JP2003074801A - Saturated steam generator - Google Patents
Saturated steam generatorInfo
- Publication number
- JP2003074801A JP2003074801A JP2001263319A JP2001263319A JP2003074801A JP 2003074801 A JP2003074801 A JP 2003074801A JP 2001263319 A JP2001263319 A JP 2001263319A JP 2001263319 A JP2001263319 A JP 2001263319A JP 2003074801 A JP2003074801 A JP 2003074801A
- Authority
- JP
- Japan
- Prior art keywords
- heat storage
- saturated steam
- water
- tank
- storage material
- 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
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/14—Thermal energy storage
Landscapes
- Apparatus For Disinfection Or Sterilisation (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は飽和水蒸気発生装置
に関し、更に詳細には過熱水蒸気を加熱源に用いて飽和
水蒸気を発生する飽和水蒸気発生装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a saturated steam generator, and more particularly to a saturated steam generator which uses superheated steam as a heating source to generate saturated steam.
【0002】[0002]
【従来の技術】病院等では治療用の包帯、メス、鉗子、
手術着等の被滅菌物の滅菌には、通常、被滅菌物が収容
された滅菌室を飽和水蒸気によって加圧して所定の圧力
・温度とした状態を一定時間保持する蒸気滅菌方法が採
用されている。かかる蒸気滅菌方法に使用される蒸気滅
菌装置のうち、大量に被滅菌物に滅菌を施すことのでき
る大型の蒸気滅菌装置には、通常、病院等に備えられた
大型ボイラーから飽和水蒸気が供給される。2. Description of the Related Art In hospitals and the like, therapeutic bandages, scalpels, forceps,
For sterilization of items to be sterilized such as surgical gowns, a steam sterilization method is usually used in which the sterilization chamber containing the items to be sterilized is pressurized with saturated steam and kept at a predetermined pressure and temperature for a certain period of time. There is. Among the steam sterilizers used in such a steam sterilization method, a large steam sterilizer capable of sterilizing a large amount of objects to be sterilized is usually supplied with saturated steam from a large boiler provided in a hospital or the like. It
【0003】しかし、大型ボイラーは灯油の燃焼を伴う
ので、環境保全の面から見て妥当ではなく、また駆動時
の騒音も問題となる。そこで、本発明者等は、図5に示
すように、飽和水蒸気を発生する飽和水蒸気発生装置に
おいて、加熱源を小型化する事ができるとともに、環境
にも優しく、且つ運転音を非常に小さくでき、ランニン
グコストの低減をも図れる飽和水蒸気発生装置を考案す
るに至っている。However, since a large boiler is accompanied by burning of kerosene, it is not appropriate from the viewpoint of environmental protection, and noise during driving also poses a problem. Therefore, the present inventors, as shown in FIG. 5, can reduce the size of the heating source in the saturated steam generator that generates saturated steam, are environmentally friendly, and can reduce the operating noise to a very low level. In addition, we have come up with a saturated steam generator that can reduce running costs.
【0004】図5の飽和水蒸気発生装置の構造の概略を
説明する。この飽和水蒸気発生装置は、蓄熱槽10と、
飽和水蒸気発生槽12とを具備している。蓄熱槽10内
には固体蓄熱材と液体蓄熱材とから成る蓄熱部11が設
けられている。この蓄熱部11内に伝熱管16が配設さ
れ、ポンプ14によって伝熱管16内に水が供給され
る。伝熱管内を通過した水は過熱され、過熱水蒸気とな
って飽和水蒸気発生槽12内に配置された加熱ヒータ2
0内に供給される。一方、蒸発槽18内に供給される飽
和水蒸気の元となる水は精密濾過、脱イオン処理等の水
処理が施された処理水であって、ポンプ9によって配管
8を通じて蒸発槽内18に供給されている。An outline of the structure of the saturated steam generator shown in FIG. 5 will be described. This saturated steam generator includes a heat storage tank 10,
And a saturated steam generation tank 12. In the heat storage tank 10, a heat storage unit 11 made of a solid heat storage material and a liquid heat storage material is provided. A heat transfer tube 16 is arranged in the heat storage section 11, and water is supplied into the heat transfer tube 16 by the pump 14. The water that has passed through the heat transfer tube is overheated, becomes superheated steam, and is a heater 2 arranged in the saturated steam generation tank 12.
It is supplied within 0. On the other hand, the water that is the source of the saturated steam supplied to the evaporation tank 18 is treated water that has been subjected to water treatment such as microfiltration and deionization, and is supplied to the evaporation tank inside 18 by the pump 9 through the pipe 8. Has been done.
【0005】従来の蓄熱槽内の構造を図6に示す。蓄熱
槽10は、上述のような蓄熱部11と、蓄熱部11内を
通過するように設けられて蓄熱部11内を加熱するため
の電気ヒータ15が設けられている。ここで、示す各電
気ヒータ15は、伝熱管16の水の導入口側と過熱水蒸
気の吐出口側とにわたって全体を加熱可能に設けられて
いる。蓄熱槽10の加熱は、電気ヒータ15へ主として
安価な深夜電力を通電することによって行なわれる。深
夜電力を10時間ほど通電しておくと、その後蓄熱槽1
0からは7時間半から8時間程度は安定して500℃程
の過熱水蒸気が得られる。FIG. 6 shows the structure of a conventional heat storage tank. The heat storage tank 10 is provided with the heat storage unit 11 as described above, and an electric heater 15 provided so as to pass through the heat storage unit 11 and heat the inside of the heat storage unit 11. Here, each electric heater 15 shown is provided so as to be capable of heating the whole of the heat transfer tube 16 over the water inlet side and the superheated steam outlet side. The heating of the heat storage tank 10 is performed by mainly supplying an inexpensive electric power to the electric heater 15 at midnight. If power is applied for about 10 hours at midnight, then the heat storage tank 1
From 0 to 7 hours and a half to 8 hours, superheated steam of about 500 ° C. is stably obtained.
【0006】[0006]
【発明が解決しようとする課題】上述した構造の飽和水
蒸気発生装置では、蓄熱槽内を通過する水は、伝熱管の
導入口側で最も蓄熱部から熱を吸収する。このため、こ
の位置での蓄熱部の温度が最も低下しやすい。したがっ
て、飽和水蒸気発生行程時には、蓄熱槽の伝熱管の導入
口側を重点的に再加熱して蓄熱槽全体を一定の温度に維
持したいという課題があった。In the saturated steam generator having the above structure, the water passing through the heat storage tank absorbs the most heat from the heat storage section at the inlet side of the heat transfer tube. Therefore, the temperature of the heat storage section at this position is most likely to drop. Therefore, during the saturated steam generation process, there is a problem in that the inlet side of the heat transfer tube of the heat storage tank is intensively reheated to maintain the temperature of the entire heat storage tank at a constant temperature.
【0007】また、処理水の水質の変動については、飽
和水蒸気発生装置の運転には何ら考慮されておらず、水
質が悪化した場合の対処が求められる可能性もあった。Further, regarding the fluctuation of the water quality of the treated water, no consideration is given to the operation of the saturated steam generator, and there is a possibility that it is required to deal with the deterioration of the water quality.
【0008】また、蓄熱槽への給水はポンプのオン−オ
フによって行なわれていたが、ポンプのオン−オフ制御
だけでは飽和水蒸気の発生のオーバーシュート及びアン
ダーシュートが大きくなってしまうので、安定した飽和
水蒸気の発生が望まれているという課題もあった。Further, the water supply to the heat storage tank has been performed by turning the pump on and off, but the overshoot and undershoot of the generation of the saturated steam become large only by controlling the pump on and off, so that it is stable. There is also a problem that the generation of saturated steam is desired.
【0009】なお、蓄熱槽への水の給水と、飽和水蒸気
発生槽への処理水の供給は別々のポンプによって行なわ
れていたので稼動部品が多く、メンテナンス性を向上さ
せるべきであるという課題や、装置の部品点数の削減等
も望まれているという課題や、従来飽和水蒸気発生槽で
オーバーフローした処理水はそのまま排水されており、
処理水を無駄に廃棄していてランニングコストが高くつ
くなどの課題もあった。Since water is supplied to the heat storage tank and treated water is supplied to the saturated steam generation tank by separate pumps, there are many moving parts, and it is necessary to improve maintainability. , The problem that reduction of the number of parts of the device is also desired, and the treated water that overflowed in the conventional saturated steam generation tank is drained as it is,
There were also problems such as wasted disposal of treated water and high running costs.
