EP3012839B1 - Zementierverfahren und zementiervorrichtung für borsäurehaltigen flüssigabfall - Google Patents

Zementierverfahren und zementiervorrichtung für borsäurehaltigen flüssigabfall Download PDF

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Publication number
EP3012839B1
EP3012839B1 EP14814441.3A EP14814441A EP3012839B1 EP 3012839 B1 EP3012839 B1 EP 3012839B1 EP 14814441 A EP14814441 A EP 14814441A EP 3012839 B1 EP3012839 B1 EP 3012839B1
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Prior art keywords
quartz sand
cement
zeolite
kneaded product
kneading
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French (fr)
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EP3012839A4 (de
EP3012839A1 (de
Inventor
Hirofumi Okabe
Yuichi Shoji
Yoshiko HARUGUCHI
Tatsuaki Sato
Ryo Yamamoto
Keijiro YASUMURA
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Toshiba Corp
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Toshiba Corp
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    • G—PHYSICS
    • G21—NUCLEAR PHYSICS; NUCLEAR ENGINEERING
    • G21F—PROTECTION AGAINST X-RADIATION, GAMMA RADIATION, CORPUSCULAR RADIATION OR PARTICLE BOMBARDMENT; TREATING RADIOACTIVELY CONTAMINATED MATERIAL; DECONTAMINATION ARRANGEMENTS THEREFOR
    • G21F9/00—Treating radioactively contaminated material; Decontamination arrangements therefor
    • G21F9/04—Treating liquids
    • G21F9/06—Processing
    • G21F9/16—Processing by fixation in stable solid media
    • G21F9/162—Processing by fixation in stable solid media in an inorganic matrix, e.g. clays, zeolites
    • G21F9/165—Cement or cement-like matrix
    • G—PHYSICS
    • G21—NUCLEAR PHYSICS; NUCLEAR ENGINEERING
    • G21F—PROTECTION AGAINST X-RADIATION, GAMMA RADIATION, CORPUSCULAR RADIATION OR PARTICLE BOMBARDMENT; TREATING RADIOACTIVELY CONTAMINATED MATERIAL; DECONTAMINATION ARRANGEMENTS THEREFOR
    • G21F9/00—Treating radioactively contaminated material; Decontamination arrangements therefor
    • G21F9/04—Treating liquids
    • G21F9/06—Processing
    • G21F9/12—Processing by absorption; by adsorption; by ion-exchange
    • G—PHYSICS
    • G21—NUCLEAR PHYSICS; NUCLEAR ENGINEERING
    • G21F—PROTECTION AGAINST X-RADIATION, GAMMA RADIATION, CORPUSCULAR RADIATION OR PARTICLE BOMBARDMENT; TREATING RADIOACTIVELY CONTAMINATED MATERIAL; DECONTAMINATION ARRANGEMENTS THEREFOR
    • G21F9/00—Treating radioactively contaminated material; Decontamination arrangements therefor
    • G21F9/28—Treating solids
    • G21F9/34—Disposal of solid waste
    • G21F9/36—Disposal of solid waste by packaging; by baling

Definitions

  • Embodiments described herein relate generally to a cement-solidification method and a cement-solidification apparatus for a boric acid-containing waste liquid.
  • a large amount of boric acid-containing waste liquid which has been used for power adjustment of a nuclear reactor and the like is generated. Further, in a boiling water type nuclear power plant, a boric acid solution to be urgently injected into the nuclear reactor is stored and a boric acid-containing waste liquid is sometimes generated.
  • the boric acid-containing waste liquid is subjected to a neutralization treatment using a sodium hydroxide, a lithium hydroxide or the like, and then solidified with cement or asphalt.
  • a boric acid interferes with a setting reaction of cement, resulting in substantial hardening retardation or decrease in strength of a solidified body. Therefore, from the viewpoint of cement-solidifying the boric acid-containing waste liquid while increasing the volume reduction, various kinds of suggestion such as adding a calcium hydroxide or the like as a pretreatment agent for solidification and so on.
  • a method of solidifying the radioactive boric acid-containing waste liquid there is suggested a method of making the boric acid-containing waste liquid into a dry powder, then mixing an alkaline silicate binding agent aqueous solution, and further mixing an auxiliary agent composed of an acidic hardening agent, a hardening retarder, quartz sand or the like for solidification (refer to, for example, Patent Refrence 2).
