JPH03284311A - Sintered wire net filter medium and filter element using the same - Google Patents

Sintered wire net filter medium and filter element using the same

Info

Publication number
JPH03284311A
JPH03284311A JP2086177A JP8617790A JPH03284311A JP H03284311 A JPH03284311 A JP H03284311A JP 2086177 A JP2086177 A JP 2086177A JP 8617790 A JP8617790 A JP 8617790A JP H03284311 A JPH03284311 A JP H03284311A
Authority
JP
Japan
Prior art keywords
wire mesh
sintered
wire net
filter
wire
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP2086177A
Other languages
Japanese (ja)
Other versions
JPH0757292B2 (en
Inventor
Ryuichi Yamamoto
隆一 山本
Saburo Tamura
田村 三郎
Yoshiaki Murakami
善朗 村上
Osamu Takahashi
修 高橋
Yoshihiro Nozawa
野沢 義宏
Tatsunori Masuda
桝田 達則
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.)
Kimura Chemical Plants Co Ltd
Power Reactor and Nuclear Fuel Development Corp
Original Assignee
Kimura Chemical Plants Co Ltd
Power Reactor and Nuclear Fuel Development Corp
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 Kimura Chemical Plants Co Ltd, Power Reactor and Nuclear Fuel Development Corp filed Critical Kimura Chemical Plants Co Ltd
Priority to JP8617790A priority Critical patent/JPH0757292B2/en
Publication of JPH03284311A publication Critical patent/JPH03284311A/en
Publication of JPH0757292B2 publication Critical patent/JPH0757292B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E30/00Energy generation of nuclear origin
    • Y02E30/30Nuclear fission reactors
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies

Landscapes

  • Filtering Materials (AREA)

Abstract

PURPOSE:To form a sintered wire net with the clogging reduced by placing two twilled wire nets with the longitudinal and lateral opening being extremely fine on each other so that the angle between the warp and weft is controlled to 90 deg. and sintering the laminate. CONSTITUTION:A protective wire net 1, a sintered wire net filter medium 2, a protective wire net 3, a reinforcing wire net 4 and a reinforcing wire net 5 are successively arranged from a filtrate contact surface to constitute a filter element. The reinforcing wire nets 4 and 5 are used to reinforce the filter medi um against the filtration pressure exerted on the filter medium 2 surface. The wire nets 4 and 5 are a twilled wire net of a stainless steel wire and having about 12 longitudinal mesh and about 64 lateral mesh, and the nets are placed on each other so that the angle between the warp and weft is controlled to 90 deg., pressed on the inner side face of the protective wire net 3 and sintered to weld the respective contacts. The effect in separating a current to the rein forcing wire nets 4 and 5 is enhanced by the protective wire net 3.

Description

【発明の詳細な説明】 [産業上の利用分野〕 本発明は濾過器、特に原子力発電所より受は入れた使用
済核燃料再処理工場の清澄工程における濾過器に使用す
る、ミクロン単位の極めて微小な不溶解固形粒子を濾別
するための金網焼結濾材、及びこの金網焼結濾材を使用
したフィルタエレメントに関するものである。
[Detailed Description of the Invention] [Industrial Application Field] The present invention is directed to a filter, particularly an extremely small one in the micron range, used in a filter in the clarification process of a spent nuclear fuel reprocessing plant received from a nuclear power plant. The present invention relates to a wire mesh sintered filter material for filtering out undissolved solid particles, and a filter element using this wire mesh sintered filter material.

[従来の技術] 原子力発電所等より受は入れた使用済核燃料の再処理工
場における溶液清澄工程においては、使用済核燃料の溶
解溶/fL(硝酸溶液)中に含まれる粒径5〜]0ミク
ロンの極めて微小な固形粒子を95%以上除去すること
が要求される。
[Prior art] In the solution clarification process at a reprocessing plant for spent nuclear fuel received from nuclear power plants, etc., the particle size contained in the dissolved solution/fL (nitric acid solution) of spent nuclear fuel is 5 to 0. It is required to remove 95% or more of extremely fine solid particles of micron size.

従来、このような条件を満足する濾過器としては、ステ
ンレス金属粉末を焼結した金属粉末焼結フィルタエレメ
ントを使用したパルスフィルタが用いられる。
Conventionally, a pulse filter using a sintered metal powder filter element made of sintered stainless steel metal powder has been used as a filter that satisfies these conditions.

