JPS6080082A - Plate type evaporator - Google Patents
Plate type evaporatorInfo
- Publication number
- JPS6080082A JPS6080082A JP18881683A JP18881683A JPS6080082A JP S6080082 A JPS6080082 A JP S6080082A JP 18881683 A JP18881683 A JP 18881683A JP 18881683 A JP18881683 A JP 18881683A JP S6080082 A JPS6080082 A JP S6080082A
- Authority
- JP
- Japan
- Prior art keywords
- liquid
- passage
- steam
- heat
- shell
- 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.)
- Granted
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D9/00—Heat-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
- F28D9/0031—Heat-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
- F28D9/0043—Heat-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
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28C—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA COME INTO DIRECT CONTACT WITHOUT CHEMICAL INTERACTION
- F28C3/00—Other direct-contact heat-exchange apparatus
- F28C3/06—Other direct-contact heat-exchange apparatus the heat-exchange media being a liquid and a gas or vapour
- F28C3/08—Other 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
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D1/00—Heat-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
- F28D1/02—Heat-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
- F28D1/04—Heat-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
- F28D1/053—Heat-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
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D3/00—Heat-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
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
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, and a liquid to be evaporated is fed to one passage, and a liquid to be evaporated is fed to the other. The present invention relates to a plate-type evaporator that evaporates liquid by supplying heating fluid to the passages of the plate.
口、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
せき式などといったものがあり、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(2)
し得るものではない。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って増大するため液深に
よっ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。したがって、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
要するといった欠点を有する。BACKGROUND OF THE INVENTION 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, these conventional devices are not satisfactory (2). 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, it is necessary to have a long falling liquid film. As a result, the height of the entire evaporator becomes extremely high, and an increase in pump power for liquid circulation is unavoidable. Therefore, it also has the disadvantage that not only the cost of the evaporator itself is high, but also a large amount of cost is required for piping, a frame, etc.
ハ0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提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。OBJECT OF THE INVENTION The present invention aims to provide a plate-type evaporator having a structure that can overcome the above-mentioned drawbacks of the prior art. 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.
二0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(3)
え、かつ、加熱流体の供給口(4)ならびに排出口(5
)を備えたシェル(1) ;シェル(1)内に収容され
、ガスケント(13) (14,〜143)を介し互い
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(151〜154)にてシェル(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、
シェル(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)と連絡
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数のプレー) (9)i第1の通
路(B)の上部および側部の開口(14,〜143)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;シェル(1)の内部で
かつプレート(1)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)
iを包含する。20 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) in the upper part and a concentrated liquid outlet (3) in the lower part, and , heating fluid supply port (4) and discharge port (5)
); housed within the shell (1) and having openings (151 to 151) in the upper part, both sides and the lower part; a first passage (B) that communicates with the internal space (C) of the shell (1) at 154) and is closed to the heating fluid supply port (4) and the discharge port (5);
Vertically extending passages that close the internal space (C) of the shell (1) and alternately form second passages (A) communicating with the heating fluid supply port (4) and the discharge port (5). (9) i Inject the liquid to be evaporated inward from the openings (14, to 143) at the top and side of the first passage (B). a group of nozzles (16) arranged in multiple stages for
D); and from the concentrate outlet (3) to the nozzle (16)
A liquid circulation pump (19) connected to a pipe (18) leading to
includes i.
(4)
ホ0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流下し、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
奪って蒸発する。生成した蒸気は下方の開口(15斗)
から蒸気導出空間(D)を経て上方の蒸気排出口(2)
へ向かう。(4) The liquid injected from the nozzle (16) into the first passage (B) flows down on the heat transfer surface of the plate (1) in the form of a thin film. It evaporates by taking heat from the heating fluid flowing in the passage (A). The generated steam is released through the downward opening (15 to)
From the upper steam outlet (2) through the steam derivation space (D)
Head to.
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(1B)へ循環せし
められる。The unevaporated liquid, that is, the concentrated liquid, is circulated from the concentrated liquid outlet (3) to the nozzle (1B) by the liquid circulation pump (19).
へ0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
たがっ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(5)
供することができる。Effects of the Invention According to this invention, a plate with a relatively short heat transfer length is used, and the liquid is injected to form a thin film on the heat transfer surface, so that the circulation of the concentrated liquid is improved. The flow rate is small, and therefore the power of the circulation pump can be saved. 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 (5) 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
に逆らっ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 direct contact of the liquid injected from the nozzle with the already generated vapor accelerates evaporation compared to simply creating a falling liquid film on the heat transfer surface. Furthermore, since the liquid is injected from the top and side openings toward the inside of the passage, a sealing effect is achieved, preventing the generated steam from escaping out of the passage against the flow, and allowing it to quickly flow into the bottom opening. can lead.
