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JPS60150883A - Concentration device - Google Patents

Concentration device

Info

Publication number
JPS60150883A
JPS60150883A JP429884A JP429884A JPS60150883A JP S60150883 A JPS60150883 A JP S60150883A JP 429884 A JP429884 A JP 429884A JP 429884 A JP429884 A JP 429884A JP S60150883 A JPS60150883 A JP S60150883A
Authority
JP
Japan
Prior art keywords
waste liquid
salt solution
salt
temp
radioactive waste
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
JP429884A
Other languages
Japanese (ja)
Inventor
Shoichi Yoshida
正一 吉田
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.)
Nippon Genshiryoku Jigyo KK
Nippon Atomic Industry Group Co Ltd
Original Assignee
Nippon Genshiryoku Jigyo KK
Nippon Atomic Industry Group Co 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 Nippon Genshiryoku Jigyo KK, Nippon Atomic Industry Group Co Ltd filed Critical Nippon Genshiryoku Jigyo KK
Priority to JP429884A priority Critical patent/JPS60150883A/en
Publication of JPS60150883A publication Critical patent/JPS60150883A/en
Pending legal-status Critical Current

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  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

PURPOSE:To concentrate efficiently under ordinary temps. and pressure by controlling the temp. difference between a treating liquid and a salt soln. which are supplied on both sides of a membrane within the preset range. CONSTITUTION:The salt concn. C4 in a salt soln. to be charged into a salt soln. chamber 4 is sufficiently increased by a salt soln. concentrator 7, and the difference in salt concn. from the salt concn. C3 in the radioactive waste liquid is kept large. The temp. T3 of the radioactive waste liquid is simultaneously made higher than the temp. T4 by a temp. controller 8 to increase the temp. difference, and to promote the transfer of water from the radioactive waste liquid to the salt soln. The treatment is efficiently carried out in this way.

Description

【発明の詳細な説明】 [発明の技術分野] 本発明は、例えば沸騰水形原子力発電所等の放射性物質
取扱いM設において発生する放射性廃液等を濃縮処理J
−る濃縮装置に関する。
Detailed Description of the Invention [Technical Field of the Invention] The present invention provides a method for concentrating radioactive waste liquid, etc. generated in facilities handling radioactive materials such as boiling water nuclear power plants.
- Concerning a concentration device.

[発明の技術的背景とその問題点] 一般に、原子力発電所等の放射性物質取扱い施設で発生
する放射性廃液は、蒸発式!1a縮装置、逆漫誘式1l
jl縮装冒等の濃縮装置によね濃縮された4υ−乾燥固
化され処理されている。しかしながら、このような従来
の濃縮装置では、放射性廃液を高温もしくは高圧で処理
するため、装置および装量材料の腐食が激しく耐久性に
乏しく、また耐圧性をもlこせるために装置が高価とな
る、等の欠点があった。
[Technical background of the invention and its problems] In general, radioactive waste liquid generated at facilities handling radioactive materials such as nuclear power plants is evaporative! 1a compression device, reverse manga type 1l
4υ is concentrated using a concentrator such as a condenser, and is then dried and solidified. However, in such conventional concentrators, the radioactive waste liquid is treated at high temperature or high pressure, which causes severe corrosion of the equipment and charging materials, resulting in poor durability.Also, the equipment is expensive due to its pressure resistance. There were drawbacks such as.

近時、このようなテ「点を解消したずなわち常温常It
で濃縮処理が可能という隔膜式濃縮装置が提案されてき
ている。この濃縮装置ひは隔膜を隔てて一方に放射性廃
液を、他方にそれより高濃度の塩溶液を供給して、両者
の塩の温度差を利用して放射性廃液中の水分を塩溶液側
に移行させることにより、放射性廃液が濃縮処理される
Recently, this problem has been solved, which means that it can be used at room temperature.
A diaphragm-type concentrator has been proposed that can perform concentration treatment. This concentrator is separated by a diaphragm, and supplies radioactive waste liquid to one side and a salt solution with a higher concentration to the other side, and uses the temperature difference between the two salts to transfer water in the radioactive waste liquid to the salt solution side. By doing so, the radioactive waste liquid is concentrated.