[発明か解決しようとする課題] しかし、上記のようなミクロン単位の極めて微小な固体
粒子を濾別するための金属粉末焼結濾材は、その補集効
率は極めて優れているが、濾材の層が厚く、形成された
濾過孔の形状は複雑で、がっ、液の通路が屈折している
ため濾過抵抗が大きく、微粒子の目詰まりによる濾過速
度の低下も大きい。また目詰すりが激しく、更に洗浄(
逆洗)による目詰まりの回復も充分な効果を得ることが
困難である。従ってこのような従来の濾材を使用したフ
ィルタエレメントは交換頻度がきわめて多いという欠点
がある。
[Problem to be solved by the invention] However, although the metal powder sintered filter medium for filtering out extremely small solid particles on the micron scale as described above has extremely excellent collection efficiency, the layer of the filter medium The filtration holes are thick, the shape of the filtration holes is complicated, and the liquid passage is bent, resulting in high filtration resistance, and the filtration speed is greatly reduced due to clogging with particulates. In addition, the clogging is severe, and further cleaning (
It is also difficult to obtain a sufficient effect in clogging recovery by backwashing. Therefore, filter elements using such conventional filter media have the disadvantage that they must be replaced extremely frequently.

しかるに、核燃料等の放射性物質を取り扱う場合、汚染
が外部に拡大することを防止するためにはフィルタの交
換に際し、事前にフィルタの洗浄を行い、更に交換時液
の滴下により輸送キャスクや作業エリヤが汚染しないよ
う充分な液切りと自然乾燥を行う必要があり、従って稼
働率の低下を招いている。
However, when handling radioactive materials such as nuclear fuel, in order to prevent contamination from spreading outside, filters must be cleaned before replacing them, and the transport cask and work area may be damaged by dripping liquid during replacement. It is necessary to drain the liquid sufficiently and dry it naturally to avoid contamination, which results in a decrease in the operating rate.

また、交換頻度が多いことから高レベルの放射性廃棄物
としてのフィルタエレメントが多くなることも問題とな
っている。
Another problem is that because filter elements are frequently replaced, the number of filter elements becomes high-level radioactive waste.

本発明は従来の技術の有するこのような問題点に鑑みな
されたものであり、その目的とするところは、濾過抵抗
が小さく、かつ目詰まりの度合いが少なく、更に目詰ま
り時においても洗浄により容易に目詰まりが除去できる
、ミクロン単位の極めて微小な固形粒子を濾別できる金
網焼結濾材、及びこの金網焼結濾材を使用したフィルタ
エレメントを提供しようとするものである。
The present invention has been developed in view of the above-mentioned problems of the conventional technology, and its objectives are to have low filtration resistance, a low degree of clogging, and to be easier to clean even in the event of clogging. The present invention aims to provide a wire mesh sintered filter material that can remove clogging and filter out extremely fine solid particles on the micron scale, and a filter element using this wire mesh sintered filter material.

[課題を解決するための手段J 上記目的を達成するために、本発明における金網焼結濾
材は縦、または横方向の一方の目開きが極めて微細な綾
畳織金網2枚を、それぞれの縦線、及び横線が互いに交
差角が90度になるよう重ね合わせた後加圧、焼結し一
体化するものである。
[Means for Solving the Problems J] In order to achieve the above object, the wire mesh sintered filter medium of the present invention consists of two pieces of twilled woven wire mesh with extremely fine openings in either the vertical or horizontal direction, each vertically or horizontally. The wires and horizontal wires are overlapped so that the intersection angle is 90 degrees, and then pressurized and sintered to integrate them.

更に、本発明フィルタエレメントは、濾液接触面より保
護金網、本発明金網焼結濾材、保護金網、補強金網を順
次配設することにより構成される。
Furthermore, the filter element of the present invention is constructed by sequentially disposing a protective wire mesh, a wire mesh sintered filter medium of the present invention, a protective wire mesh, and a reinforcing wire mesh from the filtrate contact surface.

以下、本発明を実施例につき図面に基づいて詳細に説明
する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described in detail below with reference to the drawings.

本実施例においては基本金網として、縦325メツシュ
(線径0 、035 i+m) 、横2400メツシュ
(線径0.025m1)のステンレス鋼線製の綾畳織金
網を使用し、この基本金網2枚をそれぞれの縦線、及び
横線が互いに交差角が90度になるように重ね合わせた
後、加圧、焼結すれば、縦線、及び横線は互いに接触し
たその交差点において結合される。本発明の金網焼結濾
材は以上のように構成される。
In this example, a twill woven wire mesh made of stainless steel wire with a length of 325 meshes (wire diameter 0,035 i+m) and a width of 2400 meshes (wire diameter 0.025m1) was used as the basic wire mesh, and two pieces of this basic wire mesh were used. are overlapped so that the respective vertical lines and horizontal lines intersect with each other at a 90 degree angle, and then pressurized and sintered to bond the vertical lines and horizontal lines at their intersections where they touch each other. The wire mesh sintered filter medium of the present invention is constructed as described above.

