JPS61208407A - Purifier for drain system of feedwater heater - Google Patents
Purifier for drain system of feedwater heaterInfo
- Publication number
- JPS61208407A JPS61208407A JP4834885A JP4834885A JPS61208407A JP S61208407 A JPS61208407 A JP S61208407A JP 4834885 A JP4834885 A JP 4834885A JP 4834885 A JP4834885 A JP 4834885A JP S61208407 A JPS61208407 A JP S61208407A
- Authority
- JP
- Japan
- Prior art keywords
- resin
- drain
- cation
- feed water
- equipment
- 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.)
- Pending
Links
Landscapes
- Treatment Of Water By Ion Exchange (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
〔発明の利用分野〕
本発明は、発電プラント用の給水加熱器ドレン系の浄化
装置に係り、特に、給水加熱器ドレンタンクに回収され
るクラッド等の不純物を多く含んだドレンを復水系に戻
す際に処理して、水質を向上させるに好適な陽イオン樹
脂塔に関する。[Detailed Description of the Invention] [Field of Application of the Invention] The present invention relates to a purification device for a feedwater heater drain system for a power generation plant, and in particular, the present invention relates to a purification device for a feedwater heater drain system for a power generation plant, and in particular, the present invention relates to a purification device for a feedwater heater drain system used in a power generation plant. The present invention relates to a cation resin column suitable for improving water quality by treating condensate when returning it to a condensate system.
従来の発電プラント用の給水加熱器ドレン系で使用され
る浄化装置は、電磁フィルタがある。電磁フィルタは、
圧力容器である電磁ろ過器内に繊維状のものを充填し、
その周囲に電磁コイルを設置して、この電磁コイルに電
流を流して発生する磁力によって、電磁ろ過器内の充填
物を磁化し、ドレン中のクラッド等の磁性体を除去する
ものが知られている。〔火力原子力発電（１９８０，第
２８０号ｅｐ、５２）高勾配電磁フィルタの火力・原子
力発電所への適用〕
しかし、この電磁フィルタでは、給水加熱器からのドレ
ン中に含まれる磁化されない微細な粒子では、除去され
ず下流側へ流れ出ることとなる。Purifiers used in conventional power plant feedwater heater drain systems include electromagnetic filters. The electromagnetic filter is
A fibrous material is filled into an electromagnetic filter, which is a pressure vessel, and
It is known that an electromagnetic filter is installed around the filter, and the magnetic force generated by passing a current through the electromagnetic coil magnetizes the filling in the electromagnetic filter and removes magnetic materials such as crud in the drain. There is. [Thermal and Nuclear Power Generation (1980, No. 280 ep, 52) Application of high gradient electromagnetic filter to thermal and nuclear power plants] However, with this electromagnetic filter, fine unmagnetized particles contained in the drain from the feedwater heater In this case, it will not be removed and will flow downstream.
また、電磁ろ過器で捕捉されたクラッド等は、逆洗によ
り除去した後、電磁ろ過器を満水にして通水に備えるが
、これらの逆洗および満水工程で使用する水は、大気開
放された復水貯蔵タンクの水のため、前述の操作を行っ
た後の通水前の電磁ろ過器内の水は、溶存酸素を多量に
含んでいる。In addition, after removing the crud captured by the electromagnetic filter by backwashing, the electromagnetic filter is filled with water to prepare for water flow, but the water used in these backwashing and filling processes is not exposed to the atmosphere. Since the water is in the condensate storage tank, the water in the electromagnetic filter after the above-mentioned operation and before water flow contains a large amount of dissolved oxygen.
この状態で通水運転が行なわれると高濃度の溶存酸素の
水が復水系へ流れることになり、復水系の配管および機
器の腐食を促進するという問題がある。If water flow operation is performed in this state, water with a high concentration of dissolved oxygen will flow into the condensate system, causing a problem of accelerating corrosion of the piping and equipment of the condensate system.
本発明の第一の目的は、粒状の陽イオン交換樹脂を装荷
した陽イオン樹脂塔を設けることにより、給水加熱器ド
レン中の微細なりラッドを除去し得る浄化装置を提供す
ることにある。A first object of the present invention is to provide a purification device capable of removing fine rads from a feed water heater drain by providing a cation resin tower loaded with granular cation exchange resin.
