JPS611902A - Steam generator - Google Patents

Steam generator

Info

Publication number
JPS611902A
JPS611902A JP12065684A JP12065684A JPS611902A JP S611902 A JPS611902 A JP S611902A JP 12065684 A JP12065684 A JP 12065684A JP 12065684 A JP12065684 A JP 12065684A JP S611902 A JPS611902 A JP S611902A
Authority
JP
Japan
Prior art keywords
steam
water
pump
separator
make
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
JP12065684A
Other languages
Japanese (ja)
Other versions
JPH059683B2 (en
Inventor
外尾 暢晧
岩渕 牧男
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP12065684A priority Critical patent/JPS611902A/en
Publication of JPS611902A publication Critical patent/JPS611902A/en
Publication of JPH059683B2 publication Critical patent/JPH059683B2/ja
Granted legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E10/00Energy generation through renewable energy sources
    • Y02E10/10Geothermal energy

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は例えば火力プラント等に利用される蒸気発生装
置に関する。
DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a steam generator used in, for example, a thermal power plant.

従来の技術 第2図は従来の蒸気発生装置の系統図であり、先ずこの
図により従来の装置について説明する。
BACKGROUND OF THE INVENTION FIG. 2 is a system diagram of a conventional steam generator, and the conventional apparatus will first be explained with reference to this diagram.

1は系内への補給水及び系内から膨出した水を貯蔵する
補給水タンク、2はタンク1の出口側に設けた止め弁、
3aはタンク1がら補給水ポンプ4へ至る補給水配管、
32〜3dは補給水ポンプ4からヘッダ8へ補給量調節
弁7、逆止弁5、止め止6を直列に接続している補給水
配管である。
1 is a make-up water tank that stores make-up water into the system and water expanded from the system; 2 is a stop valve provided on the outlet side of tank 1;
3a is a make-up water pipe leading from the tank 1 to the make-up water pump 4;
Reference numerals 32 to 3d designate make-up water piping connecting the make-up water pump 4 to the header 8, the make-up amount adjusting valve 7, the check valve 5, and the stop 6 in series.

9は循環ポンプ、10は給水ポンプ9から補給水タンク
1への給水戻りラインlla 、 llb中に設けた給
水流量調節弁、13は循環ポンプ9から給水ライン12
aを介して加圧されたボイラ水が供給され、油、ガス、
電力等の熱源によって加熱して蒸気を発生する蒸気発生
設備、14は蒸気発生設備I3から蒸気12bを介して
導入される蒸気を消費して仕事をする蒸気消費設備、1
5は蒸気消費設備の出口側の蒸気ライン12c 、 1
2dの間に設けた蒸気圧力を調節するための蒸気圧力調
節弁、16は蒸気ライン12cの蒸気圧力を検出し、調
節弁15の開閉を制御する圧力調節計、17は安全弁で
ある。
9 is a circulation pump; 10 is a water supply return line lla and llb from the water supply pump 9 to the makeup water tank 1; 13 is a water supply line 12 from the circulation pump 9;
Pressurized boiler water is supplied through a, and oil, gas,
Steam generation equipment that generates steam by heating with a heat source such as electric power; 14 is a steam consumption equipment that performs work by consuming steam introduced from the steam generation equipment I3 via steam 12b;
5 is a steam line 12c on the outlet side of the steam consumption equipment, 1
2d is a steam pressure regulating valve for regulating the steam pressure; 16 is a pressure regulator that detects the steam pressure in the steam line 12c and controls opening and closing of the regulating valve 15; and 17 is a safety valve.

18は蒸気ライン12dから供給される蒸気を冷却水ラ
イン19を通る冷却水によって凝縮させるコンデンサ、
20はコンデンサ18で凝縮されたドレンを脱気器21
へ供給する復水ポンプ、22は脱気器21の水位を一定
に保つように系内の循環水量を制御する脱気器水位調節
計、23は脱気器21内の給水を加熱することにより、
給水中に溶存している酸素を除去する加熱用蒸気ライン
、12e〜12g は夫々給水ラインである。
18 is a condenser that condenses the steam supplied from the steam line 12d with cooling water passing through the cooling water line 19;
20 is a deaerator 21 for drain condensed in the condenser 18;
22 is a deaerator water level controller that controls the amount of circulating water in the system so as to keep the water level of the deaerator 21 constant; 23 is a deaerator water level controller that heats the water supply in the deaerator 21 ,
Heating steam lines 12e to 12g, which remove oxygen dissolved in the water supply, are water supply lines, respectively.

