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Thermal Oxide Reprocessing Plant

The Thermal Oxide Reprocessing Plant, or THORP, is a nuclear fuel reprocessing plant at Sellafield in Cumbria, England. THORP is owned by the Nuclear Decommissioning Authority and operated by Sellafield Ltd (which is the site licensee company).

Thermal Oxide Reprocessing Plant
The THORP building viewed from the south behind an internal rail line
CountryEngland, United Kingdom
LocationCumbria, North West England
Coordinates54°24′56″N 3°30′06″W / 54.4155°N 3.5017°W / 54.4155; -3.5017
StatusOperational
Construction began1974
Commission date1994
Decommission date2018 (ceased reprocessing, fuel storage continuing)
Construction cost£1.8–billion
Owner(s)Nuclear Decommissioning Authority
Operator(s)Sellafield Ltd
Cooling sourceForced draft cooling towers

Spent nuclear fuel from nuclear reactors was reprocessed to separate the 96% uranium and the 1% plutonium from the 3% radioactive wastes, which are treated and stored at the plant. The uranium is then made available for customers to be manufactured into new fuel, and the plutonium incorporated into mixed oxide fuel.

On 14 November 2018 it was announced that reprocessing operations had ended at THORP after earning £9bn in revenue. The receipt and storage facility (which makes up nearly half of THORP's physical footprint), will operate through to the 2070s to receive and store spent nuclear fuel from the UK's PWR and AGR fleet.[1] The decommissioning is expected to start around 2075.[2]

History edit

 
THORP's first fuel load in 1994

Between 1977 and 1978 an inquiry was held into an application by British Nuclear Fuels plc for outline planning permission to build a new plant to reprocess irradiated oxide nuclear fuel from both UK and foreign reactors. The inquiry was to answer three questions:

  1. Should oxide fuel from United Kingdom reactors be reprocessed in this country at all; whether at Windscale or elsewhere?
  2. If yes, should such reprocessing be carried on at Windscale?
  3. If yes, should the reprocessing plant be about double the estimated site required to handle United Kingdom oxide fuels and be used as to the spare capacity, for reprocessing foreign fuels?

The result of the inquiry was that the new plant, the Thermal Oxide Reprocessing Plant, was given the go-ahead in 1978.[3]

Construction of THORP started in 1979, and was completed in 1994. The plant went into operation in August 1997. Build cost was £1.8 billion.[4]

THORP's first irradiated fuel rod was sheared in March 1994, which was followed in January of 1995 by the chemical separation plant processing the irradiated fuel feed solution that had been produced in the previous year by the Head End plant. By the Spring of 1998 over 1400 t of irradiated fuel has been reprocessed in THORP, and the plant was steadily and successfully ramped up to its normal operating throughput throughout this time. At this time, the performance of the THORP Chemical Separation Plant had been excellent, above all, the uranium-plutonium separation stage, which received extensive development to deal with the effects of the fission product technetium, has given an overall separation performance well in excess of the minimum flowsheet requirement. THORP's discharges represented a small fraction of overall discharges from the wider Sellafield site.[5][6]

On 14 November 2018 it was announced that reprocessing operations had ended at THORP after all existing reprocessing contracts had been fulfilled. It had reprocessed 9,331 tonnes of used nuclear fuel from 30 customers in nine countries, earning £9bn in revenue. The receipt and storage facility within THORP continues to operate.[1][7]

Decommissioning will take place after several decades to allow radiation levels to decline, and is expected to occur between 2075 and 2095. The estimated cost of decommissioning is forecast as £4 billion at 2018 prices.[4]

Design edit

The chemical flowsheet for THORP is designed to add less non-volatile matter to the first cycle PUREX raffinate. One way in which this is done is by avoiding the use of ferrous compounds as plutonium reducing agents. In this plant the reduction is done using either hydrazine or HAN (hydroxylamine nitrate). The plant releases gaseous emissions of krypton-85, a radioactive beta-emitter with a half-life of 10.7 years. The Radiological Protection Institute of Ireland (RPII) commenced 24-hour atmospheric monitoring for krypton-85 in 1993, prior to the plant's commissioning.[8][9]

