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JP4548907B2 - Operation method of high temperature filter - Google Patents
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JP4548907B2 - Operation method of high temperature filter - Google Patents

Operation method of high temperature filter Download PDF

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JP4548907B2
JP4548907B2 JP2000195684A JP2000195684A JP4548907B2 JP 4548907 B2 JP4548907 B2 JP 4548907B2 JP 2000195684 A JP2000195684 A JP 2000195684A JP 2000195684 A JP2000195684 A JP 2000195684A JP 4548907 B2 JP4548907 B2 JP 4548907B2
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temperature
tower
filter
valve
pressure
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JP2002011310A (en
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昭吾 梅本
利夫 森田
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Organo Corp
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Organo Corp
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Description

【0001】
【発明の属する技術分野】
本発明は、たとえば発電所における給水系やヒータドレン系における高温水を濾過処理する高温濾過装置の運転方法に関する。
【0002】
【従来の技術】
発電所等では、給水系やヒータドレン系において100℃以上の高温水を濾過処理することがあるが、この高温濾過装置には、高温水に耐え得る耐熱性のフィルタを用いる必要がある。従来から、金属フィルタやセラミックフィルタ等の使用が検討されているが、近年、疎水性の高分子フィルタの使用が検討され始めている。
【0003】
疎水性高分子フィルタは、一旦乾燥されてしまうと、疎水性が発揮されて水を通さなくなり、濾過機能が失われる性質を有している。そのため、たとえば通水初期に、フィルタ差圧(フィルタ圧力損失)や高温水処理システムの差圧、あるいは水温との関係で、フィルタの二次側の圧力が処理する高温水の飽和蒸気圧以下になると、被処理水はフィルタ面で蒸気に変化し、フィルタが乾いてフィルタによる水処理そのものが不可能になり、系統へ濾過処理された水として回収できなくなる場合がある。疎水性高分子フィルタが一度乾燥してしまうと、性能を復元させるためには、薬品による湿潤化作業が必要となる。したがって、高分子フィルタを適用する場合には、常時、該フィルタが乾燥に至らない条件を採用することが望まれる。
【0004】
一方、金属フィルタやセラミックフィルタは、発電所におけるヒータドレン水のような200℃程度の温度条件下でも使用可能であるが、除鉄性能が不安定であること、差圧が上昇しやすいこと、溶出物が出やすいこと等の問題を抱えており、本格導入には至っていない。このような問題を解決するために高分子フィルタの適用が検討されつつあるが、高分子フィルタは前述の如き別の問題を抱えている。
【0005】
さらに、上記の如きフィルタの材質に関する問題とは別に、一般に高温水を濾過処理する系統においては、系内に蒸気を発生させないという基本的な前提条件が要求されることが多い。これは、フィルタの材質にかかわらず要求されるものであり、とくに前述の如き高分子フィルタを使用する場合には、フィルタの性能を確保する面からも、蒸気を発生させないことが強く望まれる。
【0006】
【発明が解決しようとする課題】
そこで本発明の課題は、上記のような問題および要求に鑑み、高温水を蒸気に変えることなく液体状態のまま所定の濾過処理を行うことができ、濾過処理後の水を適切に回収可能な、高温濾過装置の運転方法を提供することにある。
【0007】
【課題を解決するための手段】
上記課題を解決するために、本発明に係る高温濾過装置の運転方法は、高温水を濾過処理する高温濾過装置の運転方法において、高温濾過装置の一次側と二次側を連通するバイパス路と、該バイパス路を開閉可能なバイパス弁と、高速濾過装置の入口側と出口側にそれぞれ配置される入口側開閉弁および出口側開閉弁を設け、高温濾過装置内に設けられたフィルタの二次側の温度と圧力を検出して、該圧力が前記温度における飽和蒸気圧に対し予め定められた所定差まで近づいたとき、バイパス弁が開かれることにより、前記フィルタの二次側の圧力が飽和蒸気圧以上に保たれるように、高温濾過装置への通水の流量制御を行うことを特徴とする方法からなる。
【0008】
この方法においては、高温濾過装置の一次側と二次側を連通するバイパス路と、該バイパス路を開閉可能なバイパス弁とを設け、高温濾過装置への通水の流量制御とバイパス弁の開閉とを連動させるようにし、それによって、フィルタの二次側の圧力が飽和蒸気圧以上に保たれるように高温濾過装置への通水の流量制御を行う
【0009】
あるいは通常時に高温水を濾過処理する高温濾過装置の本塔に対し、高温濾過装置の予備塔を並列に接続し、前記予備塔の入口側と出口側にそれぞれ配置される予備塔入口側開閉弁および予備塔出口側開閉弁と、予備塔入口側開閉弁の一次側と二次側を連通する予備塔入口側バイパス路と、該予備塔入口側バイパス路を開閉可能な予備塔入口側バイパス弁とを設け、本塔におけるフィルタの二次側の温度と圧力を検出して、該圧力が前記温度における飽和蒸気圧に対し予め定められた所定差まで近づいたとき、予備塔入口側バイパス弁および予備塔出口側開閉弁が開かれ、次に予備塔入口側開閉弁が開かれるとともに予備塔入口側バイパス弁が閉じられて予備塔で濾過処理が行われることにより、本塔への通水に加え予備塔への通水を並行して行うようにし、それによって、本塔のフィルタの二次側の圧力が飽和蒸気圧以上に保たれるように本塔への通水の流量制御を行うことができる。このようにすれば、被処理水である高温水は、常に、本塔と予備塔で濾過処理されることになるので、必ず濾過処理された処理水が送り出されることになる。