【0010】したがって、本発明は上記課題を解決すべ
くなされ、その目的とするところは、蓄熱部の伝熱管の
導入口側を十分な温度に再加熱可能な飽和水蒸気発生装
置、処理水の水質の変動を考慮して運転可能な飽和水蒸
気発生装置、飽和水蒸気の安定した発生ができる飽和水
蒸気発生装置を提供することにある。Therefore, the present invention has been made to solve the above problems, and an object thereof is to provide a saturated steam generator capable of reheating the inlet side of the heat transfer tube of the heat storage section to a sufficient temperature, and the quality of treated water. It is an object of the present invention to provide a saturated steam generator that can be operated in consideration of fluctuations in the above, and a saturated steam generator that can stably generate saturated steam.
【0011】[0011]
【課題を解決するための手段】本発明は、上記課題を解
決するために次の構成を備える。すなわち、本発明にか
かる飽和水蒸気発生装置によれば、蓄熱槽と飽和水蒸気
発生槽とを具備し、該蓄熱槽内で過熱されて得られた過
熱水蒸気によって飽和水蒸気発生槽内の水を加熱して飽
和水蒸気を発生させる飽和水蒸気発生装置であって、前
記蓄熱槽に設けられた固体蓄熱材と液体蓄熱材とが充填
されて成る蓄熱部内には、前記固体蓄熱材及び液体蓄熱
材を加熱するヒータと、内部を通過する水を過熱して過
熱水蒸気とする伝熱管とが設けられ、前記ヒータは、伝
熱管における水の導入口側が過熱された過熱水蒸気の吐
出口側よりも高温となるように、前記固体蓄熱材及び液
体蓄熱材を加熱可能に設けられていることを特徴として
いる。この構成を採用することによって、他の部位より
も温度低下が著しい伝熱管の導入口側を十分に再加熱
し、蓄熱槽内の温度の均一化を図ることができる。The present invention has the following constitution in order to solve the above problems. That is, according to the saturated steam generator of the present invention, the saturated steam generation tank is provided with a heat storage tank, and the water in the saturated steam generation tank is heated by the superheated steam obtained by overheating in the heat storage tank. Is a saturated steam generator for generating saturated steam, and heats the solid heat storage material and the liquid heat storage material in a heat storage section that is filled with a solid heat storage material and a liquid heat storage material provided in the heat storage tank. A heater and a heat transfer tube that superheats water passing through it to become superheated steam are provided, and the heater has a temperature higher than that of the discharge port side of the superheated steam that is overheated on the water inlet side of the heat transfer tube. In addition, the solid heat storage material and the liquid heat storage material can be heated. By adopting this configuration, it is possible to sufficiently reheat the inlet side of the heat transfer tube whose temperature is significantly lower than that of other parts, and to make the temperature in the heat storage tank uniform.
【0012】また、前記ヒータは、少なくとも伝熱管に
おける水の導入口側と過熱された過熱水蒸気の吐出口側
との前記固体蓄熱材及び液体蓄熱材を別々のヒータで加
熱可能となるように複数設けられていることによれば、
伝熱管の導入口側の再加熱を効率よく行なうことができ
る。さらに、前記複数のヒータのうち伝熱管における水
の導入口側に配置された一のヒータは、過熱された過熱
水蒸気の吐出口側に配置された他のヒータよりも高温と
なるものであることを特徴とすれば、伝熱管の導入口側
を十分に再加熱することが可能である。[0012] Further, the heater has a plurality of heaters so that at least the water inlet side of the heat transfer tube and the outlet side of the superheated steam that has been overheated can heat the solid heat storage material and the liquid heat storage material by separate heaters. According to what is provided,
It is possible to efficiently reheat the inlet side of the heat transfer tube. Further, among the plurality of heaters, one heater arranged on the water inlet side of the heat transfer tube has a higher temperature than the other heater arranged on the discharge port side of the overheated steam. With the feature, it is possible to sufficiently reheat the inlet side of the heat transfer tube.
【0013】本発明にかかる飽和水蒸気発生装置によれ
ば、蓄熱槽と飽和水蒸気発生槽とを具備し、該蓄熱槽内
で過熱されて得られた過熱水蒸気によって飽和水蒸気発
生槽内の水を加熱して飽和水蒸気を発生する飽和水蒸気
発生装置であって、前記蓄熱槽に設けられた固体蓄熱材
と液体蓄熱材とが充填されて成る蓄熱部内には、前記固
体蓄熱材及び液体蓄熱材を加熱するヒータと、内部を通
過する水を過熱して過熱水蒸気とする伝熱管とが設けら
れ、該伝熱管から供給される過熱水蒸気と接触して飽和
水蒸気を発生させる水を飽和水蒸気発生槽に供給する給
水管の中途部には、前記水を一旦貯留する貯留槽が設け
られ、前記飽和水蒸気発生槽および/または貯留槽に
は、給水水質を測定する水質測定手段が設けられている
ことを特徴としている。この構成を採用することによっ
て、飽和水蒸気を発生させる水質を管理することによ
り、清浄な飽和水蒸気を提供できる。According to the saturated steam generating apparatus of the present invention, the saturated steam generating tank is provided with a heat storage tank and the saturated steam generating tank, and the water in the saturated steam generating tank is heated by the superheated steam obtained by overheating in the heat storage tank. Is a saturated steam generator for generating saturated steam, wherein the solid heat storage material and the liquid heat storage material provided in the heat storage tank are filled in the heat storage portion, and the solid heat storage material and the liquid heat storage material are heated. Is provided with a heater and a heat transfer tube that superheats the water passing through it into superheated steam, and supplies water to the saturated steam generation tank to generate saturated steam by contacting the superheated steam supplied from the heat transfer tube. A storage tank for temporarily storing the water is provided at an intermediate portion of the water supply pipe to be used, and a water quality measuring unit for measuring the quality of the supplied water is provided in the saturated steam generation tank and / or the storage tank. As . By adopting this configuration, it is possible to provide clean saturated steam by controlling the quality of water that generates saturated steam.
【0014】また、前記水質測定手段によって、飽和水
蒸気となるべき水の水質が低下したことが測定された場
合には、飽和水蒸気発生の運転を停止させるように制御
する第1の制御手段を具備するので、より確実に飽和水
蒸気の質を向上させ、清浄な飽和水蒸気のみを提供でき
る。さらに、前記飽和水蒸気発生槽内でオーバーフロー
した水を前記貯留槽へ戻すためのオーバーフロー配管が
設けられていることを特徴とすると、オーバーフローし
た水を廃棄しないようにすることができ、水を無駄にし
ないようにしてランニングコストの低減を図ることがで
きる。なお、飽和水蒸気発生槽には、該飽和水蒸気発生
槽で発生した飽和水蒸気を吐出する給蒸管が設けられ、
該給蒸管内で凝縮したドレンを給蒸管から排出して前記
貯留槽へ戻すためのドレン配管が設けられていることと
すれば、給蒸管内のドレンを廃棄せず再利用するので、
水を無駄にしないようにしてランニングコストの低減を
図れる。Further, when the water quality measuring means determines that the quality of the water to be saturated steam is lowered, it comprises first control means for controlling so as to stop the operation of generating saturated steam. Therefore, the quality of saturated steam can be improved more reliably, and only clean saturated steam can be provided. Further, when the overflow pipe for returning the water overflowed in the saturated steam generation tank to the storage tank is provided, it is possible to prevent the overflowed water from being discarded and waste the water. By not doing so, the running cost can be reduced. The saturated steam generation tank is provided with a steam supply pipe for discharging the saturated steam generated in the saturated steam generation tank,
If a drain pipe for discharging the drain condensed in the steam supply pipe from the steam supply pipe and returning it to the storage tank is provided, the drain in the steam supply pipe is reused without being discarded,
The running cost can be reduced by not wasting water.
【0015】本発明にかかる飽和水蒸気発生装置によれ
ば、蓄熱槽と飽和水蒸気発生槽とを具備し、該蓄熱槽内
で過熱されて得られた過熱水蒸気によって飽和水蒸気発
生槽で水を加熱して飽和水蒸気を発生する飽和水蒸気発
生装置であって、前記蓄熱槽に設けられた固体蓄熱材と
液体蓄熱材とが充填されて成る蓄熱部内には、前記固体
蓄熱材及び液体蓄熱材を加熱するヒータと、内部を通過
する水を過熱して過熱水蒸気とする伝熱管とが設けら
れ、前記伝熱管へ水を供給するための給水ポンプが設け
られ、前記飽和水蒸気発生槽で発生した飽和水蒸気圧力
を測定する圧力測定手段が設けられ、該圧力測定手段に
よって測定された飽和水蒸気圧力値が入力され、該飽和
水蒸気圧力値が常時一定となるように前記給水ポンプを
制御する第2の制御手段が設けられていることを特徴と
している。この構成を採用することによって、より安定
した飽和水蒸気の出力が期待できる。According to the saturated steam generator of the present invention, it is provided with a heat storage tank and a saturated steam generation tank, and the superheated steam obtained by overheating in the heat storage tank heats water in the saturated steam generation tank. Is a saturated steam generator that generates saturated steam, and heats the solid heat storage material and the liquid heat storage material in a heat storage section that is filled with a solid heat storage material and a liquid heat storage material provided in the heat storage tank. A heater and a heat transfer tube that superheats water passing through it into superheated steam are provided, a water supply pump for supplying water to the heat transfer tube is provided, and the saturated steam pressure generated in the saturated steam generation tank is provided. Second control for controlling the feed water pump so that the saturated water vapor pressure value measured by the pressure measuring means is input and the saturated water vapor pressure value is always constant Is characterized in that stage is provided. By adopting this configuration, more stable saturated steam output can be expected.