給水ライン12gは分岐して一方はへラダ8へ連結して
いるとともに、他方は脱気水流量調節弁24に連結して
いる。そしてこの調節弁24は脱気水戻りライン25を
介して補給水タンク1へ連結されている。なお、脱気水
流量調節弁24は、補給水量調節弁7と共に脱気器水位
調節計22によって開閉量が制御される。
The water supply line 12g is branched, and one side is connected to the spatula 8, and the other side is connected to the deaerated water flow rate control valve 24. This control valve 24 is connected to the make-up water tank 1 via a deaerated water return line 25. The amount of opening and closing of the deaerated water flow rate control valve 24 is controlled by the deaerator water level controller 22 together with the make-up water amount control valve 7.

さてこのように構成された従来の蒸気発生装置は、給水
ポンプ9、蒸気発生設備13、蒸気消費設備14、蒸気
圧力調節弁15、コンデンサ18、復水ポンプ20及び
脱気器21が、給水及び蒸気循環ラインを形成する管路
12a〜12g及びヘッダ8によって閉路を形成してい
る。そして、蒸気発生設備13で発生した所要条件の蒸
気は、蒸気消費設備14に供給され、ここを出た蒸気は
圧力調節弁15にて減圧された後コンデンサ1Bへ供給
される。コンデンサ]8では蒸気は常温付近の温度1で
冷却されて凝縮し、ボイラ水となって復水ポンプ20に
よって脱気器21へ供給して1oo0c以上に加熱され
る。脱気器21はボイラ水中に溶存している酸素を、そ
のボイラ水を加熱することによって除去する装置であっ
て、温度を上げると水中に溶存しうる酸素の量が減少す
ることを利用して脱気するものである。
Now, in the conventional steam generator configured as described above, the feed water pump 9, the steam generation equipment 13, the steam consumption equipment 14, the steam pressure control valve 15, the condenser 18, the condensate pump 20, and the deaerator 21 are connected to the water supply and The pipes 12a to 12g and the header 8 forming a steam circulation line form a closed path. Then, the steam generated in the steam generation equipment 13 under the required conditions is supplied to the steam consumption equipment 14, and the steam exiting here is depressurized by the pressure control valve 15 and then supplied to the condenser 1B. In the condenser] 8, the steam is cooled to a temperature 1 near normal temperature and condensed to become boiler water, which is supplied to a deaerator 21 by a condensate pump 20 and heated to 1oo0c or higher. The deaerator 21 is a device that removes oxygen dissolved in boiler water by heating the boiler water. It deaerates the air.

そして、脱気器21に保有されるボイラ水は、ヘッダ8
を介して給水ポンプ9の吸込側へ供給されて循環ループ
が構成される。このとき、系の運転状態に応じて脱気器
21の保有水の水位が変動しようとするが、脱気性能を
良好な状態に維持するためには、その水位を一定に保つ
必要があり、その制御が水位調節計22によって行なわ
れる。
The boiler water held in the deaerator 21 is then transferred to the header 8.
The water is supplied to the suction side of the water supply pump 9 through the water supply pump 9 to form a circulation loop. At this time, the water level held in the deaerator 21 tends to fluctuate depending on the operating state of the system, but in order to maintain good deaeration performance, it is necessary to keep the water level constant. This control is performed by a water level controller 22.

すなわち、脱気器21の水位が上がれば水位調節計22
によって、脱気水流量調節弁24を開いて。
That is, if the water level of the deaerator 21 rises, the water level controller 22
Open the deaerated water flow control valve 24.