なお、本実施例においては基本金網として縦325メツ
シュ、横2400メツシュの綾畳織金網を使用したが、
場合により更に口数の少ない縦270メツシュ、横20
00メツシュ、あるいは口数の多い縦500メツシュ、
横3600メツツユの綾畳織金網も使用できる。メツシ
ュがあまり小さいと粒子の捕集効率が低下し、メツシュ
があまり大きいと金網の製作が困難で、かつ強度に問題
があり、本発明の金網焼結濾材を構成する基本金網とし
ては縦270〜50oメツンユ、tl!12000〜3
600メツシュの綾畳織金網を使用すると好適である。
In this example, a twill woven wire mesh with 325 meshes in length and 2400 meshes in width was used as the basic wire mesh.
Depending on the case, the number of meshes may be even smaller by 270 meshes in height and 20 meshes in width.
00 meshes, or 500 vertical meshes with many words,
Twill woven wire mesh with a width of 3,600 mm can also be used. If the mesh is too small, the particle collection efficiency will decrease, and if the mesh is too large, it will be difficult to manufacture the wire mesh and there will be problems with its strength. 50o metsunyu, tl! 12000~3
It is preferable to use a 600 mesh twill wire mesh.

第1図は本発明の金網焼結濾材を使用したフィルタエレ
メントの構成を説明するためのその要部斜視断面図で、
濾液接触面より保護金網(1)、本発明の金網焼結濾材
(2)、保護金網(3)、補強金網(4)、補強金網(
5)が順次配設され本発明のフィルタエレメントが構成
される。
FIG. 1 is a perspective cross-sectional view of the essential parts for explaining the configuration of a filter element using the wire mesh sintered filter medium of the present invention.
From the filtrate contact surface, the protective wire mesh (1), the wire mesh sintered filter medium of the present invention (2), the protective wire mesh (3), the reinforced wire mesh (4), and the reinforced wire mesh (
5) are sequentially arranged to constitute the filter element of the present invention.

保護金網(1)、(3)は、いずれらは金網焼結濾材(
2)を保護するもので、300メツシュ(線径0.1m
m)のステンレス鋼線製の平織の金網で、金網焼結濾材
(2)をはさみその両側面に加圧、焼結される。なお、
保護金網(3)は金網焼結濾材(2)を保護するのみな
らず、補強金網(/I)、(5)への分流効果を向上せ
しめる効果かある。
The protective wire mesh (1) and (3) are both wire mesh sintered filter media (
2) with 300 mesh (wire diameter 0.1m)
The wire mesh sintered filter medium (2) is sandwiched between the stainless steel wire plain weave wire mesh (m), and both sides thereof are pressed and sintered. In addition,
The protective wire mesh (3) not only protects the wire mesh sintered filter medium (2) but also has the effect of improving the effect of dividing the flow to the reinforcing wire meshes (/I) and (5).

補強金網(4)、(5)はいずれも濾材(2)面にかか
る濾過圧力に対抗して濾材を補強するもので、補強金網
(4)、(5)はいずれも縦!2メツシュ(線径0.6
mm)、横64メツシュ(線径0.4mm)のステンレ
ス鋼線製の平畳織金網で、それぞれの縦線、及び横線の
交差角が90度になるよう重ねあわせ保護金網(3)の
内側面に加圧、焼結しそれぞれの接触部を溶着せしめる
The reinforcing wire meshes (4) and (5) are both used to reinforce the filter material against the filtration pressure applied to the surface of the filter material (2), and both of the reinforcing wire meshes (4) and (5) are vertical! 2 mesh (wire diameter 0.6
mm), a flat tatami-woven wire mesh made of stainless steel wire with a width of 64 mesh (wire diameter 0.4 mm), stacked inside the protective wire mesh (3) so that the intersection angle of each vertical line and horizontal line is 90 degrees. Pressure is applied to the sides, sintering is performed, and each contact area is welded.

次ぎに、上記実施例に示す本発明の金網焼結濾材フィル
タエレメントを使用したパルスフィルタの微粒子捕集効
率と濾過速度の変化を測定し、従来の金属粉末焼結フィ
ルタエレメントを使用したパルスフィルタと対比した。
Next, changes in particulate collection efficiency and filtration speed of the pulse filter using the wire mesh sintered filter element of the present invention shown in the above example were measured, and compared with the pulse filter using the conventional metal powder sintered filter element. Contrasted.