  • This method is for performing solidification using water glass as a main component of a solidifying material and not cement as the main component.
  • the conventional cement-solidification method for a boric acid-containing waste liquid has a problem such as the need for higher volume reduction.
  • the present invention has been made to solve the above problem and its object is to provide a cement-solidification method and a cement-solidification apparatus for a boric acid-containing waste liquid, capable of making the boric acid-containing waste liquid into a stable cement-solidified product with high volume reduction.
  • An aspect of the cement-solidification method as set out in claim 1 for a boric acid-containing waste liquid according to the present invention is a method of cement-solidifying a radioactive boric acid-containing waste liquid, including: a volume reduction step of adding a sodium hydroxide to the boric acid-containing waste liquid and reducing a volume thereof to prepare a matter to be solidified; a first kneading step of kneading the matter to be solidified, a kneading water, and a hydraulic solidifying material to prepare a first kneaded product; and a second kneading step of kneading quartz sand and the first kneaded product to prepare a second kneaded product, wherein a weight ratio of the quartz sand to the hydraulic solidifying material (a weight of the quartz sand/a weight of the hydraulic solidifying material) is 1.5 to 3.0.
  • An aspect of the cement-solidification apparatus for a boric acid-containing waste liquid according to the present invention is an apparatus as set out in claim 9 for cement-solidifying a radioactive boric acid-containing waste liquid, including: a kneader; a to-be-solidified matter supply device that adds a sodium hydroxide to the boric acid-containing waste liquid and reduces a volume thereof to prepare a matter to be solidified, and supplies the matter to be solidified to the kneader; a kneading water supply device that supplies a kneading water to the kneader; a hydraulic solidifying material supply device that supplies a hydraulic solidifying material to the kneader to prepare a first kneaded product; and a quartz sand supply device that supplies quartz sand to the kneader to prepare a second kneaded product, wherein a weight ratio of the quartz sand to the hydraulic solidifying material (a weight of the quartz s
  • Fig. 1 is a flowchart illustrating steps of a cement-solidification method for a boric acid-containing waste liquid according to an embodiment of the present invention.
  • Fig. 2 is a schematic block diagram illustrating a cement-solidification apparatus for a boric acid-containing waste liquid according to an embodiment of the present invention.
  • an embodiment of the present invention will be described referring to Fig. 1 and Fig. 2 .
  • the cement-solidification method illustrated in Fig. 1 has: a step (S101) of adding a sodium hydroxide 2 to a boric acid-containing waste liquid 1; a volume reduction step (S102) of drying the boric acid-containing waste liquid 1 with the sodium hydroxide 2 added thereto to prepare a dry powder 3; a first kneading step (S103) of kneading the dry powder 3, a kneading water 4, and a hydraulic solidifying material 5 to prepare a first kneaded product; and a second kneading step (S104) of kneading the first kneaded product and quartz sand 6 to prepare a second kneaded product.
  • a cement-solidification apparatus 10 illustrated in Fig. 2 includes a kneader 11, a to-be-solidified matter supply device 12 that supplies a matter to be solidified to the kneader 11, and a kneading water supply device 13 that supplies the kneading water 4 to the kneader 11.
  • the cement-solidification apparatus 10 further includes a hydraulic solidifying material supply device 14 that supplies the hydraulic solidifying material 5 to the kneader 11, and a quartz sand supply device 15 that supplies the quartz sand 6 to the kneader 11.
  • the to-be-solidified matter supply device 12 includes a volume reduction device (not illustrated) for reducing the volume of the boric acid-containing waste liquid 1 into the matter to be solidified.
  • the matter to be solidified is the dry powder 3 obtained by drying the boric acid-containing waste liquid 1 or a concentrated waste liquid obtained by concentrating the boric acid-containing waste liquid 1.
  • the volume reduction device for example, heats and dries the boric acid-containing waste liquid 1 into the dry powder 3 or reduces its volume into the concentrated waste liquid.
  • the quartz sand supply device 15 is provided with a quartz sand supply rate adjusting device 16 that adjusts the quartz sand supply rate of the quartz sand supply device 15 to a predetermined rate.
  • a numeral 17 denotes a solidification container that houses therein and solidifies the second kneaded product kneaded by the kneader 11.
  • the object of cement solidification in this embodiment is a radioactive waste liquid containing boric acid (boric acid-containing waste liquid 1).
  • the first step in this embodiment is a step of adding the sodium hydroxide 2 to the boric acid-containing waste liquid 1.
