JPH02171693A - Treatment of washing waste water of cement kneader - Google Patents
Treatment of washing waste water of cement kneaderInfo
- Publication number
- JPH02171693A JPH02171693A JP32730688A JP32730688A JPH02171693A JP H02171693 A JPH02171693 A JP H02171693A JP 32730688 A JP32730688 A JP 32730688A JP 32730688 A JP32730688 A JP 32730688A JP H02171693 A JPH02171693 A JP H02171693A
- Authority
- JP
- Japan
- Prior art keywords
- cement
- sludge
- washing
- kneader
- waste liquid
- 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
Links
- 239000004568 cement Substances 0.000 title claims abstract description 45
- 239000002351 wastewater Substances 0.000 title claims abstract description 29
- 238000005406 washing Methods 0.000 title claims abstract description 25
- 239000010802 sludge Substances 0.000 claims abstract description 34
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 20
- 239000006228 supernatant Substances 0.000 claims abstract description 14
- 238000004898 kneading Methods 0.000 claims abstract description 12
- 239000002901 radioactive waste Substances 0.000 claims abstract description 7
- 238000000034 method Methods 0.000 claims description 26
- 239000007788 liquid Substances 0.000 claims description 18
- 239000002699 waste material Substances 0.000 claims description 18
- 238000004140 cleaning Methods 0.000 claims description 14
- 239000000203 mixture Substances 0.000 claims description 6
- 238000007711 solidification Methods 0.000 claims description 6
- 230000008023 solidification Effects 0.000 claims description 6
- 239000000126 substance Substances 0.000 claims description 3
- 239000002002 slurry Substances 0.000 abstract description 5
- 230000003292 diminished effect Effects 0.000 abstract 1
- 238000003756 stirring Methods 0.000 description 7
- 239000002245 particle Substances 0.000 description 3
- KGBXLFKZBHKPEV-UHFFFAOYSA-N boric acid Chemical compound OB(O)O KGBXLFKZBHKPEV-UHFFFAOYSA-N 0.000 description 2
- 239000004327 boric acid Substances 0.000 description 2
- 229910001385 heavy metal Inorganic materials 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 238000004065 wastewater treatment Methods 0.000 description 2
- 240000005979 Hordeum vulgare Species 0.000 description 1
- 235000007340 Hordeum vulgare Nutrition 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000006703 hydration reaction Methods 0.000 description 1
- 210000003127 knee Anatomy 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- VLCLHFYFMCKBRP-UHFFFAOYSA-N tricalcium;diborate Chemical compound [Ca+2].[Ca+2].[Ca+2].[O-]B([O-])[O-].[O-]B([O-])[O-] VLCLHFYFMCKBRP-UHFFFAOYSA-N 0.000 description 1
- 238000009489 vacuum treatment Methods 0.000 description 1
- 229910052902 vermiculite Inorganic materials 0.000 description 1
- 235000019354 vermiculite Nutrition 0.000 description 1
- 239000010455 vermiculite Substances 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
Landscapes
- Preparation Of Clay, And Manufacture Of Mixtures Containing Clay Or Cement (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、放射性廃棄物や重金属のような有害物質を含
有する廃液を、セメント固化により処理する場合の、セ
メント混練機の洗浄廃水の処理方法に関する。Detailed Description of the Invention [Field of Industrial Application] The present invention is directed to the treatment of cleaning wastewater from a cement kneading machine when wastewater containing harmful substances such as radioactive waste and heavy metals is treated by cement solidification. Regarding the method.
(従来の技術)
上記のような廃液のセメント固化処理法には、インドラ
ム方式、アウトドラム方式および真空方式がある。 イ
ンドラム方式の処理法は、ドラム缶の中で廃液とセメン
トとを混練してそのまま固化する方法でおり、アウトド
ラム方式は、ある程度まとまった量の廃液とセメントを
混練機で均質に混練し、混練物をドラム缶に注入して固
化させる方法である。 真空方式の処理法は、ドラム缶
にセメントとバーミキュライトを詰め、その中へ廃液を
真空下で注入し、全体に浸透させて固化させる方法であ
る。(Prior Art) The cement solidification treatment method for waste liquid as described above includes an in-drum method, an out-drum method, and a vacuum method. The in-drum treatment method is a method in which waste liquid and cement are kneaded in a drum and then solidified as is.In the out-drum method, a certain amount of waste liquid and cement are homogeneously kneaded in a kneader, and the mixture is kneaded. This is a method in which the substance is poured into a drum and allowed to solidify. The vacuum treatment method involves filling a drum with cement and vermiculite, injecting the waste liquid into the drum under vacuum, allowing it to permeate throughout and solidify.
