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WO1997038785A1 - Metal fluorides separation - Google Patents

Metal fluorides separation Download PDF

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Publication number
WO1997038785A1
WO1997038785A1 PCT/GB1997/001023 GB9701023W WO9738785A1 WO 1997038785 A1 WO1997038785 A1 WO 1997038785A1 GB 9701023 W GB9701023 W GB 9701023W WO 9738785 A1 WO9738785 A1 WO 9738785A1
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WIPO (PCT)
Prior art keywords
mof
gas
fluoπne
separation
band
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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.)
Ceased
Application number
PCT/GB1997/001023
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French (fr)
Inventor
Mark Fields
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Sellafield Ltd
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British Nuclear Fuels PLC
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Filing date
Publication date
Application filed by British Nuclear Fuels PLC filed Critical British Nuclear Fuels PLC
Publication of WO1997038785A1 publication Critical patent/WO1997038785A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D59/00Separation of different isotopes of the same chemical element
    • B01D59/34Separation by photochemical methods

Definitions

  • This invention relates to the separation of metal fluo ⁇ des and specifically to the separauon of molybdenum hexafluo ⁇ de from uranium hexafluo ⁇ de.
  • the rnixture will be present in the form of a UF 6 gas stream in which the MoF 6 is present as an unpu ⁇ ty
  • Uranium may be en ⁇ ched by converting it to UF 6 and usmg cent ⁇ fuges to separate the 235 isotope.
  • va ⁇ ous metal fluo ⁇ des are present as impu ⁇ ues.
  • the vapour pressures of several hexafluo ⁇ des are similar to that of UF 6 and therefore fractional disullation is not a suitable techmque for separating out these impu ⁇ ues.
  • MoF 6 may be present as an impu ⁇ ty if the UF 6 has been prepared from uranium ore.
  • the present invention provides a method of removing MoF 6 from a gas containing both UF 6 and MoF 6 , the method comprising irradiating the gas with ultraviolet light and allowmg the M0F 5 which is formed to condense from said gas.
  • Photolysis was carried out through the quartz window of the vacuum shroud using a mercury lamp to provide UV radiation, the wavelength being 254nm.
  • Each of the deposited samples was examined by infrared spectroscopy before and after irradiation with UV light. .All infrared spectra were recorded with 2cm ' resoluuon and 128 scans or 0.5cm ' resoluuon and 256 scans.
  • the results obtained at the cryogenic temperatures used here can be directly translated to gaseous samples.
  • the matrix-isolauon technique has been used for ease of handling the samples. In fact, the process is expected to be more efficient in the gas phase due to the much greater mobility of the species. and 621cm "1 which are attributed to MoF 6 and UF 6 respectively. In addition a band was observed for MoF 6 at 264cm "1 .