【0010】
また、フィルタの二次側の圧力が飽和蒸気圧以上であるか否かを判断するためにはフィルタの二次側の温度と圧力を検出して飽和蒸気圧との関係を判定し、該判定に基づいて高温濾過装置への通水の流量制御を行う
【0011】
本発明で対象とする高温水は、たとえば水温が100℃以上の水であり、飽和蒸気圧より下回ると蒸気に変化するものである。
【0012】
なお、本発明における高温濾過装置への通水の流量制御は、流量制御弁を用いて行うことも可能であるが、弁による圧力損失を極力低く抑えてフィルタ装置全体としての圧力降下を低く抑えるために、弁自体の圧力損失が小さい単なる開閉弁を用いることが好ましい。
【0013】
上記のような本発明に係る高温濾過装置の運転方法においては、フィルタの二次側の圧力が低下して飽和蒸気圧に近づくと、該圧力が飽和蒸気圧以上に保たれるように、高温濾過装置への通水量が抑制される。この通水量の制御においては、高温濾過装置に対しバイパス路を設ける場合には、高温濾過装置への通水量を小さく絞るとともに、残りをバイパス路に逃がすようにすればよい。また、本塔と予備塔を並列に接続する場合には、本塔におけるフィルタの二次側の圧力に応じて、つまり、本塔のフィルタ二次側の圧力が飽和蒸気圧に近づいたら、予備塔への通水を並行して行い、本塔への通水量を小さく抑えればよい。バイパス路を設ける方式の場合には、高温濾過装置への通水量が低減されると、それだけ高温濾過装置における圧力損失、とくにフィルタ圧力損失が小さくなるので、その分フィルタ二次側の圧力が高く維持されて、フィルタ二次側の圧力が確実に飽和蒸気圧以上に保たれる。二次側圧力が飽和蒸気圧以上に保たれることにより、フィルタ面での蒸気発生が防止され、ひいては系統内に蒸気が発生することが防止される。また、本塔と予備塔を並列に接続する場合には、本塔のフィルタ二次側の圧力が低下して飽和蒸気圧に近づいたら、予備塔への通水が開始されて本塔への通水量が小さく抑えられるから、同様に、高温濾過装置としての本塔における圧力損失が小さく抑えられ、フィルタ二次側の圧力が飽和蒸気圧以上に保たれて、フィルタ面での蒸気発生、系統内での蒸気発生が防止される。この本塔と予備塔を並列に接続する方式では、蒸気動作後に、通水を完全に本塔から予備塔に切り換えて、本塔を濾過系から切り離し、本塔のフィルタ二次側の圧力が低下した原因を確認することもできる。
【0014】
【発明の実施の形態】
以下に、本発明の望ましい実施の形態を、図面を参照して説明する。
図1は、本発明の第1実施態様に係る方法を実施するための高温濾過装置の系統を示している。図1において、1は高温水の供給ライン、2は濾過処理後の水の回収ラインを示しており、供給ライン1と回収ライン2との間に高温濾過装置3が設けられている。高温濾過装置3の入口側および出口側には、各々、開閉弁4、5が設けられている。
【0015】
高温濾過装置3内には、本実施態様では、中空糸状あるいはスパイラル状あるいはプリーツ状等に加工された疎水性高分子からなるフィルタ6が配設されている。このフィルタ6の形式については、後述の如く他の形式のものを採用することも可能である。
【0016】
高温濾過装置3には、フィルタ6の二次側の温度(T)を検出する温度センサ7と、圧力(P)を検出する圧力センサ8が付設されている。これら温度センサ7と圧力センサ8からの検知信号は、制御装置9に送られ、フィルタ6の二次側における圧力が飽和蒸気圧以上に保たれているか否かの判定に供される。
【0017】
高温濾過装置3の一次側と二次側との間には、より正確には、開閉弁4の上流側と開閉弁5の下流側の位置間には、高温濾過装置3の一次側と二次側を連通可能なバイパス路10が設けられている。バイパス路10には、該バイパス路10を開閉可能なバイパス弁11が設けられている。このバイパス路10のバイパス弁11は、高温濾過装置3への通水の制御、つまり開閉弁4、5の開閉制御と連動させて作動される。
【0018】
このように構成れた高温濾過装置の系統を用いて、本発明に係る方法は次のように実施される。
通常時には、バイパス路10のバイパス弁11は閉じられ、開閉弁4、5が全開されて、供給されてきた高温水は全量高温濾過装置3を通過され、フィルタ6によって濾過処理される。この濾過処理においては、高温水がフィルタ6を通過することによる圧力損失によって、フィルタ6の二次側の圧力は、供給側の圧力に比べ低下する。したがって、この圧力損失が大きいと、フィルタ6の二次側の圧力の低下度合が大きくなり、該圧力が飽和蒸気圧以下になるおそれが生じる。
【0019】
フィルタ6の二次側の圧力は、圧力センサ8で直接検知され、飽和蒸気圧は、温度センサ7によるそのときの検知温度に対する飽和蒸気圧として、制御装置9により演算、または予め記憶された状態線図から読み取られる。そして、制御装置9により、圧力センサ8によるフィルタ6の二次側の検知圧力が、飽和蒸気圧以上であるか否か、および、飽和蒸気圧との間にどの程度の差があるかが判断、演算される。
【0020】
本実施態様では、圧力センサ8による検知圧力が、飽和蒸気圧に対し、予め定めた所定差まで近づいたとき、先ずバイパス弁11が開かれてバイパス路10が開かれ、次に弁4、5が絞られる。バイパス路10での圧力損失は小さいので、供給されてきた高温水の大半はバイパス路10を流れ、残りが、高温濾過装置3を通過する。高温濾過装置3を通過する流量が小さく絞られることにより、高温濾過装置3通過による圧力損失(圧力低下)は大幅に低減され、フィルタ6の二次側における圧力が飽和蒸気圧以下となることはなく、蒸気発生が確実に防止される。また、フィルタ6の二次側での蒸気発生が防止されることにより、回収ライン2を通して回収される処理水中にも蒸気は発生せず、系統内での蒸気の発生も確実に防止される。
【0021】
なお、フィルタ6の二次側における圧力低下の原因が、フィルタ6の目詰まりによるものであり、フィルタ6が交換あるいは再生時期に達したと判断される場合は、弁4、5を完全に閉じ、高温水の全量をバイパス路10に流す状態にて、フィルタ6を交換すればよい。
【0022】
上記第1実施態様においては、フィルタ6として、中空糸状、スパイラル状、あるいはプリーツ状等に加工された疎水性高分子フィルタを用いたが、他の形式のフィルタを使用することも可能である。たとえば、原子力発電所等で使われている濾過脱塩装置のように、疎水性高分子の樹脂を粉末とし、それをフィルタエレメントにプリコートしたものを使用することができる。あるいは、砂濾過装置や復水脱塩装置のように、砂やイオン交換樹脂等の粒状体からなる濾材によって濾層を形成して濾過を行うこともできる。たとえば、疎水性高分子を適当な粒径の粒状体に調製し、その粒状体によって濾材を形成して濾過を行うことができる。
