JPH0211834B2 - - Google Patents

Info

Publication number
JPH0211834B2
JPH0211834B2 JP58188816A JP18881683A JPH0211834B2 JP H0211834 B2 JPH0211834 B2 JP H0211834B2 JP 58188816 A JP58188816 A JP 58188816A JP 18881683 A JP18881683 A JP 18881683A JP H0211834 B2 JPH0211834 B2 JP H0211834B2
Authority
JP
Japan
Prior art keywords
shell
outlet
passage
steam
liquid
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 - Lifetime
Application number
JP58188816A
Other languages
Japanese (ja)
Other versions
JPS6080082A (en
Inventor
Hiroyuki Sumitomo
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 JP18881683A priority Critical patent/JPS6080082A/en
Publication of JPS6080082A publication Critical patent/JPS6080082A/en
Publication of JPH0211834B2 publication Critical patent/JPH0211834B2/ja
Granted 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
    • F28D9/00Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D9/0031Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other
    • F28D9/0043Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other the plates having openings therein for circulation of at least one heat-exchange medium from one conduit to another
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28CHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA COME INTO DIRECT CONTACT WITHOUT CHEMICAL INTERACTION
    • F28C3/00Other direct-contact heat-exchange apparatus
    • F28C3/06Other direct-contact heat-exchange apparatus the heat-exchange media being a liquid and a gas or vapour
    • F28C3/08Other direct-contact heat-exchange apparatus the heat-exchange media being a liquid and a gas or vapour with change of state, e.g. absorption, evaporation, condensation
    • 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
    • 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
    • F28D3/00Heat-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 flows in a continuous film, or trickles freely, over the conduits

Description

【発明の詳細な説明】 イ 技術分野 この発明は、互いに掌合して相互間に交互の通
路を形成する複数のプレートを有し、一方の通路
に蒸発すべき液体を送給するとともに他方の通路
に加熱流体を送給することにより、液体を蒸発せ
しめるようにしたプレート式蒸発器に関する。
Detailed Description of the Invention A. Technical Field The present invention has a plurality of plates that face each other to form alternating passages between them. The present invention relates to a plate-type evaporator that evaporates liquid by supplying heating fluid to a passage.

ロ 従来技術 この種の蒸発器としては従来より、自然循環式
あるいはせき式などといつたものがあり、それぞ
れ実用に供されている。しかし、近年のエネルギ
ー事情の下でヒートポンプ等の用に供する場合を
考慮すると、これらの従来装置は満足し得るもの
はない。すなわち、自然循環式の場合、溶液の比
重がプロセスの進行に伴つて増大するため液深に
よつて蒸発しにくいという点が指摘されるし、ま
た、せき式の場合、流下液膜を長くとる必要があ
るため蒸発器全体の高さが非常に高くなり、液循
環用のポンプ動力の上昇は避けられない。したが
つて、また、蒸発器自体のコストもさることなが
ら、配管や架台等に多大の費用を要するといつた
欠点を有する。
B. Prior art This type of evaporator has conventionally been of the natural circulation type or the weir type, each of which has been put to practical use. However, considering the use of heat pumps and the like under recent energy conditions, none of these conventional devices are satisfactory. In other words, in the case of the natural circulation type, it is pointed out that the specific gravity of the solution increases as the process progresses, making it difficult to evaporate depending on the liquid depth, and in the case of the weir type, the falling liquid film is long. As a result, the height of the entire evaporator becomes very high, and an increase in pump power for liquid circulation is unavoidable. Therefore, the evaporator itself has the disadvantage that not only the cost of the evaporator itself is high, but also that a large amount of money is required for the piping, the frame, and the like.