膨出分のボイラ水を補給水タンク1へ貯蔵し、逆に水位
が下がれば補給水量調節弁7を開いて給水ポンプ9の吸
込側ヘタンク1から給水を行なう。
The bulging boiler water is stored in the make-up water tank 1, and conversely, when the water level drops, the make-up water amount control valve 7 is opened to supply water from the tank 1 to the suction side of the water supply pump 9.

従来技術の問題点 ところで、上記のような従来の蒸気発生装置には、次の
ような問題があった。すなわち(力 蒸気発生設備13
で発生した蒸気をコンデンサ18で常温付近の温度迄凝
縮させた後、再び脱気器21で100°C以上の温水に
加熱した上で給水ポンプ9へ送ると云うボイラ水循環ラ
インとなっている為装置の熱効率が悪い。
Problems with the Prior Art The conventional steam generator as described above has the following problems. In other words, (force steam generation equipment 13
This is because the boiler water circulation line is such that the steam generated in the boiler is condensed to a temperature near room temperature in the condenser 18, then heated again to hot water of 100°C or higher in the deaerator 21, and then sent to the water supply pump 9. Thermal efficiency of the device is poor.

(イ)系の循環量を決める給水ポンプ9は大気圧付近か
ら運転圧力迄昇圧可能な高ヘツドポンプが必要であり機
能的に複雑・高出力のものが必要である。
(a) The water supply pump 9, which determines the amount of circulation in the system, needs to be a high-head pump that can raise the pressure from near atmospheric pressure to operating pressure, and needs to be functionally complex and high-output.

(つ)蒸気発生設備13人口のボイラ水温度条件は、1
00°C程度である為、一般に高圧で運転される蒸気発
生設備13で所要の蒸気を得るには大きな加熱源が必要
である。
(1) Boiler water temperature conditions for 13 steam generation facilities are 1
Since the temperature is approximately 00°C, a large heating source is required to obtain the required steam in the steam generation equipment 13, which is generally operated at high pressure.

発明の目的 本発明は、上記のような従来の問題点を除去した蒸気発
生装置を提供することを目的としてなされたものである
OBJECTS OF THE INVENTION The present invention has been made for the purpose of providing a steam generator that eliminates the above-mentioned conventional problems.

問題点を解決するための手段 従来の問題点を解決するために、本発明では、脱気器に
代えて気水分離器及びサブターラを備えた循環系を構成
している。
Means for Solving the Problems In order to solve the problems of the conventional art, the present invention includes a circulation system that includes a steam separator and a sub-colander in place of the deaerator.

実施例 以下、本発明の一実施例を第1図を参照して詳細に説明
する。なお第1図において第2図と同一部分には同一符
号を附して示しである。
EXAMPLE Hereinafter, an example of the present invention will be explained in detail with reference to FIG. In FIG. 1, the same parts as in FIG. 2 are designated by the same reference numerals.

第1図において、補給水タンク1、止め弁2、補給水ポ
ンプ4、逆止弁5、止め弁6、ヘッダ8、循環ポンプ9
、蒸気発生設備13、蒸気消費設備14は従来のものと
同様であり、これらは配管3a、3b、3d、3e、1
2a、]2bによって連結されている。循環ポンプ9と
蒸気発生設備130間には循環水流量調節弁31が設け
られている。
In Fig. 1, a make-up water tank 1, a stop valve 2, a make-up water pump 4, a check valve 5, a stop valve 6, a header 8, and a circulation pump 9.
, steam generation equipment 13, and steam consumption equipment 14 are the same as conventional ones, and these are pipes 3a, 3b, 3d, 3e, 1
2a, ]2b. A circulating water flow rate control valve 31 is provided between the circulation pump 9 and the steam generation equipment 130.

蒸気消費設備14を出た蒸気は蒸気ライン12cを介し
て気水分離器33へ供給される。気水分離器33には、
安全弁34、脱気用ベルト弁35及び後述する水位調節
計36が設けられている。気水分離器33は連絡管3’
7a、 37b 、 ヘッダ38a。
Steam exiting the steam consumption equipment 14 is supplied to the steam separator 33 via the steam line 12c. In the steam/water separator 33,
A safety valve 34, a deaeration belt valve 35, and a water level regulator 36, which will be described later, are provided. The steam/water separator 33 is connected to the connecting pipe 3'
7a, 37b, header 38a.

