JPS6325496A - Heat exchanger - Google Patents
Heat exchangerInfo
- Publication number
- JPS6325496A JPS6325496A JP16915186A JP16915186A JPS6325496A JP S6325496 A JPS6325496 A JP S6325496A JP 16915186 A JP16915186 A JP 16915186A JP 16915186 A JP16915186 A JP 16915186A JP S6325496 A JPS6325496 A JP S6325496A
- Authority
- JP
- Japan
- Prior art keywords
- heat exchanger
- corrosion
- heat
- gas
- tube
- 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
Links
- 239000007788 liquid Substances 0.000 claims abstract description 33
- 238000005260 corrosion Methods 0.000 claims abstract description 24
- 230000007797 corrosion Effects 0.000 claims abstract description 22
- 239000000463 material Substances 0.000 claims abstract description 15
- 239000006185 dispersion Substances 0.000 claims abstract description 10
- 230000002093 peripheral effect Effects 0.000 claims abstract description 10
- 229920000642 polymer Polymers 0.000 claims abstract description 5
- BFKJFAAPBSQJPD-UHFFFAOYSA-N tetrafluoroethene Chemical group FC(F)=C(F)F BFKJFAAPBSQJPD-UHFFFAOYSA-N 0.000 claims description 4
- 238000000034 method Methods 0.000 abstract 2
- 238000010521 absorption reaction Methods 0.000 description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 11
- 238000012360 testing method Methods 0.000 description 8
- 238000000576 coating method Methods 0.000 description 7
- 239000011248 coating agent Substances 0.000 description 6
- 230000000694 effects Effects 0.000 description 4
- 239000003112 inhibitor Substances 0.000 description 4
- WMFOQBRAJBCJND-UHFFFAOYSA-M Lithium hydroxide Chemical compound [Li+].[OH-] WMFOQBRAJBCJND-UHFFFAOYSA-M 0.000 description 3
- 239000006096 absorbing agent Substances 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- QRUDEWIWKLJBPS-UHFFFAOYSA-N benzotriazole Chemical compound C1=CC=C2N[N][N]C2=C1 QRUDEWIWKLJBPS-UHFFFAOYSA-N 0.000 description 2
- 239000012964 benzotriazole Substances 0.000 description 2
- 229910052802 copper Inorganic materials 0.000 description 2
- 239000010949 copper Substances 0.000 description 2
- CPELXLSAUQHCOX-UHFFFAOYSA-M Bromide Chemical compound [Br-] CPELXLSAUQHCOX-UHFFFAOYSA-M 0.000 description 1
- 229910000532 Deoxidized steel Inorganic materials 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 238000001311 chemical methods and process Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 230000002542 deteriorative effect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- NMHMDUCCVHOJQI-UHFFFAOYSA-N lithium molybdate Chemical compound [Li+].[Li+].[O-][Mo]([O-])(=O)=O NMHMDUCCVHOJQI-UHFFFAOYSA-N 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000012085 test solution Substances 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
この発明は、吸収式ヒートポンプなどに使用される熱交
換器に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a heat exchanger used in an absorption heat pump or the like.
従来、この種の熱交換器として、例えば特開昭61−4
4261号公報に示すものがあった。これを図について
説明すると、図において、1は伝熱管、2は伝熱管1表
面の気液界面であす、PII液の流れにより変動する。Conventionally, as this type of heat exchanger, for example, Japanese Patent Application Laid-Open No. 61-4
There was one shown in Publication No. 4261. To explain this with reference to the figure, in the figure, 1 is the heat exchanger tube, 2 is the gas-liquid interface on the surface of the heat exchanger tube 1, and it changes depending on the flow of the PII liquid.
3a、3bは上、下管板であり、1本以上の伝熱管1を
固定している。4は上、下管板3a、3b間に設けた胴
1)の上部に設けた吸収液入口であす、濃厚溶液が胴1
)内に送り込むためのものである。5a1.tilfl
厚な吸収液、5bl:j濃厚な吸収液5aが流下し、水
蒸気を吸収し稀薄になった吸収液である。6は分散板で
あり、乙の分散板6に遊挿された伝熱管1との間に隙間
があり、吸収液5aを各電熱管1に分散して流下させる
。7ば胴1)の分散板6下方部分に設けた水蒸気入口、
8は胴1)下部に設けた吸収液の出口であり、水蒸気を
吸収して稀薄になった溶液が送り出される。9は下管板
3b下方に設けた水の入口であり、10は上管板3a上
方に設は水が気化して生成した水蒸気の出口である。3a and 3b are upper and lower tube plates, on which one or more heat exchanger tubes 1 are fixed. 4 is an absorption liquid inlet provided at the top of the body 1) provided between the upper and lower tube plates 3a and 3b.
