JPH06254534A - Vacuum-evaporation water generator - Google Patents

Vacuum-evaporation water generator

Info

Publication number
JPH06254534A
JPH06254534A JP4273593A JP4273593A JPH06254534A JP H06254534 A JPH06254534 A JP H06254534A JP 4273593 A JP4273593 A JP 4273593A JP 4273593 A JP4273593 A JP 4273593A JP H06254534 A JPH06254534 A JP H06254534A
Authority
JP
Japan
Prior art keywords
chamber
seawater
vacuum evaporation
condenser
water supply
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
Application number
JP4273593A
Other languages
Japanese (ja)
Other versions
JP3183986B2 (en
Inventor
Hideharu Miyata
秀晴 宮田
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.)
Sasakura Engineering Co Ltd
Original Assignee
Sasakura Engineering Co 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 Sasakura Engineering Co Ltd filed Critical Sasakura Engineering Co Ltd
Priority to JP04273593A priority Critical patent/JP3183986B2/en
Publication of JPH06254534A publication Critical patent/JPH06254534A/en
Application granted granted Critical
Publication of JP3183986B2 publication Critical patent/JP3183986B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Abstract

PURPOSE:To miniaturize a feed water heater when provided and to reduce the production cost in the vacuum-evaporation water generator in which seawater in a vacuum evaporation chamber is heated by a heater to boil and evaporate the seawater and the generated steam is condensed by a shell-and-tube condenser with seawater as the cooling source to produce fresh water. CONSTITUTION:Partition plates 6a and 7a are provided respectively in both headers 6 and 7 in a condenser 4 to divide the headers into the cooling seawater inlet section 11a and outlet section 12a and the feed water inlet section 10a and outlet section 9a communicated with the heat-transfer tubes 5a as a part of many heat-transfer tubes. A feed water pipeline 16 from the feed water outlet section 9a is connected to a vacuum-evaporation chamber 1, while a communicating hole 17 is formed in the partition plate 7a to communicate the cooling seawater outlet section 12a with the feed water inlet section 10a.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、海水から淡水を真空蒸
発によって製造するための真空蒸発式造水装置のうち、
給水加熱器を備えた真空蒸発式造水装置の改良に関する
ものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a vacuum evaporation type water producing apparatus for producing fresh water from seawater by vacuum evaporation.
The present invention relates to an improvement in a vacuum evaporation type water producing apparatus equipped with a feed water heater.

【0002】[0002]

【従来の技術】一般に、この種の真空蒸発式造水装置
は、真空蒸発室内の海水を、ボイラーからの蒸気又はデ
ィーゼル機関に対する循環冷却水等を加熱源とする間接
熱交換式の加熱器にて加熱することによって沸騰蒸発
し、前記真空蒸発室内で発生した蒸気を、海水を冷却源
とする多管式の凝縮器にて凝縮することによって、淡水
を製造する一方、前記凝縮器から排出される冷却用海水
の一部を、前記真空蒸発室内に供給すると言う構成にし
ている。
2. Description of the Related Art Generally, a vacuum evaporation type water producing apparatus of this type is used as an indirect heat exchange type heater in which sea water in a vacuum evaporation chamber is heated by steam from a boiler or circulating cooling water for a diesel engine. It is boiled and evaporated by heating by heating, and the steam generated in the vacuum evaporation chamber is condensed in a multi-tube condenser using seawater as a cooling source to produce fresh water, while it is discharged from the condenser. A part of the cooling seawater is supplied into the vacuum evaporation chamber.

【0003】ところで、前記凝縮器から排出される冷却
用海水の温度は、真空蒸発室内における温度よりも可成
り低いから、従来の真空蒸発式造水装置においては、例
えば、実公昭53−26436号公報等に記載されてい
るように、前記凝縮器から排出される冷却用海水の一部
を、前記真空蒸発室内で発生した蒸気を加熱源とする間
接熱交換式の給水加熱器に導いて、その温度を更に高め
たのち前記真空蒸発室内に供給することによって、熱効
率の向上を図るように構成している。
By the way, since the temperature of the cooling seawater discharged from the condenser is considerably lower than the temperature in the vacuum evaporation chamber, in a conventional vacuum evaporation type water producing apparatus, for example, Japanese Utility Model Publication No. 53-26436. As described in the publication etc., a part of the cooling seawater discharged from the condenser is introduced to an indirect heat exchange type feedwater heater using the steam generated in the vacuum evaporation chamber as a heating source, The temperature is further raised and then supplied into the vacuum evaporation chamber to improve the thermal efficiency.

