JPS61295335A - Apparatus for removing impurity in liquid metal - Google Patents

Apparatus for removing impurity in liquid metal

Info

Publication number
JPS61295335A
JPS61295335A JP13426985A JP13426985A JPS61295335A JP S61295335 A JPS61295335 A JP S61295335A JP 13426985 A JP13426985 A JP 13426985A JP 13426985 A JP13426985 A JP 13426985A JP S61295335 A JPS61295335 A JP S61295335A
Authority
JP
Japan
Prior art keywords
liquid metal
impurity
impurities
cold trap
recirculation pipe
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
Application number
JP13426985A
Other languages
Japanese (ja)
Inventor
Teruhisa Nakashiba
中芝 輝久
Yoshito Soma
惣万 芳人
Tamotsu Sano
佐野 保
Kikuo Nakamura
喜久男 中村
Kozo Yoshikawa
孝三 吉川
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kansai Electric Power Co Inc
Mitsubishi Heavy Industries Ltd
Original Assignee
Kansai Electric Power Co Inc
Mitsubishi Heavy Industries Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kansai Electric Power Co Inc, Mitsubishi Heavy Industries Ltd filed Critical Kansai Electric Power Co Inc
Priority to JP13426985A priority Critical patent/JPS61295335A/en
Publication of JPS61295335A publication Critical patent/JPS61295335A/en
Pending legal-status Critical Current

Links

Landscapes

  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Abstract

PURPOSE:To constitute the titled apparatus capable of reducing size of apparatus and releasing impurity easily to an outer system, by connecting a liquid metal layer of impurity separating vessel, an exit and an inlet of a cold trap for liquid metal flow by a liquid metal recirculation pipe. CONSTITUTION:If impurity is accumulated at a mesh part 4 in the cold trap 1, valves 11a, 12a of the melt 2 and the exist 3, and valves 5a, 6a of gas flowing pipes 5, 6 are opened, to start regenerating operation. Hereupon, the part 4 is heated by a heater, etc. provided at the trap 1 outer periphery to melt impurity at the part 4. The impurity is sent to a vessel 4 together with liquid metal circulating as the part 4 a liquid metal recirculation pipe 12 impurity separating vessel 14 the liquid metal recirculation pipe 11 the part 4. H2 in the impurity is transferred to cover gas space part from liquid metal, and the purified liquid metal is returned to the trap 1. Repeating the circulation, the impurity accumulated at the part 4 is removed.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は液体金属中の不純物を除去する不純物除去装置
に関するものである。
DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to an impurity removal device for removing impurities from liquid metal.

(従来の技術) 液体金属冷却型高速増殖炉では、冷却材として液体金属
(なお液体金属の代表例は、Naで、その外にに、Na
Kがある)を用いるが、液体金属は、不純物の濃度を充
分に低くして、材料の腐食等を防止する必要がある。こ
のため、第2図に示す液体金属中の不純物除去装置が設
けられている。
(Prior art) In liquid metal cooled fast breeder reactors, liquid metal is used as a coolant (a typical example of liquid metal is Na;
However, the concentration of impurities in the liquid metal must be sufficiently low to prevent corrosion of the material. For this reason, an apparatus for removing impurities from the liquid metal as shown in FIG. 2 is provided.

同第2図において、(1)がコールドトラップで。In Figure 2, (1) is a cold trap.

同コールドトラップ(1)の中には、不純物を捕獲する
メツシュ部(4)が設けられ、液体金属が入口(2)か
らコールドトラップ(1)内に入って、同メツシュ部(
4)を通過することにより、不純物が析出、捕獲される
。同液体金属の温度は、入口(2)側の配管を流れると
き、或いはコールドトラップ(1)向上部を流れてメツ
シュ部(4)に入るときに。
A mesh part (4) for capturing impurities is provided in the cold trap (1), and the liquid metal enters the cold trap (1) from the inlet (2).
4), impurities are precipitated and captured. The temperature of the liquid metal changes when it flows through the pipe on the inlet (2) side or when it flows through the upper part of the cold trap (1) and enters the mesh part (4).