). 5a1. tilfl
Thick absorption liquid, 5bl:j The thick absorption liquid 5a flows down, absorbs water vapor, and becomes diluted. 6 is a dispersion plate, and there is a gap between the dispersion plate 6 and the heat transfer tubes 1 loosely inserted, and the absorption liquid 5a is distributed to each heating tube 1 and flows down. 7. A water vapor inlet provided in the lower part of the dispersion plate 6 of the body 1);
Reference numeral 8 denotes an outlet for the absorption liquid provided at the lower part of the body 1), through which the solution that has become diluted by absorbing water vapor is sent out. 9 is an inlet for water provided below the lower tube plate 3b, and 10 is an outlet for water vapor generated by vaporization of water provided above the upper tube plate 3a.
次に動作について説明する。吸収液人口4より送り込ま
れてくる濃厚な吸収液5aが胴1)内の分散板6上に溜
り、一定の流速で伝熱管1の表面を流下する。吸収液5
aには、インヒビターが添加されており、これと接触す
る構成材料が防食されている。そして、胴1)内の分散
板6下方に水蒸気人ロアから送り込まれる水蒸気を吸収
して、稀薄になっtこ吸収液5bは吸収液の出口8より
排出され、図示しない発生器に送られS縮されて循環す
る。水蒸気の吸収の際に発生する熱は、水の入口9より
送り込まれる水と熱交換し、水は蒸気となってその出口
10より化学プロセスへ供給される。Next, the operation will be explained. The concentrated absorbing liquid 5a sent from the absorbing liquid port 4 accumulates on the dispersion plate 6 in the shell 1) and flows down the surface of the heat exchanger tube 1 at a constant flow rate. Absorption liquid 5
An inhibitor is added to a to prevent corrosion of the constituent materials that come into contact with the inhibitor. Then, the water vapor sent from the steam lower part is absorbed into the lower part of the dispersion plate 6 in the shell 1), and the absorbed liquid 5b becomes diluted.The absorbed liquid 5b is discharged from the absorption liquid outlet 8 and sent to a generator (not shown). It is shrunk and circulated. The heat generated during the absorption of water vapor exchanges heat with the water fed through the water inlet 9, and the water is turned into steam and supplied to the chemical process through the outlet 10.
従来の熱交換器は、以上のように構成されており、伝熱
管1は銅製であるので、気液界面2の近傍の気相部にあ
る伝熱管外周面は、吸収液の飛沫が付着する部分では吸
収液中のインヒビターの効果が及ばないことにより、腐
食しやすいという問題点があった。The conventional heat exchanger is constructed as described above, and since the heat exchanger tube 1 is made of copper, droplets of absorption liquid adhere to the outer peripheral surface of the heat exchanger tube in the gas phase near the gas-liquid interface 2. There was a problem in that the inhibitor in the absorption liquid was not effective in some areas, making them susceptible to corrosion.
この発明は、前記のような問題点を解決するためになさ
れたもので、伝熱管外周面の気液界面近傍の気中部の腐
食を防止して、長期間にわたり高い信頼性を有する熱交
換器を安価に、しかも熱交換特性をほとんど低下させる
ことなく提供することを目的としている。This invention was made to solve the above-mentioned problems, and provides a heat exchanger that has high reliability over a long period of time by preventing corrosion in the air region near the gas-liquid interface on the outer peripheral surface of the heat exchanger tube. The aim is to provide this at a low cost and with almost no deterioration in heat exchange characteristics.
この発明は、上述したような熱交換器において、伝熱管
外周面の気液界面部に耐食性材料を被覆したものである
。The present invention provides a heat exchanger as described above, in which the gas-liquid interface on the outer peripheral surface of the heat transfer tube is coated with a corrosion-resistant material.
乙の発明における熱交換器では、伝熱管の分散板上に位
置する部分は、伝熱に関与しない部分であるため、耐食
性材料の被覆をしても、熱交換特性を低下させることが
なく、また伝熱管外周面の気液界面に近傍の気相部は腐
食しやすいが、この部分の腐食は気液界面部を耐食性材
料で被覆することで防止でき、耐食性材料で被覆する部
分の長さが短いため、耐食性材料の被覆に要する量が少
なくてすみ、材料費が安く、さらに被覆作業も容易にで
きる。In the heat exchanger according to the invention of B, the portion of the heat transfer tube located on the distribution plate is a portion that does not participate in heat transfer, so even if it is coated with a corrosion-resistant material, the heat exchange characteristics will not be deteriorated. In addition, the gas phase near the gas-liquid interface on the outer circumferential surface of the heat transfer tube is prone to corrosion, but corrosion in this area can be prevented by coating the gas-liquid interface with a corrosion-resistant material, and the length of the portion covered with the corrosion-resistant material Since the length is short, the amount of corrosion-resistant material required for coating is small, the material cost is low, and the coating process is easy.