しかしながらこの上うな濃縮装置では、条件が緩和であ
る反面、従来の蒸発式濃縮装置や逆浸透式濃縮装置に比
べ処1q!能率が低いという難点がある。
However, although the conditions for this type of concentrator are relaxed, it is only 1q lower than conventional evaporative concentrators and reverse osmosis concentrators. The problem is that efficiency is low.

[発明の目的] 本発明はこのような従来の事情に対処してなされたもの
で、常温、常圧に近い条件下で、しかも効率良く濃縮づ
ることのできる濃縮装置を提供しにうとするものである
[Object of the Invention] The present invention has been made in response to the above-mentioned conventional circumstances, and aims to provide a concentrating device that can efficiently concentrate under conditions close to normal temperature and normal pressure. It is.

[発明の概要] tなりち本発明の濃縮装置は、被処理液中の水をそれよ
り高濃度の塩溶液中に透過させる隔膜を備えた濃縮装置
において、前記隔膜を隔てて供給される前記被処理液お
よび塩溶液の温1良を検出し、その温度差をあらかじめ
定められた範囲内に制御する温度制御装置を配設したこ
とを特徴と覆る。
[Summary of the Invention] The concentration device of the present invention is provided with a diaphragm that allows water in a liquid to be treated to permeate into a salt solution with a higher concentration. The present invention is characterized by the provision of a temperature control device that detects the temperatures of the liquid to be treated and the salt solution and controls the temperature difference within a predetermined range.

[発明の実施例] 以下本発明の詳細を図面に示す一実施例について説明す
る。
[Embodiment of the Invention] The details of the present invention will be described below with reference to an embodiment shown in the drawings.

図面は本発明の一実施例のi1a縮装回を示すもので、
IIi用性用液廃液理対象どした濃縮装置である。
The drawing shows an i1a reduction circuit according to an embodiment of the present invention.
This is a concentrating device designed for liquid waste liquid management.

図において、4基の濃縮槽1a11b、1C11dが直
列に配置され、それぞれ隔膜2により廃液室3と塩溶液
室4に二分されている。
In the figure, four concentration tanks 1a11b and 1C11d are arranged in series, and each is divided into two by a diaphragm 2 into a waste liquid chamber 3 and a salt solution chamber 4.

これらの濃縮槽1a、 1b、lc、idの各廃液室3
は廃液用配管5により直列に接続され、その上流に配設
されたポンプP1により放口・1性廃液が濃縮槽1aJ
:すIn縮槽11)、1C11dを順に通過して放出さ
れるようになっている。また濃縮+01a 、1b 、
1c 、1dの各塩溶液室4は塩溶液用配管6にJ:り
直列に接続され、この塩溶液用配管6はさらに例えば蒸
発濃縮器等からなるJi溶液淵濃縮7おにびポンプP2
が介挿されてループを形成しており、塩溶液がポンプP
2にJ:り濃縮槽1dの塩溶液室4から濃縮槽1aの塩
溶液室4方向へ流れ]n溶a濃縮器7で高濃度に濃縮さ
れて再び濃縮槽1dの塩溶液室4へ循環するにうになっ
ている。なお、塩溶液濃縮器7には濃縮により発生覆る
蒸気t9を放出する配管が接続されている。
Each waste liquid chamber 3 of these concentration tanks 1a, 1b, lc, and id
are connected in series by a waste liquid pipe 5, and a pump P1 disposed upstream discharges the discharged monochromatic waste liquid to the concentration tank 1aJ.
1) and 1C11d in order to be discharged. Also concentrated +01a, 1b,
Each of the salt solution chambers 1c and 1d is connected in series to a salt solution piping 6, and this salt solution piping 6 is further connected to a Ji solution concentration 7 comprising, for example, an evaporative concentrator or the like pump P2.
is inserted to form a loop, and the salt solution flows through the pump P.
2: Flows from the salt solution chamber 4 of the concentration tank 1d to the salt solution chamber 4 of the concentration tank 1a] It is concentrated to a high concentration in the concentration tank 7 and circulated again to the salt solution chamber 4 of the concentration tank 1d. It's getting better. Note that the salt solution concentrator 7 is connected to a pipe for discharging the steam t9 generated by concentration.

