間隔をおいて配位した対向流
型熱交換器において、熱交換用パイプ列の両端側におい
て、パイプ21の上下からシート22又は23が接着さ
れ、パイプとシートの隙間はシールされてシール部4,
5が形成され、上記シートの外側端縁は中央から交互に
上方及び下方に折り曲げて接合され、左右にシート巾の
半分づつ接合部と開口部とが形成され、パイプ列が一段
おきに積層されて熱交換要素2が構成され、パイプの内
を流れる流体とパイプの外を流れる流体とが、パイプ列
の両端部で別々の層に分けられ、その際各層の中央を境
としてパイプの内外を流れる流体が左右に交互に流入し
又流出することを特徴とする対向型全熱交換器。 2 前記の熱交換要素2はケーシング1に収納されてい
ることを特徴とする特許 1項記載の対向流型全熱交換器。 3 前記のケーシング1は両端の中央に中央分離枠14
を有していることを特徴とする前記特許請求の範囲第1
項記載の対向流型全熱交換器。 4 前記パイプ21に吸湿剤処理をしていることを特徴
とする前記特許請求の範囲第1項記載の対向流型全熱交
換器。
[Claims] 1. In a counterflow type heat exchanger in which heat exchange pipes are arranged at predetermined intervals, sheets 22 or 23 are adhered from above and below the pipes 21 at both ends of the row of heat exchange pipes. , the gap between the pipe and the seat is sealed and the seal part 4,
5 is formed, the outer edge of the sheet is bent and joined alternately upward and downward from the center, a joint part and an opening part are formed on the left and right sides by half the width of the sheet, and the pipe rows are stacked every other row. The heat exchange element 2 is configured such that the fluid flowing inside the pipes and the fluid flowing outside the pipes are separated into separate layers at both ends of the pipe row. An opposed total heat exchanger characterized in that flowing fluid alternately flows in and out from the left and right sides. 2. The counterflow type total heat exchanger described in Patent No. 1, wherein the heat exchange element 2 is housed in a casing 1. 3 The casing 1 has a central separation frame 14 at the center of both ends.
Claim 1 characterized in that it has
Counterflow type total heat exchanger as described in . 4. The counterflow type total heat exchanger according to claim 1, wherein the pipe 21 is treated with a moisture absorbent.
JP8093880A 1980-06-17 1980-06-17 Counterflow type total heat exchanger Expired JPS595835B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8093880A JPS595835B2 (en) 1980-06-17 1980-06-17 Counterflow type total heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8093880A JPS595835B2 (en) 1980-06-17 1980-06-17 Counterflow type total heat exchanger

Publications (2)

Publication Number Publication Date
JPS5710082A JPS5710082A (en) 1982-01-19
JPS595835B2 true JPS595835B2 (en) 1984-02-07

Family

ID=13732402

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8093880A Expired JPS595835B2 (en) 1980-06-17 1980-06-17 Counterflow type total heat exchanger

Country Status (1)

Country Link
JP (1) JPS595835B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5963491A (en) * 1982-10-05 1984-04-11 Japan Vilene Co Ltd Counterflow type heat exchanger
JPS6060576U (en) * 1983-09-27 1985-04-26 三菱電機株式会社 Counterflow type total heat exchanger
JP2536344B2 (en) * 1991-08-30 1996-09-18 カシオ計算機株式会社 Printer

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JPS5710082A (en) 1982-01-19

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