The cooled oxide fuel is chopped up in the Shear Cell and the fuel dissolved in nitric acid. It is chemically conditioned before passing to the chemical separation plant. Pulsed columns (designated HA/HS) are used to initially separate the majority of the uranium and plutonium from the fission products by transferring them into the solvent phase, which comprises tri-butyl phosphate in odourless kerosene (TBP/OK). The transfer is done in the HA column with the HS column providing further removal of fission products. 2 further pulsed columns (designated BS/BX) and a mixer/settler assembly (1BXX) then separate the uranium and plutonium into separate streams. Plutonium is reduced to the +3 oxidation state, which is insoluble in the solvent phase so ends up in the aqueous phase exiting the 1BX column.

The 1BXX mixer/settler completes the removal of Pu from the solvent phase. The 1BS column removes any remaining Uranium from the aqueous phase by the use of fresh solvent.

Pulsed columns then purify the plutonium, removing the troublesome fission products that remain. A mixer/settlet (1C) is used to transfer (washes) the uranium across to the aqueous phase ready for the next stage. Uranium purification is achieved using three mixer settlers (UP1 - UP3) similar to those in use on the existing Magnox reprocessing plant. Evaporation of the two product streams then occurs before further processing is undertaken. Uranium is converted to UO3 powder while the plutonium is converted to PuO2 powder and sent to storage.

Pulsed columns were chosen to avoid the risk of a criticality incident occurring within the plant. This can happen if sufficient fissile material comes together to start an uncontrolled chain reaction, producing a large release of neutrons. The risks and mechanisms are well understood and the plant design is arranged to prevent its occurrence, i.e.: intrinsically safe.

2005 internal leak edit

On 9 May 2005 it was announced that THORP suffered a large leak of a highly radioactive solution, which had first started in July 2004. British Nuclear Group's board of inquiry determined that a design error led to the leak, while a complacent culture at the plant delayed detection for nine months. Operations staff did not discover the leak until safeguards staff reported major fluid accountancy discrepancies.

Altogether 83 cubic metres (82,966 litres) of hot nitric acid solution leaked from a small fractured feedpipe, which was discovered when a remote camera was sent in to examine THORP's Feed Clarification Cell on 19 April 2005. All the fluids collected under gravity into the secondary containment, which is a stainless steel tub embedded in 2-metre thick reinforced concrete, capable of holding 250 cubic metres of fluids.

The solution from the spill was estimated to contain 20 metric tons of uranium and 160 kilograms of plutonium. The leaked solution was safely recovered into primary containment using originally installed steam ejectors. Radiation levels in the cell precluded entry of humans.

The pipe fractured due to lateral motion of an accountancy tank, which measures volume by weight and moves horizontally and vertically in the process. The tank's original design had restraint blocks to prevent lateral motion, but these were later removed from the design for seismic uncoupling.

The incident was classified as Level 3 out of 7 on the International Nuclear Event Scale (INES), a "serious incident", due to the amount of radioactive inventory that leaked from primary to secondary containment without discovery over a number of months.[10] This was initially considered by BNFL to be surprisingly high, but the specifications of the scale required it.

The British Nuclear Group was convicted for breaches of health and safety regulations following the accident, and fined £500,000.[11]

Production at the plant restarted in late 2007, but in early 2008 stopped again for the repair of an underwater lift that moved fuel for reprocessing.[12]

