Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPH0454481B2 - - Google Patents
[go: Go Back, main page]

JPH0454481B2 - - Google Patents

Info

Publication number
JPH0454481B2
JPH0454481B2 JP12669485A JP12669485A JPH0454481B2 JP H0454481 B2 JPH0454481 B2 JP H0454481B2 JP 12669485 A JP12669485 A JP 12669485A JP 12669485 A JP12669485 A JP 12669485A JP H0454481 B2 JPH0454481 B2 JP H0454481B2
Authority
JP
Japan
Prior art keywords
heating element
shell
heating
heated
steam
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
JP12669485A
Other languages
Japanese (ja)
Other versions
JPS61287401A (en
Inventor
Kenichi Yamada
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.)
Hisaka Works Ltd
Original Assignee
Hisaka Works 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 Hisaka Works Ltd filed Critical Hisaka Works Ltd
Priority to JP12669485A priority Critical patent/JPS61287401A/en
Publication of JPS61287401A publication Critical patent/JPS61287401A/en
Publication of JPH0454481B2 publication Critical patent/JPH0454481B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、薄膜流下型蒸発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 thin film falling type evaporator.

従来の技術 薄膜流下型蒸発器としては、例えば実公昭58−
30562号公報に開示された流下フイルム式蒸発装
置がある。この流下フイルム式蒸発装置は、第7
図に示す如く、円筒状をしたシエル1と、シエル
1内に設けられた複数個の中空プレート状をした
加熱素子2と、加熱素子2の上方に設けられ、加
熱素子2外表面上に被加熱用液体を供給するデイ
ストリビユータ3と、シエル1の底部に溜つた被
加熱用流体を循環パイプ4を介してデイストリビ
ユータ3に循環させる循環ポンプ5とからなつて
いる。又、上記シエル1の上端部には、加熱素子
2の外表面から発生する蒸発蒸気をシエル1の外
部に導出させるための蒸発蒸気出口6が、シエル
1の上部外周面には、シエル1内に設けた加熱素
子2の中空部内に加熱用蒸気を供給するためめの
加熱蒸気入口7が、又、シエル1の下部外周面に
は、シエル1の底部に被加熱用流体を供給するた
めの被加熱用流体供給口8がそれぞれ設けてあ
る。更に、加熱素子2の下端には、加熱素子2の
中空部内を通過した加熱用蒸気を収集し、シエル
1の外部に排出するためのコンデンセート出口9
を有するコンデンセートヘツダ10が取付けてあ
る。
Conventional technology As a thin film falling type evaporator, for example,
There is a falling film type evaporator disclosed in Japanese Patent No. 30562. This falling film type evaporator is the seventh
As shown in the figure, there is a cylindrical shell 1, a plurality of hollow plate-shaped heating elements 2 provided inside the shell 1, and a heating element 2 provided above the heating element 2 and covered on the outer surface of the heating element 2. It consists of a distributor 3 that supplies heating liquid, and a circulation pump 5 that circulates the fluid to be heated accumulated at the bottom of the shell 1 to the distributor 3 via a circulation pipe 4. Further, an evaporative vapor outlet 6 is provided at the upper end of the shell 1 for guiding the evaporative vapor generated from the outer surface of the heating element 2 to the outside of the shell 1, and an evaporative vapor outlet 6 is provided on the upper outer circumferential surface of the shell 1 for discharging the evaporative vapor generated from the outer surface of the heating element 2 to the outside of the shell 1. A heating steam inlet 7 for supplying heating steam into the hollow part of the heating element 2 provided at A heated fluid supply port 8 is provided respectively. Further, at the lower end of the heating element 2, there is a condensate outlet 9 for collecting the heating steam that has passed through the hollow part of the heating element 2 and discharging it to the outside of the shell 1.
A condensate header 10 having a diameter is installed.

