ADDITIONAL PROTOCOL

to the Agreement between the Republic of Austria, the Kingdom of Belgium, the Kingdom of Denmark, the Republic of Finland, the Federal Republic of Germany, the Hellenic Republic, Ireland, the Italian Republic, the Grand Duchy of Luxembourg, the Kingdom of the Netherlands, the Portuguese Republic, the Kingdom of Spain, the Kingdom of Sweden, the European Atomic Energy Community and the International Atomic Energy Agency in implementation of Article III(1) and (4) of the Treaty on the Non-proliferation of Nuclear weapons(1)

(notified under document number COM(1998) 314)

(1999/188/Euratom)

PREAMBLE

Whereas the Republic of Austria, the Kingdom of Belgium, the Kingdom of Denmark, the Republic of Finland, the Federal Republic of Germany, the Hellenic Republic, Ireland, the Italian Republic, the Grand Duchy of Luxembourg, the Kingdom of the Netherlands, the Portuguese Republic, the Kingdom of Spain, the Kingdom of Sweden (hereinafter referred to as ‘the States’) and the European Atomic Energy Community (hereinafter referred to as ‘the Community’) are parties to an Agreement between the States, the Community and the International Atomic Energy Agency (hereinafter referred to as the ‘the Agency’) in implementation of Article III(1) and (4) of the Treaty on the Non-proliferation of Nuclear Weapons (hereinafter referred to as the ‘Safeguards Agreement’), which entered into force on 21 February 1997;

Aware of the desire of the international community to further enhance nuclear non-proliferation by strengthening the effectiveness and improving the efficiency of the Agency's safeguards system;

Recalling that the Agency must take into account in the implementation of safeguards the need to avoid hampering the economic and technological development in the Community or international cooperation in the field of peaceful nuclear activities, to respect health, safety, physical protection and other security provisions in force and the rights of individuals, and to take every precaution to protect commercial, technological and industrial secrets as well as other confidential information coming to its knowledge;

Whereas the frequency and intensity of activities described in this Protocol shall be kept to the minimum consistent with the objective of strengthening the effectiveness and improving the efficiency of Agency safeguards;

Now therefore the Community, the States and the Agency have agreed as follows:

RELATIONSHIP BETWEEN THE THE PROTOCOL AND THE SAFEGUARDS AGREEMENT

Article 1

The provisions of the Safeguards Agreement shall apply to this Protocol to the extent that they are relevant to and compatible with the provisions of this Protocol. In case of conflict between the provisions of the Safeguards Agreement and those of this Protocol, the provisions of this Protocol shall apply.

PROVISION OF INFORMATION

Article 2

(a) Each State shall provide the Agency with a declaration containing the information identified in sub-paragraphs (i), (ii), (iv), (ix) and (x). The Community shall provide the Agency with a declaration containing the information identified in sub-paragraphs (v), (vi) and (vii). Each State and the Community shall provide the Agency with a declaration containing the information identified in sub-paragraphs (iii) and (viii).

(i) A general description of and information specifying the location of nuclear fuel cycle-related research and development activities not involving nuclear material carried out anywhere that are funded, specifically authorised or controlled by, or carried out on behalf of, the State concerned.

(ii) Information identified by the Agency on the basis of expected gains in effectiveness or efficiency, and agreed to by the State concerned, on operational activities of safeguards relevance at facilities and locations outside facilities where nuclear material is customarily used.

(iii) A general description of each building on each site, including its use and, if not apparent from that description, its contents. The description shall include a map of the site.

(iv) A description of the scale of operations for each location engaged in the activities specified in Annex I to this Protocol.

(v) Information specifying the location, operational status and the estimated annual production capacity of uranium mines and concentration plants and thorium concentration plants in each State, and the current annual production of such mines and concentration plants. The Community shall provide, on request by the Agency, the current annual production of an individual mine or concentration plant. The provision of this information does not require detailed nuclear material accountancy.

(vi) Information regarding source material which has not reached the composition and purity suitable for fuel fabrication or for being isotopically enriched, as follows:

(a) the quantities, the chemical composition, the use or intended use of such material, whether in nuclear or non-nuclear use, for each location in the States at which the material is present in quantities exceeding 10 tonnes of uranium and/or 20 tonnes of thorium, and for other locations with quantities of more than 1 tonne, the aggregate for the States as a whole if the aggregate exceeds 10 tonnes of uranium or 20 tonnes of thorium. The provision of this information does not require detailed nuclear material accountancy;

(b) The quantities, the chemical composition and the destination of each export from the States to a State outside the Community, of such material for specifically non-nuclear purposes in quantities exceeding:

(1) 10 tonnes of uranium, or for successive exports of uranium to the same state, each of less than 10 tonnes, but exceeding a total of 10 tonnes for the year;

(2) 20 tonnes of thorium, or for successive exports of thorium to the same State, each of less than 20 tonnes, but exceeding a total 20 tonnes for the year;

(c) the quantities, chemical composition, current location and use or intended use of each import into the Sates from outside the Community of such material for specifically non-nuclear purposes in quantities exceeding:

(1) 10 tonnes of uranium, or for successive imports of uranium each of less than 10 tonnes, but exceeding a total of 10 tonnes for the year;

(2) 20 tonnes of thorium, or for successive imports of thorium each of less than 20 tonnes, but exceeding a total of 20 tonnes for the year;

it being understood that there is no requirement to provide information on such material intended for a non-nuclear use once it is in its non-nuclear end-use form.