【0004】[0004]

【発明が解決しようとする課題】しかし、従来の真空蒸
発式造水装置においては、間接熱交換式の給水加熱器
を、凝縮器とは別個に設けると言う構造にしていること
により、この給水加熱器を配設するためのスペースを確
保しなければならないと共に、この給水加熱器を支持す
るための手段、及び前記凝縮器における冷却用海水の一
部をこの給水加熱器に導くための管路等が必要であるか
ら、真空蒸発式造水装置の大型化を招来するばかりか、
構造が複雑になると共に、製造工数が増大して、製造価
格の大幅なアップを招来すると言う問題があった。
However, in the conventional vacuum evaporation type water producing apparatus, the feed water heater of the indirect heat exchange type is provided separately from the condenser, so that the feed water is supplied. A space for arranging the heater must be secured, a means for supporting the feedwater heater, and a conduit for guiding a part of the cooling seawater in the condenser to the feedwater heater. Etc. are required, so not only will the vacuum evaporation type desalination apparatus be increased in size,
There is a problem that the structure becomes complicated and the manufacturing man-hour increases, resulting in a large increase in manufacturing price.

【0005】本発明は、この問題を解消し、給水加熱器
付き真空蒸発式造水装置の小型化と、低価格化とを図る
ことを技術的課題とするものである。
An object of the present invention is to solve this problem and to reduce the size and cost of a vacuum evaporation type fresh water producing apparatus with a feed water heater.

【0006】[0006]

【課題を解決するための手段】この技術的課題を達成す
るため本発明は、真空蒸発室と、その内部に供給した海
水に対する加熱器と、前記真空蒸発室内で発生した蒸気
に対する多管式の凝縮器とから成り、前記凝縮器の両端
に、当該凝縮器における各伝熱管に対するヘッダーを各
々設けて成る真空蒸発式造水装置において、前記凝縮器
における両ヘッダー内には、当該ヘッダー内を冷却海水
用の入口室及び出口室と凝縮器における多数本の伝熱管
のうち一部の伝熱管に連通する給水用の入口室及び出口
室とに区画する仕切り板を各々設けて、前記給水用出口
室からの給水管路を、前記真空蒸発室に接続する一方、
前記冷却海水用出口室と前記給水用入口室との間におけ
る仕切り板に、これらの相互間を連通する連通孔を設け
る構成にした。
In order to achieve this technical object, the present invention provides a vacuum evaporation chamber, a heater for seawater supplied therein, and a multitubular type for vapor generated in the vacuum evaporation chamber. A vacuum evaporation type desalination apparatus comprising a condenser and a header for each heat transfer tube in the condenser at both ends of the condenser, wherein both headers in the condenser cool the inside of the header. A partition plate is provided to partition the inlet chamber and outlet chamber for seawater and the inlet chamber and outlet chamber for water supply, which communicate with a part of the plurality of heat transfer pipes in the condenser, and the outlet for water supply is provided. While connecting the water supply line from the chamber to the vacuum evaporation chamber,
The partition plate between the cooling seawater outlet chamber and the water supply inlet chamber is provided with a communication hole that communicates with each other.

【0007】[0007]

【作 用】この構成において、真空蒸発室内における
海水は、加熱器による加熱にて沸騰蒸発し、この沸騰蒸
発で発生した蒸気は、凝縮器によって凝縮して、淡水と
して取り出される。一方、前記凝縮器のヘッダーにおけ
る冷却海水用入口室内に供給された冷却海水は、凝縮器
における各伝熱管のうち一部の伝熱管を除く各伝熱管内
を、冷却海水用出口室に向かって流れたのち、この冷却
海水用出口室から排出される一方、この冷却海水用出口
室内における冷却海水の一部が、仕切り板に設けた連通
孔から給水用入口室に流入する。
[Operation] In this structure, the seawater in the vacuum evaporation chamber is boiled by heating by the heater, and the steam generated by this boiling evaporation is condensed by the condenser and taken out as fresh water. On the other hand, the cooling seawater supplied into the cooling seawater inlet chamber in the header of the condenser is in each heat transfer tube in the condenser except for some heat transfer tubes, toward the cooling seawater outlet chamber. After flowing, the cooling seawater is discharged from the cooling seawater outlet chamber, while a part of the cooling seawater in the cooling seawater outlet chamber flows into the water supply inlet chamber through the communication hole provided in the partition plate.

【0008】このようにして給水用入口室内に流入した
海水は、凝縮器における各伝熱管のうち一部の伝熱管内
を、給水用出口室に向かって流れるとき、前記真空蒸発
室内で発生した蒸気によって温められた(給水加熱)の
ち、給水用出口室から給水管路を介して、前記真空蒸発
室内に供給されるのである。
The seawater that has flowed into the water supply inlet chamber in this way is generated in the vacuum evaporation chamber when it flows through some of the heat transfer tubes in the condenser toward the water supply outlet chamber. After being heated by the steam (heating of the water supply), the water is supplied from the water supply outlet chamber into the vacuum evaporation chamber through the water supply pipe line.

