JPH063307B2 - Steam generator - Google Patents
Steam generatorInfo
- Publication number
- JPH063307B2 JPH063307B2 JP60093596A JP9359685A JPH063307B2 JP H063307 B2 JPH063307 B2 JP H063307B2 JP 60093596 A JP60093596 A JP 60093596A JP 9359685 A JP9359685 A JP 9359685A JP H063307 B2 JPH063307 B2 JP H063307B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- porous material
- water supply
- steam
- jacket
- 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
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B1/00—Methods of steam generation characterised by form of heating method
- F22B1/28—Methods of steam generation characterised by form of heating method in boilers heated electrically
- F22B1/288—Instantaneous electrical steam generators built-up from heat-exchange elements arranged within a confined chamber having heat-retaining walls
Landscapes
- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Air Humidification (AREA)
- 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) 本発明は無重力下の宇宙ステーシヨン,宇宙船等で主と
して使用される蒸気発生装置に関するものである。TECHNICAL FIELD The present invention relates to a steam generator mainly used in a space station under zero gravity, a spacecraft and the like.
(従来の技術) 無重力下で運転される宇宙ステーシヨン,宇宙船等に
は,CO2除去装置が設置されている。このCO2除去
装置は,CO2を含む空気をCO2除去装置の吸着槽内
へ導き,CO2を同吸着槽内の吸着剤に吸着させて,空
気とCO2とを分離する一方,水蒸気を吸着槽内の吸着
剤へ供給し,同吸着剤に吸着しているCO2を脱着させ
て,回収する装置で,CO2を脱着するために水蒸気を
必要している。(Prior Art) A CO 2 removal device is installed in a space station, a spacecraft, or the like that operates under zero gravity. This CO 2 removal device guides air containing CO 2 into the adsorption tank of the CO 2 removal device, adsorbs CO 2 on the adsorbent in the adsorption tank to separate air and CO 2 , Is supplied to the adsorbent in the adsorption tank, CO 2 adsorbed on the adsorbent is desorbed and collected, and steam is required to desorb CO 2 .
(発明が解決しようとする課題) 給水を加熱して水蒸気を発生させる場合,無重力下で
は,比重差により気液境界面が形成されて,水中に発生
した水蒸気が水から容易に分離しない。また無重力下で
は,給水を加熱しても,熱対流がないために,発生した
水蒸気が伝熱面付近に留まって,水に対する伝熱効率が
低下するという問題があった。(Problems to be Solved by the Invention) When water is heated to generate water vapor, a vapor-liquid interface is formed due to a difference in specific gravity under weightlessness, and water vapor generated in water is not easily separated from water. Further, under weightlessness, even if the feed water is heated, since there is no heat convection, the generated steam stays near the heat transfer surface, and the heat transfer efficiency for water is reduced.
本考案は前記の問題点に鑑み提案するものであり、その
目的とする処は、水中に発生した水蒸気を水から容易に
分離できる。また給水に対する伝熱効率を向上できる。
さらに蒸気発生装置の全体を小型化できる蒸気発生装置
を提供しようとする点にある。The present invention is proposed in view of the above problems, and the object of the present invention is to easily separate water vapor generated in water from water. Also, the heat transfer efficiency for water supply can be improved.
Another object is to provide a steam generator that can reduce the size of the entire steam generator.
(課題を解決するための手段) 上記の目的を達成するために、本考案の蒸気発生装置
は、ジャケット内に収容した多孔質材と、同ジャケット
内の多孔質材の周りに設けられた加熱装置と、上記ジャ
ケット内の同加熱装置の周りに形成されて上記多孔質材
の一端部に連通した給水予熱通路と、上記ジャケット外
の給水圧送ポンプから上記ジャケットの他端部へ延びて
上記給水予熱通路に連通した給水管と、上記多孔質材の
他端部から上記ジャケット外へ延びた蒸気導出管とを具
え、上記給水予熱通路の略全長を水予熱部とし、上記多
孔質材の一端部側を水予熱部、中間部を蒸発部、他端部
を過熱部としている。(Means for Solving the Problems) In order to achieve the above-mentioned object, a steam generator of the present invention includes a porous material housed in a jacket and a heating device provided around the porous material in the jacket. A device, a water supply preheating passage formed around the heating device in the jacket and communicating with one end of the porous material, and a water supply pump that extends from the water supply pressure pump outside the jacket to the other end of the jacket. A water supply pipe communicating with the preheating passage and a steam outlet pipe extending from the other end of the porous material to the outside of the jacket are provided, and substantially the entire length of the water supply preheating passage is used as a water preheating portion, and one end of the porous material is provided. The part side is a water preheating part, the middle part is an evaporation part, and the other end is an overheating part.