  • the sodium hydroxide 2 reacts with boron in the boric acid-containing waste liquid 1 to generate a sodium borate.
  • the amount of the sodium hydroxide 2 is prepared to such an amount that a sodium/boron mole ratio (Na/B mole ratio) is preferably 0.2 or more, more preferably 0.2 to 0.5, and particularly preferably 0.2 to 0.3. This increases the solubility of the sodium borate to water, thereby making it possible to improve the cleaning property for the piping, dryer and so on.
  • a sodium/boron mole ratio Na/B mole ratio
  • the second step in this embodiment is a step of reducing the volume of the boric acid-containing waste liquid 1 so as to solidify a large amount of the boric acid-containing waste liquid 1 with high volume reduction.
  • the boric acid-containing waste liquid 1 is supplied to the dryer where a dry treatment is performed to obtain the dry powder 3.
  • the temperature of the boric acid-containing waste liquid 1 after addition of the sodium hydroxide 2 thereto is adjusted to the deposition temperature of the sodium borate, preferably 60°C or higher, and more preferably about 80°C to 90°C or higher, and then the boric acid-containing waste liquid 1 is supplied to the dryer.
  • the boric acid-containing waste liquid 1 is heated preferably to about 80°C or higher, more preferably about 120 to 180°C, and particularly preferably about 160°C for dry treatment.
  • the dryer is not particularly limited, but a centrifugal-film dryer is preferably used. This is because the centrifugal-film dryer has such features that it is high in thermal efficiency and therefore enables downsizing of the apparatus, a powder transfer amount to a gas phase part is small during the dry treatment, the particle size of sodium borate powder to be obtained is stable and so on.
  • the concentrated waste liquid can be obtained.
  • the boric acid-containing waste liquid 1 is concentrated by heating and prepared so that the water content in the boric acid-containing waste liquid is about 30% or less by weight ratio.
  • an additive is added to the boric acid-containing waste liquid 1 to make the sodium borate to settle down. The settled sodium borate is separated to obtain the concentrated waste liquid.
  • the same effect can be obtained by performing any of the treatments.
  • the dry powder 3 and the concentrated waste liquid after volume reduction may be cooled down to about room temperature (normal temperature: 25°C) or may be subjected to the next third step without cooling.
  • the third step in this embodiment is a step of kneading the dry powder 3, the kneading water 4, and the hydraulic solidifying material 5 using the kneader to prepare the first kneaded product.
  • the sodium borate contained in the dry powder 3 has properties of absorbing water into a salt hydrate. Accordingly, if the dry powder 3 is kneaded into a substance made by kneading cement and the kneading water as in a normal cement mixing procedure, the viscosity of the cement-kneaded product extremely increases due to the salt hydrate and may cause kneading failure and false set. For this reason, at the third step, the dry powder 3 and the kneading water 4 are mixed and stirred in advance, and during the stirring, the salt hydrate is generated in advance. Thereafter, the hydraulic solidifying material 5 such as cement is preferably kneaded. More specifically, it is preferable to knead the dry powder 3 and the kneading water 4, for example, for 10 minutes or longer in consideration of the generation time of the salt hydrate.
  • portland cement is preferably used.
  • the hydraulic solidifying material 5 a mixture of portland cement and blast-furnace slag, a mixture of portland cement and fly ash, or the like may be used.
  • the fourth step in this embodiment is a step of kneading the first kneaded product obtained at the third step and the quartz sand 6 to prepare the second kneaded product.
  • the boric acid contained in the boric acid-containing waste liquid 1 has an operation of greatly delaying the hardening of cement and an operation of decreasing the strength of a cement-solidified product 8.
  • Adding a calcium hydroxide so as to prevent the operations causes a problem of calcium borate precipitating in the piping and the dryer and adhering thereto.
  • kneading the quartz sand 6 into the first kneaded product at the fourth step makes it possible to suppress delay of hardening of cement without using calcium and improve the strength of the cement-solidified product 8 to be finally obtained.
  • the quartz sand 6 is kneaded in such an amount that the weight ratio expressed by the quartz sand 6/the hydraulic solidifying material 5 (hereinafter, called S/C) falls within a range of 1.5 to 3.0.
  • the S/C is preferably 1.7 to 2.6, and particularly preferably about 2.3. Kneading the quartz sand 6 in an amount with which the S/C becomes 1.5 to 3.0 makes it possible to improve the strength of the cement-solidified product 8 and obtain the cement-solidified product 8 excellent in solidification characteristics.