システム側の温度よりも低い温度に低下しており。The temperature has dropped to lower than the system temperature.

不純物の溶解度を下げて、不純物をメツシュ部(4)で
析出、捕獲するようになっている。なお不純物として多
いのは、酸素と水素である。上記メツシュ部(4)で不
純物の捕獲量が容量を越えると。
The solubility of impurities is lowered, and the impurities are precipitated and captured in the mesh part (4). The most common impurities are oxygen and hydrogen. When the amount of impurities captured in the mesh part (4) exceeds the capacity.

コールドトラップ(1)を交換する必要がある。この場
合、液体金属及び不純物が炉心に直接流れているライン
であれば、コールドトラップ(1)もある程度放射化し
ており、遮蔽等の大損りな作業が必要になる上に、交換
後には、廃棄物処理が問題になる。このため、初めから
予備機を設けておく場合が多いが、第2図に示すように
コールドトラップ(1)の出口(3)と吸着体を有する
水素分離器(7)とを液体金属再循環管(12)により
連絡し、同水素分離器(7)とコールドトラップ(1)
の入口(2)とを液体金属再循環管(11)により連絡
し、メツシュ部(4)に捕獲された水素成分を液体金属
とともに水素分離器(7)へ移行させて、メツシュ部(
4)の性能を回復させる液体金属中の不純物除去装置が
捷写されている。この不純物除去装置の運転方法は9次
の通りである。
Cold trap (1) needs to be replaced. In this case, if the line is where liquid metal and impurities flow directly into the reactor core, the cold trap (1) will also be activated to some extent, requiring costly work such as shielding. Processing becomes a problem. For this reason, a backup device is often provided from the beginning, but as shown in Figure 2, the outlet (3) of the cold trap (1) and the hydrogen separator (7) having an adsorbent are connected to recirculate liquid metal. A pipe (12) connects the hydrogen separator (7) and a cold trap (1).
The hydrogen component captured in the mesh section (4) is transferred together with the liquid metal to the hydrogen separator (7), and the mesh section (
A device for removing impurities in liquid metal that restores the performance of 4) is shown. The method of operating this impurity removal device is as follows.

コールドトラップ(1)を通常運転時の状態から隔離す
る。この隔離は、弁(2a) (3a)を閉じることに
より行われる。次いでコールドトラップ(1)の再生運
転に移る。この再生運転は、液体金属再循環管(11)
 (12)に設けた弁(lla) (12a)を開き、
電磁ポンプ(10)を起動させて、液体金属をメツシュ
部(4)→液体金属再循環管(12)−水素分離器(7
)→液体金属再循環管(11)−メツシュ部(4)に循
環させることにより行われる。このとき、メツシュ部(
4)を加熱等して、水素化合物を循環する液体金属中へ
溶出する一方、この水素化合物を水素分離器(7)の吸
着体へ吸着させる。
Isolate the cold trap (1) from normal operating conditions. This isolation is achieved by closing valves (2a) (3a). Next, the regeneration operation of the cold trap (1) is started. This regeneration operation is performed using the liquid metal recirculation pipe (11).
Open the valve (lla) (12a) provided in (12),
Start the electromagnetic pump (10) and transfer the liquid metal from the mesh section (4) to the liquid metal recirculation pipe (12) to the hydrogen separator (7).
)→liquid metal recirculation pipe (11) - mesh section (4). At this time, the mesh part (
4) is heated or the like to elute the hydrogen compound into the circulating liquid metal, while the hydrogen compound is adsorbed onto the adsorbent of the hydrogen separator (7).

(発明が解決しようとする問題点) 前記第2図に示す液体金属中の不純物除去装置で問題に
なるのは、水素分離器(7)に比較的大型のものが必要
になることである。またこの水素分離器(7)では、吸
着体が例えばニッケル管の中にあるため、水素の透過に
多(の時間がかかり、前述の場合と同様に予備機を設け
て1通常運転時にも予備機とで交互に再生を行う必要が
ある。
(Problems to be Solved by the Invention) A problem with the apparatus for removing impurities from liquid metal shown in FIG. 2 is that a relatively large hydrogen separator (7) is required. In addition, in this hydrogen separator (7), since the adsorbent is located in, for example, a nickel tube, it takes a long time for hydrogen to permeate, and as in the case described above, a standby unit is provided so that it can be used as a standby unit even during normal operation. It is necessary to perform playback alternately with the machine.