(作用) 本考案の蒸気発生装置は前記のように構成されており、
給水を水タンクから給水管及び給水圧送ポンプを経て蒸
気発生装置の給水予熱通路(蒸気発生装置の略全長を水
予熱部とした給水予熱通路)へ導入して、同給水予熱通
路を通るときに、加熱装置により予熱する。また同給水
予熱通路を出る給水を給水圧送ポンプからの圧力によ
り、多孔質材の一端部(水予熱部)へ導入し、多孔質材
に浸透させて、多孔質材の毛細管現象により給水の動き
を或る程度拘束しながら加熱装置により予熱し、次いで
多孔質材の中間部(蒸発部)へ導入して、上記と同様に
給水の動きを拘束しながら加熱装置により加熱し、沸
騰、気化させて、水蒸気にし、次いで水蒸気を多孔質材
の他端部(過熱部)へ導入して、上記と同様に給水の動
きを拘束しながら加熱装置により加熱し、過熱蒸気にし
て、この過熱蒸気を圧力の低い蒸気導出管内へ導出す
る。(Operation) The steam generator of the present invention is configured as described above,
When water is introduced from the water tank to the water supply preheating passage of the steam generator (water supply preheating passage with the water preheating section being approximately the entire length of the steam generator) through the water supply pipe and the water supply pressure pump, and when passing through the water supply preheating passage , Preheat with a heating device. In addition, the water supplied from the water supply preheating passage is introduced into one end (water preheating part) of the porous material by the pressure from the water supply pressure pump, and permeates into the porous material, and the water supply moves due to the capillary action of the porous material. Preheating with a heating device while restraining it to some extent, and then introducing it to the intermediate part (evaporating part) of the porous material, heating it with a heating device while restraining the movement of the water supply, boiling, and vaporizing it as described above. To steam, and then introduce the steam into the other end (superheated part) of the porous material and heat it with a heating device while restraining the movement of the feed water in the same manner as described above to make superheated steam. Discharge to the steam outlet pipe with low pressure.
(実施例) 次に本発明の蒸気発生装置第1図乃至第5図に示す一実
施例により説明すると,第1,2図の(1)がジャケッ
ト,(2)が同ジャケット(1)内に収容した多孔質材で,同
多孔質材(2)には,水に対して不溶性及び耐蝕性を有す
るセラミック,金属,耐熱性プラスチック等の材料によ
り構成されている。また(3)が同多孔質材(2)の周りに設
けられたヒータ(加熱装置),(4)が同ジャケット(1)内
の同ヒータ(3)の周りに形成されて同多孔質材(2)の一端
部に連通した給水予熱通路,(5)が同ジャケット(1)外の
給水圧送ポンプ(9)(第4図参照)から同給水予熱通路
(4)へ延びた給水管,(6)が同多孔質材(2)の他端部から
同ジャケット(1)外へ延びた蒸気導出管,(7)が上記ヒー
タ(3)へ述びた電線,(8)が上記ジャケット(1)を覆う保
温材である。また第3図の(4a)が上記給水予熱通路(4)
の略全長に相当する水予熱部,(2a)が上記多孔質材(2)
の前部に相当する水予熱部,(2b)が同多孔質材(2)の中
間部に相当する蒸発部,(2c)が同多孔質材(2)の後部に
相当する過熱部である。また第4図の(9)が上記給水管
(5)に設けた給水定量圧送ポンプ,(10)が同給水管(5)に
設けた開閉弁,(11)が同給水管(5)に設けた逆止弁,(1
2)が上記蒸気導出管(6)に設けた温度検出器,(13)が制
御器,(14)が上記蒸気導出管(6)に設けた同蒸気導出管
(6)に設けた開閉弁で,上記制御器(13)には,水蒸気を
消費する吸着槽(第5図の(24)(25)参照)で要求される
蒸気温度に蒸気導出管(6)で放熱される蒸気温度を加え
た過熱蒸気温度で設定されており,温度検出器(12)から
の温度検出信号と同設定値とを比較して得られた制御信
号に基づきヒータ(3)への電力または給水定量圧送ポン
プ(9)(給水量)を制御して,設定温度の過熱蒸気を上
記吸着槽(24)(25)へ送るようになっている。また上記逆
止弁(11)により,過熱過剰による突沸や圧力上昇等が生
じたときの水蒸気の逆流が防止するされるようになって
いる。また水蒸気が不要になったときに,開閉弁(10)を
閉じ,給水定量圧送ポンプ(9)を停止し,ヒータ(3)への
給電を止めて,水蒸気の発生を停止するようになってい
る。また第5図の(35)が上記給水定量圧送ポンプ(9)の
上流側に設けた水タンク,(20)がCO2を含有する空気
の導入管,(21)が同空気導入管(20)に設けた空気ファ
ン,(22)(23)が同空気導入管(20)に設けた開閉弁,(24)
が第1吸着槽,(25)が第2吸着槽,(28)が空気導出管,
(26)(27)が同空気導出管(28)に設けた開閉弁,(29)が同
空気導出管(28)に設けた冷却器,(30)が同空気導出管(2
8)に設けた水分離器,(33)がCO2導出管,(31)(32)が
同CO2導出管(33)に設けた開閉弁,(34)が同CO2導
出管(33)に設けたCO2ファンで,CO2を含有する空
気が空気導入管(20)から空気ファン(21)及び開閉弁(22)
(23)を経て第1吸着槽(24)または第2吸着槽(25)へ導入
され,空気中のCO2が吸着剤(図示せず)に吸着さ
れ,CO2を分離した空気が空気導出管(28)を経て冷却
器(29)へ送られ,ここで冷却されて,水分離器(30)へ送
られ,ここで気水分離が行われて,水が水タンク(35)へ
送られ,空気が外部へ放出される。一方,吸着剤に吸着
されたCO2が蒸気発生装置(1)〜(4)から蒸気導出管
(6)を経て第1吸着槽(24)または第2吸着槽(25)へ送ら
れる水蒸気により脱着され,脱着されたCO2が導出管