【0023】
図2は、本発明の第2実施態様に係る方法を実施するための高温濾過装置の系統を示しており、フィルタを、疎水性高分子粒状体を用いた濾層21から構成した場合を示している。本実施態様では、濾層21の構成上、図2では図1に比べ天地を逆転させて表示しているが、濾層21部分以外の基本構成は図1に示した態様と同一である。したがって、同一構成部分については、図2に図1に付したのと同一の符号を付すことにより説明を省略する。
【0024】
図3、図4は、本発明の第3、第4実施態様に係る方法を実施するための高温濾過装置の系統を示している。これらの実施態様では、蒸気発生の防止の他、系統の運転開始時の昇温過程における問題の発生防止も考慮されている。
【0025】
図3に示す第3実施態様においては、高温濾過装置3の入口側の開閉弁4に対し、バイパス路31およびバイパス弁32が設けられ、このバイパス弁32は、開閉弁4に比べ通水量の小さい流路の細い弁から構成されている。高温濾過装置3への通水開始時には、高温濾過装置3全体が未だ昇温されていないので、急激な昇温、それによるシール部等の不都合の発生等を回避するために、徐々に昇温させることが望まれる。そのため、通水開始時には開閉弁4を閉じ、バイパス弁32を開いて、小流量にて高温水を通水することにより高温濾過装置3を徐々に温め、高温濾過装置3が所定温度まで昇温されたときに、開閉弁4を開くとともにバイパス弁32を閉じ、所定の流量での高温濾過装置3への通水に入る。このようにすれば、通水開始時の昇温過程での不都合の発生が防止される。フィルタ6の二次側における圧力を飽和蒸気圧以上に保つ制御は、前述の第1実施態様と同様に行えばよい。
【0026】
図4に示す第4実施態様では、濾層21が疎水性高分子の粒状体から形成されている。高温濾過装置3の入口側の開閉弁4に対し、同様にバイパス路31およびバイパス弁32が設けられている。通水開始時の操作は、上記第3実施態様と同様に、フィルタ21の二次側における圧力を飽和蒸気圧以上に保つ制御は、前述の第2実施態様と同様に行えばよい。
【0027】
図5は、本発明の第5実施態様に係る方法を実施するための高温濾過装置の系統を示している。本実施態様においては、バイパス路は設けられておらず、高温濾過装置に関して、図3の第3実施態様に示したのと同等の装置が併設されている。すなわち、通常時に高温水を濾過処理する高温濾過装置としての本塔3aに対し、予備塔3bが並列に接続され、本塔3aにおけるフィルタ6の二次側の圧力に応じて、本塔3aへの通水に加え予備塔3bへの通水を並行して行うことができるようになっている。
【0028】
より詳細には、まず通水開始時には、第3実施態様におけるのと同様に、弁32を開けて弁のバイパス路31に比較的小流量で通水するとともに、弁5を開け、本塔3aでの濾過処理を開始し、本塔3aの温度が上がった時点で弁4を開け弁32を閉じて通水し、通常の濾過処理を行う。本塔3aにおけるフィルタ6の二次側の圧力が低下して飽和蒸気圧に近づいたら(つまり、フィルタ6の差圧が所定以上に上昇したら)、予備塔3b側の弁42を開けて弁のバイパス路41に比較的小流量で通水するとともに、弁43を開け、予備塔3bでの濾過処理を開始し、予備塔3bの温度が上がった時点で弁44を開け弁42を閉じて通水し、予備塔3bで通常の濾過処理を行う。この状態では、本塔3a、予備塔3bともに通常の濾過処理状態にあるが、両塔3a、3bに並列に通水されるので、本塔3aの通水量は大幅に低下され、本塔3aにおけるフィルタ6の圧力損失が大幅に低減されて、飽和蒸気圧に至ることが防止され、フィルタ6の二次側の面や系統内で蒸気が発生することが防止される。
【0029】
この並列状態の通水への切り換え後には、本塔3a側の弁4、弁5を閉じ、本塔3aを完全に濾過系から切り離すことにより、本塔3aにおけるフィルタ6の差圧が上昇した原因を確認することができる。
【0030】
なお、図5に示した第5実施態様では、制御装置を図示していないが、前述の各実施態様と同様、制御装置を設けて、予備塔3bの通水開始、予備塔3bへの切り換えを自動で行うようにすることもできる。また、図5に示した第5実施態様では、前述の各実施態様におけるバイパス路10は設けられていないが、緊急時対策用等のために、前述の各実施態様におけるのと同様に、本塔3aおよび予備塔3bに対し、共通のバイパス路10、バイパス弁11を設けておいてもよい。
【0031】
また、図5では、本塔3aと予備塔3bを区別して示したが、両塔3a、3bおよびその付帯設備は、基本的に同じものでよいので、いずれか一方を本塔、他方を予備塔として運用すればよい。
【0032】
さらに、上記各実施態様においては、フィルタにはいずれも、形式は別として、疎水性高分子を用いたが、本発明は、金属フィルタやセラミックフィルタを使用する場合にも成立する。金属フィルタやセラミックフィルタを使用する場合にあっても、本発明に係る運転方法を適用することにより、フィルタの二次側での蒸気発生が防止され、ひいては系統内に蒸気が発生することが防止される。
【0033】
【発明の効果】
以上説明したように、本発明の高温濾過装置の運転方法によれば、高温水を蒸気に変えることなく液体状態のまま確実に濾過処理できるようになり、濾過処理後の水を適切に回収することができる。
【図面の簡単な説明】
【図1】本発明の第1実施態様に係る方法を実施するための高温濾過装置を含む機器系統図である。
【図2】本発明の第2実施態様に係る方法を実施するための高温濾過装置を含む機器系統図である。
【図3】本発明の第3実施態様に係る方法を実施するための高温濾過装置を含む機器系統図である。
【図4】本発明の第4実施態様に係る方法を実施するための高温濾過装置を含む機器系統図である。
【図5】本発明の第5実施態様に係る方法を実施するための高温濾過装置を含む機器系統図である。
【符号の説明】
1 高温水の供給ライン
2 濾過処理後の水の回収ライン
3 高温濾過装置
3a 高温濾過装置としての本塔
3b 予備塔
4 入口側開閉弁
5 出口側開閉弁
6、21 フィルタ
7 温度センサ
8 圧力センサ
9 制御装置
10 バイパス路
11 バイパス弁
31 高温濾過装置入口側におけるバイパス路
32 高温濾過装置入口側におけるバイパス弁
41 予備塔入口側におけるバイパス路
42 予備塔入口側におけるバイパス弁
43 予備塔出口側開閉弁
44 予備塔入口側開閉弁