以下、この発明の一実施例について説明する。 An embodiment of the present invention will be described below.
乙の実施例では、図に示す従来の熱交換器の伝熱管1外
周面の分散板6上に位置する気液界面2の最下部以上を
四弗化エチレン重合体の熱収縮チューブで被覆した。な
お、この実施例の上述した以外の構成は、図示の従来の
熱交換器と同様である。In Example B, the lowest part and above of the gas-liquid interface 2 located on the dispersion plate 6 on the outer peripheral surface of the heat exchanger tube 1 of the conventional heat exchanger shown in the figure is covered with a heat-shrinkable tube made of tetrafluoroethylene polymer. . Note that the configuration of this embodiment other than those described above is the same as that of the conventional heat exchanger shown in the drawings.
乙の実施例の効果を確認するために、気液界面を有する
試験片により、腐食試験を行った。試験片は、脱酸鋼管
(直径10閣、長さ40論、肉厚1鴫)を使用し、この
片側半分に四弗化エチレン重合体でできた熱収縮チュー
ブを被せた。試験液は、54%臭化リヂすム水溶液に、
インヒビターとして0.2%水酸化リチウム、0.01
5%モリブデン酸リチウム、0.14%ベンゾトリアゾ
ール(BTA)を添加している。熱収縮チューブで被覆
した方を上にして、試験片を四弗化エチレン重合体製の
容器に立てかけ、この被覆していない部分が液中に没す
るまで試験液を入れる。この容器全体を密封容器に入れ
、IQOwl(にの空気とともに封入して試験した。In order to confirm the effect of Example B, a corrosion test was conducted using a test piece having a gas-liquid interface. The test piece used was a deoxidized steel tube (diameter: 10 mm, length: 40 mm, wall thickness: 1 mm), and half of one side of the tube was covered with a heat-shrinkable tube made of tetrafluoroethylene polymer. The test solution was a 54% aqueous solution of lysium bromide,
0.2% lithium hydroxide as inhibitor, 0.01
5% lithium molybdate and 0.14% benzotriazole (BTA) are added. The test piece is placed against a container made of tetrafluoroethylene polymer with the side covered with the heat shrink tube facing up, and the test liquid is poured into the container until the uncovered part is submerged in the liquid. The entire container was placed in a sealed container and sealed with IQOwl air for testing.
試験は、160℃の恒温槽内で2週間行って、試験片の
腐食状況を調べた。この結果は、下記表の実験例に示し
たとおり、局部的な侵食はなく、腐食量が1. t、g
で実用上支障のない値である。同表には比較ため、上記
チューブを被覆していない銅試片について、前述と同じ
条件で行った実験結果も示している。同表から気中にあ
る試片表面に深い侵食が生じ、腐食量もこの発明の実施
例の10倍以上であることがわかる。The test was conducted in a constant temperature bath at 160° C. for two weeks, and the corrosion status of the test piece was investigated. As shown in the experimental example in the table below, the results show that there is no local corrosion and the amount of corrosion is 1. t, g
This is a value that does not pose any practical problem. For comparison, the same table also shows the results of an experiment conducted under the same conditions as above on a copper specimen without the tube covered. From the same table, it can be seen that deep corrosion occurred on the surface of the specimen in the air, and the amount of corrosion was more than 10 times that of the examples of the present invention.
表
さらに上記実施例では、伝熱管外周面の被覆部は、伝熱
には関与しない分散板上方部分のみであり、熱交換器の
熱交換特性には影響しない。また、この実施例では、被
覆材料として四弗化エチレン共重合体の熱収縮性チュー
ブを用いたので、被覆作業が簡易で、耐熱、耐薬品性が
すぐれている。Further, in the above embodiment, the coating portion on the outer circumferential surface of the heat exchanger tube is only the upper portion of the distribution plate that does not participate in heat transfer, and does not affect the heat exchange characteristics of the heat exchanger. Furthermore, in this example, a heat-shrinkable tube of tetrafluoroethylene copolymer was used as the covering material, so the covering operation was simple and the material had excellent heat resistance and chemical resistance.
なお、上記実施例では、伝熱管1外周面の分散板6上方
部分のみに防食被覆を設けたが、胴1)内局面の濃溶w
15 aおよび稀溶液5bとの気液界面部や、伝熱管1
外周面のPIIi溶液5bとの気液界面部にも同様の現
象が生ずると考えられるので、これらの部分にも耐食性
材料よりなる防食被覆を設けろとよい。In the above embodiment, the anti-corrosion coating was provided only on the upper part of the dispersion plate 6 on the outer circumferential surface of the heat exchanger tube 1.