しかし、真空方式の場合はできた同化体が十分に均質で
はなく、またインドラム方式は、セメント粉末の飛散や
、混練俊に撹拌翼を洗浄しなければならないという問題
があり、アウトドラム方式の処理法が主流になっている
。However, in the case of the vacuum method, the resulting assimilate is not sufficiently homogeneous, and the in-drum method has problems such as scattering of cement powder and the need to clean the stirring blades before mixing. treatment methods have become mainstream.
アウトドラム方式の処理法においても、混練機に残った
スラッジは洗い流さなければならず、それにより生じた
洗浄廃水の処理が問題となる。Even in the out-drum treatment method, the sludge remaining in the kneader must be washed away, and the treatment of the resulting washing wastewater poses a problem.
現行の処理法では、洗浄廃水をいったんタンクに送って
静置し、分離した上澄水は洗浄水として再利用し、下に
たまったスラッジは真空ポンプでタンクから引き汰いて
ドラム缶に排出し、そこで自然に凝固させる。In the current treatment method, cleaning wastewater is once sent to a tank and left to stand still, the separated supernatant water is reused as cleaning water, and the sludge that has accumulated at the bottom is drawn out from the tank with a vacuum pump and discharged into a drum, where it is collected. Allow to solidify naturally.
このようにして1qられるスラッジの固化体は、均質な
ものではなく、その圧縮強度も数Kg/ ci〜数拾K
FI/cmと、放射性廃棄物の同化体に要求される海洋
投棄基準の圧縮強度’l50Kl/critにはほど遠
い。The solidified sludge produced in this way is not homogeneous, and its compressive strength ranges from several kg/ci to several tens of kilograms.
FI/cm, which is far from the compressive strength of 50Kl/crit, which is the ocean dumping standard required for assimilated radioactive waste.
本発明の目的は、廃液のセメント固化処理において、セ
メント混練機の洗浄廃水の処理方法を改良し、均質で十
分な強度をもった固化体を与えることにある。An object of the present invention is to improve a method for treating waste water from a cement kneader in cement solidification treatment of waste liquid, and to provide a solidified product that is homogeneous and has sufficient strength.
(課題を解決するための手段〕
本発明のセメント混練機の洗浄廃水処理方法は、廃液と
セメントとを混練機で混練し、その混合物をドラム缶の
ような容器に注入して固化させるアウトドラム方式のセ
メント固化処理を行なうに際して、混練機のスラッジを
洗浄することにより生じた洗浄廃水をスラッジが凝固し
ないように保存し、保存した洗浄廃水中のスラッジを混
練機に移送してセメントと混練することからなる。(Means for Solving the Problems) The cement kneading machine cleaning wastewater treatment method of the present invention is an out-drum method in which waste liquid and cement are kneaded in a kneader, and the mixture is poured into a container such as a drum and solidified. When carrying out the cement solidification process, the washing wastewater generated by washing the sludge in the kneading machine is stored so that the sludge does not solidify, and the sludge in the stored washing wastewater is transferred to the kneading machine and kneaded with cement. Consisting of
セメントとの混練を行なうまで凝固しないようにスラッ
ジを保存するには、たとえば洗浄廃水をタンクに受は撹
拌を続けていればよい。In order to preserve the sludge so that it does not solidify until it is mixed with cement, it is sufficient, for example, to keep stirring the washing waste water in a tank.
この撹拌は、スラッジの沈降と凝固を妨げる程度に弱く
行なえば足りるから、洗浄廃水タンクには上澄みが生じ
る。 この上澄みは、従来と同様に、洗浄液として再利
用することができ、これは推奨される態様である。This stirring only needs to be done weakly enough to prevent settling and coagulation of the sludge, so that a supernatant remains in the washing wastewater tank. This supernatant can be conventionally reused as a cleaning solution, which is the recommended practice.
本発明の処理方法を実施する装置は、代表的には図に示
すような構成となる。An apparatus that implements the processing method of the present invention typically has a configuration as shown in the figure.