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a method for operating a high-temperature filtration device that filters high-temperature water in, for example, a water supply system or a heater drain system in a power plant.
[0002]
[Prior art]
In a power plant or the like, high-temperature water of 100 ° C. or higher is sometimes filtered in a water supply system or a heater drain system, and it is necessary to use a heat-resistant filter that can withstand high-temperature water. Conventionally, use of a metal filter, a ceramic filter, or the like has been studied, but in recent years, use of a hydrophobic polymer filter has begun to be studied.
[0003]
Hydrophobic polymer filters have the property that once they are dried, they are hydrophobic and impervious to water and lose their filtration function. Therefore, for example, at the initial stage of water flow, the pressure on the secondary side of the filter is less than the saturated vapor pressure of the high-temperature water to be processed due to the filter differential pressure (filter pressure loss), the differential pressure of the high-temperature water treatment system or the water temperature. Then, the water to be treated changes into steam on the filter surface, the filter is dried, and the water treatment itself by the filter becomes impossible, and it may be impossible to collect the water filtered into the system. Once the hydrophobic polymer filter is dried, a chemical moistening operation is required to restore performance. Therefore, when applying a polymer filter, it is desirable to always adopt a condition in which the filter does not dry.
[0004]
On the other hand, metal filters and ceramic filters can be used even under temperature conditions of about 200 ° C such as heater drain water in power plants, but the iron removal performance is unstable, the differential pressure tends to increase, and elution It has problems such as being easy to get things out, and has not yet been fully introduced. In order to solve such a problem, application of a polymer filter is being studied, but the polymer filter has another problem as described above.
[0005]
Further, apart from the above-described problems related to the filter material, in general, a system for filtering high-temperature water often requires a basic precondition that steam is not generated in the system. This is required regardless of the material of the filter. In particular, when a polymer filter as described above is used, it is strongly desired not to generate steam from the viewpoint of ensuring the performance of the filter.
[0006]
[Problems to be solved by the invention]
Therefore, in view of the above problems and requirements, the object of the present invention is to allow a predetermined filtration process to be performed in a liquid state without changing high-temperature water into steam, and the water after the filtration process can be recovered appropriately. Another object of the present invention is to provide a method for operating a high-temperature filtration device.