【0009】[0009]

【発明の効果】すなわち、前記の構成により、多管式凝
縮器における伝熱管の一部を使用して給水加熱を行うこ
とができ、換言すると、多管式凝縮器の一部を給水加熱
器として使用することができるから、前記従来のよう
に、給水加熱器を凝縮器とは別個に配設するためのスペ
ースを確保することを省略することができるのであり、
しかも、凝縮器から排出される冷却用海水の一部を、ヘ
ッダー内に仕切り板に穿設した連通孔を介して給水用に
導くことができることにより、凝縮器から排出される冷
却海水の一部を給水用に導くための管路を完全に省略す
ることができるのである。
[Effects of the Invention] That is, according to the above-mentioned constitution, the feed water can be heated by using a part of the heat transfer tube in the multi-tube condenser. Since it can be used as, it is possible to omit securing a space for disposing the feed water heater separately from the condenser as in the conventional case,
Moreover, since a part of the cooling seawater discharged from the condenser can be introduced for water supply through the communication hole formed in the partition plate in the header, a part of the cooling seawater discharged from the condenser can be introduced. It is possible to completely omit the conduit for guiding the water to the water supply.

【0010】従って本発明によると、給水加熱器付き真
空蒸発式造水装置を、大幅に小型・軽量化できると共
に、給水加熱器に対する支持構造及び管路が簡単になっ
て、製造コストを大幅に低減できる効果を有する。
Therefore, according to the present invention, the vacuum evaporation type water producing apparatus with a feed water heater can be greatly reduced in size and weight, and the supporting structure and the pipeline for the feed water heater can be simplified, resulting in a large production cost. It has the effect that it can be reduced.

【0011】[0011]

【実施例】以下、本発明の実施例を、図面について説明
する。図1〜図5は、単効用型の真空蒸発式造水装置に
適用した場合を示す。この図において符号1は真空蒸発
室を示し、この真空蒸発室1の底部には、下端に海水供
給室3を備えた多管式の加熱器2が設けられている一
方、前記真空蒸発室1内の上部には、複数本の伝熱管を
束ねた伝熱管群5の左右両端にヘッダー6,7を備えた
多管式の凝縮器4が横向きに配設されている。
Embodiments of the present invention will be described below with reference to the drawings. 1 to 5 show a case where the present invention is applied to a single-effect type vacuum evaporation type water producing apparatus. In the figure, reference numeral 1 indicates a vacuum evaporation chamber, and at the bottom of the vacuum evaporation chamber 1, a multi-tube heater 2 having a seawater supply chamber 3 at the lower end is provided, while the vacuum evaporation chamber 1 is provided. In the upper part of the inside, a multi-tube condenser 4 having headers 6 and 7 at the left and right ends of a heat transfer tube group 5 in which a plurality of heat transfer tubes are bundled is laterally arranged.

【0012】前記海水供給室3に供給した海水を、多管
式の加熱器2に対して入口2aから入って出口2aより
流出するように供給した加熱流体にて加熱することによ
って沸騰蒸発し、この沸騰蒸発で発生した蒸気を、前記
多管式凝縮器4における伝熱管群5に導いて凝縮するこ
とにより、この凝縮水を、凝縮器4の底部における淡水
出口8より淡水として取り出すように構成する。
The seawater supplied to the seawater supply chamber 3 is boiled and evaporated by heating it with a heating fluid supplied to the multitubular heater 2 so that it enters from the inlet 2a and flows out from the outlet 2a. The vapor generated by the boiling evaporation is introduced into the heat transfer tube group 5 in the multi-tube condenser 4 and condensed, so that the condensed water is taken out as fresh water from the fresh water outlet 8 at the bottom of the condenser 4. To do.

【0013】一方、前記凝縮器4における両ヘッダー
6,7内には、当該両ヘッダー6,7内を、前記伝熱管
群5における多数本の各伝熱管をその一部における複数
本の給水加熱用伝熱管5aに連通する給水加熱用ヘッダ
ー室9,10と、その残りの大部分の凝縮用伝熱管5b
に連通する凝縮用ヘッダー室11,12とに区画するた
めの仕切り板6a,7aを各々設ける。
On the other hand, inside the headers 6 and 7 of the condenser 4, inside the headers 6 and 7, a large number of heat transfer tubes in the heat transfer tube group 5 are heated by a plurality of feed water in a part thereof. Feed water heating header chambers 9 and 10 communicating with the heat transfer tube 5a for cooling, and most of the remaining condensing heat transfer tube 5b
Partition plates 6a and 7a for partitioning into the condensation header chambers 11 and 12 that communicate with each other are provided.

【0014】前記両ヘッダー6,7のうち一方のヘッダ
ー6における凝縮用ヘッダー室11内に、当該凝縮用ヘ
ッダー室11内を冷却海水用入口室11aと折り返し室
11bとに区画する仕切り板6bを、また、他方のヘッ
ダー7における凝縮用ヘッダー室12内に、当該凝縮用
ヘッダー室12内を冷却海水用出口室12aと折り返し
室12bとに区画する仕切り板7bを各々設けて、前記
一方のヘッダー6における冷却海水用入口室11aに、
冷却海水を入口13より供給する一方、前記他方のヘッ
ダー7における冷却海水用出口室12aに設けた出口1
4より冷却海水が流出するように構成する。
A partition plate 6b for partitioning the condensation header chamber 11 into a cooling seawater inlet chamber 11a and a folding chamber 11b is provided in the condensation header chamber 11 of one of the headers 6 and 7. Further, the condensing header chamber 12 of the other header 7 is provided with a partition plate 7b for partitioning the condensing header chamber 12 into a cooling seawater outlet chamber 12a and a folding chamber 12b. In the cooling seawater inlet chamber 11a in 6,
While supplying the cooling seawater from the inlet 13, the outlet 1 provided in the cooling seawater outlet chamber 12a in the other header 7
It is configured so that the cooling seawater flows out from No. 4.