本発明は前記の問題点に対処するもので、液体金属中の
不純物をカバーガス空間部へ移行させて分離する不純物
分離容器の液体金属層と液体金属を流すコールドトラッ
プの出口及び入口とを液体金属再循環管により連絡し、
上記不純物分離容器のカバーガス空間部と不純物分離器
とをガス流通管により連絡したことを特徴とする液体金
属中の不純物除去装置に係わり、その目的とする処は。
The present invention addresses the above-mentioned problems by connecting the liquid metal layer of the impurity separation container that separates the impurities in the liquid metal by transferring them to the cover gas space, and the outlet and inlet of the cold trap through which the liquid metal flows. communicated by metal recirculation pipes,
The object of the present invention relates to an apparatus for removing impurities in liquid metal, characterized in that the cover gas space of the impurity separation container and the impurity separator are connected through a gas flow pipe.

装置を小型化できる。また不純物を系外へ容易に放出で
きる改良された液体金属中の不純物除去装置を供する点
にある。
The device can be made smaller. Another object of the present invention is to provide an improved device for removing impurities in a liquid metal that can easily release impurities out of the system.

(問題点を解決するための手段) 本発明の液体金属中の不純物除去装置は前記のように液
体金属中の不純物をカバーガス空間部へ移行させて分離
する不純物分離容器の液体金属層と液体金属を流すコー
ルドトラップの出口及び入口とを液体金属再循環管によ
り連絡し、上記不純物分離容器のカバーガス空間部と不
純物分離器とをガス流通管により連絡しており、不純物
を含む液体金属をコールドトラップの出口から液体金属
再循環管を経て不純物分離容器へ取り出して、同液体金
属中の不純物を同不純物分離容器のカバーガス空間部へ
分離したのち、ガス流通管の系統の不純物分離器へ導い
て、捕獲するので、前記従来のように大型の容器が不用
で、装置が小型化される。また不純物を上記のようにガ
ス流通管の系統の不純物分離器で捕獲するので、捕獲し
た不純物を系外へ放出する際に、不純物分離器を加熱す
る一方、ガス流通管の系統を系外に開くだけでよくて、
不純物が系外へ容易に放出される。
(Means for Solving the Problems) As described above, the device for removing impurities in liquid metal of the present invention separates the impurities from the liquid metal layer of the impurity separation container by moving the impurities in the liquid metal to the cover gas space. The outlet and inlet of the cold trap through which the metal flows are connected by a liquid metal recirculation pipe, and the cover gas space of the impurity separation container and the impurity separator are connected by a gas flow pipe, so that the liquid metal containing impurities is The liquid metal is taken out from the outlet of the cold trap through the recirculation pipe to the impurity separation vessel, and the impurities in the liquid metal are separated into the cover gas space of the impurity separation vessel, and then sent to the impurity separator in the gas distribution pipe system. Since it is guided and captured, there is no need for a large container as in the prior art, and the device can be downsized. In addition, since impurities are captured by the impurity separator in the gas distribution pipe system as described above, when releasing the captured impurities out of the system, the impurity separator is heated and the gas distribution pipe system is removed from the system. All you have to do is open it.
Impurities are easily released from the system.

