US3657012A - Process for decontaminating radioactive objects - Google Patents

Process for decontaminating radioactive objects Download PDF

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Publication number
US3657012A
US3657012A US752504A US3657012DA US3657012A US 3657012 A US3657012 A US 3657012A US 752504 A US752504 A US 752504A US 3657012D A US3657012D A US 3657012DA US 3657012 A US3657012 A US 3657012A
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US
United States
Prior art keywords
solution
acid
amino
phosphonic
tensio
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Expired - Lifetime
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US752504A
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English (en)
Inventor
Jean-Louis Verot
Rene Sarfati
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Ugine Kuhlmann SA
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Ugine Kuhlmann SA
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Application filed by Ugine Kuhlmann SA filed Critical Ugine Kuhlmann SA
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Classifications

    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D3/00Other compounding ingredients of detergent compositions covered in group C11D1/00
    • C11D3/16Organic compounds
    • C11D3/36Organic compounds containing phosphorus
    • C11D3/364Organic compounds containing phosphorus containing nitrogen

Definitions

  • ABSTRACT Foreign Application Priority A process for decontaminating radioactive objects by washing n 1 them in a solution of a-amino (alkane-phosphonic) acid and a Aug 1967 France 1 8019 tensio-active substance that has been neutralized. to a pH from 7 to 7.5 and diluted to a 10 percent concentration.
  • the wash lll ..134/26, 84/432682 effluents are decontaminated y adding to the effluents sum ⁇ 58]
  • Fie'ld 210/58 cient calcium-ions to displace the rare earths and strontium from their complexes with a-amino (alkane-phosphonic) acid 7 and thereafter scrubbing.
  • our process utilizes the complexing properties of a-amino (alkane-phosphonic) acids, and, in particular, those amino-tri (methane-phosphonic) acids produced by Monsanto Chemical Company under thetrademark Dequest.” These acids form complexes with ions having a valence equal to or greater than 2. These complexes are stable in solutions which are slightly acidic, neutral, or alkaline; yet, the complexes are sufficiently labile so that the radioactive elements may be displaced from them, for example, by an excess of precipitating agent.
  • various objects may be decontaminated by washing them with a solution at a temperature between 60 and 90 C, of a mixture of a tensio-active substance and a nearly neutral sodium salt of an a-amino (alkanephosphonic) acid in water, preferably deionized water.
  • the tensio-active substance is preferably an entirely biodegradable, for example, a heavy alcohol having a straight oxyethylated chain.
  • the wash effluents are scrubbed by coprecipitation or by treatment of zeolites after calcium-ions have been added to the effluents.
  • the tensio-active substances are preferably biodegradable products such as oxyethylation products of the heavy straight chain alcohols, for example, Plurafacs. Alcohol sulfates and sulfonates also give good results. However, tensio-active substances that are not biodegradable, or only partially so, may be used.
  • alkylaryl sulfates or sulfonates, oxyethylated derivatives of polypropylene glycol, such as Emkalyx-Pluraonics, oxyethylated alkyl-phenols and oxyethylated or oxypropylated derivatives of ethylene-diamine such as Tetronics give efficient results.
  • a solution, in deionized water, of from to 500 g/liter of a-amino (alkanephosphonic) acid solution and from to 500 g/liter of tensioactive substance is prepared.
  • This solution is neutralized, preferably with sodium hydroxide, to obtain a pH from 7 to 7.5.
  • This neutralized solution is the mother-solution.
  • the washing solution results from the dilution of approximately 10 percent of the mother-solution in water, preferably deionized water. If desired, adjuvants such as disinfectants, optical brighteners, etc. may be added.
  • the concentration of the washing solution is set in accordance with the strain degree of the objects decontaminated. The soaking of the objects to be decontaminated in the washing solution, in some cases, must be accompanied with a strong brushing.
  • the effluents resulting from the wash generally have a slight or medium activity (10 l0 Ci/m).
  • Calcium in the form of calcium nitrate or calcium chloride is added to the wash effluent in an amount to give an ionic-concentration sufiicient to displace the rare earths and strontium from their complexes with the a-amino (alkane-phosphonic) acid.
  • the a-amino (alkane-phosphonic) acid for example, the
  • calcium-ion quantity is generally less than 1/100 of equivalent-gram per liter of solution.
  • the effluents are scrubbed in the usual manner. For instance, they may be scrubbed by coprecipitation or, preferably, by means of zeolites.
  • the treatment with zeolites has an excellent scrubbing output.
  • the following examples relate to the decontamination of objects used in nuclear instruments or equipment and to the treatment of the resulting effluent.
  • EXAMPLE I Decontamination of Linen A solution in deionized water was prepared having 50 g/liter of a solution of Plurafac RA No. 20 alcohol and 50 g/liter of a solution of amino-tri(methane-phosphonic) acid. The solution was neutralized by the addition of sodium hydroxide to form the mother-solution. The mother-solution was diluted in deionized water to form a 10 percent solution. The linen was then washed in the 10 percent wash solution at a temperature between and C. At the end of the washing, the normal checking instruments indicated no radioactivity on the linen.
  • a solution in the deionized water contained 40 g/liter of solution of Plurafac RA No. 40 alcohol and 70 g/liter of amino-tri (methane-phosphonic) acid.
  • the solution was neutralized to a pH of 7 to 7.5 with sodium hydroxide to give a mother-solution.
  • the mother-solution was diluted in deionized water to obtain a solution of 10 percent concentration.
  • the 10 percent solution was brought to a temperature of 60 and the various objects were soaked with an accompanying damp brushing.
  • the first part after treatment by precipitation of calcium carbonate, had an apparent activity of 965 impulses/ml for 5 minutes.
  • the decontamination factor was 1 2.
  • the second part, after treatment by precipitation of calcium phosphate had an apparent activity of 580 impulses/ml for 5 minutes.
  • the decontamination factor was 20.
  • the third part after treatment by scattering of zeolite and filtration, had an apparent activity of 128 impulses/ml for 5 minutes.
  • the decontamination factor was 90.
  • a process for decontamination of radioactive objects comprising:
  • a process for the decontamination of radioactive objects having radioactive rare earths or strontium particles thereon comprising:

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  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Wood Science & Technology (AREA)
  • Organic Chemistry (AREA)
  • Detergent Compositions (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
US752504A 1967-08-17 1968-08-14 Process for decontaminating radioactive objects Expired - Lifetime US3657012A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR118019A FR1543305A (fr) 1967-08-17 1967-08-17 Procédé de décontamination d'objets radioactifs

Publications (1)

Publication Number Publication Date
US3657012A true US3657012A (en) 1972-04-18

Family

ID=8636938

Family Applications (1)

Application Number Title Priority Date Filing Date
US752504A Expired - Lifetime US3657012A (en) 1967-08-17 1968-08-14 Process for decontaminating radioactive objects

Country Status (11)

Country Link
US (1) US3657012A (es)
JP (1) JPS4815000B1 (es)
BE (1) BE717759A (es)
DE (1) DE1792289A1 (es)
ES (1) ES356973A1 (es)
FR (1) FR1543305A (es)
GB (1) GB1208480A (es)
IL (1) IL30424A (es)
LU (1) LU56652A1 (es)
NL (1) NL6811682A (es)
SE (1) SE335845B (es)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4401532A (en) * 1981-05-28 1983-08-30 Jackson Opha L Radioactive decontamination apparatus and process
US4803771A (en) * 1988-01-07 1989-02-14 Lyons William G Process for removing asbestos using taped troughs

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102004047572A1 (de) * 2004-09-27 2006-04-06 Alfred Kärcher Gmbh & Co. Kg Flüssigkonzentrat-Set

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2924576A (en) * 1954-09-23 1960-02-09 Dow Chemical Co Radio-active decontaminant
US3234124A (en) * 1962-10-18 1966-02-08 Monsanto Co Sequestration of metal ions

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2924576A (en) * 1954-09-23 1960-02-09 Dow Chemical Co Radio-active decontaminant
US3234124A (en) * 1962-10-18 1966-02-08 Monsanto Co Sequestration of metal ions

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4401532A (en) * 1981-05-28 1983-08-30 Jackson Opha L Radioactive decontamination apparatus and process
US4803771A (en) * 1988-01-07 1989-02-14 Lyons William G Process for removing asbestos using taped troughs

Also Published As

Publication number Publication date
BE717759A (es) 1968-12-16
SE335845B (es) 1971-06-14
JPS4815000B1 (es) 1973-05-11
ES356973A1 (es) 1970-02-16
IL30424A0 (en) 1969-07-30
GB1208480A (en) 1970-10-14
DE1792289A1 (de) 1972-02-17
NL6811682A (es) 1969-02-19
IL30424A (en) 1972-11-28
FR1543305A (fr) 1968-10-25
LU56652A1 (es) 1968-11-14

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