【0015】そして、前記両ヘッダー6,7のうち一方
のヘッダー6における給水加熱用ヘッダー室9内に、当
該給水加熱用ヘッダー室9内を給水用出口室9aと、二
つの折り返し室9b,9cとに区画するための仕切り板
6c,6dを設けて、その給水用出口室9aからの出口
15を、給水管路16を介して前記海水供給室3に接続
する。
In the header chamber 9 for heating water supply in one of the two headers 6, 7, the header chamber 9 for heating water supply is provided with an outlet chamber 9a for water supply and two folding chambers 9b, 9c. Partition plates 6c and 6d for partitioning into and are provided, and an outlet 15 from the water supply outlet chamber 9a is connected to the seawater supply chamber 3 via a water supply pipe 16.

【0016】一方、他方のヘッダー7における給水加熱
用ヘッダー室10内に、当該給水加熱用ヘッダー室10
内を給水用入口室10aと、二つの折り返し室10b,
10cとに区画するための仕切り板7c,7dを設け、
更に、ヘッダー7における仕切り板7aのうち前記給水
用入口室10aの部分に、当該給水用入口室10aと前
記冷却海水用出口室12aとを互いに連通するための連
通孔17を穿設する。
On the other hand, in the header chamber 10 for heating the feed water in the other header 7, the header chamber 10 for heating the feed water is provided.
Inside is a water supply inlet chamber 10a and two folding chambers 10b,
Partition plates 7c and 7d for partitioning into 10c are provided,
Further, a communication hole 17 for communicating the water supply inlet chamber 10a and the cooling seawater outlet chamber 12a with each other is provided in the partition plate 7a of the header 7 at the portion of the water supply inlet chamber 10a.

【0017】この構成において、一方のヘッダー6にお
ける冷却海水用入口室11aに対して入口13より供給
された冷却海水は、各凝縮用伝熱管5b内を、他方のヘ
ッダー7における冷却海水用出口室12aに向かって折
り返し状に流れたのち、この冷却海水用出口室12aに
おける出口14から排出される一方、この冷却海水用出
口室12a内における冷却海水の一部が、仕切り板7a
に設けた連通孔17から給水用入口室10a内に流入す
る。
In this structure, the cooling seawater supplied from the inlet 13 to the cooling seawater inlet chamber 11a in the one header 6 flows through the respective condensing heat transfer tubes 5b and the cooling seawater outlet chamber in the other header 7. After flowing back toward 12a, the cooling seawater is discharged from the outlet 14 in the cooling seawater outlet chamber 12a, while part of the cooling seawater in the cooling seawater outlet chamber 12a is partially discharged.
The water flows into the inlet chamber 10a for water supply from the communication hole 17 provided in the.

【0018】このようにして給水用入口室10a内に流
入した海水は、凝縮器4における伝熱管群5のうち一部
の給水加熱用伝熱管5a内を、一方のヘッダー6におけ
る給水用出口室9aに向かって折り返し状に流れると
き、前記真空蒸発室1内で発生した比較的高い温度の蒸
気によって温められた(給水加熱)のち、給水用出口室
9aから給水管路16を介して、前記海水供給室3に供
給され、加熱器2にて加熱されて沸騰蒸発したのち、ブ
ライン出口18から流出するのである。
The seawater flowing into the water supply inlet chamber 10a in this way flows through a portion of the heat transfer pipes 5a of the condenser 4 in the heat transfer pipe group 5a into the water supply outlet chamber of the header 6. When it flows back toward 9a, it is warmed by the steam having a relatively high temperature generated in the vacuum evaporation chamber 1 (water supply heating), and then, from the water supply outlet chamber 9a through the water supply conduit 16 to It is supplied to the seawater supply chamber 3, heated by the heater 2 to evaporate by boiling, and then flows out from the brine outlet 18.

【0019】この場合において、多管式凝縮器4の伝熱
管群5における一部の伝熱管5aを使用して給水加熱を
行うことができるから、前記従来のように、給水加熱器
を凝縮器とは別個に配設するためのスペースを確保する
ことを省略することができるのであり、しかも、凝縮器
から排出される冷却用海水の一部を、ヘッダー7内の仕
切り板7aに穿設した連通孔17を介して給水用に導く
ことができることにより、凝縮器4から排出される冷却
海水の一部を給水用に導くための管路を完全に省略する
ことができるのである。
In this case, since the feed water can be heated by using a part of the heat transfer tubes 5a in the heat transfer tube group 5 of the multi-tube condenser 4, the feed water heater can be replaced by a condenser as in the conventional case. It is possible to omit to secure a space for disposing the cooling seawater separately, and a part of the cooling seawater discharged from the condenser is bored in the partition plate 7a in the header 7. By being able to guide water for supply through the communication hole 17, it is possible to completely omit a pipe line for guiding a part of the cooling seawater discharged from the condenser 4 for water supply.