(実施例) 次に本発明の液体金属中の不純物除去装置を第1図に示
す一実施例により説明すると、(1)がコールドラップ
、(2)が入口、(3)が出口で、同出口(3)が分岐
して、同分岐管に液体金属再循環管(12)が連絡し、
入口(2)が分岐して、同分岐管に液体金属再循環管(
11)が連絡している。なお同液体金属再循環管(11
) (12)は、コールドトラップ(1)の胴部に設け
た入口及び出口に直接連絡してもよい。また上記液体金
属再循環管(11) (12)の他端部部は、不純物分
離容器(14)の液体金属層に連絡し、同液体金属再循
環管(12)の途中には、液体金属循環ポンプ(10)
や加熱ヒータ(図示せず)が設けられ、上記不純物分離
容器(14)のカバーガス空間部にガス流通管(5) 
(6)が連絡している。また上記ガス流通管(6)の途
中には、水素吸着体を有する不純物分離器(ペーパート
ラップ) (15)と加熱器(8)とが設けられ、上記
ガス流通管(5)の途中には、ガス循環ポンプ(9)が
設けられている。なお上記不純物分離容器(14)は、
カバーガスを有するか、カバーガスを作成できるもので
あれば、どのような機器でもよい。また上記液体金属再
循環管の系統には、必要に応じて予熱ヒータや保温材を
設け、上記カバーガス配管系にも必要に応じて予熱ヒー
タや保温材を設けてもよい。また水素ガスを蓄積する必
要のない場合には、系外へ放出するようにしてもよい。
(Example) Next, the apparatus for removing impurities in liquid metal of the present invention will be explained using an example shown in FIG. 1. (1) is a cold wrap, (2) is an inlet, (3) is an outlet, and The outlet (3) is branched and a liquid metal recirculation pipe (12) is connected to the branch pipe;
The inlet (2) branches into a liquid metal recirculation pipe (
11) is in contact. The same liquid metal recirculation pipe (11
) (12) may communicate directly with the inlet and outlet provided in the body of the cold trap (1). The other end portions of the liquid metal recirculation pipes (11) and (12) are connected to the liquid metal layer of the impurity separation container (14), and the liquid metal recirculation pipe (12) has a liquid metal layer in the middle. Circulation pump (10)
A gas flow pipe (5) is provided in the cover gas space of the impurity separation container (14).
(6) is in contact. Further, an impurity separator (paper trap) (15) having a hydrogen adsorbent and a heater (8) are provided in the middle of the gas flow pipe (6), and a heater (8) is provided in the middle of the gas flow pipe (5). , a gas circulation pump (9) is provided. Note that the impurity separation container (14) is
Any device may be used as long as it has a cover gas or can create a cover gas. Further, the liquid metal recirculation pipe system may be provided with a preheater and a heat insulating material as necessary, and the cover gas piping system may also be provided with a preheating heater and a heat insulating material as necessary. Furthermore, when there is no need to accumulate hydrogen gas, it may be discharged outside the system.

(作用) 次に前記第1図の液体金属中の不純物除去装置の作用を
説明する。コールドトラップ(1)内のメツシュ部(4
)に不純物が蓄積されると、入口(2)及び出口(3)
の弁(2a) (3a)を閉じ、液体金属再循環管(1
1) (12)の弁(lla) (12a)及びガス流
通管(5)(6)の弁(5a) (6a)を開き1次い
で液体金属循環ポンプ(10)及びガス循環ポンプ(9
)を駆動して、再生運転を開始する。このとき、メツシ
ュ部(4)部分の温度をコールドトラップ(1)の外面
に設けたヒータ等により加熱して、不純物をメツシュ部
(4)から溶解させてゆく。メツシュ部(4)で溶解し
た不純物は、メツシュ部(4)−液体金属再循環管(1
2)−不純物分離容器(14)−液体金属再循環管(1
1)−メツシュ部(4)に循環する液体金属に含まれて
(Function) Next, the function of the apparatus for removing impurities in liquid metal shown in FIG. 1 will be explained. The mesh part (4) inside the cold trap (1)
), the inlet (2) and outlet (3)
Close the valves (2a) (3a) and close the liquid metal recirculation pipe (1).
1) Open the valves (lla) (12a) of (12) and the valves (5a) (6a) of the gas circulation pipes (5) and (6).1) Then open the liquid metal circulation pump (10) and the gas circulation pump (9).
) to start regeneration operation. At this time, the temperature of the mesh part (4) is heated by a heater or the like provided on the outer surface of the cold trap (1), and the impurities are dissolved from the mesh part (4). The impurities dissolved in the mesh section (4) are removed from the mesh section (4) - liquid metal recirculation pipe (1).
2) - Impurity separation vessel (14) - Liquid metal recirculation tube (1
1) - Contained in the liquid metal circulating in the mesh section (4).