38bを介して空冷コンデンサ4oの凝縮管39に連結
されている。気水分離器33の出口側は管路12hを介
してサブクーラ42に連結され、その出口配管12gは
ヘッダ8に連結されている。従って、循環ポンプ9、循
環水量調節弁31、蒸気発生設備13、蒸気消費設備1
4、気水分離器33及びサブクーラ42が、配管12a
 、 12b 、 12c 、 12h 。
It is connected to the condensing pipe 39 of the air-cooled condenser 4o via 38b. The outlet side of the steam/water separator 33 is connected to the subcooler 42 via a pipe line 12h, and the outlet pipe 12g thereof is connected to the header 8. Therefore, the circulation pump 9, the circulating water amount control valve 31, the steam generation equipment 13, the steam consumption equipment 1
4. The steam/water separator 33 and the subcooler 42 are connected to the piping 12a
, 12b, 12c, 12h.

12g及びヘッダ8等によって閉路を形成している。12g, the header 8, etc., form a closed circuit.

なお、気水分離器33とサブクーラ42を結ぶ配管12
hは分岐されて、気水分離器33の水位を調節する水位
調節弁44及びブロー管45を介して補給水タンク1に
連結されている。この水位調節弁44は水位調節計36
によって開閉が制御される。
In addition, the piping 12 connecting the steam/water separator 33 and the subcooler 42
h is branched and connected to the make-up water tank 1 via a water level control valve 44 for regulating the water level of the steam separator 33 and a blow pipe 45. This water level control valve 44 is connected to the water level controller 36
Opening/closing is controlled by

空冷コンデンサ40にはブロワ46からダクト49aを
介して冷却用空気が送られるが、このダクト49aの途
中には冷却空気調節用ダンパ47が設けられている。そ
して、このダンパ47は気水分離器33に設けた圧力調
節計41によって開閉が制御される。捷だ、ブロア46
の出口附近でダクト49aは分岐してダク) 49bと
なり、サブクーラ用冷却空気調節ダンパ48を介してサ
ブクーラ42に連結されている。なおこのダンパ48は
サブクーラ42の出口側に設けた温度調節計43によっ
て開閉制御される。
Cooling air is sent from the blower 46 to the air-cooled condenser 40 through a duct 49a, and a damper 47 for regulating cooling air is provided in the middle of the duct 49a. Opening and closing of this damper 47 is controlled by a pressure regulator 41 provided in the steam/water separator 33. Good luck, Bloor 46
The duct 49a branches into a duct 49b near the exit of the subcooler 49, which is connected to the subcooler 42 via a cooling air adjustment damper 48 for the subcooler. Note that this damper 48 is controlled to open and close by a temperature controller 43 provided on the outlet side of the subcooler 42.

次に本発明装置の動作を説明する。Next, the operation of the device of the present invention will be explained.

循環ポンプ9、流量調節弁31、蒸気発生設備13、蒸
気消費設備14、気水分離器33、サブクーラ42等か
ら成る循環系内の循環水は、循環ポンプ9及び流量調節
弁3】によって蒸気発生設備13へ送られ、ここで加熱
されて所要の蒸気条件が整えられる。そしてこの蒸気が
蒸気消費設備14へ供給されて仕事をする。従って、蒸
気消費設備14からは気水混合の流体として排出され、
この流体は気水分離器33へ導入される。
Circulating water in a circulation system consisting of a circulation pump 9, a flow rate control valve 31, a steam generation facility 13, a steam consumption facility 14, a steam separator 33, a subcooler 42, etc. is used to generate steam by the circulation pump 9 and flow rate control valve 3. It is sent to equipment 13, where it is heated and the required steam conditions are established. This steam is then supplied to the steam consumption equipment 14 to do work. Therefore, steam is discharged from the steam consumption equipment 14 as a mixed fluid of steam and water,
This fluid is introduced into the steam separator 33.

