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US4950425A Expired / Lapsed US ⏱️ 0.0 years remaining

Method of decomposing alkyl phosphate

Assignee: Solvay Interox Ltd
•
Filing: 1989-05-11
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Granted: 1990-08-21
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Expires: 2009-05-11
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Abstract

Abstract Alkyl phosphates, undiluted or dissolved in hydrophobic solvents can be destroyed in situ by reaction with hydrogen peroxide in the presence of certain transition metal catalyst systems. The invention catalyst system comprises a chromium compound, which dissolves in the aqueous phase, typically an alkali metal chromate, which is employed in conjunction with introduction of an alkali, preferably sodium hydroxide, or in the presence of an alkali buffer to keep the pH of the aqueous phase within a window spanning mildly acidic to mildly alkaline pH during the course of progressive introduction of the hydrogen peroxide, which often lasts from 3 to 10 hours, thereby enabling the oxidation of the alkyl phosphate to continue. The reaction is preferably carried out at a temperature of at least 60° C., and particularly at about 65° to 75° C., or at about the boiling point of the aqueous phase. The window becomes somewhat wider as the reaction temperature increases, the term mildly acidic indicating a pH of at least about pH 6 at around 70° C. to at least pH 5 at around 100° C. Preferably, the solution is maintained at a pH of from 6.5 to 7.5.

Inventors

  • 👤 Kenneth T. Rowbottom
  • 👤 John N. R. Wilkinson
  • 👤 Terence M. Conboy
  • 👤 Graham V. Hutson

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-01 04:53
CPC Classifications
A; A62; A62D; A62D3/00; A62D3/30; A62D3/38; G; G21; G21F; G21F9/00; G21F9/04; G21F9/06; A62D2101/00; A62D2101/20; A62D2101/26