上記構成からなる流下フイルム式蒸発器の加熱
蒸気入口7から加熱素子2の中空部内に加熱用蒸
気を導入すると同時に、被加熱用流体供給口8か
らシエル1の底部に被加熱用流体を供給すると、
加熱用蒸気は加熱素子2の中空部を通過した後コ
ンデンセートヘツダ10に集められ、コンデンセ
ートヘツダ10と連通したコンデンセート出口9
からシエル1の外部に排出される。一方、シエル
1の底部に導入された被加熱用流体は、シエル1
の底部から循環パイプ4を通り、循環ポンプ5に
よりデイストリビユータ3に供給される。ここで
被加熱用流体は加熱素子2の外表面上に分配供給
され、当該外表面を流下し、この時加熱素子2の
中空部内を流れる加熱用蒸気との間で熱交換が行
われる。そして加熱素子2外表面上の被加熱用流
体の一部が蒸発し、蒸発蒸気は加熱素子両側方に
流出し、シエル1の上端に設けた蒸発蒸気出口6
から次段の装置に送られる。又、加熱素子2の外
表面から蒸発しなかつた被加熱用流体は、加熱素
子2の下端からシエル1の底部に落下し、シエル
1の底部に導入された被加熱用流体と共に再び循
環パイプ4を通り循環ポンプ5によりデイストリ
ビユータ3に供給される。
When heating steam is introduced into the hollow part of the heating element 2 from the heating steam inlet 7 of the falling film type evaporator having the above configuration, and at the same time, the fluid to be heated is supplied from the fluid to be heated supply port 8 to the bottom of the shell 1. ,
After the heating steam passes through the hollow part of the heating element 2, it is collected in the condensate header 10, and the condensate outlet 9 communicates with the condensate header 10.
is discharged to the outside of shell 1. On the other hand, the fluid to be heated introduced into the bottom of shell 1 is
It passes through a circulation pipe 4 from the bottom and is supplied to the distributor 3 by a circulation pump 5. Here, the fluid to be heated is distributed and supplied onto the outer surface of the heating element 2, flows down the outer surface, and at this time exchanges heat with the heating steam flowing inside the hollow part of the heating element 2. Then, a part of the heated fluid on the outer surface of the heating element 2 evaporates, and the evaporated vapor flows out to both sides of the heating element, and the evaporated vapor exit 6 provided at the upper end of the shell 1
from there to the next stage of equipment. Further, the fluid to be heated that has not evaporated from the outer surface of the heating element 2 falls from the lower end of the heating element 2 to the bottom of the shell 1, and flows back into the circulation pipe 4 together with the fluid to be heated that has been introduced into the bottom of the shell 1. is supplied to the distributor 3 by the circulation pump 5.

発明が解決しようとする問題点 上記形式の流下フイルム式蒸発装置は長い伝熱
長を要求されるが、この流下フイルム式蒸発装置
の加熱素子2は外表面が平滑面のため、伝熱長を
長く取ると必然的に加熱素子2の全長が長くな
り、装置全体の高さ方向の全長が長くなるといつ
た問題点があつた。又加熱素子2の表面を平滑面
にすると、加熱素子2の外表面を被加熱用流体が
流下する時、水平方向の液偏流が起こり、熱交換
率が低下するといつた問題点もあつた。
Problems to be Solved by the Invention The above type of falling film type evaporator is required to have a long heat transfer length, but since the heating element 2 of this falling film type evaporator has a smooth outer surface, the heat transfer length is If the heating element 2 is made longer, the total length of the heating element 2 will inevitably become longer, resulting in a problem that the overall length of the entire device in the height direction will become longer. Further, when the surface of the heating element 2 is made smooth, there is a problem that when the fluid to be heated flows down the outer surface of the heating element 2, liquid drift occurs in the horizontal direction, and the heat exchange efficiency decreases.