  • the particle size of the quartz sand 6 is preferably about 0.026 to 1.18 mm in median diameter.
  • the quartz sand 6 when kneading the quartz sand 6 at the fourth step, it is preferable to replace a part of the full weight of the quartz sand 6 to be added with zeolite 7.
  • the zeolite 7 is a solid acid, and is high in performance of adsorbing radionuclides, and therefore adding the zeolite 7 at a predetermined ratio can drastically improve the radioactivity confining property (distribution coefficient of the radionuclides) of the cement-solidified product 8. Further, the zeolite 7 adsorbs a boron ion and a boron compound that inhibit the progress of cement solidification and therefore can improve the strength of the cement-solidified product 8.
  • the boron ion and the boron compound become more likely to elute under a higher alkaline condition, but the addition of the zeolite 7 in a predetermined amount causes the added boron to adsorb alkali, thereby suppressing an increase in pH of the second kneaded product and the cement-solidified product 8. This can suppress elution of the boron ion, so that the cement-solidified product 8 excellent in solidification characteristics can be obtained.
  • the mixed amount of the zeolite 7 is preferably prepared to such an amount that the weight ratio of the zeolite 7 to the total of the zeolite 7 and the quartz sand 6 (the weight of zeolite 7/the total weight of the zeolite 7 and the quartz sand 6) is 0.05 to 0.40, more preferably prepared to 0.05 to 0.25, and particularly preferably prepared to 0.10 to 0.20.
  • Mixing the zeolite 7 in the above-described amount makes it possible to improve the strength and the radioactivity confining property of the cement-solidified product 8.
  • the value of S in the above S/C is the value of the total weight of the quartz sand 6 and the zeolite 7 in this case.
  • the particle size of the zeolite 7 is preferably about 770 ⁇ m in median diameter.
  • the ion exchange capacity of the zeolite 7 is preferably about 10 to 200 (meq)/100 (g).
  • the method of mixing the quartz sand 6 and the zeolite 7 is not particularly limited, and the quartz sand 6 and the zeolite 7 may be mixed together in advance and the mixture may be mixed into the first kneaded product, or the quartz sand 6 and the zeolite 7 may be separately mixed into the first kneaded product. In the case where the quartz sand 6 and the zeolite 7 are separately mixed, the quartz sand 6 and the zeolite 7 may be mixed in any order or at the same time.
  • the second kneaded product thus obtained has excellent viscosity characteristics. Therefore, an out-drum mixing method can be used to house the second kneaded product in a solidification container 17 such as a drum from the kneader and form it into the cement-solidified product 8 excellent in solidification characteristics.
  • the cement-solidification method in this embodiment may be performed by an in-drum mixing method. More specifically, the kneading of all of the dry powder 3, the kneading water 4, the hydraulic solidifying material 5, the quartz sand 6 and the zeolite 7 may be performed in a radioactive waste solidification container, and the second kneaded product to be obtained may be solidified as it is in this radioactive waste solidification container. In this case, it is possible to further reduce the facility cost and the operating cost.
  • the cement-solidification method in this embodiment is excellent in operability because the second kneaded product has excellent viscosity characteristics. Further, the method does not use calcium and therefore causes no problem of adherence of a waste liquid component to the piping and the like. Further, according to the cement-solidification method in this embodiment, mixing the quartz sand 6 at a predetermined ratio makes it possible to obtain the cement-solidified product 8 excellent in solidification characteristics whose strength is further improved.
  • the sodium hydroxide was input into an aqueous solution of 12 % by weight of the boric acid heated to about 60°C to adjust a Na/B mole ratio to 0.25 to thereby obtain an aqueous solution of the sodium borate (S101 illustrated in Fig. 1 ).
  • the sodium borate aqueous solution was regarded as a simulated waste liquid and supplied in a fixed amount into the centrifugal thin film dryer whose heating temperature was set to about 160°C, whereby a sodium borate dry powder was obtained (S102 illustrated in Fig. 1 ).
  • the characteristics of the second kneaded product were excellent rheological characteristics that the viscosity was 9 dPa•s and the filling density was 1.99.
  • the cement-solidified product had a bleeding rate (bleeding from the cement-solidified product) of 0 vol% after 24 hours and a uniaxial compressive strength at a material age of 7 days of 8.9 MPa, and therefore excellent solidification characteristics were also obtained.