【0016】また、前記給水ポンプは、前記伝熱管およ
び前記飽和水蒸気発生槽へ水を供給するために下流側で
分岐し、該分岐先がそれぞれ前記伝熱管および前記飽和
水蒸気発生槽へ接続されて成る給水管に1つ設けられて
いるので、稼動部品である給水ポンプの数を従来よりも
減らして1つとし、メンテナンスが容易となり且つ部品
点数の削減も図れる。The water supply pump is branched on the downstream side to supply water to the heat transfer pipe and the saturated steam generation tank, and the branch destinations are connected to the heat transfer pipe and the saturated steam generation tank, respectively. Since one water supply pipe is provided, the number of water supply pumps that are operating parts can be reduced to one compared with the conventional one, and maintenance can be facilitated and the number of parts can be reduced.
【0017】[0017]
【発明の実施の形態】本発明に係る飽和水蒸気発生装置
の一例を示す略線図を図1に示す。図1に示す飽和水蒸
気発生装置30は、蓄熱槽32と飽和水蒸気発生槽34
とを具備する。まず、水の供給系統について説明する。
本飽和水蒸気発生装置30の蓄熱槽32で過熱されるた
めの水、および飽和水蒸気発生槽34内で飽和水蒸気と
なる水は、共に精密濾過、脱イオン処理等を行なった純
水、RO(reverse osmosis)水、軟水等の処理水が用
いられる。そして、処理水を供給するための給水元管3
5は、蓄熱槽32用と飽和水蒸気発生槽34用で合わせ
て1本のみが配設されている。FIG. 1 is a schematic diagram showing an example of a saturated steam generator according to the present invention. The saturated steam generator 30 shown in FIG. 1 includes a heat storage tank 32 and a saturated steam generator tank 34.
And. First, the water supply system will be described.
The water to be overheated in the heat storage tank 32 of the saturated steam generating device 30 and the water that becomes saturated steam in the saturated steam generating tank 34 are both pure water subjected to microfiltration and deionization, RO (reverse) osmosis) Water, treated water such as soft water is used. And the water supply source pipe 3 for supplying the treated water
5 is for the heat storage tank 32 and for the saturated steam generation tank 34, and only one is provided in total.
【0018】給水元管35は、貯留槽36に接続され、
供給された処理水はここで一旦貯留される。貯留槽36
から蓄熱槽32と飽和水蒸気発生槽34の両者へ給水す
るための給水管38が接続されている。給水管38の途
中にはストレーナ39が設けられている。給水管38に
は、給水ポンプ40が設けられており、この給水ポンプ
40によって処理水が蓄熱槽32と飽和水蒸気発生槽3
4へ移送される。The water source pipe 35 is connected to a storage tank 36,
The supplied treated water is temporarily stored here. Storage tank 36
A water supply pipe 38 for supplying water from both the heat storage tank 32 and the saturated steam generation tank 34 is connected. A strainer 39 is provided in the middle of the water supply pipe 38. The water supply pipe 38 is provided with a water supply pump 40, and the water supply pump 40 causes the treated water to store the treated water in the heat storage tank 32 and the saturated steam generation tank 3.
Transferred to 4.
【0019】給水管38は、給水ポンプ40の下流側で
蓄熱槽32へ向かう蓄熱槽側給水管42と飽和水蒸気発
生槽34へ向かう発生槽側供給管44の2つに分岐して
いる。蓄熱槽側給水管42は、途中にモータバルブ45
が設けられ、先端が蓄熱槽32内の伝熱管76(図2,
図4参照)に接続されている。発生槽側供給管44は、
途中にモータバルブ47が設けられ、先端が飽和水蒸気
発生槽34に接続されている。The water supply pipe 38 is branched downstream of the water supply pump 40 into a heat storage tank side water supply pipe 42 directed to the heat storage tank 32 and a generation tank side supply pipe 44 directed to the saturated steam generation tank 34. The heat storage tank side water supply pipe 42 has a motor valve 45
Is provided, and the tip of the heat transfer tube 76 (see FIG.
(See FIG. 4). The generation tank side supply pipe 44 is
A motor valve 47 is provided on the way, and its tip is connected to the saturated steam generation tank 34.
【0020】次に、蓄熱槽32で過熱された過熱水蒸気
の給蒸系統について説明する。先ほど説明したように、
蓄熱槽32への蓄熱槽側給水管42は蓄熱槽32内の伝
熱管76の一方の端部(図2の符号76a)に接続さ
れ、処理水が伝熱管76内に供給される。伝熱管76内
を通過する処理水は蓄熱部72によって過熱されて過熱
水蒸気(Superheated Vapor)となる。伝熱管76の他
方の端部(図2の符号76b)には過熱水蒸気を飽和水
蒸気発生槽34へ供給するための供給管46が接続され
ている。Next, a steam supply system for superheated steam superheated in the heat storage tank 32 will be described. As I explained earlier,
The heat storage tank side water supply pipe 42 to the heat storage tank 32 is connected to one end portion (reference numeral 76 a in FIG. 2) of the heat transfer pipe 76 in the heat storage tank 32, and the treated water is supplied into the heat transfer pipe 76. The treated water passing through the inside of the heat transfer tube 76 is superheated by the heat storage section 72 and becomes superheated steam (Superheated Vapor). A supply pipe 46 for supplying the superheated steam to the saturated steam generation tank 34 is connected to the other end portion (reference numeral 76b in FIG. 2) of the heat transfer pipe 76.
【0021】供給管46は、飽和水蒸気発生槽34内の
加熱管48の一端に接続されており、加熱管48内に過
熱水蒸気を供給する。加熱管48は、飽和水蒸気発生槽
34内部に配置されており、外表面に小孔が穿設され、
この小孔から過熱水蒸気を噴出可能となっている。加熱
管48から噴出した過熱水蒸気は、飽和水蒸気発生槽3
4内に貯留している処理水を直接加熱して処理水を蒸発
させて飽和水蒸気を発生させる。なお、飽和水蒸気発生
槽34内に貯留されている処理水内に噴出した過熱水蒸
気は熱交換の結果ドレン化して水に戻る。The supply pipe 46 is connected to one end of a heating pipe 48 in the saturated steam generation tank 34 and supplies superheated steam into the heating pipe 48. The heating pipe 48 is arranged inside the saturated steam generation tank 34, and a small hole is formed on the outer surface thereof.
Superheated steam can be ejected from this small hole. The superheated steam ejected from the heating pipe 48 is the saturated steam generation tank 3
The treated water stored in 4 is directly heated to evaporate the treated water and generate saturated steam. The superheated steam jetted into the treated water stored in the saturated steam generation tank 34 is drained as a result of heat exchange and returns to water.
【0022】次に、飽和水蒸気発生槽34への処理水の
供給・排出系統について説明する。先ほど説明したよう
に、発生槽側給水管44は飽和水蒸気発生槽34に接続
され、処理水を飽和水蒸気発生槽34内に供給する。加
熱管48から噴出する過熱水蒸気により加熱された処理
水は、飽和水蒸気と化して給蒸管50から給蒸される。
なお、飽和水蒸気発生槽34には緊急用の排水管51が
接続されている。Next, a system for supplying and discharging treated water to the saturated steam generation tank 34 will be described. As described above, the generation tank side water supply pipe 44 is connected to the saturated steam generation tank 34 and supplies the treated water into the saturated steam generation tank 34. The treated water heated by the superheated steam ejected from the heating pipe 48 is converted into saturated steam and steamed from the steam supply pipe 50.
An emergency drain pipe 51 is connected to the saturated steam generation tank 34.