ハ 発明の目的 この発明は上に述べたごとき従来の欠点を解消
し得る構造のプレート式蒸発器を堤供せんとする
ものである。すなわち、この発明の主たる目的は
小さなポンプ動力で所期の能力を発揮し得る経済
的なプレート式蒸発器を提供することである。
C. Purpose of the Invention The present invention aims to provide a plate-type evaporator having a structure that can eliminate the conventional drawbacks as described above. That is, the main object of the present invention is to provide an economical plate-type evaporator that can exhibit desired performance with a small pump power.

ニ 発明の構成 かかる目的を達成するために、この発明のプレ
ート式蒸発器は、上部に蒸気排出口2を備えると
ともに下部に濃縮液排出口3を備え、かつ、加熱
流体の供給口4ならびに排出口5を備えやシエル
1;シエル1内に収容され、ガスケツト13,1
1〜143を介して互いに掌合して相互間に、上
部、両側部ならびに下部における開口151〜1
4にてシエル1の内部空間Cと連絡する一方、
加熱流体の供給口4ならびに排出口5に対して閉
塞した第1の通路Bと、シエル1の内部空間Cに
対して閉塞するとともに加熱流体の供給口4なら
びに排出口5を連絡する第2の通路Aとを交互に
形成する、鉛直に延在する伝熱長さの短い複速の
プレート9;第1の通路Bの上部および側部の開
口151〜154から通路内方に向けて蒸発すべき
液体を噴射するための多段に配置したノズル16
群;シエル1の内部でかつプレート9の外側に画
成された蒸気導出空間D;および濃縮液排出口3
からノズル16へ通ずる管路18に接続した液循
環ポンプ19;を包含する。
D. Structure of the Invention In order to achieve the above object, the plate type evaporator of the present invention is provided with a steam outlet 2 at the upper part, a concentrated liquid outlet 3 at the lower part, and a heating fluid supply port 4 and a discharge outlet. Shell 1 with outlet 5; housed within shell 1 and with gaskets 13,1
Openings 15 1 to 1 in the upper part, both sides, and the lower part are placed between the palms of the palms through 4 1 to 14 3 .
While communicating with the internal space C of Ciel 1 at 5 4 ,
A first passage B is closed to the heating fluid supply port 4 and the discharge port 5, and a second passage B is closed to the internal space C of the shell 1 and communicates the heating fluid supply port 4 and the discharge port 5. vertically extending multi-speed plates 9 with short heat transfer lengths forming alternating passages A; from openings 15 1 to 15 4 at the top and side of the first passage B toward the inside of the passage; Nozzles 16 arranged in multiple stages for spraying liquid to be evaporated
group; a vapor derivation space D defined inside the shell 1 and outside the plate 9; and a concentrate outlet 3
a liquid circulation pump 19 connected to a conduit 18 leading from the nozzle 16 to the nozzle 16;

ホ 発明の作用 ノズル16から第1の通路B内に噴射された液
体はプレート1の伝熱面上を薄膜状に落下し、そ
の際隣位の第2の通路A内を流れる加熱流体より
熱を奪つて蒸発する。生成した蒸発は下方の開口
154から蒸発導出空間Dを経て上方の蒸気排出
口2へ向かう。
E. Effect of the Invention The liquid injected into the first passage B from the nozzle 16 falls on the heat transfer surface of the plate 1 in the form of a thin film, and at this time, the liquid is heated by the heated fluid flowing in the adjacent second passage A. It takes away and evaporates. The generated evaporation flows from the lower opening 154 through the evaporation outlet space D to the upper steam outlet 2.

未蒸発の液体つまり濃縮液は液循環ポンプ19
により、濃縮液排出口3からノズル16へ循環せ
しめられる。
The unevaporated liquid, that is, the concentrated liquid, is sent to the liquid circulation pump 19.
As a result, the concentrated liquid is circulated from the concentrate outlet 3 to the nozzle 16.