第二の目的は、陽イオン樹脂塔の陽イオン交換樹脂を復
水系の脱塩装置の再生設備へ移送するための管路および
樹脂再生後再び陽イオン樹脂塔へ戻すための管路である
樹脂移送系統を提供するものである。The second purpose is to provide a pipe for transporting the cation exchange resin from the cation resin tower to the regeneration equipment of the condensate desalination equipment, and a pipe for returning the resin to the cation resin tower after resin regeneration. It provides a transport system.
また、第三の目的は、陽イオン交換樹脂を陽イオン樹脂
塔に装荷した状態で、樹脂の再生・逆洗が出来る様に、
再生・逆洗に必要な水・空気・薬品の管路を陽イオン樹
脂塔に接続し、供給できるような再生系統を提供するも
のである。The third purpose is to enable regeneration and backwashing of the cation exchange resin while it is loaded in the cation resin column.
This system provides a regeneration system that connects and supplies water, air, and chemicals necessary for regeneration and backwashing to the cation resin tower.
さらに第四の目的は、樹脂を再生した後、給水加熱器ド
レンの通水前に陽イオン樹脂塔内の溶存酸素を多量に含
んだ水を除去するため、陽イオン樹脂塔出口管路より分
岐した管路を給水加熱器ドレンタンクに接続することに
よって、陽イオン樹脂塔に循環流を与え高濃度溶存酸素
の除去を行い得る再循環系統を提供するものである。Furthermore, the fourth purpose is to remove water containing a large amount of dissolved oxygen in the cation resin tower after regenerating the resin and before passing water through the feed water heater drain. By connecting the pipe line to the feed water heater drain tank, a recirculation system is provided which can provide a circulating flow to the cation resin column and remove high concentration dissolved oxygen.
本発明は、給水加熱器ドレンポンプの出口側に粒状の陽
イオン交換樹脂を充填した陽イオン樹脂塔を設け、給水
加熱器からの微細なりラッドを含む不純物の除去を行い
、さらに、樹脂再生直後の陽イオン樹脂塔内の高濃度溶
存酸素の水を再循環系統により、給水加熱器ドレンタン
クと循環を行ない混合希釈することによって、給水加熱
器ドレン系の水質を改善するようにしたものである。The present invention provides a cation resin column filled with granular cation exchange resin on the outlet side of the feed water heater drain pump, removes impurities including fine rads from the feed water heater, and further removes impurities immediately after resin regeneration. The high concentration dissolved oxygen water in the cation resin tower is circulated through the feed water heater drain tank and mixed and diluted using a recirculation system, thereby improving the water quality of the feed water heater drain system. .
本発明の実施例を第１図により説明する。 An embodiment of the present invention will be explained with reference to FIG.
給水加熱器６をタービンからの管路１１のタービン抽気
により加熱した後の凝縮したドレンの流れは、給水加熱
器６より管１２．弁１３を経て、給水加熱器ドレンタン
ク１４に流入する。流入したドレンは、給水加熱器ドレ
ンタンク１４の出口の管１５．弁１６を経て、給水加熱
器ドレンポンプ１７により加圧され、給水加熱器ドレン
ポンプ１７の出口の弁１８．弁１９．管２０を通り、管
２０より分岐した管３１ａ、３１ｂ、３１ｃを介して陽
イオン樹脂塔３３ａ、３３ｂ、３３ｃに入る。この管３
１ａ、３１ｂ、３１ｃには、止弁である弁３２ａ、３２
ｂ、３２ｃが設けられている。After the feedwater heater 6 is heated by the turbine bleed air in the line 11 from the turbine, the condensed condensate flows from the feedwater heater 6 to the line 12. It flows through valve 13 into feedwater heater drain tank 14 . The inflowing drain is transferred to the outlet pipe 15 of the feed water heater drain tank 14. Pressurized via valve 16 by feedwater heater drain pump 17 and at the outlet of feedwater heater drain pump 17 via valve 18. Valve 19. It passes through the pipe 20 and enters the cation resin columns 33a, 33b, 33c via pipes 31a, 31b, 31c branched from the pipe 20. This tube 3
1a, 31b, 31c include valves 32a, 32 which are stop valves.
b, 32c are provided.