【0020】図6〜図12は、二重効用型の真空蒸発式
造水装置に適用した場合を示す。この図において、符号
20は、一つの密閉缶胴を示し、該密閉缶胴20内は、
仕切り板20aによって第1段真空蒸発室21と、第2
段蒸発室22とに区画されている。前記両真空蒸発室2
1,22内の底部には、各々多管式の加熱器23,24
が設けられ、前記第1段真空蒸発室21内において、当
該第1段真空蒸発室21内における海水を、ボイラーか
らの蒸気等の熱源とする第1段加熱器23による加熱に
て沸騰蒸発し、この発生蒸気を、蒸気出口25aからダ
クト25を介して、前記第2段加熱器24に導いてその
熱源とすることにより、第2真空蒸発室22内における
海水を加熱して、沸騰蒸発し、この発生蒸気を、前記密
閉缶胴20内の上部に設けた多管式の凝縮器26にて凝
縮し、この凝縮水を凝縮器26における底部の淡水出口
27より取り出すように構成されている。
FIGS. 6 to 12 show a case where the invention is applied to a double-effect type vacuum evaporation type water producing apparatus. In this figure, reference numeral 20 indicates one closed can body, and the inside of the closed can body 20 is
The first-stage vacuum evaporation chamber 21 and the second
It is partitioned into a step evaporation chamber 22. Both vacuum evaporation chambers 2
At the bottoms of the insides of the pipes 1 and 22, there are multitubular heaters 23 and 24 respectively.
In the first-stage vacuum evaporation chamber 21, the seawater in the first-stage vacuum evaporation chamber 21 is boiled by being heated by a first-stage heater 23 that uses a steam or other heat source as a heat source. The generated steam is guided from the steam outlet 25a through the duct 25 to the second-stage heater 24 and used as a heat source for heating the seawater in the second vacuum evaporation chamber 22 to evaporate it to boiling. The generated steam is condensed by a multi-tube condenser 26 provided in the upper portion of the closed can body 20, and the condensed water is taken out from a fresh water outlet 27 at the bottom of the condenser 26. .

【0021】なお、前記第1段真空蒸発室21内におい
て蒸発した後の海水(ブライン)は、管路28を介して
第2段真空蒸発室22に供給され、この第2段真空蒸発
室22内において蒸発した後の海水(ブライン)は、ブ
ライン出口29から排出される。また、前記両真空蒸発
室21,22内の上部には、蒸発蒸気中のミストを捕集
するためのデミスター30,31が各々設けられてい
る。
The seawater (brine) that has evaporated in the first-stage vacuum evaporation chamber 21 is supplied to the second-stage vacuum evaporation chamber 22 via a pipe 28, and the second-stage vacuum evaporation chamber 22 is supplied. The seawater (brine) that has evaporated inside is discharged from the brine outlet 29. Further, demisters 30 and 31 for collecting the mist in the vaporized vapor are provided in the upper portions of the vacuum evaporation chambers 21 and 22, respectively.

【0022】そして、凝縮器26における左右両ヘッダ
ー32,33の間には、多数本の凝縮用伝熱管34と、
複数本の給水加熱用伝熱管35とを、一つ束の伝熱管群
として設ける一方、前記各凝縮用伝熱管34と、各給水
加熱用伝熱管35との間に仕切り板36を設けて、前記
各凝縮用伝熱管34の表面に、前記第2段真空蒸発室2
2内で発生した蒸気を導き、前記各給水加熱用伝熱管3
5の表面に、前記第1段真空蒸発室21内で発生した高
い温度の蒸気を導くように構成する。
A large number of condensing heat transfer tubes 34 are provided between the left and right headers 32 and 33 of the condenser 26.
A plurality of feed water heating heat transfer tubes 35 are provided as a bundle of heat transfer tube groups, while a partition plate 36 is provided between each condensation heat transfer tube 34 and each feed water heating heat transfer tube 35, The second stage vacuum evaporation chamber 2 is provided on the surface of each heat transfer tube 34 for condensation.
The steam generated in 2 is introduced to the heat transfer pipes 3 for heating the respective feed water.
The high temperature vapor generated in the first-stage vacuum evaporation chamber 21 is guided to the surface of No. 5.