ヘ 発明の効果 この発明によれば、比較的短い伝熱長さのプレ
ートを使用し、しかも、伝熱面上に薄い膜を形成
するように液を噴射するのであるから、濃縮液の
循環流量が少なく、したがつて循環ポンプの動力
節減を図ることができる。これに加えて大掛かり
な架台等を要しないこともコスト低減に寄与す
る。かくして省エネルギーに対する要求に応え得
る経済的なプレート式蒸発器を提供することがで
きる。
F. Effects of the Invention According to this invention, since a plate with a relatively short heat transfer length is used and the liquid is injected so as to form a thin film on the heat transfer surface, the circulating flow rate of the concentrated liquid is Therefore, the power of the circulation pump can be reduced. In addition to this, not requiring a large frame etc. also contributes to cost reduction. In this way, it is possible to provide an economical plate-type evaporator that can meet the demand for energy conservation.

また、この発明のプレート式蒸発器は、生成し
た蒸気を蒸気導出空間を介して下方から上方へ概
ねU字状に導いて排出する構成であるため、蒸気
からミストを効果的に分離せしめることができ
る。
Furthermore, since the plate-type evaporator of the present invention is configured to guide and discharge the generated steam from the bottom to the top in a generally U-shape through the steam outlet space, it is possible to effectively separate mist from the steam. can.

さらに、また、ノズルから噴射された液体が、
既に生成している蒸気と直接接触することによ
り、伝熱面に流下液膜をつくるだけの場合に比べ
て蒸発が促進される。なお、上部および側部の開
口から通路内方へ向けて液を噴射するので、シー
ル効果を得られ、生成した蒸気が流れに逆らつて
通路外へ逃げるのを防止して、すばやく下部の開
口へ導くことができる。
Furthermore, the liquid sprayed from the nozzle
Direct contact with already formed vapor accelerates evaporation compared to simply creating a falling film on the heat transfer surface. In addition, since the liquid is injected inward from the openings at the top and side, a sealing effect is achieved, preventing the generated steam from escaping out of the passage against the flow, and quickly filling the opening at the bottom. can lead to.

ト 実施例 以下、図面に示すこの発明の実施例について述
べる。
G. Embodiments Hereinafter, embodiments of the present invention shown in the drawings will be described.

まず第1図を参照すると、シエル1は水平方向
に延伸する楕円形断面の筒状を呈しており、上部
に蒸気排出口2を備え、下部に濃縮液排出口3を
備えている。加熱流体の供給口4ならびに排出口
5はシエル1の端面6に設けてある。シエル1の
他端は参照番号7で示すように開口しており、端
板8をフランジ止めすることにより開塞されてい
る。
First, referring to FIG. 1, the shell 1 has a cylindrical shape with an oval cross section extending in the horizontal direction, and is provided with a steam outlet 2 at the upper part and a concentrated liquid outlet 3 at the lower part. A heating fluid supply port 4 and a discharge port 5 are provided on the end face 6 of the shell 1. The other end of the shell 1 is open as indicated by reference numeral 7, and is closed by flanging an end plate 8.

複数のブレート9がシエル1と移動フレーム1
0との間にボルト等の締付け手段により緊締され
ている。各プレート9は第2図からわかるように
略矩形であつて、伝熱長さの短い(好ましくは4
m以下)伝熱面を備えるとともに、加熱流体の流
過を許容する通孔11,12を有する。プレート
9は鉛直に延在し、互いに掌合した状態では総て
の通孔11および12が各々整列し、通孔11は
加熱流体の供給口4と、また通孔12は加熱流体
の排出口5と連通する。
Multiple plates 9 move Ciel 1 and moving frame 1
0 by tightening means such as bolts. As can be seen from FIG. 2, each plate 9 is approximately rectangular and has a short heat transfer length (preferably 4
m or less) and has a heat transfer surface and through holes 11 and 12 that allow the heating fluid to flow therethrough. The plate 9 extends vertically, and in the palm-to-palm state, all the through holes 11 and 12 are aligned respectively, the through hole 11 serving as the heating fluid supply port 4, and the through hole 12 serving as the heating fluid discharge port. Connects with 5.