(33)からCO2ファン(34)を経て回収される。なお吸着
槽は2槽に限定されない。(Embodiment) The steam generator of the present invention will be described with reference to an embodiment shown in FIGS. 1 to 5. (1) in FIGS. 1 and 2 is a jacket, and (2) is inside the jacket (1). The porous material (2) is made of ceramic, metal, heat-resistant plastic or the like which is insoluble and corrosion resistant to water. In addition, (3) is a heater (heating device) provided around the porous material (2), and (4) is formed around the heater (3) in the jacket (1) and the porous material is formed. Water supply preheating passage communicating with one end of (2), (5) is the water supply preheating passage from the water supply pressure pump (9) (see Fig. 4) outside the jacket (1)
The water supply pipe extending to (4), (6) the steam outlet pipe extending from the other end of the porous material (2) to the outside of the jacket (1), and (7) the heater (3) described above. The electric wire, (8), is a heat insulating material that covers the jacket (1). Further, (4a) in FIG. 3 is the water supply preheating passage (4).
The water preheating part corresponding to substantially the entire length of (2a) is the porous material (2)
Of water, which corresponds to the front part of the porous material, (2b) corresponds to the middle part of the porous material (2), and (2c) corresponds to the rear part of the porous material (2). . In addition, (9) in Fig. 4 is the water supply pipe.
A fixed quantity water supply pump provided in (5), an on-off valve (10) provided in the water supply pipe (5), a check valve (11) provided in the water supply pipe (5), (1
2) is a temperature detector provided in the steam outlet pipe (6), (13) is a controller, and (14) is the steam outlet pipe provided in the steam outlet pipe (6).
The on-off valve provided in (6) controls the controller (13) so that the steam outlet pipe (6) can reach the steam temperature required in the adsorption tank (see (24) (25) in Fig. 5) that consumes steam. ), The temperature of the superheated steam is added to the temperature of the steam that is radiated, and the heater (3) is set based on the control signal obtained by comparing the temperature detection signal from the temperature detector (12) with the set value. It controls the electric power or the feed water constant pressure pump (9) (water supply amount) to send the superheated steam at the set temperature to the adsorption tanks (24) and (25). Further, the check valve (11) prevents the reverse flow of water vapor when bumping or pressure rise due to overheating occurs. When water vapor is no longer needed, the on-off valve (10) is closed, the feed water constant pressure pump (9) is stopped, the power supply to the heater (3) is stopped, and the generation of water vapor is stopped. There is. Further, (35) in FIG. 5 is a water tank provided on the upstream side of the feed water constant pressure pump (9), (20) is an air introducing pipe containing CO 2 , and (21) is the air introducing pipe (20). ), An air fan installed in (), an on-off valve (22) (23) installed in the air introduction pipe (20), (24)
Is the first adsorption tank, (25) is the second adsorption tank, (28) is the air outlet pipe,
(26) (27) is an on-off valve provided in the air outlet pipe (28), (29) is a cooler provided in the air outlet pipe (28), and (30) is an air outlet pipe (2).