(vii) (a)

Information regarding the quantities, uses and locations of nuclear material exempted from safeguards pursuant to Article 37 of the Safeguards Agreement;

(b) information regarding the quantities (which may be in the form of estimates) and uses at each location, of nuclear material exempted from safeguards pursuant to Article 36(b) of the Safeguards Agreement but not yet in a non-nuclear end-use form, in quantities exceeding those set out in Article 37 of the Safeguards Agreement. The provision of this information does not require detailed nuclear material accountancy.

(viii)

Information regarding the location or further processing of intermediate or high-level waste containing plutonium, high enriched uranium or uranium-233 on which safeguards have been terminated pursuant to Article 11 of the Safeguards Agreement. For the purpose of this paragraph, ‘further processing’ does not include repackaging of the waste or its further conditioning not involving the separation of elements, for storage or disposal.

(ix) The following information regarding specified equipment and non-nuclear material listed in Annex II:

(a) for each export out of the Community of such equipment and material: the identity, quantity, location of intended use in the receiving State and date or, as appropriate, expected date, of export;

(b) on specific request by the Agency, confirmation by the importing State of information provided to the Agency by a State outside of the Community concerning the export of such equipment and material to the importing State.

(x) General plans for the succeeding 10-year period relevant to the development of the nuclear fuel cycle (including planned nuclear fuel cycle-related research and development activities) when approved by the appropriate authorities in the State.

(b) Each State shall make every reasonable effort to provide the Agency with the following information:

(i) a general description of and information specifying the location of nuclear fuel cycle-related research and development activities not involving nuclear material which are specifically related to enrichment, reprocessing of nuclear fuel or the processing of intermediate or high-level waste containing plutonium, high enriched uranium or uranium-233 that are carried out anywhere in the State concerned but which are not funded, specifically authorised or controlled by, or carried out on behalf of, that State. For the purpose of this paragraph ‘processing’ of intermediate or high-level waste does not include repackaging of the waste or its conditioning not involving the separation of elements, for storage or disposal.

(ii) A general description of activities and the identity of the person or entity carrying out such activities, at locations identified by the Agency outside a site which the Agency considers might be functionally related to the activities of that site. The provision of this information is subject to a specific request by the Agency. It shall be provided in consultation with the Agency and in a timely fashion.

(c) On request by any or all of the Agency, a State or the Community, as appropriate, shall provide amplifications or clarifications of any information provided under this Article, in so far as relevant for the purpose of safeguards.

Article 3

(a) Each State or the Community, or both, as appropriate, shall provide to the Agency the information identified in Article 2(a)(i), (iii), (iv), (v), (vi)(a), (vii), and (x) and Article 2(b)(i) within 180 days of the entry into force of this Protocol.

(b) Each State or the Community, or both, as appropriate, shall provide to the Agency, by 15 May of each year, updates of the information referred to in paragraph (a) for the period covering the previous calendar year. If there has been no change to the information previously provided, each State or the Community, or both, as appropriate, shall so indicate.

(c) The Community shall provide to the Agency, by 15 May of each year, the information identified in Article 2(a)(vi)(b) and (c) for the period covering the previous calendar year.

(d) Each State shall provide to the Agency on a quarterly basis the information identified in Article 2(a)(ix)(a). This information shall be provided within 60 days of the end of each quarter.

(e) The Community and each State shall provide to the Agency the information identified in Article 2(a)(viii) 180 days before further processing is carried out and, by 15 May of each year, information on changes in location for the period covering the previous calendar year.

(f) Each State and the Agency shall agree on the timing and frequency of the provision of the information identified in Article 2(a)(ii).

(g) Each State shall provide to the Agency the information in Article 2(a)(ix)(b) within 60 days of the Agency's request.

COMPLEMENTARY ACCESS

Article 4

The following shall apply in connection with the implementation of complementary access under Article 5 of this Protocol:

(a) The Agency shall not mechanistically or systematically seek to verify the information referred to in Article 2; however, the Agency shall have access to:

(i) any location referred to in Article 5(a)(i) or (ii) on a selective basis in order to assure the absence of undeclared nuclear material and activities;

(ii) any location referred to in Article 5(b) or (c) to resolve a question relating to the correctness and completeness of the information provided pursuant to Article 2 or to resolve an inconsistency relating to that information;

(iii) any location referred to in Article 5(a)(iii) to the extent necessary for the Agency to confirm, for safeguards purposes, the Community's, or, as appropriate, a State's declaration of the decommissioned status of a facility or location outside facilities where nuclear material was customarily used.