【0023】飽和水蒸気発生槽34内に貯留されている
処理水は所定水量以上になると、水蒸気の発生効率上好
ましくないので、所定水量以上になったらこれを排出す
るオーバーフロー配管52が設けられている。オーバー
フロー配管52は中途部にバルブ54とドレントラップ
56が設けられ、先端部は貯留槽36内に配設されてい
る貯留槽伝熱管58に接続されている。貯留槽伝熱管5
8は、貯留槽36内に貯留されている処理水中に浸かる
ように設けられており、オーバーフローした水と貯留槽
36内の水とで熱交換している。すなわち、貯留槽36
内の水によりオーバーフローした発生槽34内の処理水
を冷却するとともに、貯留槽伝熱管58内を通過するオ
ーバーフローした処理水の熱により、貯留槽36に貯留
されている処理水が加熱されている。このように、貯留
槽36内の処理水が加熱されることによって、熱効率を
上げると共に貯留槽36内の処理水の脱気を行なうこと
ができる。If the amount of treated water stored in the saturated steam generation tank 34 exceeds a predetermined amount, it is not preferable in terms of steam generation efficiency. Therefore, an overflow pipe 52 is provided to discharge the treated water when the amount exceeds the predetermined amount. . A valve 54 and a drain trap 56 are provided in the middle of the overflow pipe 52, and a tip portion thereof is connected to a storage tank heat transfer pipe 58 arranged in the storage tank 36. Storage tank heat transfer tube 5
8 is provided so as to be immersed in the treated water stored in the storage tank 36, and heat exchange is performed between the overflowed water and the water in the storage tank 36. That is, the storage tank 36
The treated water in the generation tank 34 that has overflowed due to the water in the inside is cooled, and the treated water stored in the storage tank 36 is heated by the heat of the overflowed processed water that passes through the inside of the storage tank heat transfer tube 58. . As described above, by heating the treated water in the storage tank 36, it is possible to improve the thermal efficiency and deaerate the treated water in the storage tank 36.
【0024】貯留槽伝熱管58の先端は、貯留槽36内
で開口しており、オーバーフローした発生槽34内の処
理水と給水元管35から供給される処理水とが混合され
るように設けられている。このため、オーバーフローし
た発生槽34内の処理水は、再度過熱水蒸気か飽和水蒸
気に利用する事ができる。なお、オーバーフロー配管5
2と蓄熱槽側給水管42との間には、圧抜き用のバルブ
60が設けられている。The tip of the storage tank heat transfer tube 58 is open in the storage tank 36, and is provided so that the treated water in the overflow generation tank 34 and the treated water supplied from the water supply source pipe 35 are mixed. Has been. Therefore, the overflowed treated water in the generation tank 34 can be reused as superheated steam or saturated steam. In addition, overflow pipe 5
A valve 60 for pressure relief is provided between the heat storage tank side water supply pipe 42 and the heat storage tank side water supply pipe 42.
【0025】飽和水蒸気発生槽34で発生した飽和水蒸
気は、給蒸管50を通って出力される。なお、図面には
図示していないが、飽和水蒸気発生槽34と給蒸管50
との間には、飛沫同伴を防止する手段として公知の技術
であるバッフルまたはサイクロン等の構造を設けると好
適である。ただし、飛沫同伴防止手段としてはバッフル
やサイクロンに限定されることはない。The saturated steam generated in the saturated steam generation tank 34 is output through the steam supply pipe 50. Although not shown in the drawing, the saturated steam generation tank 34 and the steam supply pipe 50
A structure such as a baffle or a cyclone, which is a known technique as a means for preventing entrainment of droplets, is preferably provided between and. However, the baffle and the cyclone are not the only means for preventing entrainment.
【0026】また、給蒸管50には、途中にドレントラ
ップ69が設けられ、給蒸管50内で凝縮したドレンを
トラップしている。そして、ドレントラップ69でトラ
ップしたドレンを貯水槽36内に戻すためのドレン配管
71が、給蒸管50から分岐して配設されている。ドレ
ン配管71は、オーバーフロー配管52の中途部に接続
され、貯留槽36内に配置された貯留槽伝熱管58を経
て貯留槽36内で開口している。このような構成とした
ことで、貯留槽36内の温度を上げ、熱効率を上昇させ
ることができると共に脱気を行なうことができる。一
方、給蒸管50内で凝縮して生じたドレンを貯留槽36
に戻し、過熱水蒸気として用いるかまたは飽和水蒸気と
して用いることにより再利用ができ、処理水を有効利用
して無駄にしないようにすることができる。A drain trap 69 is provided in the steam supply pipe 50 midway to trap the drain condensed in the steam supply pipe 50. Further, a drain pipe 71 for returning the drain trapped by the drain trap 69 into the water storage tank 36 is provided so as to be branched from the steam supply pipe 50. The drain pipe 71 is connected to a midway portion of the overflow pipe 52 and opens in the storage tank 36 via the storage tank heat transfer pipe 58 arranged in the storage tank 36. With such a configuration, the temperature inside the storage tank 36 can be increased, the thermal efficiency can be increased, and deaeration can be performed. On the other hand, the drain produced by condensation in the steam supply pipe 50 is stored in the storage tank 36.
It can be reused by using it as superheated steam or as saturated steam, and the treated water can be effectively used and not wasted.
【0027】次に、飽和水蒸気を発生させるための制御
系についての説明をする。貯留槽36および飽和水蒸気
発生槽34内の、処理水が貯留されている部位には、処
理水の水質を検出するための水質検出手段62,64が
設けられている。水質検出手段62,64の一例として
は、それぞれ2枚の電極62a,62bと64a,64
bを有する電極スイッチが挙げられる。電極スイッチ
は、処理水の抵抗値(電気伝導度)を検出しており、抵
抗値が小さくなるほど不純物が増加していると判断す
る。水質検出手段62,64は制御部66に接続されて
おり、制御部66にて水質の判断が行なわれる。制御部
66では、それぞれの2枚の電極間の抵抗値を測定し、
抵抗値が小さくなって水質が低下したと判断した場合に
は、飽和水蒸気発生装置の運転を停止させることができ
る。このため、飽和水蒸気の水質を一定のレベルに維持
することができる。Next, a control system for generating saturated steam will be described. Water quality detection means 62, 64 for detecting the quality of the treated water are provided in the storage tank 36 and the saturated steam generation tank 34 at the portion where the treated water is stored. As an example of the water quality detecting means 62, 64, there are two electrodes 62a, 62b and 64a, 64, respectively.
An electrode switch having b is mentioned. The electrode switch detects the resistance value (electrical conductivity) of the treated water and determines that the impurities increase as the resistance value decreases. The water quality detecting means 62 and 64 are connected to the control unit 66, and the control unit 66 determines the water quality. The control unit 66 measures the resistance value between each of the two electrodes,
When it is determined that the resistance value has decreased and the water quality has deteriorated, the operation of the saturated steam generator can be stopped. Therefore, the water quality of the saturated steam can be maintained at a constant level.
【0028】また、飽和水蒸気発生槽34から飽和水蒸
気を出力する給蒸管50に設けられた圧力計70は、制
御部66に接続されており、発生した飽和水蒸気の圧力
を制御部66に入力させてフィードバック制御を行なう
ようにしている。制御部66では、測定された飽和水蒸
気圧に基づいて、常に一定圧の飽和水蒸気が出力される
ように、インバータ68を介して給水ポンプ40を制御
している。なお、上述してきたように、本実施形態の制
御部66は、特許請求の範囲の第1の制御手段と第2の
制御手段とを兼ね、水質維持の制御と出力される飽和水
蒸気圧を一定とする制御の両者の制御機能を有している
が、それぞれ別の機能を有する2つの制御部を設けた形
態としてもよい。さらに、上述してきたように発生した
飽和水蒸気の圧力に基づいて制御する他に、制御部66
は、発生した飽和水蒸気の蒸気量または温度を測定し、
これらの測定値に基づいて給水ポンプ40を制御しても
よい。給水ポンプ40を制御するのはインバータ68に
限られることはなく、調節弁をモータで可動させたり、
オリフィスの調整をするようにしてもよい。The pressure gauge 70 provided in the steam supply pipe 50 for outputting saturated steam from the saturated steam generation tank 34 is connected to the control unit 66, and the pressure of the generated saturated steam is input to the control unit 66. By doing so, feedback control is performed. The control unit 66 controls the water supply pump 40 via the inverter 68 so that the saturated steam having a constant pressure is always output based on the measured saturated steam pressure. As described above, the control unit 66 of the present embodiment serves both as the first control unit and the second control unit in the claims, and controls the water quality maintenance and outputs the saturated steam pressure constant. Although it has both control functions of the control described above, it may be possible to provide two control units having different functions. Further, in addition to the control based on the pressure of the saturated steam generated as described above, the control unit 66
Measures the amount or temperature of the generated saturated steam,
The water supply pump 40 may be controlled based on these measured values. The control of the water supply pump 40 is not limited to the inverter 68, and the control valve can be moved by a motor,
The orifice may be adjusted.