8) water separator, (33) CO 2 outlet pipe, (31) and (32) CO 2 outlet pipe opening / closing valve (33), (34) CO 2 outlet pipe (33) in CO 2 fans provided), air fan (21) and the opening and closing valve from air containing CO 2 air inlet pipe (20) (22)
Is introduced first adsorption tank via (23) (24) or the second adsorption tank to (25), CO 2 in the air is adsorbed by the adsorbent (not shown), the air separation of the CO 2 air outlet It is sent to the cooler (29) through the pipe (28), cooled there, and sent to the water separator (30), where air-water separation is performed, and the water is sent to the water tank (35). Air is released to the outside. On the other hand, the CO 2 adsorbed by the adsorbent is transferred from the steam generators (1) to (4) to the steam outlet pipe.
CO 2 desorbed by the steam sent to the first adsorption tank (24) or the second adsorption tank (25) via (6), and the desorbed CO 2
It is recovered from (33) through the CO 2 fan (34). The adsorption tank is not limited to two tanks.
次に前記蒸気発生装置(1)〜(4)の作用を具体的に説明す
る。給水を水タンク(35)から給水管(5)及び給水圧送ポ
ンプ(9)を経て蒸気発生装置(1)〜(4)の給水予熱通路
(蒸気発生装置(1)〜(4)略全長を水予熱部(4a)とした給
水予熱通路)(4)へ導入して、同給水予熱通路(4)を通る
ときに、ヒータ(加熱装置)(3)により予熱する。また
同給水予熱通路(4)を出る給水を給水定量圧送ポンプ(9)
からの圧力により、多孔質材(2)の一端部(水予熱部(2
a))へ導入し、多孔質材(2)に浸透させて、多孔質材(2)
の毛細管現象により給水の動きを或る程度拘束しながら
ヒータ(3)より予熱し、次いで多孔質材(2)の中間部(蒸
発部(2b)へ導入して、上記と同様に給水の動きを拘束し
ながらヒータ(3)より加熱し、沸騰、気化させて、水蒸
気にし、次いで水蒸気を多孔質材(2)の他端部(過熱部
(2c)へ導入し、上記と同様に給水の動きを拘束しながら
ヒータ(3)より加熱して、過熱蒸気にし、この過熱蒸気
を圧力の低い蒸気導出管(6)内へ導入して、第1吸着槽
(24)または第2吸着槽(25)へ送る。Next, the operation of the steam generators (1) to (4) will be specifically described. Supply water from the water tank (35) through the water supply pipe (5) and the feed water pressure pump (9) to the water supply preheating passages (steam generators (1) to (4) for approximately the entire length of the steam generators (1) to (4)). The water is introduced into the water preheating passage (4), which is the water preheating section (4a), and is preheated by the heater (heating device) (3) when passing through the water preheating passage (4). In addition, the feed water that exits the feed water preheating passage (4) is fed with a constant feed pump (9).
The pressure from the end of the porous material (2) (water preheating part (2
a)) and permeate into the porous material (2) to form the porous material (2).
Pre-heating from the heater (3) while restraining the movement of the water supply to some extent by the capillary phenomenon of the above, and then introducing it to the middle part (evaporation part (2b)) of the porous material (2) and moving it in the same way as above. While restraining the heat from the heater (3), it is boiled and vaporized to form steam, and the steam is then converted into the other end (superheated part) of the porous material (2).
Introduced into (2c), heating from the heater (3) while restraining the movement of the water supply in the same manner as described above, into superheated steam, and introducing this superheated steam into the low-pressure steam outlet pipe (6), First adsorption tank
(24) or send to the second adsorption tank (25).