[0007]
[Means for Solving the Problems]
In order to solve the above problems, the operation method of the high-temperature filtration device according to the present invention is the operation method of the high-temperature filtration device that filters high-temperature water, and a bypass passage that communicates the primary side and the secondary side of the high-temperature filtration device; A bypass valve capable of opening and closing the bypass passage, and an inlet-side on-off valve and an outlet-side on-off valve disposed on the inlet side and the outlet side of the high-speed filtration device, respectively, and a secondary of the filter provided in the high-temperature filtration device Side pressure and the pressure on the secondary side of the filter is saturated by opening the bypass valve when the pressure approaches a predetermined difference with respect to the saturated vapor pressure at the temperature. It consists of the method characterized by performing flow control of the water flow to a high temperature filtration apparatus so that it may be kept more than a vapor pressure.
[0008]
In this method, a bypass passage communicating the primary side and the secondary side of the high-temperature filtration device, and a bypass valve capable of opening and closing the bypass passage are provided to control the flow rate of water to the high-temperature filtration device and open and close the bypass valve. And thereby controlling the flow rate of water to the high-temperature filter so that the pressure on the secondary side of the filter is maintained at or above the saturated vapor pressure .
[0009]
Alternatively , the main tower of the high-temperature filtration device that normally filters high-temperature water is connected in parallel with the preliminary tower of the high-temperature filtration device, and the preliminary tower inlet-side opening and closing arranged respectively at the inlet side and the outlet side of the preliminary tower Valve and auxiliary tower outlet side opening / closing valve, auxiliary tower inlet side opening / closing valve, auxiliary tower inlet side bypass path communicating with the primary side and secondary side, and preliminary tower inlet side bypass capable of opening and closing the preliminary tower inlet side bypass path When the temperature and pressure on the secondary side of the filter in the main tower are detected, and the pressure approaches a predetermined difference with respect to the saturated vapor pressure at the temperature, the preliminary tower inlet side bypass valve And the auxiliary tower outlet side opening / closing valve is opened, and then the auxiliary tower inlet side opening / closing valve is opened and the auxiliary tower inlet side bypass valve is closed, and filtration is performed in the auxiliary tower. In addition to parallel water flow to the reserve tower As it carried out, whereby the pressure of the secondary side of the filter of the present tower can be made to flow control water passage into the tower so as to maintain on the saturated vapor pressure. If it does in this way, since the high temperature water which is to-be-processed water will always be filtered by the main tower and a preliminary | backup tower, the treated water filtered always will be sent out.
[0010]
Further, in the pressure of the secondary side of the filter determines whether or not the saturated vapor pressure is to detect the temperature and pressure of the secondary side of the filter to determine the relationship between the saturated vapor pressure, the Based on the determination, the flow rate of water to the high-temperature filter is controlled .
[0011]
The high-temperature water targeted in the present invention is, for example, water having a water temperature of 100 ° C. or higher, and changes to steam when it falls below the saturated vapor pressure.
[0012]
In addition, although the flow control of the water flow to the high temperature filtration apparatus in the present invention can be performed using a flow control valve, the pressure loss due to the valve is suppressed as low as possible to suppress the pressure drop as a whole of the filter apparatus. Therefore, it is preferable to use a simple open / close valve in which the pressure loss of the valve itself is small.
[0013]
In the operation method of the high-temperature filtration device according to the present invention as described above, when the pressure on the secondary side of the filter decreases and approaches the saturated vapor pressure, the pressure is kept high so that the pressure is maintained at or above the saturated vapor pressure. The amount of water flow to the filtration device is suppressed. In the control of the water flow rate, when a bypass path is provided for the high-temperature filter device, the water flow rate to the high-temperature filter device is narrowed down and the rest is allowed to escape to the bypass channel. Also, when the main tower and the backup tower are connected in parallel, according to the pressure on the secondary side of the filter in the main tower, that is, when the pressure on the filter secondary side of the main tower approaches the saturated vapor pressure, The water flow to the tower should be performed in parallel, and the water flow to the main tower should be kept small. In the case of a system in which a bypass is provided, the pressure loss in the high-temperature filtration device, particularly the filter pressure loss, decreases as the amount of water flow to the high-temperature filtration device decreases. The pressure on the secondary side of the filter is reliably maintained at the saturated vapor pressure or higher. By maintaining the secondary side pressure at or above the saturated vapor pressure, generation of vapor on the filter surface is prevented, and consequently generation of vapor in the system is prevented. In addition, when the main tower and the backup tower are connected in parallel, when the pressure on the filter secondary side of the main tower drops and approaches the saturated vapor pressure, water flow to the backup tower is started and Since the amount of water flow can be kept small, the pressure loss in the main tower as a high-temperature filtration device can be kept small, the pressure on the secondary side of the filter is kept above the saturated vapor pressure, and steam is generated on the filter surface. Steam generation inside is prevented. In this method of connecting the main tower and the backup tower in parallel, after steam operation, the water flow is completely switched from the main tower to the backup tower, the main tower is disconnected from the filtration system, and the pressure on the filter secondary side of the main tower is reduced. The cause of the decrease can also be confirmed.
[0014]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, preferred embodiments of the present invention will be described with reference to the drawings.
FIG. 1 shows a system of a high-temperature filtration device for carrying out the method according to the first embodiment of the present invention. In FIG. 1, reference numeral 1 denotes a high-temperature water supply line, 2 denotes a water recovery line after filtration, and a high-temperature filtration device 3 is provided between the supply line 1 and the recovery line 2. On-off valves 4 and 5 are respectively provided on the inlet side and the outlet side of the high-temperature filtration device 3.
[0015]
In this embodiment, a filter 6 made of a hydrophobic polymer processed into a hollow fiber shape, a spiral shape, a pleat shape, or the like is disposed in the high temperature filtration device 3. As the format of the filter 6, other types can be adopted as will be described later.