気水分離器33は気水混合の流体を蒸気と水に分離する
もので、蒸気は空冷コンデンサ40の凝縮管39へ導入
され、ここでブロワ46から送られる冷却用空気との熱
交換により冷却・凝縮され、気水分離器33の水相へと
戻される。空冷コンデンサ40へ導入される冷却用空気
の流量は、気水分離器33に設けた圧力調節計41によ
って、ダンパ47の開度な制御することにより、適切な
量に制御され、これによって循環系内の運転圧力は所定
の値に維持される。
The steam-water separator 33 separates a steam-water mixture into steam and water. The steam is introduced into the condensing pipe 39 of the air-cooled condenser 40, where it is cooled by heat exchange with the cooling air sent from the blower 46. - Condensed and returned to the aqueous phase of the steam/water separator 33. The flow rate of the cooling air introduced into the air-cooled condenser 40 is controlled to an appropriate amount by controlling the opening degree of the damper 47 using a pressure regulator 41 provided in the steam/water separator 33. The operating pressure within is maintained at a predetermined value.

そして、気水分離器33によって蒸気と分離されまたは
凝縮された水はサブクーラ4墾へ導入され、ここで系の
運転圧力に対する飽和温度よりも若干低い温度にされる
。これは、循環系において圧力変動等が起ったときに蒸
気フラッシュが発生するのを予防し、系の流動安定性を
保つためである。すなわちサブクーラ42は、気水分離
器33から供給される飽和温度の水を冷却して、ザブク
ール状態にするためのものである。なお、サブクーラへ
供給される冷却用空気の量は、温度調節泪43によって
駆動されるダンパ48によって変化し、これによってサ
ブクール温度を所定値に制御している。
The water separated from steam or condensed by the steam separator 33 is introduced into the subcooler 4, where it is brought to a temperature slightly lower than the saturation temperature for the operating pressure of the system. This is to prevent steam flash from occurring when pressure fluctuations occur in the circulation system, and to maintain fluid stability of the system. That is, the subcooler 42 is for cooling the water at the saturated temperature supplied from the steam/water separator 33 to bring it into a subcooled state. Note that the amount of cooling air supplied to the subcooler is changed by a damper 48 driven by a temperature control valve 43, thereby controlling the subcool temperature to a predetermined value.

一方、水位調節計36は運転条件によって変動する循環
系内の保有水容積の変化に伴なう気水分離器33内の水
位を調節するために設けられており、水位が上ったとき
は水位調節弁44を開いて循環水のブローをブロー管を
通して補給水タンク1へ戻ずようにしている。
On the other hand, the water level controller 36 is provided to adjust the water level in the steam/water separator 33 as the water volume in the circulation system changes depending on the operating conditions. The water level control valve 44 is opened to prevent the circulating water from returning to the make-up water tank 1 through the blow pipe.

なお蒸気発生装置の運転開始初期の、圧力が2〜3kg
/cylEl程度の低圧運転時には、脱気用ベント弁3
5を少し開いて、系内循環水の脱気を行なう。
In addition, at the beginning of operation of the steam generator, the pressure is 2 to 3 kg.
When operating at low pressures such as /cylEl, degassing vent valve 3
Open 5 slightly to degas the circulating water in the system.

発明の効果 以上詳述したように、本発明によれは、次のような種々
の効果を奏する蒸気発生装置が提供される。
Effects of the Invention As detailed above, the present invention provides a steam generator that provides the following various effects.

(ア)本発明にかかる蒸気発生装置は、発生蒸気を凝縮
・再循環使用するに当り、気水分離器33、サブクーラ
42等により飽和温度より若干低い程度の水に凝縮・冷
却する為、装置の熱効果が高い。
(A) The steam generator according to the present invention condenses and cools the generated steam to water slightly lower than the saturation temperature using the steam separator 33, subcooler 42, etc. when condensing and recirculating the generated steam. High thermal effect.