(発明の効果) 本発明の蒸気発生装置は前記のように給水を水タンクか
ら給水管及び給水圧送ポンプを経て蒸気発生装置の給水
予熱通路(蒸気発生装置の略全長を水予熱部とした給水
予熱通路)へ導入して、同給水予熱通路を通るときに、
加熱装置により予熱する。また同給水予熱通路を出る給
水を給水圧送ポンプからの圧力により、多孔質材の一端
部(水予熱部)へ導入し、多孔質材に浸透させて、多孔
質材の毛細管現象により給水の動きを或る程度拘束しな
がら加熱装置により予熱し、次いで多孔質材の中間部
(蒸発部)へ導入して、上記と同様に給水の動きを拘束
しながら加熱装置により加熱し、沸騰、気化させて、水
蒸気にし、次いで水蒸気を多孔質材の他端部(過熱部)
へ導入して、上記と同様に給水の動きを拘束しながら加
熱装置により加熱し、過熱蒸気にして、この過熱蒸気を
圧力の低い蒸気導出管内へ導出するので、無重力下で給
水を加熱して水蒸気を発生させる場合、比重差により気
液境界面を形成することがなくて、水中に発生した水蒸
気を水から容易に分離できる。(Effects of the Invention) In the steam generator of the present invention, as described above, the water is supplied from the water tank through the water supply pipe and the water supply pressure pump to the feed water preheating passage of the steam generator (substantially the entire length of the steam generator is used as the water preheating unit. Preheat passage), when passing through the same water supply preheat passage,
Preheat with a heating device. In addition, the water supplied from the water supply preheating passage is introduced into one end (water preheating part) of the porous material by the pressure from the water supply pressure pump, and permeates into the porous material, and the water supply moves due to the capillary action of the porous material. Preheating with a heating device while restraining it to some extent, and then introducing it to the intermediate part (evaporating part) of the porous material, heating it with a heating device while restraining the movement of the water supply, boiling, and vaporizing it as described above. To steam, and then steam is the other end of the porous material (superheated part)
In the same manner as above, while restraining the movement of the feed water, it is heated by a heating device to turn it into superheated steam, and this superheated steam is led out into the steam outlet pipe with a low pressure. When steam is generated, the steam generated in water can be easily separated from water without forming a gas-liquid interface due to the difference in specific gravity.
また無重力下で給水を加熱した場合、発生した水蒸気を
伝熱面付近に滞留させることがなくて、給水に対する伝
熱効率を向上できる。Further, when the feed water is heated under zero gravity, the generated steam does not stay near the heat transfer surface, and the heat transfer efficiency for the feed water can be improved.
また加熱装置が内表面積の非常に広い多孔質材を介して
給水を加熱するので、大型の伝熱部材を必要としなく
て、蒸気発生装置の全体を小型化できる効果がある。Further, since the heating device heats the feed water through the porous material having a very large inner surface area, there is an effect that the large-sized heat transfer member is not required and the entire steam generating device can be downsized.
以上本発明を実施例により説明したが,本発明はこのよ
うな実施例だけに限定されるものではなく,本発明の精
神を逸脱しない範囲内で種々の設計の改変を施し得るも
のである。例えば本蒸気発生装置は,無重力下でのみ使
用されるものでなく,重力下において溶剤回収装置等と
しても使用可能である。Although the present invention has been described with reference to the embodiments, the present invention is not limited to such embodiments, and various design modifications can be made without departing from the spirit of the present invention. For example, the steam generator is not only used under zero gravity, but can also be used as a solvent recovery device under gravity.
第1図は本発明に係わる蒸気発生装置の一実施例を示す
縦断側面図,第2図はその縦断正面図,第3図は加熱作
用説明図,第4,5図は本蒸気発生装置の使用例を示す
系統図である。 (1)…ジャケット、(2)…多孔質材、(2a)…多孔質材(2)
の一端部(水予熱部)、(2b)…多孔質材(2)の中間部
(蒸発部)、(2c)…多孔質材(2)の他端部(過熱部)、
(3)…加熱装置(ヒータ)、(4)…給水予熱通路、(4a)…
給水予熱通路(4)の水予熱部、(5)…給水管、(6)…蒸気
導出管、(9)…給水圧送ポンプ。FIG. 1 is a vertical sectional side view showing an embodiment of a steam generating apparatus according to the present invention, FIG. 2 is a vertical sectional front view thereof, FIG. 3 is a heating action explanatory view, and FIGS. It is a system diagram which shows a usage example. (1) ... jacket, (2) ... porous material, (2a) ... porous material (2)
One end (water preheating part), (2b) ... an intermediate part (evaporating part) of the porous material (2), (2c) ... the other end (superheating part) of the porous material (2),
(3) ... Heating device (heater), (4) ... Water supply preheating passage, (4a) ...
Water preheating section of the water supply preheating passage (4), (5) ... water supply pipe, (6) ... steam derivation pipe, (9) ... water supply pressure pump.