[0016]
The high temperature filtration device 3 is provided with a temperature sensor 7 for detecting the temperature (T) on the secondary side of the filter 6 and a pressure sensor 8 for detecting the pressure (P). The detection signals from the temperature sensor 7 and the pressure sensor 8 are sent to the control device 9 and are used to determine whether or not the pressure on the secondary side of the filter 6 is maintained at or above the saturated vapor pressure.
[0017]
More precisely, between the primary side and the secondary side of the high-temperature filtration device 3, between the upstream side of the on-off valve 4 and the downstream side of the on-off valve 5, the primary side and the secondary side of the high-temperature filtration device 3 are located. A bypass path 10 that can communicate with the next side is provided. A bypass valve 11 that can open and close the bypass path 10 is provided in the bypass path 10. The bypass valve 11 of the bypass passage 10 is operated in conjunction with the control of water flow to the high temperature filtration device 3, that is, the opening / closing control of the opening / closing valves 4, 5.
[0018]
The method according to the present invention is carried out as follows using the system of the high-temperature filtration device configured as described above.
At normal times, the bypass valve 11 of the bypass passage 10 is closed, the on-off valves 4 and 5 are fully opened, and the supplied high-temperature water passes through the high-temperature filter 3 and is filtered by the filter 6. In this filtration process, the pressure on the secondary side of the filter 6 is reduced as compared with the pressure on the supply side due to the pressure loss caused by the high-temperature water passing through the filter 6. Therefore, if this pressure loss is large, the degree of decrease in the pressure on the secondary side of the filter 6 increases, and the pressure may become equal to or lower than the saturated vapor pressure.
[0019]
The pressure on the secondary side of the filter 6 is directly detected by the pressure sensor 8, and the saturated vapor pressure is calculated by the control device 9 or stored in advance as the saturated vapor pressure corresponding to the temperature detected by the temperature sensor 7 at that time. Read from the diagram. Then, the control device 9 determines whether or not the detected pressure on the secondary side of the filter 6 by the pressure sensor 8 is equal to or higher than the saturated vapor pressure and how much difference there is between the saturated vapor pressure. Is calculated.
[0020]
In this embodiment, when the pressure detected by the pressure sensor 8 approaches a predetermined difference with respect to the saturated vapor pressure, the bypass valve 11 is opened first, the bypass passage 10 is opened, and then the valves 4, 5 are opened. Is squeezed. Since the pressure loss in the bypass passage 10 is small, most of the supplied high-temperature water flows through the bypass passage 10 and the rest passes through the high-temperature filtration device 3. By reducing the flow rate passing through the high temperature filtration device 3, the pressure loss (pressure drop) due to the passage through the high temperature filtration device 3 is greatly reduced, and the pressure on the secondary side of the filter 6 is less than the saturated vapor pressure. And generation of steam is reliably prevented. Further, since the generation of steam on the secondary side of the filter 6 is prevented, no steam is generated in the treated water recovered through the recovery line 2, and the generation of steam in the system is reliably prevented.
[0021]
In addition, when the cause of the pressure drop on the secondary side of the filter 6 is due to clogging of the filter 6 and it is determined that the filter 6 has reached the replacement or regeneration time, the valves 4 and 5 are completely closed. The filter 6 may be replaced in a state where the entire amount of high-temperature water is passed through the bypass passage 10.
[0022]
In the first embodiment, the filter 6 is a hydrophobic polymer filter processed into a hollow fiber shape, a spiral shape, a pleat shape, or the like, but other types of filters can be used. For example, as in a filtration desalination apparatus used in nuclear power plants and the like, it is possible to use a hydrophobic polymer resin powdered and pre-coated on a filter element. Alternatively, filtration can be performed by forming a filter layer with a filter medium made of granular material such as sand or ion exchange resin, such as a sand filtration device or a condensate demineralization device. For example, a hydrophobic polymer can be prepared into a granular material having an appropriate particle size, and a filter medium can be formed from the granular material to perform filtration.
[0023]
FIG. 2 shows a system of a high-temperature filtration device for carrying out the method according to the second embodiment of the present invention, and shows a case where the filter is composed of a filter layer 21 using hydrophobic polymer particles. ing. In this embodiment, because of the configuration of the filter layer 21, FIG. 2 is displayed with the top and bottom reversed compared to FIG. 1, but the basic configuration other than the filter layer 21 portion is the same as the embodiment shown in FIG. Therefore, about the same component part, description is abbreviate | omitted by attaching | subjecting the same code | symbol which attached | subjected FIG. 2 to FIG.
[0024]
3 and 4 show a system of a high-temperature filtration device for carrying out the method according to the third and fourth embodiments of the present invention. In these embodiments, in addition to preventing the generation of steam, consideration is also given to preventing the occurrence of problems in the temperature rising process at the start of system operation.
[0025]
In the third embodiment shown in FIG. 3, a bypass passage 31 and a bypass valve 32 are provided for the opening / closing valve 4 on the inlet side of the high-temperature filtration device 3. It consists of a narrow valve with a small channel. At the start of water flow to the high temperature filtration device 3, the temperature of the entire high temperature filtration device 3 has not been raised yet, so that the temperature rises gradually in order to avoid sudden temperature rise and the occurrence of inconveniences such as a seal portion. It is hoped that Therefore, when the water flow starts, the on-off valve 4 is closed, the bypass valve 32 is opened, and the high-temperature filter 3 is gradually warmed by passing high-temperature water at a small flow rate, and the high-temperature filter 3 is heated to a predetermined temperature. When this is done, the on-off valve 4 is opened and the bypass valve 32 is closed, and water is introduced into the high-temperature filtration device 3 at a predetermined flow rate. In this way, it is possible to prevent the occurrence of inconvenience in the temperature raising process at the start of water flow. Control for keeping the pressure on the secondary side of the filter 6 at or above the saturated vapor pressure may be performed in the same manner as in the first embodiment.