(イ)蒸気発生装置の循環系は、全体が発生蒸気圧力に
ほぼ等しく保持される。この為系の蒸気発生量に等しい
能力を有する循環ポンプ8は系内圧力損失に見合う程度
のポンプヘッドを有するものでよく、従来の蒸気発生装
置の給水ポンプに要求される、運転圧力に等しい高ヘッ
ドを有するポンプでなくてよい。
(a) The entire circulation system of the steam generator is maintained at approximately the same pressure as the generated steam. For this reason, the circulation pump 8, which has a capacity equal to the amount of steam generated in the system, may have a pump head that is sufficient to compensate for the pressure loss within the system. The pump does not have to have a head.

(つ)本蒸気発生装置は基本的には系内保有水を再循環
させることによって蒸気発生装置の機能をはだすように
なっており、運転中外部より給水補給を行なう必要がな
い。この為高ヘッドで製作コストの高い給水ポンプは蒸
気発生量に較べ給水能力が、ごく小さなものでよい。
(1) This steam generator basically performs its functions by recirculating the water held within the system, so there is no need to replenish the water supply from outside during operation. For this reason, a water supply pump with a high head and high manufacturing cost only needs to have a very small water supply capacity compared to the amount of steam generated.

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

第1図は本発明に係る蒸気発生装置の一実施例を示す系
統図、第2図は従来の蒸気発生装置を示す系統図である
。 1・・補給水タンク、4・・補給水ポンプ、9・・循環
ポンプ、13・・蒸気発生設備、14・・蒸気消費設備
、33・・気水分離器、 39・・凝縮管、40・・空
冷コンデンサ、42・・サブクーラ。 (ばか2名)
FIG. 1 is a system diagram showing an embodiment of a steam generator according to the present invention, and FIG. 2 is a system diagram showing a conventional steam generator. 1. Makeup water tank, 4. Makeup water pump, 9. Circulation pump, 13. Steam generation equipment, 14. Steam consumption equipment, 33. Steam water separator, 39. Condensing pipe, 40.・Air-cooled condenser, 42...Subcooler. (2 idiots)

Claims (1)

【特許請求の範囲】[Claims] 補給水タンクに補給水ポンプを介して接続された循環ポ
ンプと、同循環ポンプと接続された蒸気発生設備と、同
蒸気発生設備と接続された蒸気消費設備と、同蒸気消費
設備と接続されるとともに蒸気凝縮器と接続された気水
分離器と、同気水分離器と接続されかつ前記循環ポンプ
の入口側へ接続されたサブクーラとを備えたことを特徴
とする蒸気発生装置。
A circulation pump connected to the make-up water tank via a make-up water pump, a steam generation facility connected to the circulation pump, a steam consumption facility connected to the steam generation facility, and a steam consumption facility connected to the same steam consumption facility. A steam generation device comprising: a steam separator connected to a steam condenser; and a subcooler connected to the steam condenser and to an inlet side of the circulation pump.
JP12065684A 1984-06-14 1984-06-14 Steam generator Granted JPS611902A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12065684A JPS611902A (en) 1984-06-14 1984-06-14 Steam generator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12065684A JPS611902A (en) 1984-06-14 1984-06-14 Steam generator

Publications (2)

Publication Number Publication Date
JPS611902A true JPS611902A (en) 1986-01-07
JPH059683B2 JPH059683B2 (en) 1993-02-05

Family

ID=14791630

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12065684A Granted JPS611902A (en) 1984-06-14 1984-06-14 Steam generator

Country Status (1)

Country Link
JP (1) JPS611902A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63255652A (en) * 1987-03-27 1988-10-21 レイケム・コーポレイション Detector
JP2016061474A (en) * 2014-09-17 2016-04-25 三菱日立パワーシステムズ株式会社 Steam turbine plant

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5425301A (en) * 1977-07-27 1979-02-26 Hirakawa Tekkosho Condensed water tight recovery device

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5425301A (en) * 1977-07-27 1979-02-26 Hirakawa Tekkosho Condensed water tight recovery device

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63255652A (en) * 1987-03-27 1988-10-21 レイケム・コーポレイション Detector
JP2016061474A (en) * 2014-09-17 2016-04-25 三菱日立パワーシステムズ株式会社 Steam turbine plant

Also Published As

Publication number Publication date
JPH059683B2 (en) 1993-02-05

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