Claims Analysis

Total Claims: 35
Claim 1
Independent Claim 129 words
In a process for decomposing an alkylphosphate in which the alkyl-phosphate by itself or dissolved in a hydrophobic organic solvent is reacted with hydrogen peroxide in aqueous solution added progressively at a temperature that is above ambient temperature and in the presence of a transition metal catalyst, the improvement in which the catalyst comprises an effective amount of a chromium compound and the aqueous hydrogen peroxide phase is maintained in a pH window range of mildly acidic to mildly alkaline pH by the controlled introduction of alkali at a rate that is sufficient to neutralise the acid released by decomposition of the alkylphosphate, or is buffered by the presence of an alkali buffer to within the said pH range, thereby significantly accelerating the rate of decomposition of the alkylphosphate.
Claim 2
Dependent Claim 129 words
In a process for decomposing an alkylphosphate in which the alkyl-phosphate by itself or dissolved in a hydrophobic organic solvent is reacted with hydrogen peroxide in aqueous solution added progressively at a temperature that is above ambient temperature and in the presence of a transition metal catalyst, the improvement in which the catalyst comprises an effective amount of a chromium compound and the aqueous hydrogen peroxide phase is maintained in a pH window range of mildly acidic to mildly alkaline pH by the controlled introduction of alkali at a rate that is sufficient to neutralise the acid released by decomposition of the alkylphosphate, or is buffered by the presence of an alkali buffer to within the said pH range, thereby significantly accelerating the rate of decomposition of the alkylphosphate.
Claim 3
Dependent Claim 20 words
A process according to claim 1 in which the aqueous phase is maintained at a pH not exceding pH 9.0.
Claim 4
Dependent Claim 30 words
A process according to claim 1 in which the reaction is carried out at a temperature in the range of 60° C. to the boiling point of the aqueous phase.
Claim 5
Dependent Claim 24 words
A process according to claim 3 in which the reaction is carried out at a temperature in the range of 60° to 75° C.
Claim 6
Dependent Claim 24 words
A process according to claim 4 in which the reaction is carried out at a pH in the range of pH 6 to 9.
Claim 7
Dependent Claim 27 words
A process according to claim 3 in which the reaction is carried out at a temperature within 5° C. of the boiling point of the aqueous phase.
Claim 8
Dependent Claim 21 words
A process according to claim 6 in which the reaction is carried out at a pH of at least pH 5.
Claim 9
Dependent Claim 39 words
A process according to claim 1 in which the aqueous phase is maintained at a pH which is at least 0.5 pH units higher than the lower limit of the window range for pH at the temperature of operation.
Claim 10
Dependent Claim 24 words
A process according to claim 8 in which the aqueous phase is maintained at a pH in the range of pH 6.5 to 7.5.
Claim 11
Dependent Claim 24 words
A process according to claim 1 in which the aqueous phase is adjusted to the desired pH range before addition of hydrogen peroxide commences.
Claim 12
Dependent Claim 28 words
A process according to claim 1 in which the desired pH of the aqueous phase is maintained by introduction of aqueous alkali metal hydroxide solution, preferably sodium hydroxide.
Claim 13
Dependent Claim 24 words
A process according to claim 11 in which the desired pH of the aqueous phase is maintained by introduction of aqueous sodium hydroxide solution.
Claim 14
Dependent Claim 38 words
A process according to claim 1 in which the desired pH of the aqueous phase is maintained for at least part of the time by the presence of an alkali metal phosphate which acts as a pH buffer.
Claim 15
Dependent Claim 40 words
A process according to claim 1 in which the amount of catalyst employed, calculated on the basis of its chromium content, is selected within the range of 0.05 to 8 parts w/w per 100 parts by weight of alkyl phosphate.
Claim 16
Dependent Claim 40 words
A process according to claim 14 in which the amount of catalyst employed, calculated on the basis of its chromium content, is selected within the range of 0.25 to 2 parts w/w per 100 parts by weight of alkyl phosphate.
Claim 17
Dependent Claim 17 words
A process according to claim 1 in which the catalyst is introduced as an alkali metal chromate.
Claim 18
Dependent Claim 80 words
A process according to claim 1 in which the amount of hydrogen peroxide introduced is selected in a range which varies in accordance with the reaction temperature employed, the range comprising from 60 to 150 moles per mole of alkyl phosphate at a reaction temperature of up to 75° C. and varying to that of from 50 to 100 moles per mole of alkyl phosphate at a reaction temperature within 5° C. of the boiling point of the aqueous phase.
Claim 19
Dependent Claim 23 words
A process according to claim 1 in which the hydrogen peroxide solution is introduced during a period of from 3 to 10 hours.
Claim 20
Dependent Claim 31 words
A process according to claim 1 in which the hydrogen peroxide solution is introduced at such a rate that its residual concentration in the aqueous phase does not exceed 1.0% w/w.
Claim 21
Dependent Claim 41 words
A process according to claim 17 in which the hydrogen peroxide solution is introduced during a period of from 3 to 10 hours and at such a rate that its residual concentration in the aqueous phase does not exceed 1.0% w/w.
Claim 22
Dependent Claim 33 words
A process according to claim 1 in which the hydrogen peroxide solution is introduced progressively until analysis of the organic phase indicates that substantially quantitative destruction of the alkyl phosphate has been obtained.
Claim 23
Dependent Claim 27 words
A process according to claim 1 in which the concentration of the hydrogen peroxide solution introduced is selected in the range of from 35 to 70% w/w.
Claim 24
Dependent Claim 140 words
A process according to claim 17 in which the reaction is carried out at a pH which is selected in a range which varies in accordance with the reaction temperature, the range comprising pH 6 to 9 at a reaction temperature of from 60° to 75° C. and varying to a pH range of pH 5 to 7.5 as the reaction temperature is varied to within 5° of the boiling point of the aqueous phase, the pH being maintained by the introduction of an alkali solution and partly by the presence of an alkali metal phosphate buffer during at least part of the reaction period, and which employs an alkali metal chromate as catalyst in an amount calculated on the basis of its chromium content, of from 0.05 to 8 parts w/w per 100 parts by weight of alkyl phosphate.
Claim 25
Dependent Claim 40 words
A process according to claim 1 in which the reaction mixture contains at least an equal volume of aqueous phase in addition to the organic phase containing the alkylphosphate at the start of addition of the aqueous hydrogen peroxide solution.
Claim 26
Dependent Claim 47 words
A process according to claim 1 in which at least part of the aqueous phase remaining at the end of the reaction is separated from the treated organic phase and subsequently contacted with a further amount of nontreated organic phase containing alkylphosphate for destruction with hydrogen peroxide.
Claim 27
Dependent Claim 48 words
A process according to claim 24 in which the volume of the aqueous phase is maintained approximately constant during the reaction period by balancing the rate of introduction of aqueous hydrogen peroxide solution with the net rate at which water is evapourated and removed from the reaction mixture.
Claim 28
Dependent Claim 38 words
A process according to claim 1 in which the alkyl phosphate to be destroyed is present as a solution of at least 20% v/v and particularly from 20% to 50% v/v in a high boiling point hydrocarbon solvent.
Claim 29
Dependent Claim 15 words
A process according to claim 1 in which the alkyl phosphate is a trialkyl phosphate.
Claim 30
Dependent Claim 22 words
A process according to claim 1 in which the alkyl moiety in the alkyl phosphate contains from 2 to 8 carbon atoms.
Claim 31
Dependent Claim 13 words
A process according to claim 29 in which the alkyl moiety is butyl.
Claim 32
Dependent Claim 14 words
A process according to claim 29 in which the alkyl phosphate is tributyl phosphate.
Claim 33
Dependent Claim 14 words
A process according to claim 1 in which the hydrocarbon solvent is odourless kerosene.
Claim 34
Dependent Claim 22 words
A process according to claim 17 or 23 in which the alkyl phosphate comprises a butyl phosphate, optionally dissolved in odourless kerosene.
Claim 35
Dependent Claim 40 words
A process according to claim 1 or 32 in which the organic phase contains radioactive species from contact with nuclear waste and the process is continued until at least 90% of the radioactivity has been transferred to the aqueous phase.

References Cited (Backward Citations)

US3716566A Cited
US4294703A Cited
US4624792A Cited
US4588506A Cited
US4729835A Cited
JPH02192699A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1993-08-20 1994-02-19 1994-08-21 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1997-08-20 1998-02-19 1998-08-21 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2001-08-20 2002-02-19 2002-08-21 $7700.00 Window Closed / Lapsed

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