(b) (i)

Except as provided in paragraph (ii), the Agency shall give the State concerned, or for access under Article 5(a) or under Article 5(c) where nuclear material is involved, the State concerned and the Community, advance notice of access of at least 24 hours.

(ii) For access to any place on a site that is sought in conjunction with design information verification visits

or ad hoc

or routine inspections on that site, the period of advance notice shall, if the Agency so requests, be at least two hours but, in exceptional circumstances, it may be less than two hours.

(c) Advance notice shall be in writing and shall specify the reasons for access and the activities to be carried out during such access.

(d) In the case of a question or inconsistency, the Agency shall provide the State concerned and, as appropriate, the Community with an opportunity to clarify and facilitate the resolution of the question or inconsistency. Such an opportunity will be provided before a request for access, unless the Agency considers that delay in access would prejudice the purpose for which the access is sought. In any event, the Agency shall not draw any conclusions about the question or inconsistency until the State concerned and, as appropriate, the Community have been provided with such an opportunity.

(e) Unless otherwise agreed to by the State concerned, access shall only take place during regular working hours.

(f) The State concerned, or for access under Article 5(a) or under Article 5(c) where nuclear material is involved, the State concerned and the Community, shall have the right to have agency inspectors accompanied during their access by its representatives and, as appropriate, by Community inspectors provided that Agency inspectors shall not thereby be delayed or otherwise impeded in the exercise of their functions.

Article 5

Each State shall provide the Agency with access to:

(a) (i)

any place on a site;

(ii) any location identified under Article 2(a)(v) to (viii);

(iii) any decommissioned facility or decommissioned location outside facilities where nuclear material was customarily used.

(b) Any location identified by the State concerned under Article 2(a)(i), Article 2(a)(iv), Article 2(a)(ix)(b) or Article 2(b), other than those referred to in paragraph (a)(i), provided that if the State concerned is unable to provide such access, that State shall make every reasonable effort to satisfy Agency requirements, without delay, through other means.

(c) Any location specified by the Agency, other than locations referred to in paragraphs (a) and (b), to carry out location-specific environmental sampling, provided that if the State concerned is unable to provide such access, that State shall make every reasonable effort to satisfy Agency requirements, without delay, at adjacent locations or through other means.

Article 6

When implementing Article 5, the Agency may carry out the following activities:

(a) for access in accordance with Article 5(a)(i) or (iii): visual observation; collection of environmental samples; utilisation of radiation detection and measurement devices; application of seals and other identifying and tamper indicating devices specified in Subsidiary Arrangements; and other objective measures which have been demonstrated to be technically feasible and the use of which has been agreed by the Board of Governors (hereinafter referred to as ‘the Board’) and following consultations between the Agency, the Community and the State concerned.

(b) For access in accordance with Article 5(a)(ii): visual observation; item counting of nuclear material; non-destructive measurements and sampling; utilisation of radiation detection and measurement devices; examination of records relevant to the quantities, origin and disposition of the material; collection of environmental samples; and other objective measures which have been demonstrated to be technically feasible and the use of which has been agreed by the Board and following consultations between the Agency, the Community and the State concerned.

(c) For access in accordance with Article 5(b): visual observation; collection of environmental samples; utilisation of radiation detection and measurement devices; examination of safeguards relevant production and shipping records; and other objective measures which have been demonstrated to be technically feasible and the use of which has been agreed by the Board and following consultations between the Agency and the State concerned.

(d) For access in accordance with Article 5(c), collection of environmental samples and, in the event the results do not resolve the question or inconsistency at the location specified by the Agency pursuant to Article 5(c), utilisation at that location of visual observation, radiation detection and measurement devices, and, as agreed by the State concerned and, where nuclear material is involved, the Community, and the Agency, other objective measures.

Article 7

(a) On request by a State, the Agency and that State shall make arrangements for managed access under this Protocol in order to prevent the dissemination of proliferation sensitive information, to meet safety or physical protection requirements, or to protect proprietary or commercially sensitive information. Such arrangements shall not preclude the Agency from conducting activities necessary to provide credible assurance of the absence of undeclared nuclear materials and activities at the location in question, including the resolution of a question relating to the correctness and completeness of the information referred to in Article 2 or of an inconsistency relating to that information.

(b) A State may, when providing the information referred to in Article 2, inform the Agency of the places at a site or location at which managed access may be applicable.

(c) Pending the entry into force of any necessary Subsidiary Arrangements, a State may have recourse to managed access consistent with the provisions of paragraph (a).

Article 8

Nothing in this Protocol shall preclude a State from offering the Agency access to locations in addition to those referred to in Articles 5 and 9 or from requesting the Agency to conduct verification activities at a particular location. The Agency shall, without delay, make every reasonable effort to act on such a request.

Article 9

Each State shall provide the Agency with access to locations specified by the Agency to carry out wide-area environmental sampling, provided that if a State is unable to provide such access that State shall make every reasonable effort to satisfy Agency requirements at alternative locations. The Agency shall not seek such access until the use of wide-area environmental sampling and the procedural arrangements therefor have been approved by the Board and following consultations between the Agency and the State concerned.