問題点を解決するための手段 薄膜流下型蒸発器を、円筒状をし、かつ、内周
面及び外周面に傾斜溝を有する加熱素子と、この
加熱素子を収納するシエルとによつて構成し、上
記シエル内に収納された加熱素子の外周面と内周
面とにそれぞれ2種類の流体を供給することによ
り熱交換を行うようにしたものである。
Means for Solving the Problems A thin film falling type evaporator is constructed of a heating element having a cylindrical shape and having inclined grooves on the inner and outer peripheral surfaces, and a shell that houses the heating element. , heat exchange is performed by supplying two types of fluids to the outer peripheral surface and inner peripheral surface of the heating element housed in the shell, respectively.

作 用 加熱素子を円筒状に形成し、かつ、内周面及び
外周面に傾斜溝を設けておけば、加熱素子の全長
を長くすることなく伝熱長を長くできる。
Effect By forming the heating element in a cylindrical shape and providing inclined grooves on the inner and outer peripheral surfaces, the heat transfer length can be increased without increasing the overall length of the heating element.

実施例 第1図は、本発明に係る薄膜流下型蒸発器の第
1の実施例を示す図面であり、この図に示す薄膜
流下型蒸発器は、両端開口部が蓋体20a,20
bによつて閉塞された円筒状をし、かつ、その内
周面及び外周面に所定の傾斜角を有する傾斜溝イ
を設けた加熱素子ロと、この加熱素子ロを収納す
る両端が閉塞した円筒状のシエル21とによつて
構成されている。上記シエル21の上端部には、
加熱素子ロの外周面から発生する蒸発蒸気をシエ
ル21の外部に導出するための蒸発蒸気出口22
が設けてあり、シエル21の下端部には、加熱素
子ロの外周面で濃縮された濃縮液をシエル21の
外部に導出するための濃縮液排出管23が接続し
てある。又加熱素子ロの上部周面には、シエル2
1を貫通し、加熱素子ロの内部に加熱用蒸気を供
給するための加熱蒸気導入筒24が接続してあ
り、加熱素子ロの下部周面には、加熱素子ロの内
部に供給された加熱用蒸気をシエル21の外部に
排出するための排出筒25が接続してある。又加
熱素子ロの上方には、加熱素子ロの外周面に被加
熱用流体を供給するための被加熱用流体供給筒2
6の先端部が開孔している。
Embodiment FIG. 1 is a drawing showing a first embodiment of a thin film falling type evaporator according to the present invention.
A heating element (B) having a cylindrical shape and having an inclined groove (A) having a predetermined angle of inclination on its inner and outer peripheral surfaces, which is closed by (B), and both ends of which the heating element (B) is housed are closed. It is composed of a cylindrical shell 21. At the upper end of the shell 21,
An evaporative vapor outlet 22 for guiding evaporative vapor generated from the outer circumferential surface of the heating element B to the outside of the shell 21.
A concentrated liquid discharge pipe 23 is connected to the lower end of the shell 21 for discharging the concentrated liquid concentrated on the outer peripheral surface of the heating element 21 to the outside of the shell 21. In addition, there is a shell 2 on the upper circumferential surface of heating element B.
A heating steam introduction tube 24 for supplying heating steam to the inside of heating element B is connected to it, and a heating steam introduction tube 24 for supplying heating steam to the inside of heating element B is connected to the lower peripheral surface of heating element B. A discharge pipe 25 for discharging the steam to the outside of the shell 21 is connected thereto. Further, above the heating element RO, there is a heated fluid supply cylinder 2 for supplying the heated fluid to the outer peripheral surface of the heating element RO.
The tip of No. 6 is open.