陽イオン樹脂塔３３ａ、３３ｂ、３３ｃに流入したドレ
ンは、塔内に装荷された陽イオン交換樹脂により浄化さ
れる。この浄化されたドレンは、各々の陽イオン樹脂塔
３３ａ、３３ｂ、３３ｃを出て管３４ａ、３４ｂ、３４
ｃを通り、管２７に合流し、復水系の管７に流入させ、
復水器１から復水ポンプ２で抽出し、復水系のろ過装置
３と、脱塩装置４を経てポンプ５で昇圧され、給水加熱
器６で加熱された復水と合流し、下流系統へと流れる。The drain flowing into the cation resin columns 33a, 33b, and 33c is purified by the cation exchange resin loaded in the columns. This purified drain exits each cation resin column 33a, 33b, 33c and enters the pipe 34a, 34b, 34.
c, joins the pipe 27, and flows into the condensate system pipe 7,
Extracted from condenser 1 by condensate pump 2, passed through condensate system filtration device 3 and desalination device 4, pressurized by pump 5, joined with condensate heated by feed water heater 6, and sent to the downstream system. It flows.
尚、管３４ ａ ＋ ３４ ｂ ｅ ３５ ｃには、そ
れぞれ弁３６ａ、３６ｂ、３６ｃおよび陽イオン樹脂塔
３３ａ、３３ｂ、３３ｃから下流側に樹脂が流出するの
を防止するため、ストレーナ３５ａ。The pipes 34 a + 34 b e 35 c are provided with strainers 35 a to prevent the resin from flowing downstream from the valves 36 a, 36 b, 36 c and the cation resin towers 33 a, 33 b, 33 c, respectively.
３５ｂ、３５ｃｔｉ−設けている。また、管２７には。35b, 35cti- are provided. Also, in the tube 27.
給水加熱器ドレンタンク１４の水位調整のために流量調
節用の弁２８が設けられている。A flow rate adjustment valve 28 is provided to adjust the water level in the feed water heater drain tank 14.
ここで従来と異なるのは、前述のように給水加熱器ドレ
ンの処理に粒状の陽イオン交換樹脂を使用していること
であり、このイオン交換樹脂は、復水系に設置されてい
る脱塩装置４で使用しているもので、給水加熱器ドレン
の高温水でも使用できる陽イオン交換樹脂を使用するも
のである０粒状の陽イオン交換樹脂によって、給水加熱
器ドレン中に含まれている微細な粒子を除去し、復水系
に戻す際の水質を向上させる。What is different from the conventional method here is that, as mentioned above, granular cation exchange resin is used to treat the feed water heater drain, and this ion exchange resin is used in the desalination equipment installed in the condensate system. 4, which uses a cation exchange resin that can be used even with high-temperature water from the feed water heater drain.The 0-granular cation exchange resin removes fine particles contained in the feed water heater drain. Removes particles and improves water quality when returned to the condensate system.
第２＠は、樹脂の再生設備の構成を示した図であり、本
図の陽イオン樹脂再生塔４１．陰イオン樹脂再生塔４２
および樹脂貯槽４３は、第１図において復水系に設置さ
れている脱塩装置４の樹脂の薬品再生および逆洗を行う
ための設備であり。The second @ is a diagram showing the configuration of the resin regeneration equipment, and the cation resin regeneration tower 41. Anion resin regeneration tower 42
The resin storage tank 43 is a facility for chemical regeneration and backwashing of the resin in the desalination device 4 installed in the condensate system in FIG.
この設備を有効利用し給水加熱器ドレン系の陽イオン樹
脂塔３３ａ、３３ｂ、３３ｃより樹脂移送のための管路
５６，５８を陽イオン樹脂再生塔４１に接続したもので
ある。By effectively utilizing this equipment, pipes 56 and 58 for transferring resin from the cation resin towers 33a, 33b, and 33c of the feed water heater drain system are connected to the cation resin regeneration tower 41.