これら複数のプレート9がガスケツトを介して
互いに掌合することにより、プレート相互間に交
互の通路A,Bが形成される。さらに詳しく述べ
ると、第3図からよくわかるように、加熱流体の
通路Aは、プレート9の外周に沿つて延伸するガ
スケツト13によつてシエル1の内部空間Cに対
して閉塞される一方、通孔11,12と、したが
つて、また、加熱流体の供給口4ならびに排出口
5を連絡する。蒸発すべき液体の通路Bは、部分
的に切除されたガスケツト141〜143によつ通
孔11,12とは断絶する一方、ガスケツトの切
除部分すなわち上部、両側部、および下部の開口
151〜154を通じてシエル1の内部空間と連絡
している。
When these plurality of plates 9 come into contact with each other via gaskets, alternate passages A and B are formed between the plates. More specifically, as can be clearly seen from FIG. The holes 11, 12 and thus also the supply inlet 4 as well as the outlet 5 of the heating fluid communicate. The passage B of the liquid to be evaporated is separated from the through holes 11, 12 by partially cut out gaskets 14 1 to 14 3 , while the cut out parts of the gaskets, i.e. the openings 15 at the top, sides and bottom. It communicates with the internal space of Ciel 1 through 1 to 15 4 .

蒸発すべき液体を各通路B内へ噴射するための
ノズル16群を配設したヘツダー17が各々、通
路Bの上部の開口151ならびに側部の開口15
,153にノズル16をませるごとく位置する。
図示例では、ノズル群は3段に設けてあるが、必
要に応じて2段もしくは4段以上設けてもよい。
濃縮液排出口3からヘツダー17へ通ずる管路1
8には液循環ポンプ19を接続してある。液循環
ポンプ19の吐出側の管路部分には、濃縮液の取
出管20と、さらに、蒸発すべき液体の補給管2
1が接続されている。
A header 17 in which a group of nozzles 16 for injecting the liquid to be evaporated into each passage B is provided in each passage B.
2 and 15 3 so that the nozzle 16 is placed between them.
In the illustrated example, the nozzle groups are provided in three stages, but two or four or more stages may be provided as necessary.
Pipe line 1 leading from concentrate outlet 3 to header 17
8 is connected to a liquid circulation pump 19. In the discharge side pipe section of the liquid circulation pump 19, there is a take-out pipe 20 for the concentrated liquid and a replenishment pipe 2 for the liquid to be evaporated.
1 is connected.

シエル1の内部には、ブレート1が占める部分
の外に、通路B内で生成した蒸気の導出ならびに
ミスト分離のために機能する蒸気導出空間Dが画
成されている。なお、この蒸気導出空間は、図示
のごとく筒形のシエル1の軸線方向の一部分に画
成するほか、軸線に垂直な断面(第2図)におけ
るプレート1の両側に画成することもできる。2
2は蒸気排出口2に取り付けた通常のデミスター
である。
Inside the shell 1, in addition to the portion occupied by the plate 1, a steam derivation space D is defined, which functions for deriving the steam generated in the passage B and separating mist. In addition to being defined in a portion of the cylindrical shell 1 in the axial direction as shown in the figure, the steam outlet space can also be defined on both sides of the plate 1 in a cross section perpendicular to the axis (FIG. 2). 2
2 is a normal demister attached to the steam outlet 2.

次に上述のごとき構成のプレート式蒸発器にお
ける作用について述べる。
Next, the operation of the plate type evaporator constructed as described above will be described.

シエル1に設けた供給口4から供給される加熱
流体は第3図において実線で示すように、通孔1
1から改通路Aへ流入し、通孔12から流出して
排出口5へ至る。
The heating fluid supplied from the supply port 4 provided in the shell 1 is supplied to the through hole 1 as shown by the solid line in FIG.
1 into the new passageway A, flows out through the through hole 12 and reaches the outlet 5.