See also edit

Other reprocessing sites

References edit

  1. ^ a b "Reprocessing ceases at UK's Thorp plant". World Nuclear News. 14 November 2018. Retrieved 15 November 2018.
  2. ^ NDA Annual Report and Accounts 2018 to 2019. NDA, 4 July 2019
  3. ^ Brown, Paul (1 April 1999), "Sellafield says don't blame Thorp for cuts", The Guardian, UK, p. 27
  4. ^ a b Leggett, Theo (27 November 2018). "Inside Sellafield's death zone with the nuclear clean-up robots". BBC News. Retrieved 29 November 2018.
  5. ^ Philips, C. (July 1998). "The thermal oxide reprocessing plant at Sellafield: Three years of active operation in the chemical separation plant".
  6. ^ C., Phillips (16 February 1993). "Development and design of the Thermal Oxide Reprocessing Plant at Sellafield". Chemical Engineering Research and Design. 71 (A2).
  7. ^ "Sellafield Thorp site to close in 2018". BBC News Cumbria. BBC. 7 June 2012. Retrieved 22 August 2012.
  8. ^ . The Irish News. 16 January 1995. Archived from the original on 11 January 2016. Retrieved 1 May 2015.
  9. ^ McDonald, Frank (7 January 1995). . The Irish Times. Archived from the original on 11 January 2016. Retrieved 2 May 2015.
  10. ^ [1] 28 September 2007 at the Wayback Machine
  11. ^ Wilson, James (17 October 2006). "Sellafield criticised on safety as BNG fined". FT.com. Archived from the original on 11 December 2022. Retrieved 4 February 2013.
  12. ^ Geoffrey Lean, 'Shambolic' Sellafield in crisis again after damning safety report, The Independent, 3 February 2008.

External links edit

  • Nuclear Decommissioning Authority
  • Sellafield Limited
  • Nuclear unit closed after checks - BBC, 23 April 2005
  • Huge radioactive leak closes Thorp nuclear plant - The Guardian, 9 May 2005
  • , BNFL, 26 May 2005
  • - Bellona Foundation, 7 July 2005
  • - Nuclear Engineering International, 27 July 2005
  • Nuclear staff suspended over leak - BBC, 4 August 2005
  • - News & Star, 11 November 2005
  • , John Large, 13 April 2006 - includes diagrams
  • - Nuclear Engineering International, 17 January 2007
  • - Nuclear Engineering International, 25 April 2007
  • , Mr Justice Openshaw, 16 October 2006