[0026]
In the 4th embodiment shown in FIG. 4, the filter layer 21 is formed from the granular material of hydrophobic polymer. Similarly, a bypass passage 31 and a bypass valve 32 are provided for the opening / closing valve 4 on the inlet side of the high-temperature filtration device 3. As in the third embodiment, the operation at the start of water flow may be performed in the same manner as in the second embodiment described above to keep the pressure on the secondary side of the filter 21 at or above the saturated vapor pressure.
[0027]
FIG. 5 shows a system of a high temperature filtration device for carrying out the method according to the fifth embodiment of the present invention. In this embodiment, no bypass path is provided, and an apparatus equivalent to that shown in the third embodiment in FIG. In other words, a preliminary tower 3b is connected in parallel to the main tower 3a as a high-temperature filtration device that filters high-temperature water at normal times, and the main tower 3a is connected to the main tower 3a according to the pressure on the secondary side of the filter 6 in the main tower 3a. In addition to the water flow, the water flow to the preliminary tower 3b can be performed in parallel.
[0028]
More specifically, at the beginning of water flow, as in the third embodiment, the valve 32 is opened to allow water to flow through the bypass passage 31 of the valve at a relatively small flow rate, the valve 5 is opened, and the main tower 3a. When the temperature of the main tower 3a rises, the valve 4 is opened, the valve 32 is closed and water is passed through, and normal filtration is performed. When the pressure on the secondary side of the filter 6 in the main tower 3a decreases and approaches the saturated vapor pressure (that is, when the differential pressure of the filter 6 increases to a predetermined level or more), the valve 42 on the side of the preliminary tower 3b is opened to open the valve Water is passed through the bypass passage 41 at a relatively small flow rate, and the valve 43 is opened to start filtration in the preliminary tower 3b. When the temperature of the preliminary tower 3b rises, the valve 44 is opened and the valve 42 is closed. Water is used, and normal filtration is performed in the preliminary tower 3b. In this state, both the main tower 3a and the standby tower 3b are in a normal filtration state. However, since water is passed through both the towers 3a and 3b in parallel, the amount of water passing through the main tower 3a is greatly reduced. The pressure loss of the filter 6 is significantly reduced, and it is prevented from reaching the saturated vapor pressure, and the generation of steam on the secondary side surface of the filter 6 and in the system is prevented.
[0029]
After switching to this parallel water flow, the differential pressure of the filter 6 in the main tower 3a increased by closing the valves 4 and 5 on the main tower 3a side and completely disconnecting the main tower 3a from the filtration system. The cause can be confirmed.
[0030]
In the fifth embodiment shown in FIG. 5, the control device is not shown. However, as in each of the above-described embodiments, the control device is provided to start the water flow of the spare tower 3b and switch to the spare tower 3b. Can also be performed automatically. Further, in the fifth embodiment shown in FIG. 5, the bypass path 10 in each of the above-described embodiments is not provided. However, for emergency measures, etc., the same as in each of the above-described embodiments. A common bypass passage 10 and a bypass valve 11 may be provided for the tower 3a and the spare tower 3b.
[0031]
In FIG. 5, the main tower 3a and the spare tower 3b are shown separately. However, since both towers 3a and 3b and their auxiliary facilities may be basically the same, either one is the main tower and the other is the spare tower. It can be operated as a tower.
[0032]
Further, in each of the embodiments described above, a hydrophobic polymer is used for each filter, regardless of the type, but the present invention is also applicable when a metal filter or a ceramic filter is used. Even when a metal filter or a ceramic filter is used, the generation of steam on the secondary side of the filter is prevented by applying the operation method according to the present invention, and consequently the generation of steam in the system is prevented. Is done.
[0033]
【The invention's effect】
As described above, according to the operation method of the high-temperature filtration device of the present invention, the high-temperature water can be reliably filtered in a liquid state without changing the high-temperature water into steam, and the water after the filtration is appropriately recovered. be able to.
[Brief description of the drawings]
FIG. 1 is an equipment diagram including a high-temperature filtration device for carrying out a method according to a first embodiment of the present invention.
FIG. 2 is an equipment diagram including a high-temperature filtration device for carrying out a method according to a second embodiment of the present invention.
FIG. 3 is an equipment diagram including a high-temperature filtration device for carrying out a method according to a third embodiment of the present invention.
FIG. 4 is an equipment diagram including a high-temperature filtration device for carrying out a method according to a fourth embodiment of the present invention.