廃液タンク(4)からの廃液とセメントホッパー(5)
からのセメントとは、混練機(1)において混合され、
混合物はドラム缶(9)へ注入されてそこで固化する。Waste liquid from waste tank (4) and cement hopper (5)
The cement from is mixed in a mixer (1),
The mixture is poured into a drum (9) where it solidifies.
混練作業が終ると、上澄水タンク(3)の中の水を混
練機に送って、混練機内を洗浄する。 発生した洗浄廃
水は、洗浄廃水タンク(2)に送り、そこでは底部近く
を静かに撹拌する。When the kneading work is finished, the water in the supernatant water tank (3) is sent to the kneader to clean the inside of the kneader. The generated wash wastewater is sent to the wash wastewater tank (2) where it is gently agitated near the bottom.
洗浄廃水に含まれているのは水和反応が進行しつつある
セメント粒子であって、これはタンク底部に向って沈降
し、静置しておくと水和物結晶の成長とからみ合いによ
りそこで凝固してしまうが、撹拌によりそれが妨げられ
、各粒子が独立した状態で水和が進む。The cleaning wastewater contains cement particles undergoing a hydration reaction, which settle toward the bottom of the tank and, if left standing, become entangled with the growth of hydrate crystals. The particles solidify, but stirring prevents this and allows each particle to hydrate independently.
洗浄廃水タンクの上澄みは上澄水タンク(3)に送り、
上記した混練機(1)の洗浄に使用するほか、洗浄廃水
タンク(2)の洗浄や、混練機から洗浄廃水タンクへの
流路(6)の洗浄に使用する。The supernatant from the washing wastewater tank is sent to the supernatant water tank (3).
In addition to being used to clean the kneading machine (1) described above, it is also used to clean the cleaning wastewater tank (2) and the flow path (6) from the kneading machine to the cleaning wastewater tank.
洗浄廃水タンク(2)の底部に保存されたスラッジは、
セメントとの混練の時期が来たとき、スラリー移送ポン
プ(7)により混練機(1)に送られ、前記したように
セメントと混練される。The sludge stored at the bottom of the washing wastewater tank (2) is
When the time for mixing with cement comes, the slurry is sent to the kneader (1) by the slurry transfer pump (7), and is mixed with cement as described above.
必要に応じ、図示した例では洗浄タンクの上澄みの流路
や上澄水タンク(3)に、符号DWで示したように脱塩
水を加える。If necessary, in the illustrated example, demineralized water is added to the supernatant channel of the washing tank and the supernatant water tank (3) as indicated by the symbol DW.
このようにして、セメント混練機を洗浄したときに発生
する洗浄廃水中のスラッジを混練機に移送して、セメン
トと混練するため、スラッジの固化体は均質で、その圧
縮強度も放射性廃棄物の固化体に要求される海洋投棄基
準をみたすレベルに達する。 また、上澄水は、繰り返
し使用された後、セメント混練時の練り水として使用で
きるため、洗浄に伴い発生する固化体ドラム缶の本数も
少ない。In this way, the sludge in the washing wastewater generated when cleaning the cement mixer is transferred to the mixer and mixed with cement, so the solidified sludge is homogeneous and its compressive strength is also that of radioactive waste. It reaches a level that meets the ocean dumping standards required for solidified solids. Moreover, since the supernatant water can be used as mixing water during cement kneading after being used repeatedly, the number of solidified drums generated during cleaning is also small.
〔参考例1〕
原子力発電所から排出されるホウ酸含有廃液に似せた組
成の廃液を用意し、これをセメント固化処理したときに
混練機に付着したスラッジを採取した。 スラッジの組
成は、重量圧でホウ酸カルシウム:セメント:水ニー2
:1:3であった。[Reference Example 1] A waste liquid having a composition similar to a boric acid-containing waste liquid discharged from a nuclear power plant was prepared, and when this was subjected to cement solidification treatment, the sludge that adhered to a kneader was collected. The composition of the sludge is: Calcium borate: Cement: Water knee 2
:1:3.
2個のビーカーにそれぞれ水100gを入れ、前記スラ
ッジ609ずつを加えて撹拌した。 ひとつはそのまま
撹拌を続け、いまひとつは撹拌をやめて静置した。100 g of water was placed in each of two beakers, and the sludge 609 was added thereto and stirred. One was kept stirring, and the other was left to stand without stirring.