【0029】上述してきた飽和水蒸気発生装置で用いる
蓄熱槽32について、図2に基づいて説明する。なお、
以下、蓄熱槽を加熱するヒータの一例として電気ヒータ
を用いた形態を説明するが、蓄熱槽を加熱するヒータと
しては電気ヒータに限定されるものではない。電気ヒー
タ以外には、蒸気ヒータやオイルヒータ等が考えられ
る。図2に示す蓄熱槽32は、個体蓄熱材と液体蓄熱材
とが混合された蓄熱材が充填されて成る蓄熱部72内
に、蓄熱材を加熱する電気ヒータ74と処理水が供給さ
れる伝熱管76とが配設されている。更に、この蓄熱部
72は、その外周面が断熱材78によって覆われてお
り、蓄熱部72からの放熱を防止している。かかる蓄熱
部72に充填された蓄熱材には、粒径の異なる固体蓄熱
材と液体蓄熱材とが用いられ、粒径の異なる固体蓄熱材
が、大粒径の固体蓄熱材の間隙に小粒径の固体蓄熱材が
入り込むように充填されており、大粒径の固体蓄熱材と
小粒径の固体蓄熱材との間隙に液体蓄熱材が充填されて
いる。The heat storage tank 32 used in the above-described saturated steam generator will be described with reference to FIG. In addition,
Hereinafter, a mode in which an electric heater is used as an example of a heater for heating the heat storage tank will be described, but the heater for heating the heat storage tank is not limited to the electric heater. Besides the electric heater, a steam heater, an oil heater, etc. can be considered. In the heat storage tank 32 shown in FIG. 2, an electric heater 74 for heating the heat storage material and treated water are supplied into a heat storage part 72 which is filled with a heat storage material in which a solid heat storage material and a liquid heat storage material are mixed. A heat pipe 76 is provided. Furthermore, the outer peripheral surface of the heat storage section 72 is covered with a heat insulating material 78 to prevent heat release from the heat storage section 72. A solid heat storage material having a different particle size and a liquid heat storage material are used as the heat storage material filled in the heat storage section 72, and the solid heat storage material having a different particle size is formed into a small particle in a gap between the solid heat storage material having a large particle size. The solid heat storage material having a diameter is filled so as to enter, and the liquid heat storage material is filled in a gap between the solid heat storage material having a large particle diameter and the solid heat storage material having a small particle diameter.
【0030】かかる蓄熱部72における蓄熱材の充填の
状態を図3に示す。図3(a)は、大粒径の固体蓄熱材
77aと小粒径の固体蓄熱材77bとの粒径が二種類の
固体蓄熱材と液体蓄熱材80とが充填された状態であっ
て、大粒径の固体蓄熱材77aの間隙に小粒径の固体蓄
熱材77bが入り込んで充填され、固体蓄熱材77a,
77bの間隙には液体蓄熱材80が充填されている。FIG. 3 shows the state of filling the heat storage material in the heat storage section 72. FIG. 3A shows a state in which a solid heat storage material 77a having a large particle size and a solid heat storage material 77b having a small particle size are filled with two types of solid heat storage materials and a liquid heat storage material 80, The solid heat storage material 77a having a small particle diameter is inserted and filled in the gap of the solid heat storage material 77a having a large particle diameter,
A liquid heat storage material 80 is filled in the gap 77b.
【0031】また、図3(b)は、粒径が三種類の固体
蓄熱材と液体蓄熱材80とが充填された蓄熱部72の状
態を示す。この固体蓄熱材は、大粒径の固体蓄熱材77
a、小粒径の固体蓄熱材77b及び固体蓄熱材77a,
77bの中間の粒径である中粒径の固体蓄熱材77cか
ら成り、大粒径の固体蓄熱材77aの間隙に中粒径の固
体蓄熱材77cが入り込んで充填されていると共に、固
体蓄熱材77a,77cの間隙に小粒径の固体蓄熱材7
7bが入り込むように充填されている。更に、充填され
た固体蓄熱材77a,77b,77cの間隙には、液体
蓄熱材80が充填されている。この様に、図3(a)
(b)に示す様に、粒径の異なる固体蓄熱材が、大粒径
の固体蓄熱材の間隙に小粒径の固体蓄熱材が入り込むよ
うに充填され、且つ固体蓄熱材の間隙に液体蓄熱材が充
填されている蓄熱部72では、固体蓄熱材と液体蓄熱材
との充填密度を、実質的に同一粒径の固体蓄熱材と液体
蓄熱材との充填密度に比較して向上でき、蓄熱量及び伝
熱管76への熱伝導を向上できる。Further, FIG. 3B shows a state of the heat storage part 72 filled with the solid heat storage material having three kinds of particle diameters and the liquid heat storage material 80. This solid heat storage material is a solid heat storage material 77 having a large particle size.
a, a small-sized solid heat storage material 77b and a solid heat storage material 77a,
The solid heat storage material 77c having a medium particle diameter, which is an intermediate particle diameter of 77b, is filled with the solid heat storage material 77c having a medium particle diameter in a gap of the solid heat storage material 77a having a large particle diameter. Solid heat storage material 7 of small particle size in the gap between 77a and 77c
It is filled so that 7b may enter. Further, a liquid heat storage material 80 is filled in the gap between the filled solid heat storage materials 77a, 77b, 77c. Thus, FIG. 3 (a)
As shown in (b), the solid heat storage materials having different particle sizes are filled so that the solid heat storage material having a small particle size enters the gap between the solid heat storage materials having a large particle size, and the liquid heat storage material is stored in the gap between the solid heat storage materials. In the heat storage part 72 filled with the material, the packing densities of the solid heat storage material and the liquid heat storage material can be improved as compared with the packing densities of the solid heat storage material and the liquid heat storage material having substantially the same particle size, The quantity and heat transfer to the heat transfer tube 76 can be improved.
【0032】図3(a)(b)に示す固体蓄熱材として
は、マグネシア、マグネタイト、シリカ及びアルミナか
ら選ばれた一種又は二種以上の粒体を好適に用いること
ができ、液体蓄熱材としては、硝酸塩を好適に用いるこ
とができる。硝酸塩は、室温では固体であるが、142
℃以上では溶融して液体となる。蓄熱部42を形成する
蓄熱材の組成の一例としては、大粒径マグネシア55
%、小粒径マグネシア25%、及び硝酸塩20%とする
と好適である。As the solid heat storage material shown in FIGS. 3 (a) and 3 (b), one or more kinds of granules selected from magnesia, magnetite, silica and alumina can be preferably used. A nitrate can be preferably used for the above. Nitrate is a solid at room temperature
It melts and becomes a liquid above ℃. As an example of the composition of the heat storage material forming the heat storage section 42, a large particle size magnesia 55 is used.
%, Small particle size magnesia 25%, and nitrate 20% are preferred.
【0033】かかる蓄熱部42に設けられた電気ヒータ
74は、合計27kWの電気容量となるように3本の電
気ヒータが配設されて成る。具体的な例として、蓄熱槽
32全体で使用可能な電力容量が27kWであれば、蓄
熱槽32に設けられた電気ヒータは、15kWの電気ヒ
ータ74aが1本、6kWの電気ヒータ74b,74c
が2本設けられているようにする。この中で電気容量が
最も高い15kWの電気ヒータ74aは、伝熱管76の
導入口側(符号76a側)に位置するように設けられ、
残りの6kWの電気ヒータ74b,74cはそれぞれ伝
熱管76の中途部と吐出口側(符号76b)側を加熱す
るように設けられている。このように、伝熱管76の導
入口側に、最も高温となる電気ヒータを配置したこと
で、伝熱管76の導入口側を重点的に加熱可能である。
すなわち、飽和水蒸気の発生動作中には、特に伝熱管7
6の導入口側の温度の低下があるので、導入口側のみを
重点的に再加熱を図ることができるのである。The electric heater 74 provided in the heat storage section 42 is formed by disposing three electric heaters so as to have a total electric capacity of 27 kW. As a specific example, if the electric power capacity that can be used in the entire heat storage tank 32 is 27 kW, the electric heater provided in the heat storage tank 32 includes one 15 kW electric heater 74a and 6 kW electric heaters 74b and 74c.
Make sure there are two. Among them, the electric heater 74a having the highest electric capacity of 15 kW is provided so as to be located on the inlet side (the reference numeral 76a side) of the heat transfer tube 76,
The remaining 6 kW electric heaters 74b and 74c are provided so as to heat the middle portion of the heat transfer tube 76 and the discharge port side (reference numeral 76b) side, respectively. As described above, by disposing the electric heater having the highest temperature on the inlet side of the heat transfer tube 76, the inlet side of the heat transfer tube 76 can be heated intensively.