Article 10

(a) The Agency shall inform the State concerned and, as appropriate, the Community of:

(i) the activities carried out under this Protocol, including those in respect of any questions or inconsistencies the Agency had brought to the attention of the State concerned and, as appropriate, the Community within 60 days of the activities being carried out by the Agency.

(ii) The results of activities in respect of any questions or inconsistencies the Agency had brought to the attention of the State concerned and, as appropriate, the Community as soon as possible but in any case within 30 days of the results being established by the Agency.

(b) The Agency shall inform the State concerned and the Community of the conclusions it has drawn from its activities under this Protocol. The conclusions shall be provided annually.

DESIGNATION OF AGENCY INSPECTORS

Article 11

(a) (i)

The Director-General shall notify the Community and the States of the Board's approval of any Agency official as a safeguards inspector. Unless the Community advises the Director-General of the rejection of such an official as an inspector for the States within three months of receipt of notification of the Board's approval, the inspector so notified to the Community and the States shall be considered designated to the States.

(ii) The Director-General, acting in response to a request by the Community or on his own initiative, shall immediately inform the Community and the States of the withdrawal of the designation of any official as an inspector for the States.

(b) A notification referred to in paragraph (a) shall be deemed to be received by the Community and the States seven days after the date of the transmission by registered post of the notification by the Agency to the Community and the States.

VISAS

Article 12

Each State shall, within one month of the receipt of a request therefor, provide the designated inspector specified in the request with appropriate multiple entry/exit and/or transit visas, where required, to enable the inspector to enter and remain on the territory of the State concerned for the purpose of carrying out his/her functions. Any visas required shall be valid for at least one year and shall be renewed, as required, to cover the duration of the inspector's designation to the States.

SUBSIDIARY ARRANGEMENTS

Article 13

(a) Where a State or the Community, as appropriate, or the Agency indicate that it is necessary to specify in subsidiary Arrangements how measures laid down in this Protocol are to be applied, that State, or that State and the Community and the Agency shall agree on such Subsidiary Arrangements within 90 days of the entry into force of this Protocol or, where the indication of the need for such Subsidiary Arrangements is made after the entry into force of this Protocol, within 90 days of the date of such indication.

(b) Pending the entry into force of any necessary Subsidiary Arrangements, the Agency shall be entitled to apply the measures laid down in this Protocol.

COMMUNICATIONS SYSTEMS

Article 14

(a) Each State shall permit and protect free communications by the Agency for official purposes between Agency inspectors in that State and Agency Headquarters and/or Regional Offices, including attended and unattended transmission of information generated by Agency containment and/or surveillance or measurement devices. The Agency shall have, in consultation with the State concerned, the right to make use of internationally established systems of direct communications, including satellite systems and other forms of telecommunication, not in use in that State. At the request of a State, or the Agency, details of the implementation of this paragraph in that State with respect to the attended or unattended transmission of information generated by Agency containment and/or surveillance or measurement devices shall be specified in the Subsidiary Arrangements.

(b) Communication and transmission of information as provided for in paragraph (a) shall take due account of the need to protect proprietary or commercially sensitive information or design information which the State concerned regards as being of particular sensitivity.

PROTECTION OF CONFIDENTIAL INFORMATION

Article 15

(a) The Agency shall maintain a stringent regime to ensure effective protection against disclosure of commercial, technological and industrial secrets and other confidential information coming to its knowledge, including such information coming to the Agency's knowledge in the implementation of this Protocol.

(b) The regime referred to in paragraph (a) shall include, among others, provisions relating to:

(i) general principles and associated measures for the handling of confidential information;

(ii) conditions of staff employment relating to the protection of confidential information;

(iii) procedures in cases of breaches or alleged breaches of confidentiality.

ANNEXES

Article 16

(a) The Annexes to this Protocol shall be an integral part thereof. Except for the purposes of amendment of Annexes I and II, the term ‘Protocol’ as used in this instrument means this Protocol and the Annexes together.

(b) The list of activities specified in Annex I, and the list of equipment and material specified in Annex II, may be amended by the Board on the advice of an open-ended working group of experts established by the Board, any such amendment shall take effect four months after its adoption by the Board.

(c) Annex III to this Protocol specifies how measures in this Protocol shall be implemented by the Community and the States.

ENTRY INTO FORCE

Article 17

(a) This Protocol shall enter into force on the day on which the Agency receives from the Community and the States written notification that their respective requirements for entry into force have been met.

(b) The States and the Community may, at any date before this Protocol enters into force, declare that they will apply this Protocol provisionally.

(c) The Director-General shall promptly inform all Member States of the Agency of any declaration of provisional application of, and of the entry into force of, this Protocol.