FIG. 5 is an equipment diagram including a high-temperature filtration device for carrying out a method according to a fifth embodiment of the present invention.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 High temperature water supply line 2 Water recovery line after filtration 3 High temperature filtration device 3a Main tower 3b as a high temperature filtration device Preliminary tower 4 Inlet side on / off valve 5 Outlet side on / off valve 6, 21 Filter 7 Temperature sensor 8 Pressure sensor DESCRIPTION OF SYMBOLS 9 Control apparatus 10 Bypass path 11 Bypass valve 31 Bypass path 32 in high temperature filter inlet side Bypass valve 41 in high temperature filter inlet side Bypass path 42 in preliminary tower inlet side Bypass valve 43 in preliminary tower inlet side Preliminary tower outlet side opening / closing valve 44 Preliminary tower entrance side open / close valve

Claims (5)

高温水を濾過処理する高温濾過装置の運転方法において、高温濾過装置の一次側と二次側を連通するバイパス路と、該バイパス路を開閉可能なバイパス弁と、高速濾過装置の入口側と出口側にそれぞれ配置される入口側開閉弁および出口側開閉弁を設け、高温濾過装置内に設けられたフィルタの二次側の温度と圧力を検出して、該圧力が前記温度における飽和蒸気圧に対し予め定められた所定差まで近づいたとき、バイパス弁が開かれることにより、前記フィルタの二次側の圧力が飽和蒸気圧以上に保たれるように、高温濾過装置への通水の流量制御を行うことを特徴とする高温濾過装置の運転方法。In an operation method of a high-temperature filtration device for filtering high-temperature water , a bypass passage communicating the primary side and secondary side of the high-temperature filtration device, a bypass valve capable of opening and closing the bypass passage, and an inlet side and an outlet of a high-speed filtration device An inlet-side on-off valve and an outlet-side on-off valve respectively disposed on the side, and detects the temperature and pressure on the secondary side of the filter provided in the high-temperature filter, and the pressure becomes the saturated vapor pressure at the above temperature. On the other hand, the flow rate control of water flow to the high-temperature filtration device is performed so that the pressure on the secondary side of the filter is maintained at the saturated vapor pressure or higher by opening the bypass valve when approaching a predetermined difference set in advance. A method for operating a high-temperature filtration device, characterized in that: 前記圧力が前記温度における飽和蒸気圧に対し予め定められた所定差まで近づいたとき、先ずバイパス弁が開かれ、次に入口側開閉弁および出口側開閉弁が絞られる、請求項1の高温濾過装置の運転方法。The high temperature filtration according to claim 1, wherein when the pressure approaches a predetermined difference with respect to the saturated vapor pressure at the temperature, the bypass valve is first opened, and then the inlet side on-off valve and the outlet side on-off valve are throttled. How to operate the device. 高温水を濾過処理する高温濾過装置の運転方法において、通常時に高温水を濾過処理する高温濾過装置の本塔に対し、高温濾過装置の予備塔を並列に接続し、前記予備塔の入口側と出口側にそれぞれ配置される予備塔入口側開閉弁および予備塔出口側開閉弁と、予備塔入口側開閉弁の一次側と二次側を連通する予備塔入口側バイパス路と、該予備塔入口側バイパス路を開閉可能な予備塔入口側バイパス弁とを設け、本塔におけるフィルタの二次側の温度と圧力を検出して、該圧力が前記温度における飽和蒸気圧に対し予め定められた所定差まで近づいたとき、予備塔入口側バイパス弁および予備塔出口側開閉弁が開かれ、次に予備塔入口側開閉弁が開かれるとともに予備塔入口側バイパス弁が閉じられて予備塔で濾過処理が行われることにより、本塔への通水に加え予備塔への通水を並行して行い、前記フィルタの二次側の圧力が飽和蒸気圧以上に保たれるように、高温濾過装置への通水の流量制御を行うことを特徴とする高温濾過装置の運転方法。 In the operation method of the high-temperature filtration device for filtering high-temperature water, a high-temperature filter preparatory tower is connected in parallel to the main tower of the high- temperature filtration device that normally filters high-temperature water, and the preparatory tower inlet side and Preliminary tower inlet side opening / closing valve and auxiliary tower outlet side opening / closing valve respectively arranged on the outlet side, a preliminary tower inlet side opening / closing valve, a preliminary tower inlet side bypass passage communicating the primary side and secondary side, and the preliminary tower inlet A bypass column inlet side bypass valve capable of opening and closing the side bypass passage, detecting the temperature and pressure on the secondary side of the filter in the main column , and the pressure is determined in advance with respect to the saturated vapor pressure at the temperature When the difference is approached, the spare tower inlet bypass valve and spare tower outlet open / close valve are opened, and then the spare tower inlet open / close valve is opened and the spare tower inlet bypass valve is closed and filtered in the spare tower. Is done , Have rows in parallel water flow to a spare column in addition to the water passage to the tower, so that the pressure on the secondary side of the filter is kept on the saturated vapor pressure, the water flow to the hot filtration unit A method for operating a high-temperature filtration device, characterized by performing flow rate control . 予備塔入口側バイパス弁および予備塔出口側開閉弁が開かれた後、前記予備塔の温度が上がった時点で予備塔入口側開閉弁が開かれる、請求項の高温濾過装置の運転方法。The operation method of the high-temperature filtration apparatus according to claim 3 , wherein after the preliminary tower inlet side bypass valve and the preliminary tower outlet side opening / closing valve are opened, the preliminary tower inlet side opening / closing valve is opened when the temperature of the preliminary tower rises . 濾過処理される高温水の水温が100℃以上である、請求項1ないし4のいずれかに記載の高温濾過装置の運転方法。  The operation method of the high temperature filtration apparatus in any one of Claims 1 thru | or 4 whose water temperature of the high temperature water filtered is 100 degreeC or more.
JP2000195684A 2000-06-29 2000-06-29 Operation method of high temperature filter Expired - Fee Related JP4548907B2 (en)

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