  • the infrared spectrum of MoF 6 shows three new bands at 721cm “1 , 707cm *1 and 678cm “1 , all of which grew in intensity with increased irradiation.
  • the band at 737cm "1 showed a marked decrease in intensity as irradiation of the sample proceeded. In total. the sample of MoF 6 was irradiated for 225 minutes and other new bands were not observed.
  • the band at 674cm “1 is attributed to the formation of MoF 5 in the matrix.
  • the bands at 580cm “1 and 560cm “1 are attributed to UF 5 . It is apparent that both MoF 6 and UF 6 were reduced to MoF 5 and UF 5 .
  • a fluorme radical scavenger is present.
  • scavengers are xenon or carbon monoxide.
  • the photolysis reaction occurs much more rapidly because fluo ⁇ ne radicals are effectively removed from the system by the scavenger and regeneration of UF 6 then has to occur by removal of a fluo ⁇ ne radical from MoF 6 by UF 5 .
  • Figure 1 is a schematic diagram of apparatus for carrying out the method of the present mvention.
  • Figure 2 is a schematic diagram of the reaction vessel of the apparatus m Figure 1
  • the reacuon vessel 1 is fed with a mixture of UF 6 and MoF 6 from storage vessel 3 and with fluorme from vessel 5
  • the pipework between vessels 3 and 5 and vessel 1 is equipped with suitable valves 7 to allow passage of either gas mto the reaction vessel 1.
  • Reaction vessel 1 is shown in more detail m Figure 2. It is made from nickei or Monel and is passivated to prevent reaction of UF 6 with the vessel.
  • a senes of ultraviolet sources are held in the walls of the vessei at suitable positions to enable them to irradiate the whole internal volume of the vessei. These sources may be high, medium or low pressure mercury lamps, xenon lamps or any other convenient sources of UV radiation mcluding lasers operated in the UV range. They should provide sufficient energy to photodissociate MoF 6 and UF 6 .
  • the UF 6 and MoF 6 mixture is irradiated with UV radianon to remove MoF 6 from the vapour phase by reduction to invoiatile MoF 5 .
  • UF 6 is reduced to UF 5 but. smce UF 5 is more reacnve than MoF 5 , UF 6 is regenerated preferentially by the reaction of UF 5 with other molecules of MoF 6 and/or free fluo ⁇ ne atoms.
  • UF 6 is allowed to flow from the reacuon vessel through filter 11 (preventing passage of pamculate matter) mto cryogenic trap 13. Trap 13 condenses UF 6 , whilst any fluorme gas produced du ⁇ ng the process passes through the system to a fluorme store at 15 for recycling. The mvolatile MoF 5 remains in the reaction vessei. The UF 6 may then be revoiarilised and passed into a vessel 17 for storage.
  • Fluo ⁇ ne (or an aitemauve fluo ⁇ natmg agent) is then introduced into reaction vessel 1 to react with MoF 5 and regenerate MoF 6 Depending on the fluo ⁇ nating agent which is used, vessel 1 may be heated or irradiated with UV radiation to speed up the reaction to reform the MoF 6 .
  • the MoF 6 is passed through the cryogenic trap to remove any fluo ⁇ ne (for recycling) and is then passed to storage vessei 19 for disposal.
  • a senes of reaction vessels 1 are operated sequentially so as further to pu ⁇ fy the UF 6 .