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The Thermal Oxide Reprocessing Plant or THORP is a nuclear fuel reprocessing plant at Sellafield in Cumbria England THORP is owned by the Nuclear Decommissioning Authority and operated by Sellafield Ltd which is the site licensee company Thermal Oxide Reprocessing PlantThe THORP building viewed from the south behind an internal rail lineCountryEngland United KingdomLocationCumbria North West EnglandCoordinates54 24 56 N 3 30 06 W 54 4155 N 3 5017 W 54 4155 3 5017StatusOperationalConstruction began1974Commission date1994Decommission date2018 ceased reprocessing fuel storage continuing Construction cost 1 8 billionOwner s Nuclear Decommissioning AuthorityOperator s Sellafield LtdCooling sourceForced draft cooling towers edit on Wikidata Spent nuclear fuel from nuclear reactors was reprocessed to separate the 96 uranium and the 1 plutonium from the 3 radioactive wastes which are treated and stored at the plant The uranium is then made available for customers to be manufactured into new fuel and the plutonium incorporated into mixed oxide fuel On 14 November 2018 it was announced that reprocessing operations had ended at THORP after earning 9bn in revenue The receipt and storage facility which makes up nearly half of THORP s physical footprint will operate through to the 2070s to receive and store spent nuclear fuel from the UK s PWR and AGR fleet 1 The decommissioning is expected to start around 2075 2 Contents 1 History 2 Design 3 2005 internal leak 4 See also 5 References 6 External linksHistory edit nbsp THORP s first fuel load in 1994Between 1977 and 1978 an inquiry was held into an application by British Nuclear Fuels plc for outline planning permission to build a new plant to reprocess irradiated oxide nuclear fuel from both UK and foreign reactors The inquiry was to answer three questions Should oxide fuel from United Kingdom reactors be reprocessed in this country at all whether at Windscale or elsewhere If yes should such reprocessing be carried on at Windscale If yes should the reprocessing plant be about double the estimated site required to handle United Kingdom oxide fuels and be used as to the spare capacity for reprocessing foreign fuels The result of the inquiry was that the new plant the Thermal Oxide Reprocessing Plant was given the go ahead in 1978 3 Construction of THORP started in 1979 and was completed in 1994 The plant went into operation in August 1997 Build cost was 1 8 billion 4 THORP s first irradiated fuel rod was sheared in March 1994 which was followed in January of 1995 by the chemical separation plant processing the irradiated fuel feed solution that had been produced in the previous year by the Head End plant By the Spring of 1998 over 1400 t of irradiated fuel has been reprocessed in THORP and the plant was steadily and successfully ramped up to its normal operating throughput throughout this time At this time the performance of the THORP Chemical Separation Plant had been excellent above all the uranium plutonium separation stage which received extensive development to deal with the effects of the fission product technetium has given an overall separation performance well in excess of the minimum flowsheet requirement THORP s discharges represented a small fraction of overall discharges from the wider Sellafield site 5 6 On 14 November 2018 it was announced that reprocessing operations had ended at THORP after all existing reprocessing contracts had been fulfilled It had reprocessed 9 331 tonnes of used nuclear fuel from 30 customers in nine countries earning 9bn in revenue The receipt and storage facility within THORP continues to operate 1 7 Decommissioning will take place after several decades to allow radiation levels to decline and is expected to occur between 2075 and 2095 The estimated cost of decommissioning is forecast as 4 billion at 2018 prices 4 Design editThis section needs additional citations for verification Please help improve this article by adding citations to reliable sources in this section Unsourced material may be challenged and removed Find sources Thermal Oxide Reprocessing Plant news newspapers books scholar JSTOR October 2017 Learn how and when to remove this template message The chemical flowsheet for THORP is designed to add less non volatile matter to the first cycle PUREX raffinate One way in which this is done is by avoiding the use of ferrous compounds as plutonium reducing agents In this plant the reduction is done using either hydrazine or HAN hydroxylamine nitrate The plant releases gaseous emissions of krypton 85 a radioactive beta emitter with a half life of 10 7 years The Radiological Protection Institute of Ireland RPII commenced 24 hour atmospheric monitoring for krypton 85 in 1993 prior to the plant s commissioning 8 9 The cooled oxide fuel is chopped up in the Shear Cell and the fuel dissolved in nitric acid It is chemically conditioned before passing to the chemical separation plant Pulsed columns designated HA HS are used to initially separate the majority of the uranium and plutonium from the fission products by transferring them into the solvent phase which comprises tri butyl phosphate in odourless kerosene TBP OK The transfer is done in the HA column with the HS column providing further removal of fission products 2 further pulsed columns designated BS BX and a mixer settler assembly 1BXX then separate the uranium and plutonium into separate streams Plutonium is reduced to the 3 oxidation state which is insoluble in the solvent phase so ends up in the aqueous phase exiting the 1BX column The 1BXX mixer settler completes the removal of Pu from the solvent phase The 1BS column removes any remaining Uranium from the aqueous phase by the use of fresh solvent Pulsed columns then purify the plutonium removing the troublesome fission products that remain A mixer