DEFINITIONS

Article 18

For the purpose of this Protocol:

(a) ‘nuclear fuel cycle-related research and development activities’ means those activities which are specifically related to any process or system development aspect of any of the following:

— of nuclear material,

— enrichment of nuclear material,

— nuclear fuel fabrication,

— reactors,

— critical facilities,

— reprocessing of nuclear fuel,

— processing (not including repackaging or conditioning not involving the separation of elements, for storage or disposal) of intermediate or high-level waste containing plutonium, high enriched uranium or uranium-233,

but do not include activities related to theoretical or basic scientific research or to research and development on industrial radioisotope applications, medical, hydrological and agricultural applications, health and environmental effects and improved maintenance.

(b) ‘Site’ means that area delimited by the Community and a State in the relevant design information for a facility, including a closed-down facility, and in the relevant information on a location outside facilities where nuclear material is customarily used, including a closed-down location outside facilities where nuclear material was customarily used (this is limited to locations with hot cells or where activities related to conversion, enrichment, fuel fabrication or reprocessing were carried out). ‘Site’ shall also include all installations, colocated with the facility or location, for the provision or use of essential services, including: hot cells for processing irradiated materials not containing nuclear material; installations for the treatment, storage and disposal of waste; and buildings associated with specified activities identified by the State concerned under Article 2(a)(iv).

(c) ‘Decommissioned facility’ or ‘decommissioned location outside facilities’ means an installation or location at which residual structures and equipment essential for its use have been removed or rendered inoperable so that it is not used to store and can no longer be used to handle, process or utilise nuclear material.

(d) ‘Closed-down facility’ or ‘closed-down location outside facilities’ means an installation or location where operations have been stopped and the nuclear material removed but which has not been decommissioned.

(e) ‘High enriched uranium’ means uranium containing 20 % or more of the isotope uranium-235.

(f) ‘Location-specific environmental sampling’ means the collection of environmental samples (e. g. air, water, vegetation, soil, smears) at, and in the immediate vicinity of, a location specified by the Agency for the purpose of assisting the Agency to draw conclusions about the absence of undeclared nuclear material or nuclear activities at the specified location.

(g) ‘Wide-area environmental sampling’ means the collection of environmental samples (e. g. air, water, vegetation, soil, smears) at a set of locations specified by the Agency for the purpose of assisting the Agency to draw conclusions about the absence of undeclared nuclear material or nuclear activities over a wide area..

(h) ‘Nuclear material’ means any source or any special fissionable material as defined in Article XX of the Statute. The term source material shall not be interpreted as applying to ore or ore residue. Any determination by the Board under Article XX of the Statute of the Agency after the entry into force of this Protocol which adds to the materials considered to be source material or special fissionable material shall have effect under this Protocol only on acceptance by the Community and the States.

(i) ‘Facility’ means:

(i) a reactor, a critical facility, a conversion plant, a fabrication plant, a reprocessing plant, an isotope separation plant or a separate storage installation, or

(ii) any location where nuclear material in amounts greater than one effective kilogram is customarily used.

(j) ‘Location outside facilities’ means any installation or location, which is not a facility, where nuclear material is customarily used in amounts of one effective kilogram or less.

Hecho en Viena, por duplicado, el veintidós de septiembre de mil novecientos noventa y ocho, en las lenguas alemana, danesa, espaňola, finesa, francesa, griega, inglesa, italiana, neerlandesa, portuguesa y sueca siendo cada uno de estos textos igualmente auténtico, si bien, en caso de discrepancia, harán fe los textos acordados en las lenguas oficiales de la Junta de gobernadores del OIEA.

Udfærdiget i Wien den toogtyvende september nittenhundrede og otteoghalvfems i to eksemplarer på dansk, engelsk, finsk, fransk, græsk, italiensk, nederlandsk, portugisisk, spansk, svensk og tysk med samme gyldighed for alle versioner, idet teksterne på de officielle IAEA-sprog dog har fortrinsstilling i tilfælde af uoverensstemmelser.

Geschehen zu Wien am 22. September 1998 in zwei Urschriften in dänischer, deutscher, englischer, finnischer, französischer, griechischer, italienischer, niederländischer, portugiesischer, schwedischer und spanischer Sprache, wobei jeder Wortlaut gleichermaßen verbindlich, im Fall von unterschiedlichen Auslegungen jedoch der Wortlaut in den Amtssprachen des Gouverneursrats der Internationalen Atomenergie-Organisation maßgebend ist.

Έγινε στη Βιέννη εις διπλούν, την 22η ημέρα του Σεπτεμβρίου 1998, στη δανική, ολλανδική, αγγλική, φινλανδική, γαλλική, γερμανική, ελληνική, ιταλική, πορτογαλική, ισπανική και σουηδική γλώσσα τα κείμενα σε όλες τις ανωτέρω γλώσσες είναι εξίσου αυθεντικά, εκτός από περίπτωση απόκλισης, οπότε υπερισχύουν τα κείμενα που έχουν συνταχθεί στις επίσημες γλώσσες του Διοικητικού Συμβουλίου του Διεθνούς Οργανισμού Ατομικής Ενέργειας.

Done at Vienna in duplicate, on the twenty second day of September 1998 in the Danish, Dutch, English, Finnish, French, German, Greek, Italian, Portuguese, Spanish and Swedish languages, the texts of which are equally authentic except that, in case of divergence, those texts concluded in the official languages of the IAEA Board of Governors shall prevail.