15a and the gas-liquid interface with the dilute solution 5b, and the heat exchanger tube 1
Since a similar phenomenon is thought to occur at the gas-liquid interface with the PIIi solution 5b on the outer peripheral surface, it is advisable to provide an anti-corrosion coating made of a corrosion-resistant material to these areas as well.
また、上記実施例では、吸収式ヒートポンプの吸収器の
場合について説明したが、この発明は、吸収式ヒートポ
ンプの発生器や、吸収式冷凍機の吸収器および発生器の
伝熱管にも適用でき、これらでも上記実施例と同様の効
果を奏する。Further, in the above embodiment, the case of an absorber of an absorption heat pump was explained, but the present invention can also be applied to a generator of an absorption heat pump, an absorber of an absorption refrigerator, and a heat exchanger tube of the generator. These also produce the same effects as the above embodiments.
以上のように、この発明によれば、伝熱管外周面の吸収
液と接する気液界面部を耐食性材料で被覆したので、伝
熱管が腐食しに<<、高い信頼性を有し、長寿命の熱交
換器が得られ、また、施工が簡単であり、被覆材料も少
なくてすみ、安価に信頼性の高い熱交換器が得られ、熱
交換特性を低下させることもほとんどないという効果が
ある。As described above, according to the present invention, the gas-liquid interface on the outer peripheral surface of the heat exchanger tube in contact with the absorption liquid is coated with a corrosion-resistant material, so the heat exchanger tube does not corrode, has high reliability, and has a long service life. In addition, it is easy to construct, requires less coating material, provides a highly reliable heat exchanger at low cost, and has the effect of hardly deteriorating heat exchange characteristics. .
図は従来の吸収式ヒートポンプの吸収器を示す断面側面
図である。
1・・伝熱管、5a・・・吸収液、6・分散板、1)・
・胴。
なお、図中同一符号は同一または相当部分を示す。
代理人 大 岩 増 雄(外2名)
□
二1゜
ノ5b
/ :(i本管
6!4N次り
Z・)F−威λAr:)The figure is a cross-sectional side view showing an absorber of a conventional absorption heat pump. 1. Heat exchanger tube, 5a... Absorption liquid, 6. Dispersion plate, 1).
・Torso. Note that the same reference numerals in the figures indicate the same or corresponding parts. Agent Masuo Oiwa (2 others) □ 21゜ノ5b / :(i main 6!4N next Z・)F-WeiλAr:)
Claims (2)
し、熱交換をする熱交換器において、上記伝熱管外周面
の気液界面部に耐食性材料を被覆したことを特徴とする
熱交換器。(1) A heat exchanger having a dispersion plate and dispersing a solution and causing it to flow over the surface of a heat exchanger tube for heat exchange, characterized in that the gas-liquid interface on the outer peripheral surface of the heat exchanger tube is coated with a corrosion-resistant material. Heat exchanger.
収縮チューブである特許請求の範囲第1項記載の熱交換
器。(2) The heat exchanger according to claim 1, wherein the corrosion-resistant material is a heat-shrinkable tube made of tetrafluoroethylene polymer.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP16915186A JPS6325496A (en) | 1986-07-18 | 1986-07-18 | Heat exchanger |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP16915186A JPS6325496A (en) | 1986-07-18 | 1986-07-18 | Heat exchanger |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6325496A true JPS6325496A (en) | 1988-02-02 |
Family
ID=15881228
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP16915186A Pending JPS6325496A (en) | 1986-07-18 | 1986-07-18 | Heat exchanger |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6325496A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5264561A (en) * | 1991-03-22 | 1993-11-23 | Japan Tobacco Inc. | Method of manufacturing 2',3'-dideoxy-2',3'-didehydronucleosides |
KR100839227B1 (en) * | 2007-05-16 | 2008-06-19 | 현대냉열(주) | Cooler using in a chemicals |
JP2011141080A (en) * | 2010-01-07 | 2011-07-21 | Kansetsu Sangyo Kk | Method of preventing build-up of scale to heat exchanger |
-
1986
- 1986-07-18 JP JP16915186A patent/JPS6325496A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5264561A (en) * | 1991-03-22 | 1993-11-23 | Japan Tobacco Inc. | Method of manufacturing 2',3'-dideoxy-2',3'-didehydronucleosides |
KR100839227B1 (en) * | 2007-05-16 | 2008-06-19 | 현대냉열(주) | Cooler using in a chemicals |
JP2011141080A (en) * | 2010-01-07 | 2011-07-21 | Kansetsu Sangyo Kk | Method of preventing build-up of scale to heat exchanger |
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