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  • Life Sciences & Earth Sciences (AREA)
  • Biophysics (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Treating Waste Gases (AREA)

Abstract

A method of removing molybdenum hexafluoride from a gas containing both uranium hexafluoride and molybdenum hexafluoride. The method comprises irradiating the gas with ultraviolet light and allowing the molybdenum pentafluoride which is formed to condense from the gas.

Description

METAL FLUORIDES SEPARATION
This invention relates to the separation of metal fluoπdes and specifically to the separauon of molybdenum hexafluoπde from uranium hexafluoπde. Typically, the rnixture will be present in the form of a UF6 gas stream in which the MoF6 is present as an unpuπty
Uranium may be enπched by converting it to UF6 and usmg centπfuges to separate the 235 isotope. When the uranium source matenal for preparing UF6 is obtamed from irradiated nuclear reactor fuel, vaπous metal fluoπdes are present as impuπues. The vapour pressures of several hexafluoπdes are similar to that of UF6 and therefore fractional disullation is not a suitable techmque for separating out these impuπues. Additionally, MoF6 may be present as an impuπty if the UF6 has been prepared from uranium ore.
The use of visible laser radiation has been proposed for the removal of impunties from UF6. However, MoF6 has no absorption bands in the visible region and accordingly cannot be separated by this techmque.
It has also been proposed (Transuranium Elements - A Half Century ( Amencan Chemical Society 1992. authors J V Beitz and C W Williams, editors L R Morss and J Fuger) to use ultraviolet radiauon to separate the fluoπdes of neptunium and plutomum from UF6. Irradiation of NpF6, PuF6 and UF6 with ultraviolet light causes the hexafluoπdes to be reduced to NpF5, UF5 and PuF4 which are involaQle. Because of its reactivity, UF5 reacts further to remove a fluorine atom from either PuF6 or NpF6, thereby reforming UF6. In this way, separation takes place and the bulk of the UF6 is recoverable. If the reacuon is earned out m the presence of carbon monoxide, which reacts with fluorine atoms to remove them from the system, then high decontaminauon of UF6 from NpF6 and PuF6 is achieved, but approximately 20% of UF6 is lost. If the reaction is earned out without carbon monoxide present, and with the peπodic removal of fluoπne gas from the system, poorer decontaminauon is achieved, but only 4% UF,, is lost.
In their proposal, the authors (Beitz and Williams) states that their method is likely to be effective in the removal of other hexafluoπdes which are more reactive than UF6. On this basis it is postulated that AmF6, UF6 and RhF6 will probably be photochemicaily removal from UF6. is postulated that AmF6, UF6 and RhF6 will probably be photochemically removal from UF6. However, MoF6 is shown as being less reactive than UF6 and it is clear that the authors do not expect this hexafluoride to be removed from UF6.
It has now been discovered that MoF6 is in fact removable from UF6 usmg ultraviolet radiation. Accordingly the present invention provides a method of removing MoF6 from a gas containing both UF6 and MoF6, the method comprising irradiating the gas with ultraviolet light and allowmg the M0F5 which is formed to condense from said gas.
Examples showing the effect of UV light on MoF6 and on a mixture of MoF6 and UF6 will now be described.
In order to carry out the photolysis, samples were co-condensed with an excess of nitrogen onto a Csl window at 12°K to provide a satisfactory matrix. Nitrogen was used as the matrix gas. A protective layer of nitrogen was laid onto the window prior to deposition of the samples. MoF6 and UF6 were held in passivated nickel cans cooled to about approximately 150°K (methylcyclohexane slush) and 140°K (methy lcyciopentane slush) respectively, to achieve a suitably slow and controlled deposition rate onto the Csl sample window. Sample depositions of two to three hours gave the best results. Samples of MoF6 -1- UF6 were prepared by condensing both substances onto the window at the same time, in an attempt to get an intimate rnixture of the two gases rather than layers of the condensed gases.
Photolysis was carried out through the quartz window of the vacuum shroud using a mercury lamp to provide UV radiation, the wavelength being 254nm. Each of the deposited samples was examined by infrared spectroscopy before and after irradiation with UV light. .All infrared spectra were recorded with 2cm' resoluuon and 128 scans or 0.5cm' resoluuon and 256 scans. The results obtained at the cryogenic temperatures used here can be directly translated to gaseous samples. The matrix-isolauon technique has been used for ease of handling the samples. In fact, the process is expected to be more efficient in the gas phase due to the much greater mobility of the species. and 621cm"1 which are attributed to MoF6 and UF6 respectively. In addition a band was observed for MoF6 at 264cm"1.