Fait à Vienne, en deux exemplaires le 22 septembre 1998 en langues allemande, anglaise, danoise, espagnole, finnoise, française, grecque, italienne, néerlandaise, portugaise et suédoise; tous ces textes font également foi sauf que, en cas de divergence, les versions conclues dans les langues officielles du Conseil des gouverneurs de l'AΙΕΑ prévalent.

Fatto a Vienna in duplice copia, il giorno 22 del mese di settembre 1998 nelle lingue danese, finnico, francese, greco, inglese, italiano, olandese, portoghese, spagnolo, svedese e tedesco, ognuna delle quali facente ugualmente fede, ad eccezione dei testi conclusi nelle lingue ufficiali del Consiglio dei governatori dell'AIEA che prevalgono in caso di divergenza tra i testi.

Gedaan te Wenen op 22 september 1998, in tweevoud, in de Deense, de Duitse, de Engelse, de Finse, de Franse, de Griekse, de Italiaanse, de Nederlandse, de Portugese, de Spaanse en de Zweedse taal, zijnde alle teksten gelijkelijk authentiek, met dien verstande dat in geval van tegenstrijdigheid de teksten die zijn gesloten in de officiële talen van de IOAE bindend zijn.

Feito em Viena em duplo exemplar, aos vinte e dois de Setembro de 1998 em língua alemã, dinamarquesa, espanhola, finlandesa, francesa, grega, inglesa, italiana, neerlandesa, portuguesa e sueca; todos os textos fazem igualmente fé mas, em caso de divergência, prevalecem aqueles textos que tenham sido estabelecidos em línguas oficiais do Conselho dos Governadores da AIEA.

Tehty Wienissä kahtena kappaleena 22 päivänä syyskuuta 1998 tanskan, hollannin, englannin, suomen, ranskan, saksan, kreikan, italian, portugalin, espanjan ja ruotsin kielellä; kaikki kieliversiot ovat yhtä todistusvoimaisia, mutta eroavuuden ilmetessä on noudatettava niitä tekstejä, jotka on tehty Kansainvälisen atomienergiajärjestön hallintoneuvoston virallisilla kielillä.

Utfärdat i Wien i två exemplar den 22 september 1998 på danska, engelska, finska, franska, grekiska, italienska, nederländska, portugisiska, spanska, svenska och tyska språken, varvid varje språkversion skall äga lika giltighet, utom ifall de skulle skilja sig åt då de texter som ingåtts på IAEA:s styrelses officiella språk skall ha företräde.

Por el Gobierno del Reino de Bélgica

For Kongeriget Belgiens regering

Für die Regierung des Königreichs Belgien

Για την κυβέρνηση τον Βασιλείου τον Βελγίου

For the Government of the Kingdom of Belgium

Pour le gouvernement du Royaume de Belgique

Per il governo del Regno del Belgio

Voor de regering van het Koninkrijk België

Pelo Governo do Reino da Bélgica

Belgian kuningaskunnan hallituksen puolesta

För Konungariket Belgiens regering

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Por el Gobierno del Reino de Dinamarca

For Kongeriget Danmarks regering

Für die Regierung des Königreichs Dänemark

Για την κυβέρνηση τον Βασιλείον του Δανίας

For the Government of the Kingdom of Denmark

Pour le gouvernement du Royaume de Danemark

Per il governo del Regno di Danimarca

Voor de regering van het Koninkrijk Denemarken

Pelo Governo do Reino da Dinamarca

Tanskan kuningaskunnan hallituksen puolesta

För Konungariket Danmarks regering

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Por el Gobierno de la República Federal de Alemania

For Forbundsrepublikken Tysklands regering

Für die Regierung der Bundesrepublik Deutschland

Για την κυβέρνηση της Ομοσπονδιακής Δημοκρατίας της Γερμανίας

For the Government of the Federal Republic of Germany

Pour le gouvernement de la République fédérale d'Allemagne

Per il governo della Repubblica federale di Germania

Voor de regering van de Bondsrepubliek Duitsland

Pelo Governo da República Federal da Alemanha

Saksan liittotasavallan hallituksen puolesta

För Förbundsrepubliken Tysklands regering

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Por el Gobierno de la República Helénica

For Den Hellenske Republiks regering

Für die Regierung der Griechischen Republik

Για την κυβέρνηση της Ελληνικής Δημοκρατίας

For the Government of the Hellenic Republic

Pour le gouvernement de la République hellénique

Per il governo della Repubblica ellenica

Voor de regering van de Helleense Republiek

Pelo Governo da República Helénica

Helleenien tasavallan hallituksen puolesta

För Republiken Greklands regering

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Por el Gobierno del Reino de España