撹拌をつづけたサンプルは長時間にわたりスラリーのま
まで変化がなかったが、静置した方はスラッジが凝固し
た。 凝固体の圧縮強度は、2週間後に30に’J/c
rA、3力月後でも50に’l/cMにしかならなかっ
た。The sample that was continuously stirred remained a slurry for a long time without any change, but the sludge that was left to stand still solidified. The compressive strength of the solidified body increased to 30'J/c after 2 weeks.
rA, even after 3 months, it only reached 50'l/cM.
〔参考例2〕
Znおよびpbを含んでいる焼却灰をセメント同化処理
したときに混練機に付着したスラッジを採取し、参考例
1と同じ実験をした。[Reference Example 2] The same experiment as in Reference Example 1 was conducted by collecting the sludge that adhered to the kneader when incineration ash containing Zn and PB was assimilated into cement.
結果は参考例1と同様で、撹拌を続けたものは変化がな
かったが、静置したものはスラッジが凝固した。 凝固
体の圧縮強度は、2週間後が10Kg / ctA、3
力月1麦でもわずか20Kg/crAであった。The results were the same as those in Reference Example 1; there was no change when stirring was continued, but the sludge solidified when left standing. The compressive strength of the solidified body is 10Kg/ctA after 2 weeks, 3
Even with 1 barley of Chikitsuki, it was only 20Kg/crA.
〔参考例3〕
参考例1で使用したホウ酸含有廃液をセメント同化処理
したのちに、混練機に付着したスラッジを水で洗い流し
、その洗浄廃水中のスラッジを下記の割合でセメントと
混練し固化した。[Reference Example 3] After the boric acid-containing waste liquid used in Reference Example 1 was assimilated with cement, the sludge adhering to the kneader was washed away with water, and the sludge in the washed waste water was kneaded with cement at the following ratio and solidified. did.
結果は、つぎのとおりである。The results are as follows.
スラッジ セメント 圧縮1度(Kff/cm)(
Kg) (K’J ) 二」[韮 月)B
簿2.5 1.5 115 307
3.0 1.4 100 2002
.5 1.7 110 265〔実
施例〕
図に示す構成の処理装置を使用し、放射性廃棄物を含む
廃液をセメント固化して、混練機の洗浄廃水を前記のよ
うにして保存したのち、スラッジを混線工程に戻してセ
メントと混合した。Sludge Cement Compression 1 degree (Kff/cm) (
Kg) (K'J) 2" [韮月)B
Book 2.5 1.5 115 307
3.0 1.4 100 2002
.. 5 1.7 110 265 [Example] Using a treatment device with the configuration shown in the figure, the waste liquid containing radioactive waste was solidified with cement, the waste water from the kneading machine was stored as described above, and then the sludge was It was returned to the mixing process and mixed with cement.
混合比率は、スラッジ16ONy:セメント230Kg
である。The mixing ratio is 16ONy of sludge: 230Kg of cement.
It is.
得られたセメント同化体の圧縮強度は、1力月後には1
50に’J/crAを超えていた。The compressive strength of the obtained cement assimilate was 1 after 1 month.
At 50, it exceeded 'J/crA.
(発明の効果〕
本発明のセメント混練機の洗浄廃水処理方法によれば、
洗浄廃水中のスラッジはセメントと固化されるので、洗
浄スラッジだけの、不均質で強度の低い同化体ができる
ことはない。 得られる同化体は、いずれも均質かつ高
強度で、長期の保存に耐える安定な同化体である。 こ
のようにして、洗浄スラッジの処理に伴う問題点は解消
した。(Effects of the Invention) According to the cement kneader cleaning wastewater treatment method of the present invention,
Since the sludge in the washing wastewater is solidified with cement, a heterogeneous and weak assimilated product consisting of only washing sludge is not formed. The resulting assimilates are homogeneous, have high strength, and are stable enough to withstand long-term storage. In this way, the problems associated with the treatment of cleaning sludge were solved.
本発明の処理方法は、放射性廃液の処理に適用したとき
、とくに意義が大きいが、そのほか重金属を含有する廃
棄物の処理などにも有用である。The treatment method of the present invention is particularly significant when applied to the treatment of radioactive waste liquid, but is also useful for the treatment of waste containing heavy metals.