表−1に微粒子捕集効率の測定結果を示す。Table 1 shows the measurement results of particulate collection efficiency.

注;捕集効率は個数パーセントで示す。Note: Collection efficiency is expressed in number percent.

(a)        d  ≦  5μm(b)  
 5μs  <  d  ≦ 10μm(c)10μ麟
 <  d        [d;粒径]第2図は本発
明の金網焼結濾材フィルタエレメントを使用したパルス
フィルタと従来の金属粉末焼結濾材フィルタエレメント
を使用したパルスフィルタとの濾過速度を比較する曲線
で、測定条件は下記の通りである。
(a) d≦5μm (b)
5 μs < d ≦ 10 μm (c) 10 μm < d [d; Particle size] Figure 2 shows a pulse filter using the wire mesh sintered filter element of the present invention and a pulse filter using the conventional metal powder sintered filter element. This is a curve comparing the filtration speed with a filter, and the measurement conditions are as follows.

運転条件  真空度  ;  −0,9m^q逆洗圧 
 ・0.9  Kg/cI11’逆洗時間 ;   5
.0sec 濾過面積 ;   1350cm” 給液条件  残渣濃度 ;   0.6g/L残渣粒径
 ;  5〜10 μm 液  温 ;   常温(約25℃) [効果] 以上述べたごとく、本発明の金網焼結濾材フィルタエレ
メントを使用したパルスフィルタの微粒子捕集効率は、
従来の金属粉末焼結濾材フィルタエレメントを使用した
パルスフィルタと比較し遜色なく極めて優秀であるのみ
ならず、本発明の金網焼結濾材フィルタエレメントを使
用したパルスフィルタは従来の金属粉末焼結濾材フィル
タエレメントを使用したパルスフィルタと比較し、微粒
子の濾過速度とその経時変化(低下割合)は極めて優れ
ている。
Operating conditions Vacuum level: -0.9m^q Backwash pressure
・0.9 Kg/cI11' Backwash time; 5
.. 0sec Filtration area: 1350 cm" Liquid supply conditions Residue concentration: 0.6 g/L Residue particle size: 5 to 10 μm Liquid temperature: Room temperature (approximately 25°C) [Effects] As described above, the wire mesh sintered filter of the present invention The particulate collection efficiency of a pulse filter using an element is
Not only is the pulse filter using the conventional metal powder sintered filter element superior to that of the conventional metal powder sintered filter element, but the pulse filter using the wire mesh sintered filter element of the present invention is also superior to the conventional metal powder sintered filter element. Compared to a pulse filter using an element, the filtration rate of particulates and its change over time (rate of decline) are extremely superior.

また、本発明の金網焼結濾材は2枚の金網を焼結したも
のであるから従来の金属粉末焼結濾材に比較し、濾過抵
抗が小さく、かつ目詰まりも少ない。更に本発明の金網
焼結−材は主として表面濾過により微粒子を捕集するも
ので、目詰まり時においても洗浄(逆洗)による目詰ま
りの回復も容易である。従って逆洗性能は極めて良好で
、従来の金属粉末焼結濾材フィルタエレメントを使用し
たものと比較するとその処理液量(寿命)は約15倍で
ある。
Furthermore, since the wire mesh sintered filter medium of the present invention is made by sintering two wire meshes, it has lower filtration resistance and less clogging than conventional metal powder sintered filter media. Furthermore, the wire mesh sintered material of the present invention mainly collects fine particles through surface filtration, and even when clogged, it is easy to recover from the clog by washing (backwashing). Therefore, the backwash performance is extremely good, and the amount of liquid processed (life) is about 15 times that of a filter element using a conventional metal powder sintered filter element.

従って、特に原子力発電所等の使用済核燃料の再処理工
場の清澄工程における溶液中のミクロン単位の微小な不
溶解固形粒子を濾別するパルスフィルタに使用すれば、
エレメント取替え時の停止期間が少なくなるので稼働率
が向上し、また交換頻度が少ないことから放射性廃棄物
の発生量を著しく削減することができる。
Therefore, if used in a pulse filter that filters out micron-sized undissolved solid particles in a solution in the clarification process of spent nuclear fuel reprocessing plants such as nuclear power plants,
Since the downtime during element replacement is shortened, the operating rate is improved, and since the frequency of element replacement is low, the amount of radioactive waste generated can be significantly reduced.