第3図乃至第6図は、上記した薄膜流下型蒸発
器に用いる加熱素子ロの製造方法を説明するため
の図面である。この加熱素子ロは、第3図に示す
如く、平板ロ′の表面にプレス加工又はロール加
工によつて傾斜溝イ′を形成した後、この傾斜溝
イ′を有する平板ロ′を第4図に示す如く円筒状に
加工するか、又は、第5図に示す如く、長尺な帯
状板ロ″の表面に、プレス加工又はロール加工に
よつて長手方向に延びるストレートな溝イ″を形
成し、このストレートな溝イ″を有する帯状板
ロ″を第6図に示す如くスパイラル状に巻き、こ
の両端部ハ,ハをカツトすることにより、周面に
傾斜溝イを有する円筒状に加工する。尚、帯状板
ロ″をスパイラル状に巻いて円筒にする場合、帯
状板ロ″の両端部ハ,ハは第5図に示す如くフラ
ツトなままの状態にしておき、当該部分をカツト
する時、カツトが容易に行えるようにしてもよ
い。
FIGS. 3 to 6 are drawings for explaining a method of manufacturing a heating element B used in the above-mentioned thin film falling type evaporator. As shown in FIG. 3, this heating element B is made by forming an inclined groove A' on the surface of a flat plate R' by press working or roll processing, and then forming a flat plate R' having the inclined groove A' as shown in FIG. Either it is processed into a cylindrical shape as shown in Figure 5, or straight grooves extending in the longitudinal direction are formed on the surface of a long strip plate R' by press working or roll working, as shown in Figure 5. By winding this strip plate B'' having a straight groove A'' into a spiral shape as shown in Fig. 6 and cutting off both ends C and C, it is processed into a cylindrical shape having an inclined groove A on the circumferential surface. . In addition, when the strip plate R'' is wound into a cylinder in a spiral shape, both ends C and C of the strip plate R'' are kept flat as shown in Fig. 5, and when cutting the part, It may be possible to make the cutting easier.

上記構成からなる薄膜流下型蒸発器の加熱蒸気
導入筒24から加熱素子ロの内部に加熱用蒸気を
導入すると同時に、被加熱用流体供給筒26から
加熱素子ロの外周面上に被加熱素子を供給する
と、加熱用蒸気は加熱素子ロの内部を通過した
後、加熱素子ロの下部に接続された排出筒25を
通り外部に排出される。一方、被加熱用流体供給
筒26から加熱素子ロの外周面上端部に供給され
た被加熱用流体は、加熱素子ロの外周面に設けた
傾斜溝イに沿つて加熱素子ロの外周面上を旋回し
ながら流下して行く。そしてこの時、加熱素子ロ
の内部を流れる加熱用蒸気との間で熱交換が行わ
れ、被加熱用流体の一部が蒸発し、蒸発蒸気はシ
エル21の上端に設けた蒸発蒸気出口22から次
段の装置に送られる。又加熱素子ロの外周面から
蒸発しなかつた被加熱用流体は、加熱素子ロの下
端からシエル21の底部に落下し、シエル21の
底部に接続した濃縮液排出管23を通つて外部に
導出される。
In the thin film falling type evaporator having the above configuration, heating steam is introduced into the heating element B from the heated steam introduction tube 24, and at the same time, the heated element is introduced from the heated fluid supply tube 26 onto the outer peripheral surface of the heating element B. When supplied, the heating steam passes through the inside of the heating element RO, and then is discharged to the outside through the discharge tube 25 connected to the lower part of the heating element RO. On the other hand, the heated fluid supplied from the heated fluid supply tube 26 to the upper end of the outer circumferential surface of heating element B is applied onto the outer circumferential surface of heating element B along the inclined groove A provided on the outer circumferential surface of heating element B. It flows down while circling. At this time, heat exchange is performed with the heating steam flowing inside the heating element B, a part of the fluid to be heated is evaporated, and the evaporated steam is passed from the evaporative steam outlet 22 provided at the upper end of the shell 21. Sent to the next stage device. Further, the fluid to be heated that has not evaporated from the outer peripheral surface of heating element RO falls from the lower end of heating element RO to the bottom of shell 21 and is led out through the concentrated liquid discharge pipe 23 connected to the bottom of shell 21. be done.