不純物分離容器(14)に送られる。同不純物のうち。It is sent to an impurity separation container (14). Of the same impurities.

水素は液体金属からカバーガス空間部へ移行する性質を
有し、液体金属は純化されて、コールドトラップ(1)
へ戻る。この循環を繰り返し行うと。
Hydrogen has the property of moving from the liquid metal to the cover gas space, and the liquid metal is purified and sent to the cold trap (1).
Return to If you repeat this cycle.

メツシュ部(4)に蓄積された不純物が除去されてゆく
。一方、ガス流通管(5) (6)の系統には、不純物
分離器(15)があり、カバーガス空間部へ移行した水
素ガスが同不純物分離器(15)により捕獲される。こ
のとき、この水素ガスを蓄積しておかなくてもよい場合
には、ガスを系外から系内へ導入する(矢印AI参照)
一方、このガスを系外へ放出(矢印A2参照)する。
Impurities accumulated in the mesh portion (4) are removed. On the other hand, there is an impurity separator (15) in the gas distribution pipes (5) and (6), and hydrogen gas that has migrated to the cover gas space is captured by the impurity separator (15). At this time, if it is not necessary to accumulate this hydrogen gas, introduce the gas from outside the system into the system (see arrow AI)
On the other hand, this gas is released outside the system (see arrow A2).

(発明の効果) 本発明の液体金属中の不純物除去装置は前記のように液
体金属中の不純物をカバーガス空間部へ移行させて分離
する不純物分離容器の液体金r/Iq層と液体金属を流
すコールドトラップの出口及び入口とを液体金属再循環
管により連絡し、上記不純物分離容器のカバーガス空間
部と不純物分離器とをガス流通管により連絡しており、
不純物を含む液体金属をコールドトラップの出口から液
体金属再循環管を経て不純物分離容器へ取り出して、同
液体金属中の不純物を同不純物分離容器のカバーガス空
間部へ分離したのち、ガス流通管の系統の不純物分離器
へ導いて、捕獲するので、前記従来のように大型の容器
が不用で、装置を小型化できる。また不純物を上記のよ
うにガス流通管の系統の不純物分離器で捕獲するので、
捕獲した不純物を系外へ放出する際に、不純物分離器を
加熱する一方、ガス流通管の系統を系外に開くだけでよ
くて、不純物を系外へ容易に放出できる効果がある。
(Effects of the Invention) As described above, the device for removing impurities in liquid metal of the present invention separates the liquid metal from the liquid gold r/Iq layer of the impurity separation container which transfers impurities in the liquid metal to the cover gas space and separates the impurities. The outlet and inlet of the flowing cold trap are connected by a liquid metal recirculation pipe, and the cover gas space of the impurity separation container and the impurity separator are connected by a gas flow pipe,
The liquid metal containing impurities is taken out from the outlet of the cold trap through the liquid metal recirculation pipe to the impurity separation vessel, and the impurities in the liquid metal are separated into the cover gas space of the impurity separation vessel. Since the impurity is introduced into the system's impurity separator and captured, the large container required in the conventional method is unnecessary, and the device can be made smaller. In addition, since impurities are captured by the impurity separator in the gas distribution pipe system as described above,
When releasing the captured impurities out of the system, it is sufficient to heat the impurity separator and open the gas flow pipe system to the outside of the system, which has the effect of easily releasing the impurities out of the system.

以上本発明を実施例により説明したが、勿論本発明はこ
のような実施例に限定されるものではなく2本発明の精
神を逸脱しない範囲で種々の設計の改変を施しうるちの
である。
Although the present invention has been described above with reference to embodiments, it goes without saying that the present invention is not limited to these embodiments and can be modified in various ways without departing from the spirit of the present invention.