この系統構成に於いて、陽イオン樹脂塔３３ａに充填さ
れた樹脂の再生操作を行なう場合は、陽イオン樹脂塔３
３ａのドレン水出入口の弁３２ａ。In this system configuration, when performing a regeneration operation of the resin filled in the cation resin column 33a, the cation resin column 3
Valve 32a of the drain water inlet and outlet of 3a.
３６ａを閉じ、樹脂出口の弁５５ａを開け、陽イオン樹
脂再生塔４１の入口側の弁５７を開けて、水と空気によ
り陽イオン樹脂再生塔４１へ樹脂を移送する。移送され
た陽イオン交換樹脂は、水と空気によりスクラビング・
逆洗したのち、酸により薬品再生を行なう、再生後の樹
脂は、陽イオン樹脂再生塔４１の出口側を開け、管５８
を経て管６０ａに設置されている弁６１ａも開けて、陽
イオン樹脂塔３３ａに樹脂を移送し、再び、ドレンの処
理を行なう。36a is closed, the resin outlet valve 55a is opened, and the valve 57 on the inlet side of the cation resin regeneration tower 41 is opened to transfer the resin to the cation resin regeneration tower 41 using water and air. The transferred cation exchange resin is scrubbed with water and air.
After backwashing, the regenerated resin undergoes chemical regeneration using acid. The outlet side of the cation resin regeneration tower 41 is opened and the regenerated resin
The valve 61a installed in the pipe 60a is also opened to transfer the resin to the cation resin column 33a, and the drain treatment is performed again.
このように、給水加熱器ドレン系の浄化装置と脱塩装置
の再生設備と接続する管路５８，５６を設けたことによ
って、浄化装置として再生設備を設置する必要がなく機
器配置上有利であり、また。In this way, by providing the pipes 58 and 56 that connect the purification device of the feed water heater drain system and the regeneration equipment of the desalination equipment, there is no need to install regeneration equipment as a purification device, which is advantageous in terms of equipment layout. ,Also.
脱塩装置の再生設備の稼働率の向上が図られる。The operation rate of desalination equipment regeneration equipment will be improved.
尚、樹脂移送のための管路５６，５８は、同時に使用す
る操作がないことから、共用化することも可能である。Note that the pipe lines 56 and 58 for resin transfer can also be used in common since there are no operations that use them at the same time.
第３図は、給水加熱器ドレン系の浄化装置の樹脂を陽イ
オン樹脂塔内で再生するための系統の一例を示すもので
ある。FIG. 3 shows an example of a system for regenerating resin in a feed water heater drain system purification device in a cation resin tower.
第２図のように、復水系脱塩装置の再生設備を利用する
場合、陽イオン樹脂塔と脱塩装置で使用する一塔当りの
陽イオン交換樹脂がほぼ同量であることが必要であり、
この樹脂量が異なる場合、薬品量が違うために、薬品希
釈計量のタンクのレベル計の増設及び逆洗・洗浄の水・
空気の使用量も違うので、弁・配管の追加が必要となる
。また。As shown in Figure 2, when using regeneration equipment for condensate desalination equipment, it is necessary that the cation resin column and the cation exchange resin used per tower used in the desalination equipment be approximately the same amount. ,
If the amount of resin is different, the amount of chemicals will be different, so it is necessary to add a level meter in the tank for diluting and measuring the chemicals, and use water for backwashing and cleaning.
Since the amount of air used is different, additional valves and piping are required. Also.
再生設備と距離がある場合、配管が長くなり、コスト高
ともなり、さらに、運転上も複雑になるという問題が生
じる。If there is a distance from the regeneration equipment, problems arise in that the piping becomes long, the cost increases, and the operation becomes complicated.
そこで、自系統内で樹脂の薬品再生、逆洗のために設備
が必要となるが、脱塩装置と同様に再生設備を設けた場
合は、設備費が高くなるので、陽イオン樹脂塔３３ａ、
３３ｂ、３３ｃ内で出来るよう、薬品、水、空気を供給
するための管路８１゜７０．７３を設けている。また、
薬品設備からの移送の管７６、弁７７と薬品を規定濃度
まで希釈するためのエゼクタ８０を設けている。陽イオ
ン蘭脂塔内での再生操作の方法は従来と同じであり。Therefore, equipment is required for chemical regeneration and backwashing of the resin within the own system, but if regeneration equipment is provided in the same way as a desalination equipment, the equipment cost will be high, so the cation resin column 33a,
Pipe lines 81°70.73 for supplying chemicals, water, and air are provided within 33b and 33c. Also,
A pipe 76 for transferring from the chemical equipment, a valve 77, and an ejector 80 for diluting the chemical to a specified concentration are provided. The method of regeneration operation in the cationic orchid resin tower is the same as before.