第2図は本発明に係る薄膜流下型蒸発器の第2
の実施例を示す図面であり、この図に示す薄膜流
下型蒸発器は、両端が開口した円筒状をし、か
つ、その内周面及び外周面に、第1の実施例と同
じく所定の傾斜角を有する傾斜溝イを設けた加熱
素子ロと、この加熱素子ロを収納する両端が閉塞
した円筒状のシエル30とによつて構成されてい
る。上記シエル30の上端部には、加熱素子ロの
内周面から発生する蒸発蒸気をシエル30の外部
に導出するための蒸発蒸気出口31が設けてあ
り、シエル30の下端部には、加熱素子ロの内周
面で濃縮された濃縮液をシエル30の外部に導出
するための濃縮液排出筒32が接続してある。又
上記加熱素子ロはシエル30内の上部及び下部に
配置した仕切板33a,33bによつて支持され
ており、この仕切板33a,33bによつて加熱
素子ロの外周にリング状の密閉された空間34が
形成してある。又図中35は上記空間4内に加熱
用蒸気を供給するため、シエル30の上部周面に
設けた加熱蒸気導入口、36は空間34内に供給
された加熱蒸気をシエル30の外部に排出するた
め、シエル30の下部周面に設けた排出口、37
はシエル30内の上部に配置した仕切板33aの
上面に先端部が開孔した被加熱用流体供給筒であ
る。
FIG. 2 shows the second thin film falling type evaporator according to the present invention.
The thin film falling type evaporator shown in this figure has a cylindrical shape with both ends open, and has a predetermined slope on its inner and outer peripheral surfaces as in the first embodiment. It is composed of a heating element (b) provided with an inclined groove (a) having an angle, and a cylindrical shell (30) with both ends closed, which accommodates the heating element (b). An evaporative vapor outlet 31 is provided at the upper end of the shell 30 to lead out the evaporative vapor generated from the inner peripheral surface of the heating element RO to the outside of the shell 30. A concentrated liquid discharge pipe 32 is connected to the shell 30 for discharging the concentrated liquid concentrated on the inner peripheral surface of the shell 30 to the outside of the shell 30. The heating element B is supported by partition plates 33a and 33b arranged at the upper and lower parts of the shell 30, and a ring-shaped hermetic seal is formed around the outer periphery of the heating element B by the partition plates 33a and 33b. A space 34 is formed. Further, in the figure, 35 is a heating steam inlet provided on the upper peripheral surface of the shell 30 for supplying heating steam into the space 4, and 36 is a heating steam inlet provided in the upper peripheral surface of the shell 30 for discharging the heating steam supplied into the space 34 to the outside of the shell 30. In order to
1 is a heated fluid supply cylinder whose tip end is opened on the upper surface of a partition plate 33a disposed in the upper part of the shell 30.