That is, during the operation of generating saturated steam, the heat transfer tube 7 is
Since there is a decrease in the temperature on the inlet side of No. 6, it is possible to focus reheating only on the inlet side.
【0034】なお、電気ヒータの配置についての他の実
施形態について図4に基づいて説明する。すなわち、上
述した実施形態の電気ヒータ74の配置は、合計の消費
電力を従来の物と同一にし、その配分を伝熱管76導入
口側が大きくなるように傾斜配分させたものであった。
しかし、深夜電力を用いた蓄熱と、温度低下が著しい導
入口側を再加熱する場合とでは別の電気ヒータを用いる
ようにしても好適である。つまり、電気ヒータ82の配
置は、9kWの電気ヒータ82a,82b,82cの3
本を用いることにより深夜電力を用いて蓄熱し、この3
本の電気ヒータとは別に導入口側のみを加熱する電気ヒ
ータ82dを設けるのである。この導入口側のみを加熱
する電気ヒータ82dの電気容量は、蓄熱槽32全体に
使用できる電力全てを用いることができるように27k
Wにするとよい。つまり、飽和水蒸気発生中あるいは発
生後の再加熱時にはこの電気ヒータ82dのみに通電す
ることで、特に温度低下が著しい導入口側を重点的に再
加熱することができる。Another embodiment of the arrangement of the electric heater will be described with reference to FIG. That is, in the arrangement of the electric heaters 74 of the above-described embodiment, the total power consumption is the same as that of the conventional one, and the distribution thereof is inclined so that the heat transfer tube 76 introduction port side becomes larger.
However, it is preferable to use different electric heaters for heat storage using late-night power and for reheating the inlet side where the temperature drop is remarkable. That is, the arrangement of the electric heater 82 is 3 kW of the 9 kW electric heaters 82a, 82b, 82c.
By using a book to store heat using late-night power,
In addition to the electric heater of the book, an electric heater 82d for heating only the inlet side is provided. The electric capacity of the electric heater 82d that heats only the inlet side is 27 k so that all the electric power that can be used for the entire heat storage tank 32 can be used.
Set to W. That is, during reheating after or after the generation of saturated steam, by energizing only the electric heater 82d, it is possible to reheat the inlet side where the temperature drop is particularly remarkable.
【0035】さらに、電気ヒータの配置の他の実施形態
としては、電気容量の等しい3本の電気ヒータを導入口
側、中間部、吐出口側に配置し、それぞれ独立して制御
可能としてもよい(図示せず)。このよう配置した場合
であっても導入口側だけを重点的に加熱可能となる。Further, as another embodiment of the arrangement of the electric heaters, three electric heaters having the same electric capacity may be arranged on the introduction port side, the intermediate portion, and the discharge port side so that they can be independently controlled. (Not shown). Even in the case of such an arrangement, it is possible to heat only the introduction port side.
【0036】なお、電気ヒータ74,82を用いること
によって、クリーンなエネルギーである電気によって蓄
熱材を加熱でき、且つ低コストな深夜電力によって蓄熱
材を加熱できるため、クリーンで且つ安価な過熱水蒸気
を得ることができる。ここで、過熱水蒸気を連続して8
時間以上も吐出することができる通常のボイラー、つま
り重油等の燃料を炊くボイラーでは、燃料タンク、燃料
配管、空気ダクト、排ガスダクト等の付属設備を必要と
し、そのサイズが極めて大きくなる。この点、図2およ
び図4に示す蓄熱槽32では、電気ヒータ74,82を
蓄熱材の加熱ヒータとして採用するため、燃料タンク等
の付属設備を不要とすることができ、蓄熱槽を極めてコ
ンパクトとすることができる。By using the electric heaters 74 and 82, the heat storage material can be heated by electricity which is clean energy, and the heat storage material can be heated by low-cost midnight power, so that clean and inexpensive overheated steam can be generated. Obtainable. Here, the superheated steam is continuously supplied for 8
A normal boiler capable of discharging for more than a time, that is, a boiler that cooks fuel such as heavy oil requires auxiliary equipment such as a fuel tank, a fuel pipe, an air duct, and an exhaust gas duct, and its size becomes extremely large. In this respect, in the heat storage tank 32 shown in FIGS. 2 and 4, since the electric heaters 74 and 82 are used as the heaters for heating the heat storage material, auxiliary equipment such as a fuel tank can be eliminated, and the heat storage tank is extremely compact. Can be
【0037】なお、上述してきた実施形態は、過熱水蒸
気を直接飽和水蒸気発生槽34内に貯留された処理水に
直接接触させるようにしたが(バブリング加熱)、過熱
水蒸気は飽和水蒸気発生用の処理水に直接接触させず、
加熱用の管を通して熱交換することにより加熱するよう
にしてもよい(間接加熱)。In the embodiment described above, the superheated steam is brought into direct contact with the treated water stored in the saturated steam generating tank 34 (bubbling heating), but the superheated steam is treated for generating saturated steam. Without direct contact with water,
You may make it heat by exchanging heat through the tube for heating (indirect heating).
【0038】また、上述した実施形態によるヒータの電
気容量の具体的な数値はあくまで一例として説明しただ
けであって、上述したような数値のヒータに限定される
ものではない。さらに、水質検出手段としては電極スイ
ッチに限定されず、水質を検出できるものであればよ
い。Further, the specific numerical value of the electric capacity of the heater according to the above-mentioned embodiment is described only as an example, and is not limited to the heater having the numerical value as described above. Further, the water quality detecting means is not limited to the electrode switch, and any means capable of detecting the water quality may be used.
【0039】[0039]
【発明の効果】本発明に係る飽和水蒸気発生装置は、ヒ
ータを伝熱管における水の導入口側が過熱された過熱水
蒸気の吐出口側よりも高温となるように、固体蓄熱材及
び液体蓄熱材を加熱可能に設けたので、他の部位よりも
温度低下が著しい伝熱管の導入口側を十分に再加熱する
ことができる。また、ヒータを、少なくとも伝熱管にお
ける水の導入口側と過熱された過熱水蒸気の吐出口側と
の前記固体蓄熱材及び液体蓄熱材を別々のヒータで加熱
可能となるように複数設けることで、伝熱管の導入口側
の再加熱を効率よく行なうことができる。さらに、複数
のヒータのうち伝熱管における水の導入口側に配置され
た一のヒータは、過熱された過熱水蒸気の吐出口側に配
置された他のヒータよりも高温となるものであることを
特徴とすれば、伝熱管の導入口側を効率よく十分に再加
熱することが可能である。EFFECT OF THE INVENTION The saturated steam generator according to the present invention uses a solid heat storage material and a liquid heat storage material so that the heater has a temperature higher than that of a discharge port side of superheated steam on the water inlet side of the heat transfer tube. Since it is provided so that it can be heated, it is possible to sufficiently reheat the inlet side of the heat transfer tube where the temperature drop is more remarkable than other parts. In addition, by providing a plurality of heaters, at least the solid heat storage material and the liquid heat storage material of the water inlet side of the heat transfer tube and the discharge side of the superheated steam that has been overheated can be heated by separate heaters, It is possible to efficiently reheat the inlet side of the heat transfer tube. Further, among the plurality of heaters, one heater arranged on the water inlet side of the heat transfer tube has a higher temperature than the other heater arranged on the outlet side of the overheated steam. Characteristically, the inlet side of the heat transfer tube can be efficiently and sufficiently reheated.