ドレン処理によって飽和した陽イオン樹脂塔３３ａの樹
脂の再生は、樹脂塔の出入口の弁３２ａ。The resin in the cation resin tower 33a saturated by the drain treatment is regenerated by the valve 32a at the entrance and exit of the resin tower.
３６ａを閉じ、弁７５ａを開けて、管７３．７４ａから
の空気によりスクラビングを行なう、その後。36a is closed, valve 75a is opened and scrubbing is performed with air from pipes 73, 74a, then.
薬品再生のため、薬品設備からの管７６の弁７７を開け
て薬品を移送し、エゼクタ８０で弁７９を開け、管７０
．７８からの水により希釈して、陽イオン樹脂塔３３ａ
の入口の弁８３ａを開けて、エゼクタからの薬品は、管
８１，８２ａを経て陽イオン樹脂塔３３ａに入り薬品に
より樹脂の再生が行なわれる。薬品再生後は、陽イオン
樹脂塔の水入口の弁７２ａを開け、管７０，７１ａから
の水により薬品の押し出し洗浄が行なわれる。To regenerate chemicals, open the valve 77 of the pipe 76 from the chemical equipment to transfer the medicine, open the valve 79 with the ejector 80, and transfer the medicine.
．． Diluted with water from 78, cation resin column 33a
The inlet valve 83a is opened, and the chemicals from the ejector enter the cation resin column 33a through pipes 81 and 82a, where the resin is regenerated by the chemicals. After regenerating the chemicals, the valve 72a at the water inlet of the cation resin column is opened, and the chemicals are extruded and washed with water from the pipes 70 and 71a.
この様に、薬品系統を設は樹脂塔内で再生する方式にす
ることにより、再生設備の簡略化が図れ。In this way, the regeneration equipment can be simplified by setting up the chemical system so that it regenerates within the resin tower.
機器配置上、コストダウト上効果的である。It is effective in terms of equipment layout and cost reduction.
第４図は、前述の樹脂再生後の陽イオン樹脂塔内の水に
多量に含まれた溶存酸素の除去を行うための循環系統を
示したものである。FIG. 4 shows a circulation system for removing a large amount of dissolved oxygen contained in the water in the cation resin tower after the resin regeneration described above.
陽イオン樹脂塔３３ｂ、３３ｃは、通常の給水加熱器ド
レンの処理を行っている塔として、樹脂再生後の陽イオ
ン樹脂塔３３ａの循環運転は、樹脂塔３３ａの入口の弁
３２ａを開け、給水加熱器ドレンタンク１４．ポンプ１
７からのドレン水を流入させる。次に、陽イオン樹脂塔
３３ａの出口側の管３４ａより分岐した管９０ａに設け
られた弁９１ａおよび給水加熱器ドレンタンク１４の入
口側の弁９３を開けて、陽イオン樹脂塔３３ａの水をド
レンタンクへ戻す循環を行う。この循環運転で給水加熱
器ドレンタンク１４でドレン水と混合し、高濃度の溶存
酸素を希釈することが出来る。The cation resin towers 33b and 33c are used as towers that perform normal drain treatment for the feed water heater, and the circulation operation of the cation resin tower 33a after resin regeneration is performed by opening the valve 32a at the inlet of the resin tower 33a and shutting down the water supply. Heater drain tank 14. pump 1
Let the drain water from 7 flow in. Next, the valve 91a provided on the pipe 90a branched from the pipe 34a on the outlet side of the cation resin column 33a and the valve 93 on the inlet side of the feed water heater drain tank 14 are opened to drain the water in the cation resin column 33a. Circulate the water back to the drain tank. By this circulation operation, the dissolved oxygen can be mixed with drain water in the feed water heater drain tank 14 to dilute high concentration dissolved oxygen.