蒸気すばき液体は、第3図において破線で示す
ように、ノズル16から通路B内へ噴射され通路
Bに面するプレート1の伝熱面上を薄膜状に流下
する。
The vaporized liquid is injected from the nozzle 16 into the passage B and flows down in a thin film over the heat transfer surface of the plate 1 facing the passage B, as shown by the broken line in FIG.

その際、隣位の通路Aが流れる加熱流体による
加熱により、蒸気が発生する。未蒸発液体つまり
濃縮液は通路Bの下部の開口154からシエル1
の底部へ落下し、液循環ポンプ20によつて排出
口3から管路18を通つてヘツダー17へ循環せ
しめられる。濃縮液は取出管20から適宜取り出
され、また、それに応じて、あるいはそれとは独
立して一定の、新たな蒸気すべき液体が補給管2
1より供給される。
At this time, steam is generated due to heating by the heating fluid flowing through the adjacent passage A. The unevaporated liquid, that is, the concentrated liquid, is transferred from the opening 154 at the bottom of passage B to shell 1.
The liquid drops to the bottom of the tank and is circulated from the outlet 3 through the pipe 18 to the header 17 by the liquid circulation pump 20. The concentrated liquid is taken out from the take-out pipe 20 as appropriate, and a certain amount of new liquid to be vaporized is accordingly or independently taken out from the supply pipe 20.
1.

通路B内で生成した蒸発は、第1図および第3
図において鎖線で示すように通路Bの下部の開口
154から一旦蒸気導出空間Dへ向かつて流出し、
しかる後蒸気排出口2へ向かう。この間、蒸気は
概ねU字形の通路をたどるが、下方の開口154
から上方の蒸気排出口2へと方向転換する際、第
1図において破線で示すように、ミストは蒸気よ
り分離してシエル1の底部に沈滞する。なおも蒸
気中に混在するミスト等があれば、デミスター2
2にて捕捉される。
The evaporation generated in passage B is shown in Figures 1 and 3.
As shown by the chain line in the figure, the steam flows out from the opening 154 at the bottom of the passage B to the steam derivation space D.
After that, it heads to the steam outlet 2. During this time, the steam follows a generally U-shaped path, with the lower opening 15 4
When changing direction from the steam outlet 2 to the upper steam outlet 2, the mist is separated from the steam and settles at the bottom of the shell 1, as shown by the broken line in FIG. If there is still mist mixed in the steam, remove the demister 2.
Captured at 2.

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

図面はこの発明のプレート式蒸発器の一実施例
を示すもので、第1図は模式的縦断面図、第2図
は第1図の−線に沿う横断面図、第3図はプ
レートの重合要領および流通状態を示す分解斜視
図である。 1……シエル、2……蒸気排出口、3……濃縮
液排出口、4……加熱流体供給口、5……加熱流
体排出口、9……プレート、11,12……通
孔、13,141〜143……ガスケツト、151
〜154……開口、16……ノズル、18……管
路、19……液循環ポンプ、A……加熱流体の通
路、B……蒸気すべき液体の通路。
The drawings show an embodiment of the plate-type evaporator of the present invention, in which Fig. 1 is a schematic longitudinal cross-sectional view, Fig. 2 is a cross-sectional view taken along the - line in Fig. 1, and Fig. 3 is a cross-sectional view of the plate. FIG. 3 is an exploded perspective view showing the polymerization procedure and distribution state. DESCRIPTION OF SYMBOLS 1... Shell, 2... Steam outlet, 3... Concentrated liquid outlet, 4... Heating fluid supply port, 5... Heating fluid outlet, 9... Plate, 11, 12... Through hole, 13 , 14 1 ~ 14 3 ...Gasket, 15 1
~15 4 ...Opening, 16...Nozzle, 18...Pipe line, 19...Liquid circulation pump, A...Passway for heated fluid, B...Passway for liquid to be vaporized.