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。Examples Embodiments of the invention shown in the drawings will be described below.
まず第1図を参照すると、シェル(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(6)
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)はシェル(1)の端面(6)に
設けである。シェル(1)の他端は参照番号7で指すよ
うに開口しており、端板(8)をフランジ止めすること
により閉塞されている。First, referring to Figure 1, the shell (1) has a cylindrical shape with an elliptical cross section extending in the horizontal direction, with a steam outlet (2) at the top and a concentrated liquid outlet (6) at the bottom. (3). Heating fluid supply port (4
) as well as the outlet (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 the end plate (8).
複数のプレート(9)がシェル(1)と移動フレーム(
10)との間にボルト等の締付は手段により緊締されて
いる。各プレート(9)は第2図かられかるように略矩
形であって、伝熱長さの短い(好ましくは4m以下)伝
熱面を備えるとともに、加熱流体の流通を許容する通孔
(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)
#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)と連通ずる。A plurality of plates (9) connect the shell (1) and the moving frame (
10) A bolt or the like is tightened by a means. As shown in FIG. 2, each plate (9) is approximately rectangular and has a heat transfer surface with a short heat transfer length (preferably 4 m or less) and through holes (11 ) (12). The plates (9) extend vertically, and in the state where their palms touch each other, all the through holes (11)
# and (12) are aligned, and the through hole (11) communicates with the heating fluid supply port (4), and the through hole (12) communicates with the heating fluid outlet (5).
これら複数のプレート(9)がガスケットを介して互い
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。These plurality of plates (9) come into contact with each other via gaskets, so that alternate passages (
A) (B) is formed.
(7)
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)の外周に沿っ
て延伸するガスケット(13)によってシェル(1)の
内部空間(C)に対しては閉塞される一方、通孔(11
) (12)と、したがって、また、加熱流体の供給口
(4)ならびに排出口(5)と連絡する。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) (
14,〜143)により通孔(11) (12)とは断
絶する一方、ガスケットの切除部分すなわち上部、両側
部、および下部の開口(15,〜154)を通じてシェ
ル(1)の内部空間(C)と連絡している。(7) To explain in more detail, as can be clearly seen from Figure 3,
The heating fluid passage (A) is closed off to the internal space (C) of the shell (1) by a gasket (13) extending along the outer periphery of the plate (9), while the through hole (11
) (12) and therefore also with the supply (4) and the discharge (5) of the heating fluid. The passage (B) for the liquid to be evaporated is a partially cut out gasket) (
The internal space (C ) are in contact.
蒸気すべき液体を各通路(B)内へ噴射するためのノズ
ル(16)群を配設したヘッダー(17)が各々、通路
(B)の上部の開口(15,)ならびに側部の開口(1
5,) (153)にノズル(16)を臨ませるごとく
位置する。図示例ではノズル群は3段に設けであるが、
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(8)
(3)からヘッダー(17)へ通ずる管路(18)には
液循環ポンプ(19)を接続しである。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(21)が接続
されている。A header (17) equipped with a group of nozzles (16) for injecting the liquid to be vaporized into each passage (B) each has an opening (15,) at the top of the passage (B) as well as an opening at the side ( 1
5,) (153) is located so that the nozzle (16) is facing. In the illustrated example, the nozzle group is provided in three stages, but
A liquid circulation pump (19) is connected to the conduit (18) leading from the concentrate outlet (8) (3) to the header (17), which may be provided in two or four or more stages as necessary. . Liquid circulation pump (
19), there is a concentrate take-out pipe (20
) is further connected to a supply pipe (21) for the liquid to be evaporated.
シェル(1)の内部には、プレート(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、図示例のごとく
筒形のシェル(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。 (22)は蒸気排出
口(2)に取り付けた通常のデミスタ−である。Inside the shell (1), outside the area occupied by the plate (1), a steam outlet space (D) is defined which functions for the outlet of the steam generated in the passageway (B) and for mist separation. There is. The steam outlet space is defined not only in a part of the cylindrical shell (1) in the axial direction as shown in the figure, but also in the plate (1) in the cross section perpendicular to the axis (Fig. 2).
It can also be defined on both sides. (22) 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.
シェル(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(11)
から各通路(A)へ流入し、(9)
通孔(12)から流出して排出口(5)へ至る。The heating fluid is supplied from the supply port (4) provided in the shell (1) through the through hole (11) as shown by the solid line in FIG.