ここで、陽イオン樹脂塔３３ａと給水加熱器ドレンタン
ク１４の間で循環を行うため；給水加熱器ドレンポンプ
１７の容量は、通常のドレン水移送量に循環水量も含め
たものとする必要がある。Here, in order to circulate between the cation resin tower 33a and the feed water heater drain tank 14; the capacity of the feed water heater drain pump 17 must include the amount of circulating water in the normal amount of drain water transferred. be.
第５図および第６図は、本発明の一実施例を示す。5 and 6 show one embodiment of the present invention.
第５図において第４図と異なるのは、陽イオン樹脂塔３
３ａ、３３ｂ、３３ｃ出口の管９０゜９２を復水器１に
接続させたことである。このことによって陽イオン樹脂
塔の循環運転時、溶存酸素を含んだ水を復水器１へ流し
、復水器１で脱気を行うと共に、復水器１内の復水と混
合・希釈を行い得るものとした。また、管９２には、樹
脂の流出防止のためのストレーナ９６と復水器１内は真
空であるため圧力調節ができるもの（弁９５）を設けて
いる。What is different in Fig. 5 from Fig. 4 is the cation resin tower 3.
3a, 33b, 33c outlet pipes 90°92 are connected to the condenser 1. As a result, during the circulation operation of the cation resin tower, water containing dissolved oxygen flows to the condenser 1, where it is degassed and mixed and diluted with the condensate in the condenser 1. It was decided that it could be done. The pipe 92 is also provided with a strainer 96 to prevent the resin from flowing out and a valve 95 that can adjust the pressure since the inside of the condenser 1 is a vacuum.
第６図も第４図の他の一実施例を示すもので。FIG. 6 also shows an embodiment other than that shown in FIG. 4.
陽イオン樹脂塔３３ａ、３３ｂ、３３ｃ出口の管９２を
復水回収タンク１００に接続したものである。これは、
第５図の復水器１の設置場所が離れている場合、配管引
き廻しが大変で、配管も長くなりコスト高となるため、
一時復水回収タンク１００へ循環水を送り、タンクに設
置のポンプ１０１により復水器へ移送して脱気を行なう
。The pipes 92 at the exits of the cation resin columns 33a, 33b, and 33c are connected to a condensate recovery tank 100. this is,
If the condenser 1 shown in Figure 5 is installed far away, it will be difficult to route the piping, and the piping will be long, resulting in high costs.
Circulating water is sent to a temporary condensate recovery tank 100, and transferred to a condenser using a pump 101 installed in the tank for deaeration.
本発明によれば、プラント全体の樹脂コスト低減が図れ
、再生装置の利用率向上及びコスト低減が図れ、また、
機器配置スペースの低減、系統構成の簡略化が図れる効
果がある。According to the present invention, it is possible to reduce the resin cost of the entire plant, improve the utilization rate and reduce the cost of the regeneration equipment, and
This has the effect of reducing equipment arrangement space and simplifying the system configuration.
第１図は、本発明の一実施例の給水加熱器ドレン系の浄
化装置の系統図、第２図は、本発明の脱塩装置再生設備
への樹脂移送系統図、第３図は浄化装置の薬品系統図、
第４図は循環系統図、第５図、第６図は、本発明の応用
例の系統図である。
１・・・復水器、６・・・給水加熱器、３３ ａ 、
３３ ｂ ＊３３ｃ・・・陽イオン樹脂塔、１４・・・
給水加熱器ドレンタンク、１６・・・給水加熱器ドレン
ポンプ。Fig. 1 is a system diagram of a feed water heater drain system purification device according to an embodiment of the present invention, Fig. 2 is a system diagram of resin transfer to the desalination equipment regeneration equipment of the present invention, and Fig. 3 is a purification device. drug family tree,
FIG. 4 is a circulation system diagram, and FIGS. 5 and 6 are system diagrams of application examples of the present invention. 1... Condenser, 6... Feed water heater, 33 a,
33 b *33c...Cation resin tower, 14...
Feed water heater drain tank, 16... Feed water heater drain pump.