Claims (1)
ヤケツト内の多孔質材の周りに設けられた加熱装置と、
上記ジヤケツト内の同加熱装置の周りに形成されて上記
多孔質材の一端部に連通した給水予熱通路と、上記ジヤ
ケツト外の給水圧送ポンプから上記ジヤケツトの他端部
へ延びて上記給水予熱通路に連通した給水管と、上記多
孔質材の他端部から上記ジヤケツト外へ延びた蒸気導出
管とを具え、上記給水予熱通路の略全長を水予熱部と
し、上記多孔質材の一端部側を水予熱部、中間部を蒸発
部、他端部を過熱部としたことを特徴とする蒸気発生装
置。1. A porous material housed in a jacket, and a heating device provided around the porous material in the jacket,
A water supply preheating passage formed around the same heating device in the jacket and communicating with one end of the porous material, and from the water supply pressure pump outside the jacket to the other end of the jacket and extending to the water supply preheating passage. A water supply pipe communicating with the porous material, and a steam outlet pipe extending from the other end of the porous material to the outside of the jacket are provided, and substantially the entire length of the water supply preheating passage is used as a water preheating part, and one end side of the porous material is provided. A steam generating device characterized in that a water preheating section, an intermediate section is an evaporation section, and the other end is an overheating section.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60093596A JPH063307B2 (en) | 1985-05-02 | 1985-05-02 | Steam generator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60093596A JPH063307B2 (en) | 1985-05-02 | 1985-05-02 | Steam generator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61252443A JPS61252443A (en) | 1986-11-10 |
| JPH063307B2 true JPH063307B2 (en) | 1994-01-12 |
Family
ID=14086689
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60093596A Expired - Lifetime JPH063307B2 (en) | 1985-05-02 | 1985-05-02 | Steam generator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH063307B2 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6317302A (en) * | 1986-07-09 | 1988-01-25 | 住友重機械工業株式会社 | Small-sized fixed-quantity steam generator |
| JP4599635B2 (en) * | 1999-08-24 | 2010-12-15 | 株式会社Ihi | Evaporator |
| JP5182246B2 (en) * | 2009-07-27 | 2013-04-17 | 株式会社Ihi | Condenser for microgravity environment |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5321876U (en) * | 1976-07-31 | 1978-02-23 | ||
| JPS5486949A (en) * | 1977-12-22 | 1979-07-10 | Matsushita Electric Ind Co Ltd | Steam ejector |
| JPS5523814A (en) * | 1978-08-02 | 1980-02-20 | Matsushita Electric Ind Co Ltd | Hot air heater |
-
1985
- 1985-05-02 JP JP60093596A patent/JPH063307B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61252443A (en) | 1986-11-10 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP3671064B2 (en) | Method and apparatus for regenerating refrigerant | |
| US4309196A (en) | Coal gasification apparatus | |
| KR940013567A (en) | Low Temperature Liquid Evaporator and Method | |
| JPH0436299B2 (en) | ||
| US6339678B1 (en) | Method for vaporizing and superheating a sterilizing agent and device therefor | |
| JPH09508696A (en) | Equipment for superheating steam | |
| US6938583B2 (en) | Blowdown heat recovery | |
| US4915793A (en) | Water treatment apparatus | |
| JPH063307B2 (en) | Steam generator | |
| US984585A (en) | Solar-heat motor. | |
| RU2661121C2 (en) | Shell-and-tube apparatus for heat recovery from hot process stream | |
| EP0878242A3 (en) | Device for vaporising and/or nebulising a liquid | |
| JPS6316032A (en) | Supply of regeneration steam in carbon dioxide removing apparatus using ion exchange resin | |
| RU2133914C1 (en) | Water heater | |
| JP2006138522A (en) | Heater | |
| US5186710A (en) | Transport incubator having an integrated energy store | |
| GB1515793A (en) | Flameless reboiler for reconcentrating liquid desiccant | |
| KR200279678Y1 (en) | A water distiller with monolithic condensing chamber and boiler using thermoelectric module | |
| JP4873308B2 (en) | Pure steam production equipment | |
| GB1128659A (en) | Process and apparatus for separating components contained in a liquid by evaporation | |
| JPS60245991A (en) | Vapor type heat transfer | |
| JPH04290556A (en) | Heating and cooling device | |
| JPS6071803U (en) | steam generator | |
| JPH0467084B2 (en) | ||
| JPS5842719Y2 (en) | Low-temperature liquefied gas vaporization equipment |