【0023】一方、前記凝縮器26における両ヘッダー
32,33内には、当該両ヘッダー32,33内を、前
記各給水加熱用伝熱管35に連通する給水加熱用ヘッダ
ー室37,38と、前記各凝縮用伝熱管34に連通する
凝縮用ヘッダー室39,40とに区画するための仕切り
板32a,33aを各々設ける。前記両ヘッダー32,
33のうち一方のヘッダー32における凝縮用ヘッダー
室39内に、当該凝縮用ヘッダー室39内を冷却海水用
入口室39aと折り返し室39bとに区画する仕切り板
32bを、また、他方のヘッダー33における凝縮用ヘ
ッダー室40内に、当該凝縮用ヘッダー室40内を冷却
海水用出口室40aと折り返し室40bとに区画する仕
切り板33bを各々設けて、前記一方のヘッダー32に
おける冷却海水用入口室32aに、冷却海水を入口41
より供給する一方、前記他方のヘッダー33における冷
却海水用出口室40aに設けた出口42より冷却海水が
流出するように構成する。
On the other hand, inside the headers 32 and 33 of the condenser 26, there are provided feed water heating header chambers 37 and 38 which communicate the insides of the headers 32 and 33 with the feed water heating heat transfer tubes 35, respectively. Partitioning plates 32a and 33a for partitioning the condensation header chambers 39 and 40, which communicate with the condensation heat transfer tubes 34, are provided. Both headers 32,
A partition plate 32b for partitioning the condensation header chamber 39 into a cooling seawater inlet chamber 39a and a folding chamber 39b is provided in the condensation header chamber 39 of one of the headers 33, and the other header 33 is also provided. A partition plate 33b for partitioning the condensation header chamber 40 into a cooling seawater outlet chamber 40a and a folding chamber 40b is provided in the condensation header chamber 40, and the cooling seawater inlet chamber 32a in the one header 32 is provided. At the inlet 41 of the cooling seawater
While supplying more, the cooling seawater is configured to flow out from the outlet 42 provided in the cooling seawater outlet chamber 40a in the other header 33.

【0024】そして、前記両ヘッダー32,33のうち
一方のヘッダー32における給水加熱用ヘッダー室37
内に、当該給水加熱用ヘッダー室37内を三つの折り返
し室37a,37b,37cに区画するための仕切り板
32c,32dを設ける。また、前記他方のヘッダー3
3における給水加熱用ヘッダー室38内に、当該給水加
熱用ヘッダー室38内を給水用入口室38aと、二つの
折り返し室38b,38cと、給水用出口室38dとに
区画するための仕切り板33c,33d,33eを設
け、更に、ヘッダー33における仕切り板33aのうち
前記給水用入口室38aの部分に、当該給水用入口室3
8aと前記冷却海水用出口室40aとを互いに連通する
ための連通孔43を穿設する一方、前記給水用出口室3
8dの出口44を、給水管路45を介して前記第1真空
蒸発室21に対する海水供給口46に接続する。
A header chamber 37 for heating the feed water is provided in one of the headers 32 and 33.
Partition plates 32c, 32d for partitioning the interior of the header chamber 37 for heating the feed water into three folding chambers 37a, 37b, 37c are provided therein. Also, the other header 3
A partition plate 33c for partitioning the inside of the water supply heating header chamber 38 into a water supply inlet chamber 38a, two folding chambers 38b and 38c, and a water supply outlet chamber 38d. , 33d, 33e are provided, and further, in the partition plate 33a of the header 33, at the portion of the water supply inlet chamber 38a, the water supply inlet chamber 3 is provided.
8a and the cooling seawater outlet chamber 40a are provided with a communication hole 43 for communicating with each other, while the water supply outlet chamber 3 is provided.
The outlet 44 of 8d is connected to a seawater supply port 46 for the first vacuum evaporation chamber 21 via a water supply conduit 45.

【0025】この構成において、凝縮器26における一
方のヘッダー32における冷却海水用入口室39aに対
して入口41より供給された冷却海水は、各凝縮用伝熱
管34内を、他方のヘッダー33における冷却海水用出
口室40aに向かって折り返し状に流れたのち、この冷
却海水用出口室40aにおける出口42から排出される
一方、この冷却海水用出口室40a内における冷却海水
の一部が、仕切り板33aに設けた連通孔43から給水
用入口室38a内に流入する。
In this structure, the cooling seawater supplied from the inlet 41 to the cooling seawater inlet chamber 39a in the one header 32 of the condenser 26 is cooled in the respective condensing heat transfer tubes 34 and in the other header 33. After flowing back toward the seawater outlet chamber 40a, it is discharged from the outlet 42 in the cooling seawater outlet chamber 40a, while a part of the cooling seawater in the cooling seawater outlet chamber 40a is parted by the partition plate 33a. It flows into the water supply inlet chamber 38a from the communication hole 43 provided in the.

【0026】このようにして給水用入口室38a内に流
入した海水は、凝縮器26における各給水加熱用伝熱管
35内を、他方のヘッダー33における給水用出口室3
8dに向かって折り返し状に流れるとき、前記第1段真
空蒸発室21内で発生した高い温度の蒸気によって温め
られた(給水加熱)のち、給水用出口室38dから給水
管路45を介して、前記第1段真空蒸発室21内に供給
され、加熱器23にて加熱されて沸騰蒸発するのであ
る。
The seawater thus flowing into the water supply inlet chamber 38a passes through the inside of each heat exchanger 35 for heating the water supply in the condenser 26 and the water outlet chamber 3 in the other header 33.
When flowing in a folded shape toward 8d, after being warmed by the high temperature steam generated in the first-stage vacuum evaporation chamber 21 (water supply heating), from the water supply outlet chamber 38d via the water supply conduit 45, It is supplied into the first-stage vacuum evaporation chamber 21, heated by the heater 23, and evaporated by boiling.