Claims (1)
加熱した後の凝縮したドレンをドレンタンクに回収し、
ドレンポンプによつて再び復水器へ戻す給水加熱器ドレ
ン系において、 前記給水加熱器ドレン中の不純物を除去するために、粒
状の陽イオン交換樹脂を装荷した陽イオン樹脂塔を設け
たことを特徴とする給水加熱器ドレン系の浄化装置。 ２、タービンの復水を処理する復水脱塩装置に使用され
る粒状の前記陽イオン交換樹脂の再生および逆洗するた
めに設置されている再生設備を利用して、前記給水加熱
器ドレン系の前記陽イオン交換樹脂の再生を行い得るよ
う、前記復水脱塩装置の前記再生設備と接続する樹脂移
送系統を設けたことを特徴とする特許請求の範囲第１項
記載の給水加熱器ドレン系の浄化装置。 ３、前記陽イオン交換樹脂の前記再生処理および逆洗・
洗浄を前記陽イオン樹脂塔内でできるよう前記陽イオン
樹脂塔に逆洗・洗浄のための水および空気配管を接続し
、また薬品設備からの通薬配管を接続した系統を設けた
ことを特徴とする特許請求の範囲第１項記載の給水加熱
器ドレン系の浄化装置。 ４、樹脂を再生処理した後、再び前記給水加熱器ドレン
の処理を行う前に、前記陽イオン樹脂塔の出口から前記
ドレンタンクを介し前記ドレンポンプを経て再び前記陽
イオン樹脂塔に戻すことによつて、前記陽イオン樹脂塔
に循環流を与えるために、複数基設置されている前記陽
イオン樹脂塔の出口管路より分岐させた管路を前記ドレ
ンタンクに接続する循環系統を設けたことを特徴とする
特許請求の範囲第１項記載の給水加熱器ドレン系の浄化
装置。[Claims] 1. Collecting condensed condensate in a drain tank after heating the feedwater heater of a power generation plant with the bleed air of a turbine;
In the feed water heater drain system which is returned to the condenser by the drain pump, a cation resin column loaded with granular cation exchange resin is installed in order to remove impurities in the feed water heater drain. Features: Feed water heater drain system purification equipment. 2. The feedwater heater drain system is installed using regeneration equipment installed to regenerate and backwash the granular cation exchange resin used in the condensate desalination equipment that processes condensate from the turbine. The feedwater heater drain according to claim 1, further comprising a resin transfer system connected to the regeneration equipment of the condensate desalination apparatus so as to regenerate the cation exchange resin. System purification device. 3. The regeneration treatment and backwashing of the cation exchange resin
A system is provided in which water and air piping for backwashing and cleaning are connected to the cation resin tower so that cleaning can be performed within the cation resin tower, and a system is also connected to a drug passage pipe from a chemical equipment. A purifying device for a feed water heater drain system according to claim 1. 4. After regenerating the resin, before processing the feed water heater drain again, returning it from the outlet of the cation resin tower to the cation resin tower via the drain tank and the drain pump. Therefore, in order to provide a circulation flow to the cation resin tower, a circulation system is provided in which a pipe branched from the outlet pipe of the plurality of cation resin towers is connected to the drain tank. A feedwater heater drain system purification device according to claim 1, characterized in that:
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4834885A JPS61208407A (en) | 1985-03-13 | 1985-03-13 | Purifier for drain system of feedwater heater |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4834885A JPS61208407A (en) | 1985-03-13 | 1985-03-13 | Purifier for drain system of feedwater heater |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS61208407A true JPS61208407A (en) | 1986-09-16 |
Family
ID=12800874
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4834885A Pending JPS61208407A (en) | 1985-03-13 | 1985-03-13 | Purifier for drain system of feedwater heater |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS61208407A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH03175197A (en) * | 1990-10-24 | 1991-07-30 | Fuji Electric Co Ltd | Tandem type mechanical seal device for pump |
-
1985
- 1985-03-13 JP JP4834885A patent/JPS61208407A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH03175197A (en) * | 1990-10-24 | 1991-07-30 | Fuji Electric Co Ltd | Tandem type mechanical seal device for pump |
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