Claims (1)

【特許請求の範囲】[Claims] 1 上部に蒸気排出口を備えるとともに下部に濃
縮液排出口を備え、かつ、加熱流体の供給口なら
びに排出口を備えたシエル:該シエル内に収容さ
れ、ガスケツトを介して互いに掌合して相互間に
上部、両側部ならびに下部における開口にて前記
シエルの内部空間と連絡する一方、前記加熱流体
の供給口ならびに排出口に対して閉塞した第1の
通路と、前記シエルの内部空間に対して閉塞する
とともに前記加熱流体の供給口ならびに排出口と
連絡する第2の通路とを交互に形成する、鉛直に
延在する伝熱長さの短い複数のプレート;前記第
1の通路の上部および側部の開口から通路内方に
向けて蒸発すべき液体を噴射するための多段に配
置したノズル群;前記シエルの内部でかつ前記プ
レートの外側に画成された蒸気導出空間;および
前記濃縮液排出口から前記ノズル群へ通ずる管路
に接続した液循環ポンプ;を包含してなり、而し
て前記第1の通路内で生成した蒸気を前記第1の
通路の下部の開口から前記蒸気導出空間を経て前
記蒸気排出口から取り出すようにしたことを特徴
とするプレート式蒸発器。
1. A shell that is equipped with a steam outlet in the upper part, a concentrated liquid outlet in the lower part, and a heating fluid supply inlet and an outlet; a first passage that communicates with the internal space of the shell through openings at the top, both sides, and the bottom, and is closed to the heating fluid supply and discharge ports, and to the internal space of the shell; a plurality of vertically extending plates with short heat transfer lengths that alternately form second passages that are closed and communicate with the supply and discharge ports of the heating fluid; an upper portion and a side of the first passage; a group of nozzles arranged in multiple stages for injecting the liquid to be evaporated inward from the opening of the shell; a vapor lead-out space defined inside the shell and outside the plate; and the concentrated liquid discharge space. a liquid circulation pump connected to a pipe line leading from the outlet to the nozzle group; and the steam generated in the first passage is transferred from the opening in the lower part of the first passage to the steam extraction space. A plate type evaporator, characterized in that the steam is taken out through the steam outlet.
JP18881683A 1983-10-08 1983-10-08 Plate type evaporator Granted JPS6080082A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18881683A JPS6080082A (en) 1983-10-08 1983-10-08 Plate type evaporator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18881683A JPS6080082A (en) 1983-10-08 1983-10-08 Plate type evaporator

Publications (2)

Publication Number Publication Date
JPS6080082A JPS6080082A (en) 1985-05-07
JPH0211834B2 true JPH0211834B2 (en) 1990-03-15

Family

ID=16230313

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18881683A Granted JPS6080082A (en) 1983-10-08 1983-10-08 Plate type evaporator

Country Status (1)

Country Link
JP (1) JPS6080082A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4914064A (en) * 1987-10-14 1990-04-03 Exxon Research And Engineering Company Highly aromatic polyurea/urethane membranes and their use for the separation of aromatics from non-aromatics
US5055632A (en) * 1987-10-14 1991-10-08 Exxon Research & Engineering Company Highly aromatic polyurea/urethane membranes and their use for the separation of aromatics from non-aromatics
JP6516435B2 (en) * 2014-10-23 2019-05-22 株式会社アイホー Cooking device

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5538413A (en) * 1978-09-08 1980-03-17 Rosenblad Corp Method of selective condensation of vapor contaminated by volatile substance and dropped film heat exchanger and apparatus for excecuting same method

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5538413A (en) * 1978-09-08 1980-03-17 Rosenblad Corp Method of selective condensation of vapor contaminated by volatile substance and dropped film heat exchanger and apparatus for excecuting same method

Also Published As

Publication number Publication date
JPS6080082A (en) 1985-05-07

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