It flows into each passage (A) from (9) and flows out from the through hole (12) to reach the discharge port (5).
蒸気すべき液体は、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 liquid to be vaporized is as shown by the broken line in FIG.
Injected from the nozzle (16) into the passage (B)
It flows down in a thin film on the heat transfer surface of the plate (1) facing.
その際、隣位の通路(A)を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)からシェル(1)の底
部へ落下し、液循環ポンプ(20)によって排出口(3
)から管路(18)を通ってヘッダー(17)へ循環せ
しめられる。At this time, steam is generated by heating by the heating fluid flowing through the adjacent passage (A). The unevaporated liquid, that is, the concentrated liquid, falls from the lower opening (154) of the passageway (B) to the bottom of the shell (1), and is removed by the liquid circulation pump (20) to the outlet (3).
) is circulated through line (18) to header (17).
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
蒸発すべき液体が補給管(21)より供給される。The concentrated liquid is taken out from the withdrawal pipe (20) as appropriate, and a certain amount of new liquid to be evaporated is supplied from the replenishment pipe (21) accordingly or independently.
通路(B)内で生成した蒸気は、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(1
54)から一旦蒸気導出空間(D)へ向かって流出し、
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(lO)
進路をたどるが、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ェル(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−(22)にて捕捉される。The steam generated in the passage (B) flows through the opening (1
54) once flows out toward the steam derivation space (D),
The steam then heads towards the steam outlet (2), during which it follows a generally U-shaped (lO) path, but when changing direction from the lower opening (154) to the upper steam outlet (2), the As shown by the broken line in Figure 1, the mist separates from the steam and forms a shell (1).
stagnates at the bottom. If there is still mist mixed in the steam, it will be captured by the demister (22).
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n−
n線に沿う横断面図、第3図はプレートの重合要領およ
び流体の流通状態を示す分解斜視図である。
(1)−・−シェル、(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) (14,〜143)・−
・・ガスケット、(151〜15+) −関口、(16
) −・ノズル、(1B) −管路、(19) −−−
−一液循環ポンプ、(A)−・加熱流体の通路、(B)
・−蒸発すべき液体の通路。
(11)
第1図The drawings show an embodiment of the plate type evaporator of the present invention, in which FIG. 1 is a schematic vertical sectional view, and FIG.
FIG. 3 is an exploded perspective view showing how the plates overlap and the state of fluid flow. (1)--shell, (2')-steam outlet, (3)
-・Concentrate discharge port, (4) -Heating fluid supply port, (5)
- Heated fluid outlet, (9) - Plate, (11)
(12) - through hole, (13) (14,~143)・-
... Gasket, (151~15+) - Sekiguchi, (16
) - Nozzle, (1B) - Pipeline, (19) ---
- One-liquid circulation pump, (A) - Heating fluid passage, (B)
- Pathway for the liquid to be evaporated. (11) Figure 1
Claims (1)
液排出口を備え、かつ、加熱流体の供給口ならびに排出
口を備えたシェル;該シェル内に収容され、ガスケット
を介して互いに掌合して相互間に上部、両側部なdびに
下部における開口にて前記シェ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、前記シェ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;前記シェ
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(1) 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; a plurality of vertically extending plates with short heat transfer lengths that close the space and alternately form second passages communicating with the supply port and the discharge port of the heating fluid; the first passage; a group of nozzles arranged in multiple stages for injecting liquid to be evaporated inward from the upper and side openings of the passageway; a vapor extraction space defined inside the shell and outside the plate; and The concentrated liquid (1) includes a liquid circulation pump connected to a pipe line leading from the discharge port to the nozzle group, and the vapor generated in the first passage is sent to the lower part of the first passage. 1. A plate type evaporator, characterized in that the steam is taken out from the opening through the steam outlet space and through the steam exhaust port.
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 true JPS6080082A (en) | 1985-05-07 |
JPH0211834B2 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) |
Cited By (3)
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 |
JP2016084949A (en) * | 2014-10-23 | 2016-05-19 | 株式会社アイホー | Heating cooking device |
Citations (1)
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 |
-
1983
- 1983-10-08 JP JP18881683A patent/JPS6080082A/en active Granted
Patent Citations (1)
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 |
Cited By (3)
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 |
JP2016084949A (en) * | 2014-10-23 | 2016-05-19 | 株式会社アイホー | Heating cooking device |
Also Published As
Publication number | Publication date |
---|---|
JPH0211834B2 (en) | 1990-03-15 |
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