After photolysis, the infrared spectrum of MoF6 shows three new bands at 721cm"1, 707cm*1 and 678cm"1, all of which grew in intensity with increased irradiation. The band at 737cm"1 showed a marked decrease in intensity as irradiation of the sample proceeded. In total. the sample of MoF6 was irradiated for 225 minutes and other new bands were not observed.
As a result of irradiation of the rnixture of MoF6 and UF6, new infrared bands were observed at 674cm" 1 , 580cm"1 and 560cm" . Other bands observed during photolysis of pure MoF6 were only present as indistinct shoulders. The intensity of the 737cm" band of MoF6 and the 621cm'1 band of UF6 dropped markedly during photolysis.
The band at 674cm"1 is attributed to the formation of MoF5 in the matrix. The bands at 580cm"1 and 560cm"1 are attributed to UF5. It is apparent that both MoF6 and UF6 were reduced to MoF5 and UF5.
On warming the matrix to 26°K (1 minute) in order to anneal it, and recooling it to 12°K. sigmficant changes in the infrared spectrum were observed. The bands at 560 and 580cm"1 completely disappeared whilst the peak at 678cm"' decreased in intensity. The areas of the bands at 737cm'1 and 621cm"1 increased. At 12°K the MoF6 and UF6 molecules and their photolysis products are held rigidly by the nitrogen molecules which make up the matrix. On annealing, the structure becomes considerably less rigid, allowing the fluorine radicals, produced by photolysis, to move through the matrix then recombine with MoF5 and UF5 molecules. Continued irradiation of the sample further reduced the intensity (and area) of both the MoF6 band at 737cm" 1 and the UFό band at 621cm" . However, die bands attributed to UF5 formation were not apparent in the spectrum, even with prolonged irradiation.
Comparison of the band areas of the UF6 band (621cm'1) and the MoF6 band (737cm" 1), before photolysis and after annealing of the matrix, shows tiiat the band area of the UF6 band returned to 84% of its original area, whilst that of MoF6 only returned to 50% of its original area after annealing. Thus, it can be concluded that UF5 is a more reactive species than MoF5, smce it more readily reforms the hexafiuoπde than MoF5.
These results show that the important factor in the separation of MoF0 from UF6 is not the relative reactivities of the hexafluoπdes. Rather it is the relative ease with which the pentafluoπdes produced by photolysis react to reform the hexafluoπdes.
In a preferred process according to the present invenuon, a fluorme radical scavenger is present. Examples of such scavengers are xenon or carbon monoxide. With a scavenger present, the photolysis reaction occurs much more rapidly because fluoπne radicals are effectively removed from the system by the scavenger and regeneration of UF6 then has to occur by removal of a fluoπne radical from MoF6 by UF5.
An example of a method in accordance with the present mvention will now be descnbed. by way of example only, and with reference to the accompanying drawings, in which: -
Figure 1 is a schematic diagram of apparatus for carrying out the method of the present mvention; and
Figure 2 is a schematic diagram of the reaction vessel of the apparatus m Figure 1
Referring to Figure 1 of the accompanying drawings, the reacuon vessel 1 is fed with a mixture of UF6 and MoF6 from storage vessel 3 and with fluorme from vessel 5 The pipework between vessels 3 and 5 and vessel 1 is equipped with suitable valves 7 to allow passage of either gas mto the reaction vessel 1.
Reaction vessel 1 is shown in more detail m Figure 2. It is made from nickei or Monel and is passivated to prevent reaction of UF6 with the vessel. A senes of ultraviolet sources are held in the walls of the vessei at suitable positions to enable them to irradiate the whole internal volume of the vessei. These sources may be high, medium or low pressure mercury lamps, xenon lamps or any other convenient sources of UV radiation mcluding lasers operated in the UV range. They should provide sufficient energy to photodissociate MoF6 and UF6. Withm vessel 1 , the UF6 and MoF6 mixture is irradiated with UV radianon to remove MoF6 from the vapour phase by reduction to invoiatile MoF5. Additionally, UF6 is reduced to UF5 but. smce UF5 is more reacnve than MoF5, UF6 is regenerated preferentially by the reaction of UF5 with other molecules of MoF6 and/or free fluoπne atoms.
On completion of the punfication. UF6 is allowed to flow from the reacuon vessel through filter 11 (preventing passage of pamculate matter) mto cryogenic trap 13. Trap 13 condenses UF6, whilst any fluorme gas produced duπng the process passes through the system to a fluorme store at 15 for recycling. The mvolatile MoF5 remains in the reaction vessei. The UF6 may then be revoiarilised and passed into a vessel 17 for storage.
Fluoπne (or an aitemauve fluoπnatmg agent) is then introduced into reaction vessel 1 to react with MoF5 and regenerate MoF6 Depending on the fluoπnating agent which is used, vessel 1 may be heated or irradiated with UV radiation to speed up the reaction to reform the MoF6.
On compleuon of the reaction, the MoF6 is passed through the cryogenic trap to remove any fluoπne (for recycling) and is then passed to storage vessei 19 for disposal.
In an alternative embodiment, a senes of reaction vessels 1 are operated sequentially so as further to puπfy the UF6.