上記構成からなる薄膜流下型蒸発器の加熱蒸気
導入口35から加熱素子ロの外周に設けた空間3
4内に加熱用蒸気を導入すると同時に、被加熱用
流体供給筒37から仕切板33aの上面に被加熱
用流体を供給すると、加熱用蒸気は加熱素子ロの
外周に設けた空間34を通過した後、シエル30
の下部周面に設けた排出口36から外部に排出さ
れる。一方、被加熱用流体供給筒37から仕切板
33aの上面に供給された被加熱用流体は、仕切
板33aの上面から加熱素子ロの内周面に流入
し、加熱素子ロの内周面に設けた傾斜溝イに沿つ
て加熱素子ロの内周面上を旋回しながら流下して
行く。そしてこの時、加熱素子ロの外周を流れる
加熱用蒸気との間で熱交換が行われ、被加熱用流
体の一部が蒸発し、蒸発蒸気は、シエル30の上
端に設けた蒸発蒸気出口31から次段の装置に送
られる。又加熱素子ロの内周面から蒸発しなかつ
た被加熱用流体は、加熱素子ロの下端からシエル
30の底部に落下し、シエル30の底部に接続し
た濃縮液排出筒32を通つて外部に導出される。
A space 3 provided from the heated steam inlet 35 to the outer periphery of the heating element B of the thin film falling type evaporator having the above configuration.
At the same time as the heating steam was introduced into the heating element 4, the heated fluid was supplied from the heated fluid supply cylinder 37 to the upper surface of the partition plate 33a, and the heating steam passed through the space 34 provided around the outer periphery of the heating element 4. After, Ciel 30
It is discharged to the outside from a discharge port 36 provided on the lower circumferential surface. On the other hand, the heated fluid supplied from the heated fluid supply cylinder 37 to the upper surface of the partition plate 33a flows from the upper surface of the partition plate 33a to the inner circumferential surface of heating element B, and flows into the inner circumferential surface of heating element B. It flows down the inner circumferential surface of the heating element B along the provided inclined groove A while turning around on the inner circumferential surface of the heating element B. At this time, heat exchange is performed with the heating steam flowing around the outer periphery of the heating element B, a part of the fluid to be heated is evaporated, and the evaporated steam is transferred to the evaporative steam outlet 31 provided at the upper end of the shell 30. from there to the next stage of equipment. The fluid to be heated that has not evaporated from the inner circumferential surface of the heating element RO falls from the lower end of the heating element RO to the bottom of the shell 30 and passes through the concentrate discharge pipe 32 connected to the bottom of the shell 30 to the outside. derived.

尚、上記2つの実施例は、シエル21,30内
に円筒状をした加熱素子ロを1つだけ収納した例
について説明したが、シエル21,30内には複
数本の加熱素子ロを収納し、各加熱素子ロの内周
面及び外周面に加熱用蒸気及び被加熱用流体を供
給してもよい。又、それぞれ径の異なる加熱素子
ロを複数本用意しておき、この加熱素子ロをシエ
ル21,30内に同心円状に配置し、各加熱素子
ロ間に形成される空間内に加熱用蒸気及び被加熱
用流体を交互に供給してもよい。又、シエル2
1,30の形状は、円筒形以外でもよい。
In the above two embodiments, only one cylindrical heating element B is housed in the shells 21 and 30, but a plurality of heating elements B may be housed in the shells 21 and 30. , heating steam and heated fluid may be supplied to the inner peripheral surface and outer peripheral surface of each heating element. In addition, a plurality of heating elements RO having different diameters are prepared, and the heating elements RO are arranged concentrically within the shells 21 and 30, and heating steam and heat are placed in the space formed between each heating element RO. The fluid to be heated may be supplied alternately. Also, Ciel 2
The shapes of 1 and 30 may be other than cylindrical.

発明の効果 上記した如く、シエル内に収納する加熱素子を
円筒状に形成し、かつ、その内周面及び外周面に
傾斜溝を設けておけば、加熱素子の全長を長くす
ることなく伝熱長を長くできる。従つて装置全体
の高さ方向の全長を短くでき、薄膜流下型蒸発器
の小型化が可能となる。又、加熱素子の周面に傾
斜溝を設けておけば、加熱素子の周面を被加熱用
流体が流下する時、被加熱用流体は傾斜溝に沿つ
て流下するため、液偏流が起こるのを防止でき
る。
Effects of the Invention As described above, if the heating element housed in the shell is formed into a cylindrical shape and inclined grooves are provided on the inner and outer peripheral surfaces, heat can be transferred without increasing the overall length of the heating element. You can make the length longer. Therefore, the total length of the entire device in the height direction can be shortened, and the thin film falling type evaporator can be downsized. Furthermore, if an inclined groove is provided on the circumferential surface of the heating element, when the heated fluid flows down the circumferential surface of the heating element, the heated fluid flows down along the inclined groove, which prevents liquid drift from occurring. can be prevented.