【0027】この場合においても、多管式凝縮器26に
おける一部の伝熱管35を使用して給水加熱を行うこと
ができるから、前記従来のように、給水加熱器を凝縮器
とは別個に配設するためのスペースを確保することを省
略することができるのであり、しかも、凝縮器から排出
される冷却用海水の一部を、ヘッダー33内の仕切り板
33aに穿設した連通孔43を介して給水用に導くこと
ができることにより、凝縮器26から排出される冷却海
水の一部を給水用に導くための管路を完全に省略するこ
とができるのである。
Also in this case, since the feed water can be heated by using a part of the heat transfer tubes 35 in the multi-tube condenser 26, the feed water heater is separated from the condenser as in the conventional case. It is possible to omit to secure a space for disposing it, and moreover, a part of the cooling seawater discharged from the condenser is provided in the partition plate 33a in the header 33 with the communication hole 43 formed therein. By being able to lead to the water supply through the pipe, it is possible to completely omit the pipe line for leading a part of the cooling seawater discharged from the condenser 26 to the water supply.

【0028】なお、前記実施例は、単効用及び二重効用
型について説明したが、本発明は、これに限らず、その
他の多重効用型についても同様に適用できることは言う
までもない。
Although the above-described embodiments have been described with respect to the single-effect type and the double-effect type, the present invention is not limited to this, and it goes without saying that the same can be applied to other multi-effect types.

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

【図1】本発明における第1の実施例を示す縦断正面図
である。
FIG. 1 is a vertical sectional front view showing a first embodiment of the present invention.

【図2】図1のII−II視拡大断面図である。FIG. 2 is an enlarged sectional view taken along line II-II of FIG.

【図3】図1のIII −III 視拡大断面図である。FIG. 3 is an enlarged sectional view taken along line III-III in FIG.

【図4】図1のIV−IV視拡大断面図である。FIG. 4 is an enlarged sectional view taken along line IV-IV of FIG.

【図5】図1のV−V視拡大断面図である。5 is an enlarged sectional view taken along line VV of FIG.

【図6】本発明における第2の実施例を示す縦断正面図
である。
FIG. 6 is a vertical sectional front view showing a second embodiment of the present invention.

【図7】図6のVII −VII 視拡大断面図である。FIG. 7 is an enlarged sectional view taken along line VII-VII of FIG.

【図8】図6のVIII−VIII視拡大断面図である。8 is an enlarged sectional view taken along line VIII-VIII of FIG.

【図9】図8のIX−IV視断面図である。9 is a sectional view taken along line IX-IV of FIG.

【図10】図8のX−X視断面図である。10 is a cross-sectional view taken along line XX of FIG.

【図11】図8のXI−XI視断面図である。11 is a sectional view taken along line XI-XI of FIG.

【図12】図8のXII −XII 視断面図である。12 is a sectional view taken along line XII-XII of FIG.

【符号の説明】[Explanation of symbols]

1,21,22 真空蒸発室 2,23,24 加熱器 4,26 凝縮器 6,7,32,33 ヘッダー 5b,34 凝縮用伝熱管 5a,35 給水加熱用伝熱管 6a,7a,32a,33a 仕切り板 11a,39a 冷却海水用入口室 12a,40a 冷却海水用出口室 10a,38a 給水用入口室 9a,38d 給水用出口室 17,43 連通孔 1,2,22 Vacuum evaporation chamber 2,23,24 Heater 4,26 Condenser 6,7,32,33 Header 5b, 34 Condensation heat transfer pipe 5a, 35 Feed water heating heat transfer pipe 6a, 7a, 32a, 33a Partition plate 11a, 39a Cooling seawater inlet chamber 12a, 40a Cooling seawater outlet chamber 10a, 38a Water supply inlet chamber 9a, 38d Water supply outlet chamber 17,43 Communication hole

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】真空蒸発室と、その内部に供給した海水に
対する加熱器と、前記真空蒸発室内で発生した蒸気に対
する多管式の凝縮器とから成り、前記凝縮器の両端に、
当該凝縮器における各伝熱管に対するヘッダーを各々設
けて成る真空蒸発式造水装置において、前記凝縮器にお
ける両ヘッダー内には、当該ヘッダー内を冷却海水用の
入口室及び出口室と凝縮器における多数本の伝熱管のう
ち一部の伝熱管に連通する給水用の入口室及び出口室と
に区画する仕切り板を各々設けて、前記給水用出口室か
らの給水管路を、前記真空蒸発室に接続する一方、前記
冷却海水用出口室と前記給水用入口室との間における仕
切り板に、これらの相互間を連通する連通孔を設けたこ
とを特徴とする真空蒸発式造水装置。
1. A vacuum evaporation chamber, a heater for seawater supplied into the vacuum evaporation chamber, and a multi-tube condenser for vapor generated in the vacuum evaporation chamber, and both ends of the condenser,
In a vacuum evaporation type water producing apparatus provided with a header for each heat transfer pipe in the condenser, in both headers in the condenser, the header is provided with an inlet chamber and an outlet chamber for cooling seawater and a large number of condensers. A partition plate that divides into a water supply inlet chamber and an outlet chamber that communicates with a part of the heat transfer pipes of the book is provided, and the water supply pipe line from the water supply outlet chamber is connected to the vacuum evaporation chamber. A vacuum evaporation type fresh water producing apparatus, characterized in that, while being connected, a partition plate between the cooling seawater outlet chamber and the water supply inlet chamber is provided with a communication hole that communicates between them.
JP04273593A 1993-03-03 1993-03-03 Vacuum evaporation type fresh water generator Expired - Lifetime JP3183986B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP04273593A JP3183986B2 (en) 1993-03-03 1993-03-03 Vacuum evaporation type fresh water generator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP04273593A JP3183986B2 (en) 1993-03-03 1993-03-03 Vacuum evaporation type fresh water generator