本発明においては、さらに各濃縮槽1a11b11C1
1dの廃液室3と塩溶液室4おにび塩溶液濃縮器7に接
続され、これらに流入するh(躬性廃液および塩溶液の
温度を検知し、隔膜2を隔てて接覆る放射性廃液と塩溶
液の温度差を好適範囲に制御する温度制御装置8が配設
されている。
In the present invention, each concentration tank 1a11b11C1
The waste liquid chamber 3 and the salt solution chamber 1d are connected to the salt solution concentrator 7. A temperature control device 8 is provided to control the temperature difference of the salt solution within a suitable range.

以上のように構成された放射性廃液の濃縮装置では、放
射性廃液はポンプP1により廃液用配管5を通って濃縮
槽1a、ib、 1c、 1dの各廃液室3を順に通過
する間に、ポンプP2により塩溶液部t111器7から
塩溶液用配管6を通って送られてきた高淵疫の塩溶液、
例えば硫酸ナトリウム、リン酸水素カリウム等の塩溶液
と、隔膜2を隔てて接するために、各濃縮槽において敢
口1性廃液中の水分が塩濃度の高い塩溶液中へ移行する
こと(XJ:す、順次濃縮されて高温度放射性廃液とし
て/Iり出される。
In the radioactive waste liquid concentrating device configured as described above, while the radioactive waste liquid passes through the waste liquid piping 5 by the pump P1 and sequentially passes through each waste liquid chamber 3 of the concentration tanks 1a, ib, 1c, and 1d, the pump P2 The Takabuchi salt solution sent from the salt solution section t111 vessel 7 through the salt solution piping 6,
For example, in order to contact a salt solution such as sodium sulfate or potassium hydrogen phosphate with the diaphragm 2 in between, the water in the waste liquid in each concentration tank moves into a salt solution with a high salt concentration (XJ: It is then sequentially concentrated and discharged as a high-temperature radioactive waste liquid.

ここで、各i1!縮槽1a、11)、1C11〔1にお
ける水分の移行に着目すると、放射性廃液から1!2溶
液方向への水の流1t)Qは次式で与えられる。
Here, each i1! Focusing on the movement of moisture in the condensation tanks 1a, 11) and 1C11[1], the water flow 1t)Q from the radioactive waste liquid toward the 1!2 solution is given by the following equation.

すなわち Q=D (d C/dx) −D’ ・(1−C) (
d T、−’dX) * (D (C4−03) −D
’ ・<1−C2)X(T4 T:+))/ぶ 式中、Cは塩のモル分率、■は温度、℃は隔膜2の厚さ
、D、D’ は拡散定数であり、また添付数字ば2が隔
膜、3が廃液室、4が塩溶液室を示1、下しするへ 上式は、放射性廃液の濃縮が塩澗度差と温度差に大きく
影響されることを示している。
That is, Q=D (d C/dx) -D' ・(1-C) (
d T, -'dX) * (D (C4-03) -D
'・<1-C2) In addition, the attached number 2 indicates the diaphragm, 3 indicates the waste liquid chamber, and 4 indicates the salt solution chamber. ing.

しかして本発明においては、塩溶液室4に流入される塩
溶液の塩1膣度C4を塩溶液濃縮器7にJ:り十分高<
bC1放躬性廃液のjn)農度C3とのjH′m度差(
C4−C3)を大きく保つとともに、温度制御装置r’
l 8により放射性廃液の温度T3をjn)合液の>F
a Ia ’r 4 、J:り高くして、その温度差<
T4−T3)を十分負に保ち放射性廃液から塩溶液への
水の移行を促進している。なお、理論的には温度差1°
Cは20 kg/ c+に程度の加圧に相当する。
Therefore, in the present invention, the salt concentration C4 of the salt solution flowing into the salt solution chamber 4 is transferred to the salt solution concentrator 7 at a sufficiently high level.
bC1 jH'm degree difference between radioactive wastewater jn) and agricultural degree C3 (
C4-C3) is kept large, and the temperature control device r'
The temperature T3 of the radioactive waste liquid is determined by l8)>F of the combined liquid.
a Ia 'r 4 , J: Increase the temperature and make the temperature difference <
T4-T3) is kept sufficiently negative to promote water transfer from the radioactive waste liquid to the salt solution. In addition, theoretically, the temperature difference is 1°
C corresponds to a pressurization of about 20 kg/c+.