For Kongeriget Spaniens regering

Für die Regierung des Königreichs Spanien

Για την κυβέρνηση του Βασιλείου της Ισπανίας

For the Government of the Kingdom of Spain

Pour le gouvernement du Royaume d'Espagne

Per il governo del Regno di Spagna

Voor de regering van het Koninkrijk Spanje

Pelo Governo do Reino de Espanha

Espanjan kuningaskunnan hallituksen puolesta

För Konungariket Spaniens regering

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Por el Gobierno de Irlanda

For Irlands regering

Für die Regierung Irlands

Για την κυβέρνηση της Ιρλανδίας

For the Government of Ireland

Pour le gouvernement de l'Irlande

Per il governo delľ lrlanda

Voor de regering van Ierland

Pelo Governo da Irlanda

Irlannin hallituksen puolesta

För Irlands regering

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Por el Gobierno de la República Italiana

For Den Italienske Republiks regering

Für die Regierung der Italienischen Republik

Για την κυβέρνηση της Ιταλικής Δημοκρατίας

For the Government of the Italian Republic

Pour le gouvernement de la République italienne

Per il governo della Repubblica italiana

Voor de regering van de Italiaanse Republiek

Pelo Governo da República Italiana

Italian tasavallan hallituksen puolesta

För Republiken Italiens regering

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Por el Gobierno del Gran Ducado de Luxemburgo

For Storhertugdømmet Luxembourgs regering

Für die Regierung des Großherzogtums Luxemburg

Για την κυβέρνηση του Μεγάλου Δουκάτου του Λουξεμβούργου

For the Government of the Grand Duchy of Luxembourg

Pour le gouvernement du Grand-Duché de Luxembourg

Per il governo del Granducato di Lussemburgo

Voor de regering van het Groothertogdom Luxemburg

Pelo Governo do Grão-Ducado do Luxemburgo

Luxemburgin suurherttuakunnan hallituksen puolesta

För Storhertigdömet Luxemburgs regering

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Por el Gobierno del Reino de los Países Bajos

For Kongeriget Nederlandenes regering

Für die Regierung des Königreichs der Niederlande

Για την κυβέρνηση τον Βασιλείου των Κάτω Χωρών

For the Government of the Kingdom of the Netherlands

Pour le gouvernement du Royaume des Pays-Bas

Per il governo del Regno dei Paesi Bassi

Voor de regering van het Koninkrijk der Nederlanden

Pelo Governo do Reino dos Países Baixos

Alankomaiden kuningaskunnan hallituksen puolesta

För Konungariket Nederländernas regering

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Por el Gobierno de la República de Austria

For Republikken Østrigs regering

Für die Regierung der Republik Österreich

Για την κυβέρνηση της Δημοκρατίας της Αυστρίας

For the Government of the Republic of Austria

Pour Ie gouvernement de la République d'Autriche

Per il governo della Repubblica d'Austria

Voor de regering van de Republiek Oostenrijk

Pelo Governo da República da Austria

Itävallan tasavallan hallituksen puolesta

För Republiken Österrikes regering

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Por el Gobierno de la República Portuguesa

For Den Portugisiske Republiks regering

Für die Regierung der Portugiesischen Republik

Για την κυβέρνηση της Πορτογαλικής Δημοκρατίας

For the Government of the Portuguese Republic

Pour le gouvernement de la République portugaise

Per il governo della Repubblica portoghese

Voor de regering van de Portugese Republiek

Pelo Governo da República Portuguesa

Portugalin tasavallan hallituksen puolesta

För Republiken Portugals regering

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Por el Gobierno de la República de Finlandia

For Republikken Finlands regering

Für die Regierung der Republik Finnland

Για την κυβέρνηση της Φινλανδικής Δημοκρατίας

For the Government of the Republic of Finland

Pour le gouvernement de la République de Finlande

Per il governo della Repubblica di Finlandia

Voor de regering van de Republiek Finland

Pelo Governo da República da Finlândia

Suomen tasavallan hallituksen puolesta

För Republiken Finlands regering

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Por el Gobierno del Reino de Suecia

For Kongeriget Sveriges regering

Für die Regierung des Königreichs Schweden

Για την κυβέρνηση τον Βασιλείου της Σονηδίας

For the Government of the Kingdom of Sweden

Pour Ie gouvernement du Royaume de Suède

Per il governo del Regno di Svezia

Voor de regering van het Koninkrijk Zweden

Pelo Governo do Reino da Suécia

Ruotsin kuningaskunnan hallituksen puolesta

För Konungariket Sveriges regering

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Por la Comunidad Europea de la Energía Atómica

For Det Europæiske Atomenergifællesskab

Für die Europäische Atomgemeinschaft

Για την Ευρωπαϊκή Κοινότητα Ατομικής Ενέργειας

For the European Atomic Energy Community

Pour la Communauté européenne de l'énergie atomique

Per la Comunità europea dell'energia atomica

Voor de Europese Gemeenschap voor Atoomenergie

Pela Comunidade Europeia da Energia Atómica

Euroopan atomienergiayhteisön puolesta

För Europeiska atomenergigemenskapen

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Por el Organismo Internacional de Energía Atómica