【0040】本発明にかかる飽和水蒸気発生装置によれ
ば、飽和水蒸気発生槽へ水を供給するための給水管の中
途部には、水を一旦貯留する貯留槽が設けられ、飽和水
蒸気発生槽および/または貯留槽には、給水水質を測定
する水質測定手段が設けられているので、飽和水蒸気を
発生させる水質を管理することにより、清浄な飽和水蒸
気を提供できる。また、水質測定手段によって、飽和水
蒸気となるべき水の水質が低下したことが測定された場
合には、飽和水蒸気発生の運転を停止させるように制御
する第1の制御手段を具備するので、より確実に飽和水
蒸気の質を向上させ、清浄な飽和水蒸気のみを提供でき
る。さらに、飽和水蒸気発生槽内でオーバーフローした
水を貯留槽へ戻すためのオーバーフロー配管が設けたこ
とにより、オーバーフローした水を廃棄しないようにす
ることができ、水を無駄にしないようにしてランニング
コストの低減を図ることができる。なお、給蒸管内で凝
縮したドレンを給蒸管から排出して前記貯留槽へ戻すた
めのドレン配管が設けられているので、給蒸管内のドレ
ンを廃棄せず再利用するので、水を無駄にしないように
してランニングコストの低減を図れる。According to the saturated steam generator of the present invention, a storage tank for temporarily storing water is provided in the middle of a water supply pipe for supplying water to the saturated steam generation tank. Since the storage tank is provided with water quality measuring means for measuring the quality of the supplied water, it is possible to provide clean saturated steam by controlling the quality of water that produces saturated steam. Further, when the water quality measuring unit measures that the water quality of the water to be saturated steam has deteriorated, it is provided with the first control unit for controlling so as to stop the operation of the saturated steam generation. It is possible to reliably improve the quality of saturated steam and provide only clean saturated steam. Further, by providing the overflow pipe for returning the overflowed water in the saturated steam generation tank to the storage tank, it is possible to prevent the overflowed water from being discarded and to prevent the water from being wasted and to reduce the running cost. It can be reduced. Since the drain pipe for discharging the drain condensed in the steam supply pipe to the storage tank and returning it to the storage tank is reused without discarding the drain in the steam supply pipe, water is wasted. It is possible to reduce the running cost by not doing so.
【0041】本発明にかかる飽和水蒸気発生装置によれ
ば、圧力測定手段によって測定された飽和水蒸気圧力値
が入力され、飽和水蒸気圧力値に基づいて給水ポンプを
制御する第2の制御手段が設けられているので、より安
定した飽和水蒸気の出力が期待できる。また、伝熱管お
よび飽和水蒸気発生槽へ水を送り込む給水ポンプを共通
化して1つだけ設けたので、稼動部品である給水ポンプ
の数を従来よりも減らして1つとしたので、メンテナン
スが容易となり且つ部品点数の削減も図れる。According to the saturated steam generator of the present invention, the saturated steam pressure value measured by the pressure measuring means is input, and the second control means for controlling the water supply pump based on the saturated steam pressure value is provided. Therefore, a more stable output of saturated steam can be expected. In addition, since only one water supply pump that feeds water to the heat transfer tube and the saturated steam generation tank is provided in common, the number of water supply pumps that are operating parts is reduced to one compared with the conventional one, and maintenance is easy. The number of parts can be reduced.
【図1】本発明に係る飽和水蒸気発生装置の一例を説明
する略線図である。FIG. 1 is a schematic diagram illustrating an example of a saturated steam generator according to the present invention.
【図2】図1に用いられている蓄熱槽の構造を説明する
ための断面図である。FIG. 2 is a cross-sectional view for explaining the structure of the heat storage tank used in FIG.
【図3】蓄熱部における蓄熱材の充填の状態を説明する
説明図である。FIG. 3 is an explanatory diagram illustrating a state of filling a heat storage material in a heat storage unit.
【図4】蓄熱槽の構造において他の実施形態を示す断面
図である。FIG. 4 is a cross-sectional view showing another embodiment of the structure of the heat storage tank.
【図5】従来の飽和水蒸気発生装置を説明する略線図で
ある。FIG. 5 is a schematic diagram illustrating a conventional saturated steam generator.
【図6】従来の飽和水蒸気発生装置に用いられている蓄
熱槽の構造を説明するための断面図である。FIG. 6 is a cross-sectional view for explaining the structure of a heat storage tank used in a conventional saturated steam generator.
30 飽和水蒸気発生装置 32 蓄熱槽 34 発生槽 35 給水元管 36 貯留槽 38 給水管 39 ストレーナ 40 給水ポンプ 42 蓄熱槽側管 44 飽和水蒸気発生槽側管 45,47,60 バルブ 46 供給管 48 加熱管 50 給蒸管 51 排水管 52 オーバーフロー配管 56,69 ドレントラップ 58 貯留槽伝熱管 62,64 水質検出手段 66 制御部 68 インバータ 71 ドレン配管 72 蓄熱部 74,82 電気ヒータ 76 伝熱管 77a,77b,77c 固体蓄熱材 78 断熱材 80 液体蓄熱材 30 Saturated steam generator 32 heat storage tank 34 Generation tank 35 Water source pipe 36 Storage tank 38 Water pipe 39 Strainer 40 water pump 42 Heat storage tank side tube 44 Saturated steam generation tank side tube 45, 47, 60 valves 46 Supply pipe 48 heating tube 50 steam supply pipe 51 drain pipe 52 Overflow piping 56,69 drain trap 58 Storage tank heat transfer tube 62,64 Water quality detection means 66 control unit 68 Inverter 71 Drain piping 72 Heat storage part 74,82 Electric heater 76 heat transfer tube 77a, 77b, 77c Solid heat storage material 78 Insulation 80 Liquid heat storage material
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) F28D 20/00 B ─────────────────────────────────────────────────── ─── Continuation of front page (51) Int.Cl. 7 Identification code FI theme code (reference) F28D 20/00 B
Claims (9)
該蓄熱槽内で過熱されて得られた過熱水蒸気によって飽
和水蒸気発生槽内の水を加熱して飽和水蒸気を発生させ
る飽和水蒸気発生装置であって、 前記蓄熱槽に設けられた固体蓄熱材と液体蓄熱材とが充
填されて成る蓄熱部内には、前記固体蓄熱材及び液体蓄
熱材を加熱するヒータと、内部を通過する水を過熱して
過熱水蒸気とする伝熱管とが設けられ、 前記ヒータは、伝熱管における水の導入口側が過熱され
た過熱水蒸気の吐出口側よりも高温となるように、前記
固体蓄熱材及び液体蓄熱材を加熱可能に設けられている
ことを特徴とする飽和水蒸気発生装置。1. A heat storage tank and a saturated steam generation tank are provided,
A saturated steam generator that heats water in a saturated steam generation tank by superheated steam obtained by being overheated in the heat storage tank to generate saturated steam, wherein a solid heat storage material and a liquid provided in the heat storage tank In the heat storage section filled with the heat storage material, a heater that heats the solid heat storage material and the liquid heat storage material, and a heat transfer tube that superheats water passing through to become superheated steam are provided, and the heater is The saturated steam generation is characterized in that the solid heat storage material and the liquid heat storage material can be heated so that the water inlet side of the heat transfer tube becomes higher in temperature than the discharge side of the superheated steam that has been overheated. apparatus.
る水の導入口側と過熱された過熱水蒸気の吐出口側との
前記固体蓄熱材及び液体蓄熱材を別々のヒータで加熱可
能となるように複数設けられていることを特徴とする請
求項1記載の飽和水蒸気発生装置。2. A plurality of heaters are provided such that at least the solid heat storage material and the liquid heat storage material on the water inlet side and the superheated steam outlet side of the heat transfer tube can be heated by separate heaters. The saturated steam generator according to claim 1, wherein the saturated steam generator is provided.
水の導入口側に配置された一のヒータは、過熱された過
熱水蒸気の吐出口側に配置された他のヒータよりも高温
となるものであることを特徴とする請求項2記載の飽和
水蒸気発生装置。3. One of the plurality of heaters disposed on the water inlet side of the heat transfer tube has a higher temperature than other heaters disposed on the outlet side of the overheated steam. The saturated steam generator according to claim 2, wherein
該蓄熱槽内で過熱されて得られた過熱水蒸気によって飽
和水蒸気発生槽内の水を加熱して飽和水蒸気を発生する
飽和水蒸気発生装置であって、 前記蓄熱槽に設けられた固体蓄熱材と液体蓄熱材とが充
填されて成る蓄熱部内には、前記固体蓄熱材及び液体蓄
熱材を加熱するヒータと、内部を通過する水を過熱して
過熱水蒸気とする伝熱管とが設けられ、 該伝熱管から供給される過熱水蒸気と接触して飽和水蒸
気を発生させる水を飽和水蒸気発生槽に供給する給水管
の中途部には、前記水を一旦貯留する貯留槽が設けら
れ、 前記飽和水蒸気発生槽および/または貯留槽には、給水
水質を測定する水質測定手段が設けられていることを特
徴とする飽和水蒸気発生装置。4. A heat storage tank and a saturated steam generation tank are provided,
A saturated steam generator that heats water in a saturated steam generation tank by superheated steam obtained by being overheated in the heat storage tank to generate saturated steam, wherein a solid heat storage material and a liquid provided in the heat storage tank. In the heat storage part filled with the heat storage material, a heater for heating the solid heat storage material and the liquid heat storage material, and a heat transfer tube for superheating water passing through the inside to be superheated steam are provided. A storage tank for temporarily storing the water is provided in the middle of a water supply pipe that supplies water that generates saturated steam by contacting with superheated steam supplied from the saturated steam generation tank. A saturated water vapor generator characterized in that the storage tank is provided with water quality measuring means for measuring the quality of the supplied water.