このように本発明装置においては、)品度差の制御を;
j[1えることにより、塩11i1度差のみによる濃縮
の限胃を越えてその処理効率を向−ヒさせることができ
る。
In this way, the device of the present invention can control quality differences;
By adding 1 to 1, the processing efficiency can be increased beyond the concentration limit due to only 1 degree difference in salt 11i.

なお、以上述べた実施例では放射性廃液を処理対象とし
て説明したが、本発明の濃縮装置は放射性廃液に限らず
あらゆる濃縮処理を必要とする希溶液に適用可能である
In the above-described embodiments, radioactive waste liquid is treated as a treatment target, but the concentrating device of the present invention is applicable not only to radioactive waste liquid but also to any dilute solution requiring concentration treatment.

[′R,明の効果] 以上)ホベたJこうに本発明の濃縮装置によれば、各種
溶液を効率良く濃縮処理することができる。
['R, Effect of Light] Above) According to the concentrating device of the present invention, various solutions can be efficiently concentrated.

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

図面は本発明の濃縮装置の一実施例を示J配?a系統図
である。 1a 、 1b 、lc 、1d −FJ縮槽2・・・
・・・・・・・・・隔 膜 3・・・・・・・・・・・・廃液室 4・・・・・・・・・・・・塩溶液室 7・・・・・・・・・・・・塩溶液濃縮器8・・・・・
・・・・・・・渇度制御装置代理人弁即十 須 山 ν
1−
The drawing shows an embodiment of the concentrating device of the present invention. a Systematic diagram. 1a, 1b, lc, 1d -FJ contraction tank 2...
・・・・・・・・・Diameter 3・・・・・・・・・Waste liquid chamber 4・・・・・・・・・Salt solution chamber 7・・・・・・・・・...Salt solution concentrator 8...
・・・・・・Thirst level control device agent valve Sokujusuyama ν
1-

Claims (2)

【特許請求の範囲】[Claims] (1)被処理液中の水をそれより高濃度の塩溶液中に透
過させる隔膜を備えた′mIi!装置において、前記隔
膜を隔てて供給される前記被処理液おJ:び塩溶液の温
度を検出し、その温度差をあらかじめ定められた範囲内
に制御する温度制御装置を配設したことを特徴とする濃
縮装置。
(1) 'mIi!' is equipped with a diaphragm that allows water in the liquid to be treated to permeate into a salt solution with a higher concentration. The apparatus is characterized by being provided with a temperature control device that detects the temperature of the liquid to be treated and the salt solution supplied across the diaphragm and controls the temperature difference within a predetermined range. A concentrator that uses
(2)被処理液は放射性廃液である特8′[請求の範囲
第1項記載の濃縮装置。
(2) The liquid to be treated is a radioactive waste liquid.
JP429884A 1984-01-13 1984-01-13 Concentration device Pending JPS60150883A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP429884A JPS60150883A (en) 1984-01-13 1984-01-13 Concentration device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP429884A JPS60150883A (en) 1984-01-13 1984-01-13 Concentration device

Publications (1)

Publication Number Publication Date
JPS60150883A true JPS60150883A (en) 1985-08-08

Family

ID=11580603

Family Applications (1)

Application Number Title Priority Date Filing Date
JP429884A Pending JPS60150883A (en) 1984-01-13 1984-01-13 Concentration device

Country Status (1)

Country Link
JP (1) JPS60150883A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008152749A1 (en) * 2007-06-13 2008-12-18 Water Re-Use Promotion Center Water desalination system and water desalination method
JP2012236124A (en) * 2011-05-10 2012-12-06 Kobe Univ Method and apparatus for concentrating water to be treated
JP2013509295A (en) * 2009-10-28 2013-03-14 オアシス ウォーター,インコーポレーテッド Forward osmosis separation method
JP2016150308A (en) * 2015-02-17 2016-08-22 株式会社ササクラ Concentration apparatus and concentration method for oral or external application

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008152749A1 (en) * 2007-06-13 2008-12-18 Water Re-Use Promotion Center Water desalination system and water desalination method
JP2013509295A (en) * 2009-10-28 2013-03-14 オアシス ウォーター,インコーポレーテッド Forward osmosis separation method
JP2012236124A (en) * 2011-05-10 2012-12-06 Kobe Univ Method and apparatus for concentrating water to be treated
JP2016150308A (en) * 2015-02-17 2016-08-22 株式会社ササクラ Concentration apparatus and concentration method for oral or external application

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