  • the characteristics of the second kneaded product were excellent rheological characteristics that the viscosity was 10 dPa•s and the filling density was 2.02.
  • the cement-solidified product had a bleeding rate of 0 vol% after 24 hours and a uniaxial compressive strength at a material age of 7 days of 9.6 MPa, and therefore excellent solidification characteristics were also obtained.
  • the characteristics of the second kneaded product were excellent rheological characteristics that the viscosity was 12 dPa•s and the filling density was 2.04.
  • the cement-solidified product had a bleeding rate of 0 vol% after 24 hours and a uniaxial compressive strength at a material age of 7 days of 12.2 MPa, and therefore excellent solidification characteristics were also obtained.
  • the characteristics of the second kneaded product were excellent rheological characteristics that the viscosity was 100 dPa•s and the filling density was 2.07.
  • the cement-solidified product had a bleeding rate of 0 vol% after 24 hours and a uniaxial compressive strength at a material age of 7 days of 11.9 MPa, and therefore excellent solidification characteristics were also obtained.
  • the characteristics of the second kneaded product were excellent rheological characteristics that the viscosity was 100 dPa•s and the filling density was 2.09.
  • the cement-solidified product had a bleeding rate of 0 vol% after 24 hours and a uniaxial compressive strength at a material age of 7 days of 8.7 MPa, and therefore excellent solidification characteristics were also obtained.
  • the characteristics of the second kneaded product were excellent rheological characteristics that the viscosity was 70 dPa•s and the filling density was 2.0.
  • the cement-solidified product had a bleeding rate of 0 vol% after 24 hours, a uniaxial compressive strength at a material age of 7 days of 9.6 MPa, and a uniaxial compressive strength at a material age of 28 days of 12 MPa, and therefore excellent solidification characteristics were also obtained.
  • the second kneaded product was prepared as in Example 1 and a cement-solidified product was produced as in Example 1, and their physical properties were evaluated.
  • the cement-solidified product had a uniaxial compressive strength at a material age of 28 days of 8.9 MPa, and therefore excellent solidification characteristics could be obtained.
  • a kneaded product was produced without mixing the quartz sand in Example 1. More specifically, by adjusting the kneading water to 392 g, the normal portland cement to750 g, and the sodium borate dry powder to 315 g, the kneaded product was obtained as in Example 1. The physical properties of the kneaded product were measured, and then a cement-solidified product was produced as in Example 1 and its physical properties were evaluated.
  • the kneaded product had such characteristics that the viscosity was 150 dPa•s and the filling density was 1.95.
  • the cement-solidified product had a bleeding rate of 0 vol% after 24 hours and a uniaxial compressive strength at a material age of 7 days of 2.9 MPa, and it was found that the strength was insufficient.
  • Example 1 Example 2
  • Example 3 Example 4
  • Example 5 Example 6
  • Example 7 Comparative Example 1
  • Sodium Borate Dry Powder [g] 315 315 315 315 315 312 312 315 Kneading Water
  • 392 392 392 392 390 390 392 Normal Portland Cement [g] 375 375 375 375 375 375 375 750
  • Quartz Sand [g] 650 750 850 950 1125 680 765 0 Zeolite [g] 0 0 0 0 0 170 85 0 S/C 1.73 2.00 2.27 2.53 3.00 2.27 2.27 0 Zeolite/Quartz Sand (Weight Ratio) - - - - - - 20/80 10/90 - Kneaded Product Viscosity [dPs • S] 9 10 12 100 100 70 24 150 Kneaded Product Filling Density 1.99 2.02 2.04 2.07 2.

Claims (9)

  1. Verfahren zur Zementverfestigung einer radioaktive Borsäure enthaltenden Abfallflüssigkeit, Folgendes beinhaltend:
    einen Schritt der Volumenreduzierung des Hinzufügens eines Natriumhydroxids zu der Abfallflüssigkeit zum Bilden einer radioaktives Natriumborat enthaltenden Lösung und des Trocknens der Lösung zum Bilden eines trockenen Pulvers, welches das radioaktive Natriumborat enthält;
    einen ersten Knetschritt des Knetens des trockenen Pulvers, eines Knetwassers und eines hydraulisch verfestigenden Materials zum Bilden eines ersten gekneteten Produkts; und
    einen zweiten Knetschritt des Knetens von Quarzsand und des ersten gekneteten Produkts zum Bilden eines zweiten gekneteten Produkts;
    wobei ein Gewichtsverhältnis zwischen dem Quarzsand und dem hydraulisch verfestigenden Material 1,5 bis 3,0 beträgt.