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

第1図は本発明の金網焼結濾材を使用したフィルタエレ
メントの構成を説明する要部斜視断面図、第2図は本発
明の金網焼結濾材フィルタエレメントを使用したパルス
フィルタと従来の金属粉末焼結濾材フィルタエレメント
を使用したパルスフィルタとの濾過速度を比較する曲線
である。 】、3・・保護金網、  2・・金網焼結濾材4.5・
・補強金網 A・・本発明の金網焼結−材フィルタエレメントを使用
したパルスフィルタの濾過速度曲線 B・・従来の金属粉末焼結濾材フィルタエレメントを使
用したパルスフィルタの濾過速度曲線
Fig. 1 is a perspective cross-sectional view of a main part illustrating the configuration of a filter element using the sintered wire mesh filter medium of the present invention, and Fig. 2 shows a pulse filter using the sintered wire mesh filter element of the present invention and a conventional metal powder filter. 1 is a curve comparing filtration speed with a pulse filter using a sintered filter element. ], 3. Protective wire mesh, 2. Sintered wire mesh filter material 4.5.
- Reinforced wire mesh A...Filtration speed curve of a pulse filter using the sintered wire mesh material filter element of the present invention B...Filtration speed curve of a pulse filter using a conventional metal powder sintered filter material filter element

Claims (1)

【特許請求の範囲】 1、縦、または横方向の一方の目開きが極めて微細な綾
畳織金網2枚を、それぞれの縦線、及び横線が互いに交
差角が90度となるよう重ね合わせた後加圧、焼結し一
体化せしめたことを特徴する金網焼結濾材。 2、綾畳織金網が、縦270〜500メッシュ、横20
00〜3600メッシュの綾畳織金網である請求項1記
載の金網焼結濾材。 3、濾液接触面より、保護金網、金網焼結濾材、保護金
網、補強金網を順次配設してなるフィルタエレメントに
おいて、前記金網焼結濾材を請求項1又は2記載の金網
焼結濾材で構成したことを特徴とするフィルタエレメン
ト。
[Claims] 1. Two pieces of twilled tatami wire mesh with extremely fine openings in either the vertical or horizontal direction are superimposed so that the vertical and horizontal lines intersect with each other at a 90 degree angle. A wire mesh sintered filter material characterized by being integrated after being pressurized and sintered. 2. Twill tatami wire mesh, length 270-500 mesh, width 20
The wire mesh sintered filter medium according to claim 1, which is a twilled wire mesh of 00 to 3600 mesh. 3. A filter element in which a protective wire mesh, a wire mesh sintered filter medium, a protective wire mesh, and a reinforcing wire mesh are sequentially arranged from the filtrate contact surface, wherein the wire mesh sintered filter medium is constituted by the wire mesh sintered filter medium according to claim 1 or 2. A filter element characterized by:
JP8617790A 1990-03-30 1990-03-30 Wire mesh sintered filter material and filter element using the wire mesh sintered filter material Expired - Fee Related JPH0757292B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8617790A JPH0757292B2 (en) 1990-03-30 1990-03-30 Wire mesh sintered filter material and filter element using the wire mesh sintered filter material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8617790A JPH0757292B2 (en) 1990-03-30 1990-03-30 Wire mesh sintered filter material and filter element using the wire mesh sintered filter material

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JPH03284311A true JPH03284311A (en) 1991-12-16
JPH0757292B2 JPH0757292B2 (en) 1995-06-21

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0655991A (en) * 1992-06-11 1994-03-01 Sensor Technol Kk Gas filter for gas generator
JP2010075832A (en) * 2008-09-25 2010-04-08 Nichidai Filter Corp Filter for high speed filtration
JP2014166611A (en) * 2013-02-28 2014-09-11 Jfe Engineering Corp Filter body, filter device, and sea water treatment apparatus
JP2017221912A (en) * 2016-06-16 2017-12-21 株式会社東芝 Method for decreasing sulfate ions, apparatus for decreasing sulfate ions, and reactant for sulfate ions

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2017026101A (en) * 2015-07-27 2017-02-02 日本ドレッサー株式会社 Valve device

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0655991A (en) * 1992-06-11 1994-03-01 Sensor Technol Kk Gas filter for gas generator
JP2010075832A (en) * 2008-09-25 2010-04-08 Nichidai Filter Corp Filter for high speed filtration
JP2014166611A (en) * 2013-02-28 2014-09-11 Jfe Engineering Corp Filter body, filter device, and sea water treatment apparatus
JP2017221912A (en) * 2016-06-16 2017-12-21 株式会社東芝 Method for decreasing sulfate ions, apparatus for decreasing sulfate ions, and reactant for sulfate ions

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