となるべき水の水質が低下したことが測定された場合に
は、飽和水蒸気発生の運転を停止させるように制御する
第1の制御手段を具備することを特徴とする請求項4記
載の飽和水蒸気発生装置。5. When the water quality measuring means measures that the water quality of the water to be saturated steam has deteriorated, it comprises a first control means for controlling to stop the operation of generating saturated steam. The saturated steam generator according to claim 4, wherein
ーした水を前記貯留槽へ戻すためのオーバーフロー配管
が設けられていることを特徴とする請求項4または5記
載の飽和水蒸気発生装置。6. The saturated steam generator according to claim 4, further comprising an overflow pipe for returning water overflowing in the saturated steam generation tank to the storage tank.
生槽で発生した飽和水蒸気を吐出する給蒸管が設けら
れ、 該給蒸管内で凝縮したドレンを給蒸管から排出して前記
貯留槽へ戻すためのドレン配管が設けられていることを
特徴とする請求項4,5または6記載の飽和水蒸気発生
装置。7. The saturated steam generation tank is provided with a steam supply pipe for discharging saturated steam generated in the saturated steam generation tank, and drains condensed in the steam supply pipe are discharged from the steam supply pipe to store the water. The saturated steam generator according to claim 4, 5 or 6, characterized in that a drain pipe for returning to the tank is provided.
該蓄熱槽内で過熱されて得られた過熱水蒸気によって飽
和水蒸気発生槽で水を加熱して飽和水蒸気を発生する飽
和水蒸気発生装置であって、 前記蓄熱槽に設けられた固体蓄熱材と液体蓄熱材とが充
填されて成る蓄熱部内には、前記固体蓄熱材及び液体蓄
熱材を加熱するヒータと、内部を通過する水を過熱して
過熱水蒸気とする伝熱管とが設けられ、 前記伝熱管へ水を供給するための給水ポンプが設けら
れ、 前記飽和水蒸気発生槽で発生した飽和水蒸気圧力を測定
する圧力測定手段が設けられ、 該圧力測定手段によって測定された飽和水蒸気圧力値が
入力され、該飽和水蒸気圧力値が常時一定となるように
前記給水ポンプを制御する第2の制御手段が設けられて
いることを特徴とする飽和水蒸気発生装置。8. A heat storage tank and a saturated steam generation tank are provided,
A saturated steam generator for heating water in a saturated steam generation tank to generate saturated steam by superheated steam obtained by overheating in the heat storage tank, wherein a solid heat storage material and liquid heat storage provided in the heat storage tank. In the heat storage section formed by filling the material with a material, a heater that heats the solid heat storage material and the liquid heat storage material, and a heat transfer tube that superheats water passing through the inside to become superheated steam are provided, A water supply pump for supplying water is provided, pressure measuring means for measuring the saturated water vapor pressure generated in the saturated water vapor generating tank is provided, and the saturated water vapor pressure value measured by the pressure measuring means is input, A saturated steam generator, comprising second control means for controlling the water supply pump so that the saturated steam pressure value is always constant.
ために下流側で分岐し、該分岐先がそれぞれ前記伝熱管
および前記飽和水蒸気発生槽へ接続されて成る給水管に
1つ設けられていることを特徴とする請求項8記載の飽
和水蒸気発生装置。9. The water supply pump branches downstream to supply water to the heat transfer tube and the saturated steam generation tank, and the branch destinations are connected to the heat transfer tube and the saturated steam generation tank, respectively. The saturated water vapor generator according to claim 8, wherein one is provided in the water supply pipe.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2001263319A JP4674011B2 (en) | 2001-08-31 | 2001-08-31 | Saturated steam generator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2001263319A JP4674011B2 (en) | 2001-08-31 | 2001-08-31 | Saturated steam generator |
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Cited By (13)
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JP2003205019A (en) * | 2002-01-10 | 2003-07-22 | Chiyoda Manufacturing Co Ltd | Steam sterilization system |
JP2005221182A (en) * | 2004-02-06 | 2005-08-18 | Hokuriku Electric Power Co Inc:The | Heat storage tank |
JP2011513930A (en) * | 2008-03-03 | 2011-04-28 | ビョン チョル リ | Mixed plasma generating apparatus and method, and electrothermal cooking apparatus using mixed plasma |
US8168132B2 (en) | 2006-07-07 | 2012-05-01 | Scican Ltd. | Apparatus and method for drying instruments using superheated steam |
CN102777874A (en) * | 2012-08-30 | 2012-11-14 | 郑州大学 | Phase change heat accumulation system for generating steam directly and preparation method of phase change heat accumulation agent |
JP2013064593A (en) * | 2011-09-15 | 2013-04-11 | Siemens Ag | Modification of spatial temperature profile in heat exchanger of heat energy storage and recovery device |
JP2015178927A (en) * | 2014-03-19 | 2015-10-08 | 株式会社豊田中央研究所 | Heat storage system |
JP2018194283A (en) * | 2017-05-22 | 2018-12-06 | タイガー魔法瓶株式会社 | Steam generator |
CN109833488A (en) * | 2019-03-06 | 2019-06-04 | 吴克足 | A kind of biology,drug and chemical industry factory heating device |
WO2019167488A1 (en) * | 2018-02-28 | 2019-09-06 | パナソニックIpマネジメント株式会社 | Superheated steam generator and cooker |
CN111121511A (en) * | 2020-02-17 | 2020-05-08 | 沈阳世杰电器有限公司 | Heat storage and heat conversion device built by solid building blocks |
CN113521362A (en) * | 2020-04-03 | 2021-10-22 | 苏州维斯勒姆智能科技有限公司 | Automatic medical instrument boiling sterilizer |
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JPH01193502A (en) * | 1988-01-28 | 1989-08-03 | Marutaka Kogyo Kk | Steam character converter |
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Cited By (17)
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JP2003205019A (en) * | 2002-01-10 | 2003-07-22 | Chiyoda Manufacturing Co Ltd | Steam sterilization system |
JP2005221182A (en) * | 2004-02-06 | 2005-08-18 | Hokuriku Electric Power Co Inc:The | Heat storage tank |
US8168132B2 (en) | 2006-07-07 | 2012-05-01 | Scican Ltd. | Apparatus and method for drying instruments using superheated steam |
JP2011513930A (en) * | 2008-03-03 | 2011-04-28 | ビョン チョル リ | Mixed plasma generating apparatus and method, and electrothermal cooking apparatus using mixed plasma |
JP2013064593A (en) * | 2011-09-15 | 2013-04-11 | Siemens Ag | Modification of spatial temperature profile in heat exchanger of heat energy storage and recovery device |
CN102777874A (en) * | 2012-08-30 | 2012-11-14 | 郑州大学 | Phase change heat accumulation system for generating steam directly and preparation method of phase change heat accumulation agent |
CN102777874B (en) * | 2012-08-30 | 2015-02-04 | 郑州大学 | Phase change heat accumulation system for generating steam directly and preparation method of phase change heat accumulation agent |
JP2015178927A (en) * | 2014-03-19 | 2015-10-08 | 株式会社豊田中央研究所 | Heat storage system |
JP2018194283A (en) * | 2017-05-22 | 2018-12-06 | タイガー魔法瓶株式会社 | Steam generator |
WO2019167488A1 (en) * | 2018-02-28 | 2019-09-06 | パナソニックIpマネジメント株式会社 | Superheated steam generator and cooker |
CN109833488A (en) * | 2019-03-06 | 2019-06-04 | 吴克足 | A kind of biology,drug and chemical industry factory heating device |
CN111121511A (en) * | 2020-02-17 | 2020-05-08 | 沈阳世杰电器有限公司 | Heat storage and heat conversion device built by solid building blocks |
CN111121511B (en) * | 2020-02-17 | 2024-04-30 | 沈阳世杰电器有限公司 | Heat storage and heat conversion device built by solid building blocks |
CN113521362A (en) * | 2020-04-03 | 2021-10-22 | 苏州维斯勒姆智能科技有限公司 | Automatic medical instrument boiling sterilizer |
CN113521362B (en) * | 2020-04-03 | 2022-11-25 | 江苏康康同学科技有限公司 | Automatic boiling sterilizer for medical instruments |
CN113776038A (en) * | 2021-10-15 | 2021-12-10 | 鸿蒙能源(山东)有限公司 | Ultralow-consumption electromagnetic induction evaporation industrial steam system |
CN113776038B (en) * | 2021-10-15 | 2023-09-22 | 鸿蒙能源(山东)有限公司 | Ultra-low power consumption electromagnetic induction evaporation industrial steam system |
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