  2. Verfahren nach Anspruch 1,
    bei welchem der zweite Knetschritt Kneten von Quarzsand, Zeolith und dem ersten gekneteten Produkt umfasst, und
    wobei ein Gewichtsverhältnis zwischen der Gesamtmenge an Zeolith und Quarzsand und dem hydraulisch verfestigenden Material 1,5 bis 3,0 beträgt.
  3. Verfahren nach Anspruch 1 oder 2, bei welchem eine Partikelgröße des Quarzsandes 0,026 bis 1,18 mm in Bezug auf einen mittleren Durchmesser beträgt.
  4. Verfahren nach Anspruch 2 oder 3, bei welchem eine Partikelgröße des Zeoliths 770 µm in Bezug auf einen mittleren Durchmesser beträgt, und eine Ionenaustauschkapazität des Zeoliths 10 bis 200 meq/100 g beträgt.
  5. Verfahren nach einem der Ansprüche 2 bis 4, bei welchem ein Gewichtsverhältnis zwischen dem Zeolith und der Gesamtmenge an Quarzsand und Zeolith 0,05 bis 0,40 beträgt.
  6. Verfahren nach einem der Ansprüche 2 bis 5, bei welchem der zweite Knetschritt Folgendes beinhaltet:
    Mischen des Quarzsandes und des Zeoliths vor dem Mischen des gemischten Quarzsandes und Zeoliths in dem ersten gekneteten Produkt, oder
    Mischen des Quarzsandes und des Zeoliths separat in dem ersten gekneteten Produkt.
  7. Verfahren nach einem der Ansprüche 1 bis 6, bei welchem der erste Knetschritt und der zweite Knetschritt anhand eines Mischverfahrens innerhalb einer Trommel oder eines Mischverfahrens außerhalb einer Trommel durchgeführt werden.
  8. Verfahren nach einem der Ansprüche 1 bis 7, bei welchem eine Temperatur des trockenen Pulvers Normaltemperatur bis 100 °C beträgt.
  9. Gerät, welches zur Zementverfestigung einer radioaktive Borsäure enthaltenden Abfallflüssigkeit konfiguriert ist, Folgendes beinhaltend:
    eine Knetvorrichtung;
    eine Zuführvorrichtung, welche spezifisch konfiguriert ist, um ein Natriumhydroxid zu der Abfallflüssigkeit zum Bilden einer radioaktives Natriumborat enthaltenden Lösung hinzuzufügen und spezifisch konfiguriert ist, um die Lösung zum Bilden eines trockenen Pulvers, welches das radioaktive Natriumborat enthält, zu trocknen und spezifisch konfiguriert ist, um das trockene Pulver der Knetvorrichtung zuzuführen;
    eine Knetwasserzuführvorrichtung, welche konfiguriert ist, um ein Knetwasser an die Knetvorrichtung zuzuführen;
    eine Zuführvorrichtung für ein hydraulisch verfestigendes Material, welche spezifisch konfiguriert ist, um ein hydraulisch verfestigendes Material an die Knetvorrichtung zum Bilden eines ersten gekneteten Produkts zuzuführen; und
    eine Quarzsand-Zuführvorrichtung, welche spezifisch konfiguriert ist, um Quarzsand an die Knetvorrichtung zum Bilden eines zweiten gekneteten Produkts zuzuführen,
    wobei ein Gewichtsverhältnis zwischen dem Quarzsand und dem hydraulisch verfestigenden Material in der Quarzsandzufuhr 1,5 bis 3,0 beträgt.
EP14814441.3A 2013-06-18 2014-06-11 Zementierverfahren und zementiervorrichtung für borsäurehaltigen flüssigabfall Active EP3012839B1 (de)

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JP2013127110A JP6139288B2 (ja) 2013-06-18 2013-06-18 ホウ酸含有廃液のセメント固化処理方法及びセメント固化処理装置
PCT/JP2014/003112 WO2014203498A1 (ja) 2013-06-18 2014-06-11 ホウ酸含有廃液のセメント固化処理方法及びセメント固化処理装置

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JP2015001485A (ja) 2015-01-05
JP6139288B2 (ja) 2017-05-31
WO2014203498A1 (ja) 2014-12-24
EP3012839A1 (de) 2016-04-27

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