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

第1図は本発明に係わる液体金属中の不純物除去装置の
一実施例を示す系統図、第2図は従来の液体金属中の不
純物除去装置を示す系統図である。 (1)・・・コールドトラップ、(2)・・・入口、(
3)・・・出口、 (5)(6)・・・ガス流通管、 
(11)(12)・・・液体金属再循環管、 (14)
  ・・・不純物分離容器、 (15)  ・・・不純
物分離器。 復代理人弁理士岡本重文外2名
FIG. 1 is a system diagram showing an embodiment of an apparatus for removing impurities in liquid metal according to the present invention, and FIG. 2 is a system diagram showing a conventional apparatus for removing impurities in liquid metal. (1)...cold trap, (2)...inlet, (
3)...Outlet, (5)(6)...Gas distribution pipe,
(11) (12)...Liquid metal recirculation pipe, (14)
... Impurity separation container, (15) ... Impurity separator. Sub-representative patent attorney Shigefumi Okamoto and two others

Claims (1)

【特許請求の範囲】[Claims] 液体金属中の不純物をカバーガス空間部へ移行させて分
離する不純物分離容器の液体金属層と液体金属を流すコ
ールドトラップの出口及び入口とを液体金属再循環管に
より連絡し、上記不純物分離容器のカバーガス空間部と
不純物分離器とをガス流通管により連絡したことを特徴
とする液体金属中の不純物除去装置。
The liquid metal layer of the impurity separation vessel, in which impurities in the liquid metal are transferred to the cover gas space and separated, and the outlet and inlet of the cold trap through which the liquid metal flows are connected by a liquid metal recirculation pipe, and the impurity separation vessel is An apparatus for removing impurities in liquid metal, characterized in that a cover gas space and an impurity separator are connected through a gas flow pipe.
JP13426985A 1985-06-21 1985-06-21 Apparatus for removing impurity in liquid metal Pending JPS61295335A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13426985A JPS61295335A (en) 1985-06-21 1985-06-21 Apparatus for removing impurity in liquid metal

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13426985A JPS61295335A (en) 1985-06-21 1985-06-21 Apparatus for removing impurity in liquid metal

Publications (1)

Publication Number Publication Date
JPS61295335A true JPS61295335A (en) 1986-12-26

Family

ID=15124341

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13426985A Pending JPS61295335A (en) 1985-06-21 1985-06-21 Apparatus for removing impurity in liquid metal

Country Status (1)

Country Link
JP (1) JPS61295335A (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5837139A (en) * 1981-08-26 1983-03-04 Power Reactor & Nuclear Fuel Dev Corp Regeneration of cold trap

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5837139A (en) * 1981-08-26 1983-03-04 Power Reactor & Nuclear Fuel Dev Corp Regeneration of cold trap

Similar Documents

Publication Publication Date Title
US4479927A (en) Regenerable cold trap for aluminum chloride effluent
US5149493A (en) Installation to regenerate cold traps loaded with the hydride and oxide of a liquid metal
JPS61295335A (en) Apparatus for removing impurity in liquid metal
JP2568100Y2 (en) Reactor water purification system
CN101857323A (en) Method and device for power station condensed water fine treatment
JPS6226000B2 (en)
JPS61295336A (en) Apparatus for removing impurity in liquid metal
JP2667528B2 (en) Gas recovery method and device used therefor
JPS59226132A (en) Purifying device for liquid metal
JPS6154846B2 (en)
JPS6057493B2 (en) liquid metal refining equipment
JPS61208407A (en) Purifier for drain system of feedwater heater
JPS61188865A (en) High temperature filtering device for cooling water of fuel cell
JPH05203788A (en) System for purifying reactor water and fuel pool water
JPH0218872A (en) High temperature adsorption treatment device
JPS6329724Y2 (en)
JPH01104385A (en) Purifier for high pressure water
JPS62193617A (en) Magnetic separator
JPH0432639Y2 (en)
JPS5834400A (en) Device for cleaning hydrogen and its isotope
JPS60178394A (en) Refrigerant purifying system of nuclear reactor
JPS58166293A (en) Liquid metal purification device
Iniotakis et al. Method of hydrogen isotope isolation from inert gas flow
JPH02309296A (en) Burst slug detector
JPH0425798A (en) Condensate purification system