settlet 1C is used to transfer washes the uranium across to the aqueous phase ready for the next stage Uranium purification is achieved using three mixer settlers UP1 UP3 similar to those in use on the existing Magnox reprocessing plant Evaporation of the two product streams then occurs before further processing is undertaken Uranium is converted to UO3 powder while the plutonium is converted to PuO2 powder and sent to storage Pulsed columns were chosen to avoid the risk of a criticality incident occurring within the plant This can happen if sufficient fissile material comes together to start an uncontrolled chain reaction producing a large release of neutrons The risks and mechanisms are well understood and the plant design is arranged to prevent its occurrence i e intrinsically safe 2005 internal leak editOn 9 May 2005 it was announced that THORP suffered a large leak of a highly radioactive solution which had first started in July 2004 British Nuclear Group s board of inquiry determined that a design error led to the leak while a complacent culture at the plant delayed detection for nine months Operations staff did not discover the leak until safeguards staff reported major fluid accountancy discrepancies Altogether 83 cubic metres 82 966 litres of hot nitric acid solution leaked from a small fractured feedpipe which was discovered when a remote camera was sent in to examine THORP s Feed Clarification Cell on 19 April 2005 All the fluids collected under gravity into the secondary containment which is a stainless steel tub embedded in 2 metre thick reinforced concrete capable of holding 250 cubic metres of fluids The solution from the spill was estimated to contain 20 metric tons of uranium and 160 kilograms of plutonium The leaked solution was safely recovered into primary containment using originally installed steam ejectors Radiation levels in the cell precluded entry of humans The pipe fractured due to lateral motion of an accountancy tank which measures volume by weight and moves horizontally and vertically in the process The tank s original design had restraint blocks to prevent lateral motion but these were later removed from the design for seismic uncoupling The incident was classified as Level 3 out of 7 on the International Nuclear Event Scale INES a serious incident due to the amount of radioactive inventory that leaked from primary to secondary containment without discovery over a number of months 10 This was initially considered by BNFL to be surprisingly high but the specifications of the scale required it The British Nuclear Group was convicted for breaches of health and safety regulations following the accident and fined 500 000 11 Production at the plant restarted in late 2007 but in early 2008 stopped again for the repair of an underwater lift that moved fuel for reprocessing 12 See also edit nbsp Cumbria portalNuclear fuel cycle Reprocessed uranium Red oil PUREX Pyrometalurgical ProcessingOther reprocessing sitesCOGEMA La Hague site Rokkasho Reprocessing Plant West Valley Reprocessing Plant Mayak Tōkai Ibaraki Tokaimura nuclear accident References edit a b Reprocessing ceases at UK s Thorp plant World Nuclear News 14 November 2018 Retrieved 15 November 2018 NDA Annual Report and Accounts 2018 to 2019 NDA 4 July 2019 Brown Paul 1 April 1999 Sellafield says don t blame Thorp for cuts The Guardian UK p 27 a b Leggett Theo 27 November 2018 Inside Sellafield s death zone with the nuclear clean up robots BBC News Retrieved 29 November 2018 Philips C July 1998 The thermal oxide reprocessing plant at Sellafield Three years of active operation in the chemical separation plant C Phillips 16 February 1993 Development and design of the Thermal Oxide Reprocessing Plant at Sellafield Chemical Engineering Research and Design 71 A2 Sellafield Thorp site to close in 2018 BBC News Cumbria BBC 7 June 2012 Retrieved 22 August 2012 Risk doubles for heavy fish eater The Irish News 16 January 1995 Archived from the original on 11 January 2016 Retrieved 1 May 2015 McDonald Frank 7 January 1995 Report says radon a more serious threat than Sellafield plant The Irish Times Archived from the original on 11 January 2016 Retrieved 2 May 2015 1 Archived 28 September 2007 at the Wayback Machine Wilson James 17 October 2006 Sellafield criticised on safety as BNG fined FT com Archived from the original on 11 December 2022 Retrieved 4 February 2013 Geoffrey Lean Shambolic Sellafield in crisis again after damning safety report The Independent 3 February 2008 External links editNuclear Decommissioning Authority Sellafield Limited Bellona Foundation Excellent Site for Detailed Info on Sellafield and associated environmental issues Nuclear unit closed after checks BBC 23 April 2005 Huge radioactive leak closes Thorp nuclear plant The Guardian 9 May 2005 THORP Fractured Pipe Board of Inquiry Report BNFL 26 May 2005 Thorp officials work to restore UK nuke reprocessing facility Bellona Foundation 7 July 2005 Thorp board of enquiry report released Nuclear Engineering International 27 July 2005 Nuclear staff suspended over leak BBC 4 August 2005 Workload forces delay over Thorp reopening News amp Star 11 November 2005 Leak of Radioactive Liquor in the Feed Clarification Cell at BNG THORP Sellafield Review of the Management and Technical Aspects of the Failure and its Implications for the Future of THORP John Large 13 April 2006 includes diagrams Thorp restart approved Nuclear Engineering International 17 January 2007 Culture clubbed Nuclear Engineering International 25 April 2007 HSE report into the THORP leak The sentencing of British Nuclear Group over the accident at THORP Mr Justice Openshaw 16 October 2006 Retrieved from https en wikipedia org w index php title Thermal Oxide Reprocessing Plant amp oldid 1218294315, wikipedia, wiki, book, books, library,

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