Publications (2)

Publication Number Publication Date
JPH06254534A true JPH06254534A (en) 1994-09-13
JP3183986B2 JP3183986B2 (en) 2001-07-09

Family

ID=12644297

Family Applications (1)

Application Number Title Priority Date Filing Date
JP04273593A Expired - Lifetime JP3183986B2 (en) 1993-03-03 1993-03-03 Vacuum evaporation type fresh water generator

Country Status (1)

Country Link
JP (1) JP3183986B2 (en)

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20020038201A (en) * 2000-11-17 2002-05-23 최성환 Apparatus for producting drinking water by using seawater
WO2004113234A1 (en) * 2003-06-17 2004-12-29 Sasakura Engineering Co. Ltd. Plate type fresh water generator
CN103204557A (en) * 2012-01-16 2013-07-17 笹仓机械工程有限公司 Vacuum evaporation desalination device
JP2014018736A (en) * 2012-07-18 2014-02-03 Miura Co Ltd Fresh water generator
CN104250026A (en) * 2013-06-25 2014-12-31 笹仓机械工程有限公司 Vacuum Evaporation Type Fresh Water Generator
CN106277116A (en) * 2012-01-16 2017-01-04 笹仓机械工程有限公司 Vacuum evaporation desalination device
KR20190014464A (en) 2017-08-02 2019-02-12 가부시키가이샤 사사꾸라 Fresh water generation device
JP2019025471A (en) * 2017-08-02 2019-02-21 株式会社ササクラ Multiple-effect fresh water generator
JP2019025449A (en) * 2017-08-02 2019-02-21 株式会社ササクラ Fresh water generator
JP2019195750A (en) * 2018-05-08 2019-11-14 株式会社ササクラ Fresh water generator
JP2022051869A (en) * 2017-08-02 2022-04-01 株式会社ササクラ Multiple-effect fresh water generator

Cited By (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20020038201A (en) * 2000-11-17 2002-05-23 최성환 Apparatus for producting drinking water by using seawater
WO2004113234A1 (en) * 2003-06-17 2004-12-29 Sasakura Engineering Co. Ltd. Plate type fresh water generator
EP1650166A1 (en) * 2003-06-17 2006-04-26 Sasakura Engineering Co. Ltd. Plate type fresh water generator
EP1650166A4 (en) * 2003-06-17 2010-12-08 Sasakura Eng Co Ltd Plate type fresh water generator
CN103204557A (en) * 2012-01-16 2013-07-17 笹仓机械工程有限公司 Vacuum evaporation desalination device
JP2018114501A (en) * 2012-01-16 2018-07-26 株式会社ササクラ Vacuum evaporation type fresh water generator
CN106277116A (en) * 2012-01-16 2017-01-04 笹仓机械工程有限公司 Vacuum evaporation desalination device
JP2014018736A (en) * 2012-07-18 2014-02-03 Miura Co Ltd Fresh water generator
JP2015006640A (en) * 2013-06-25 2015-01-15 株式会社ササクラ Vacuum evaporation type fresh water generator
KR20150000805A (en) 2013-06-25 2015-01-05 가부시키가이샤 사사꾸라 Vacuum evaporation desalination system
CN104250026A (en) * 2013-06-25 2014-12-31 笹仓机械工程有限公司 Vacuum Evaporation Type Fresh Water Generator
KR20190014464A (en) 2017-08-02 2019-02-12 가부시키가이샤 사사꾸라 Fresh water generation device
JP2019025471A (en) * 2017-08-02 2019-02-21 株式会社ササクラ Multiple-effect fresh water generator
JP2019025449A (en) * 2017-08-02 2019-02-21 株式会社ササクラ Fresh water generator
TWI757508B (en) * 2017-08-02 2022-03-11 日商笹倉機械工程股份有限公司 Fresh water generation device
JP2022051869A (en) * 2017-08-02 2022-04-01 株式会社ササクラ Multiple-effect fresh water generator
KR20220123364A (en) 2017-08-02 2022-09-06 가부시키가이샤 사사꾸라 Fresh water generation device
JP2019195750A (en) * 2018-05-08 2019-11-14 株式会社ササクラ Fresh water generator

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