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

第1図は本発明に係る薄膜流下型蒸発器の第1
の実施例を示す部分断面図、第2図は第2の実施
例を示す部分断面図、第3図乃至第6図は本発明
に係る加熱素子の製造方法を説明するための説明
図、第7図は薄膜流下型蒸発器の従来例を示す斜
視図である。 イ……傾斜溝、ロ……加熱素子、21,30…
…シエル。
FIG. 1 shows a first example of a thin film falling type evaporator according to the present invention.
FIG. 2 is a partial sectional view showing the second embodiment; FIGS. 3 to 6 are explanatory views for explaining the method of manufacturing a heating element according to the present invention; FIG. 7 is a perspective view showing a conventional example of a thin film falling type evaporator. A... Slanted groove, B... Heating element, 21, 30...
...Ciel.

Claims (1)

【特許請求の範囲】[Claims] 1 円筒状をし、かつ、内周面及び外周面に傾斜
溝を有する加熱素子と、この加熱素子を収納する
シエルとからなり、上記シエル内に収納された加
熱素子の外周面と内周面とにそれぞれ2種類の流
体を供給することにより熱交換を行うことを特徴
とする薄膜流下型蒸発器。
1 Consisting of a heating element that is cylindrical and has inclined grooves on its inner and outer circumferential surfaces, and a shell that houses this heating element, the outer and inner circumferential surfaces of the heating element that are housed in the shell. A thin film falling type evaporator characterized in that heat exchange is performed by supplying two types of fluids to each.
JP12669485A 1985-06-11 1985-06-11 Thin film falling type evaporator Granted JPS61287401A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12669485A JPS61287401A (en) 1985-06-11 1985-06-11 Thin film falling type evaporator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12669485A JPS61287401A (en) 1985-06-11 1985-06-11 Thin film falling type evaporator

Publications (2)

Publication Number Publication Date
JPS61287401A JPS61287401A (en) 1986-12-17
JPH0454481B2 true JPH0454481B2 (en) 1992-08-31

Family

ID=14941533

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12669485A Granted JPS61287401A (en) 1985-06-11 1985-06-11 Thin film falling type evaporator

Country Status (1)

Country Link
JP (1) JPS61287401A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4932468A (en) * 1988-12-19 1990-06-12 E. L. Nickell Co., Inc. Vertical falling film multi-tube heat exchanger
JP6532193B2 (en) * 2014-05-20 2019-06-19 国立大学法人 東京大学 Surface flow down concentration apparatus and surface flow down concentration method

Also Published As

Publication number Publication date
JPS61287401A (en) 1986-12-17

Similar Documents

Publication Publication Date Title
US4434112A (en) Heat transfer surface with increased liquid to air evaporative heat exchange
US4249596A (en) Condenser and method of construction
US3854530A (en) Heat exchanger
JPH0221519B2 (en)
US1782409A (en) Heat exchanger
GB2058327A (en) Shell and tube type condenser with heat transfer
US4382465A (en) Cleaning arrangement for heat exchange tubes
JPH0454481B2 (en)
WO1989000669A1 (en) Shell and tube heat exchanger
JP2537981Y2 (en) Selective condenser
US4327801A (en) Cylindrical heat exchanger using heat pipes
CA1075677A (en) Header arrangement in a shell and tube heat exchanger
JPH0539990A (en) Heat transfer heat transfer pipe and compressed air dehumidifier
JP2714904B2 (en) Spiral heat exchanger
SU874085A1 (en) Film-type evaporative apparatus
JPH01244286A (en) Shell tube type heat exchanger
JP2604531Y2 (en) Heat exchanger structure
JP2972420B2 (en) Reboiler
JPS5812042Y2 (en) Netsukou Kanki
SU1366843A1 (en) Heat-exchanger
RU2080536C1 (en) Heat exchanger
SU1339388A1 (en) Heat exchanger
JPH0118161Y2 (en)
JPS6438469U (en)
JPS5885165U (en) Heat exchanger for liquid cooling

Legal Events

Date Code Title Description
LAPS Cancellation because of no payment of annual fees