Claims

1. A method of removing MoF6 from a gas contaimng both UF6 and MoF6, the method compnsmg irradiatmg the gas with ultraviolet light and allowing the MoF5 which is formed to condense from such gas.
2. A method according to Claim 1 in which the MoF5 is reacted with a fluoπnating agent to regenerate MoF6.
3. A method according to Claim 2 wherem the fluoπnating agent is fluoπne.
4. A method according to any of the preceding claims wherem the irradiation with UV light is earned out in the presence of a fluoπne radical scavenger.
5. A method according to Claim 4 wherem the fluoπne radical scavenger is xenon or carbon monoxide.
6. A method according to Claim 1 and substanually descnbed herem.
7 A method of removing MoF6 from a gas containmg both UF6 and MoF6 substanually as descnbed herewith with reference to the accompanying drawings.
PCT/GB1997/001023 1996-04-17 1997-04-15 Metal fluorides separation Ceased WO1997038785A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GBGB9607901.7A GB9607901D0 (en) 1996-04-17 1996-04-17 Metal flourides separation
GB9607901.7 1996-04-17

Publications (1)

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WO1997038785A1 true WO1997038785A1 (en) 1997-10-23

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104870370A (en) * 2012-11-16 2015-08-26 霍尼韦尔国际公司 Separation and recovery of molybdenum from uranium process distillates
WO2020188048A1 (en) * 2019-03-21 2020-09-24 Technische Universität München Preparation of metal fluorides and separation processes
CN115608023A (en) * 2022-10-31 2023-01-17 中核四0四有限公司 A device for filtering and purifying liquid-phase uranium hexafluoride
RU2817671C2 (en) * 2019-03-21 2024-04-19 Технише Универзитет Мюнхен Preparation of metal fluorides and separation processes

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4555318A (en) * 1984-01-06 1985-11-26 The United States Of America As Represented By The United States Department Of Energy Removal of fluoride impurities from UF6 gas

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4555318A (en) * 1984-01-06 1985-11-26 The United States Of America As Represented By The United States Department Of Energy Removal of fluoride impurities from UF6 gas

Non-Patent Citations (4)

* Cited by examiner, † Cited by third party
Title
CHEM. PHYS. LETT., vol. 53, no. 3, 1 May 1978 (1978-05-01), NL, pages 435 - 438 *
DATABASE INIS INTERNATIONAL ATOMIC ENERGY AGENCY (IAEA), VIENNA, AT; EERKENS ET AL.: "LASER SEPARATION OF MEDICAL ISOTOPES", XP002032784 *
DATABASE INIS INTERNATIONAL ATOMIC ENERGY AGENCY (IAEA), VIENNA, AT; FREUND ET AL.: "multiple-photon isotope separation in mof6", XP002032785 *
TRANSACTIONS OF THE AMERICAN NUCLEAR SOCIETY, vol. 75, 10 November 1996 (1996-11-10) - 14 November 1996 (1996-11-14), WASHINGTON. DC, USA, pages 20 - 22 *

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104870370A (en) * 2012-11-16 2015-08-26 霍尼韦尔国际公司 Separation and recovery of molybdenum from uranium process distillates
US9567237B2 (en) 2012-11-16 2017-02-14 Honeywell International Inc. Separation and recovery of molybdenum values from uranium process distillate
WO2020188048A1 (en) * 2019-03-21 2020-09-24 Technische Universität München Preparation of metal fluorides and separation processes
US20220153607A1 (en) * 2019-03-21 2022-05-19 Technische Universität München Preparation of metal fluorides and separation processes
RU2817671C2 (en) * 2019-03-21 2024-04-19 Технише Универзитет Мюнхен Preparation of metal fluorides and separation processes
US12319589B2 (en) * 2019-03-21 2025-06-03 Technische Universitaet München Preparation of metal fluorides and separation processes
CN115608023A (en) * 2022-10-31 2023-01-17 中核四0四有限公司 A device for filtering and purifying liquid-phase uranium hexafluoride

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Publication number Publication date
GB9607901D0 (en) 1996-06-19
ZA973140B (en) 1998-01-29

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