図面は、本発明の処理方法の実施に使用する装置のフロ
ーシートでおる。
1・・・混練機
2・・・洗浄廃水タンク
3・・・上澄水タンク
4・・・廃液タンク
5・・・セメントホッパー
7・・・スラリー移送ポンプThe drawing is a flow sheet of the apparatus used to carry out the treatment method of the present invention. 1... Kneading machine 2... Washing waste water tank 3... Supernatant water tank 4... Waste liquid tank 5... Cement hopper 7... Slurry transfer pump
Claims (4)
を容器に注入して固化させるセメント固化処理を行なう
に際して、混練機のスラッジを洗浄することにより生じ
た洗浄廃水をスラッジが凝固しないように保存し、保存
した洗浄廃水中のスラッジを混練機に移送してセメント
と混練することからなるセメント混練機の洗浄廃水処理
方法。(1) When carrying out the cement solidification process, in which waste liquid and cement are kneaded in a kneader and the mixture is poured into a container and solidified, the washing wastewater generated by washing the sludge of the kneader is made to prevent the sludge from solidifying. A method for treating cleaning wastewater from a cement mixer, which comprises storing the sludge in the stored cleaning wastewater in a mixer and mixing it with cement.
り返し利用した後、セメント混練時の練り水として使用
する請求項1の処理方法。(2) The treatment method according to claim 1, wherein the supernatant water of the washing wastewater is reused for washing the kneading machine, and after being repeatedly used, it is used as mixing water during cement mixing.
方法。(4) The treatment method according to claim 1, wherein the waste liquid is a waste liquid containing harmful substances.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63327306A JPH077101B2 (en) | 1988-12-23 | 1988-12-23 | Cleaning wastewater treatment method for cement kneader |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63327306A JPH077101B2 (en) | 1988-12-23 | 1988-12-23 | Cleaning wastewater treatment method for cement kneader |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH02171693A true JPH02171693A (en) | 1990-07-03 |
JPH077101B2 JPH077101B2 (en) | 1995-01-30 |
Family
ID=18197656
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63327306A Expired - Lifetime JPH077101B2 (en) | 1988-12-23 | 1988-12-23 | Cleaning wastewater treatment method for cement kneader |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH077101B2 (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002131481A (en) * | 2000-10-26 | 2002-05-09 | Toshiba Corp | Method of solidification of radioactive waste |
JP2004008937A (en) * | 2002-06-07 | 2004-01-15 | Sumitomo Forestry Co Ltd | Method and bag for purifying cement washing water |
JP2006123484A (en) * | 2004-10-26 | 2006-05-18 | Takayuki Nomura | Method for utilizing washing wastewater generated from ready-mixed concrete facility |
JP2009023291A (en) * | 2007-07-23 | 2009-02-05 | Aizawa Koatsu Concrete Kk | Method and drum for retrieving rinse water of truck agitator drum |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5190000U (en) * | 1975-01-16 | 1976-07-19 | ||
JPS51115520A (en) * | 1975-04-04 | 1976-10-12 | Sanko Co Inc | Process for reusing the water after cleaning a mixer automobile etc* as the water for mixing raw concrete grout |
-
1988
- 1988-12-23 JP JP63327306A patent/JPH077101B2/en not_active Expired - Lifetime
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5190000U (en) * | 1975-01-16 | 1976-07-19 | ||
JPS51115520A (en) * | 1975-04-04 | 1976-10-12 | Sanko Co Inc | Process for reusing the water after cleaning a mixer automobile etc* as the water for mixing raw concrete grout |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002131481A (en) * | 2000-10-26 | 2002-05-09 | Toshiba Corp | Method of solidification of radioactive waste |
JP2004008937A (en) * | 2002-06-07 | 2004-01-15 | Sumitomo Forestry Co Ltd | Method and bag for purifying cement washing water |
JP2006123484A (en) * | 2004-10-26 | 2006-05-18 | Takayuki Nomura | Method for utilizing washing wastewater generated from ready-mixed concrete facility |
JP2009023291A (en) * | 2007-07-23 | 2009-02-05 | Aizawa Koatsu Concrete Kk | Method and drum for retrieving rinse water of truck agitator drum |
Also Published As
Publication number | Publication date |
---|---|
JPH077101B2 (en) | 1995-01-30 |
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