For Den Internationale Atomenergiorganisation

Für die Internationale Atomenergie-Organisation

Για τον Διεθνή Οργανισμό Ατομικής Ενέργειας

For the International Atomic Energy Agency

Pour l'Agence internationale de l'énergie atomique

Per l'Agenzia internazionale dell'energia atomica

Voor de Internationale Organisatie voor Atoomenergie

Pela Agência Internacional da Energia Atómica

Kansainvälisen atomienergiajärjestön puolesta

För Internationella atomenergiorganet

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(1) On 8 June 1998, the Council approved the conclusion by the Commission on behalf of the European Atomic Energy Community (the Community) not only of this Additional Protocol to the Agreement between the 13 non-nuclear-weapon Member States of the Community, the Community and the IAEA (published in O] L 51 Volume 21, dated 22 February 1978 and as IAEA document INFCIRC/193, dated 14 September 1973) but also Additional Protocols to the Agreements between the United Kingdom of Great Britain and Northern Ireland, the Community and the IAEA (published as IAEA document INFCIRC/263, dated October 1978) and between France, the Community and the IAEA (published as IAEA document INFCIRC/290, dated December 1981). All three Additional Protocols were signed by the relevant Parties in Vienna on 22 September 1998. The texts of each Additional Protocol can be accessed at the following internet address:

http://europa.eu.int/en/comm/dg17/nuclearlnuchome.htm

ANNEX I

List of activities referred to in Article 2(a)(iv) of the Protocol

(i) The manufacture of

centrifuge rotor tubes

or the assembly of

gas centrifuges

Centrifuge rotor tubes

means thin-walled cylinders as described at point 5.1.1 (b) of Annex II.

Gas centrifuges

means centrifuges as described in the introductory note to point 5.1 of Annex II.

(ii) The manufacture of

diffusion barriers.

Diffusion barriers

means thin, porous filters as described in point 5.3.1 (a) of Annex II.

(iii) The manufacture or assembly of

laser-based systems

Laser-based systems

means systems incorporating those items as described in point 5.7 of Annex II.

(iv) The manufacture or assembly of

electromagnetic isotope separators

Electromagnetic isotope separators

means those items referred to in point 5.9.1 of Annex II containing ion sources as described in 5.9.1 (a) of Annex II.

(v) The manufacture or assembly of

columns

extraction equipment

Columns

extraction equipment

means those items as described in points 5.6.1, 5.6.2, 5.6.3, 5.6.5, 5.6.6, 5.6.7 and 5.6.8 of Annex II.

(vi) The manufacture of

aerodynamic separation nozzles or vortex tubes

Aerodynamic separation nozzles

vortex tubes

means separation nozzles and vortex tubes as described respectively in points 5.5.1 and 5.5.2 of Annex II.

(vii) The manufacture or assembly of

uranium plasma generation systems

Uranium plasma generation systems

means systems for the generation of uranium plasma as described in point 5.8.3 of Annex II.

(viii)

The manufacture of

zirconium tubes

Zirconium tubes

means tubes as described in point 1.6 of Annex II.

(ix) The manufacture or upgrading of

heavy water or deuterium

Heavy water or deuterium

means deuterium, heavy water (deuterium oxide) and any other deuterium compound in which the ratio of deuterium to hydrogen atoms exceeds 1:5 000.

(x) The manufacture of

nuclear grade graphite

Nuclear grade graphite

means graphite having a purity level better than five parts per million boron equivalent and with a density greater than 1,50 g/cm

(xi) The manufacture of

flasks for irradiated fuel

flask or irradiated fuel

means a vessel for the transportation and/or storage of irradiated fuel which provides chemical, thermal and radiological protection, and dissipated decay heat during handling, transportation and storage.

(xii) The manufacture of

reactor control rods

Reactor control rods

means rods as described in point 1.4 of Annex II.

(xiii)

The manufacture of

criticality safe tanks and vessels

Criticality safe tanks and vessels

means those items as described in points 3.2 and 3.4 of Annex II.

(xiv) The manufacture of

irradiated fuel element chopping machines

Irradiated fuel element chopping machines

means equipment as described in point 3.1 of Annex II.

(xv) The construction of

hot cells

Hot cells

means a cell or interconnected cells totalling at least 6 m

in volume with shielding equal to or greater than the equivalent of 0,5 m of concrete, with a density of 3,2 g/cm

or greater, outfitted with equipment for remote operations.

ANNEX II

List of specified equipment and non-nuclear material for the reporting of exports and imports according to Article 2(a)(ix)

1. REACTORS AND EQUIPMENT THEREFOR

1.1. Complete nuclear reactors

Nuclear reactors capable of operation so as to maintain a controlled self-sustaining fission chain reaction, excluding zero energy reactors, the latter being defined as reactors with a designed maximum rate of production of plutonium not exceeding 100 grams per year.

Explanatory note

A ‘nuclear reactor’ basically includes the items within or attached directly to the reactor vessel, the equipment which controls the level of power in the core, and the components which normally contain or come in direct contact with or control the primary coolant of the reactor core.

It is not intended to exclude reactors which could reasonably be capable of modification to produce significantly more than 100 grams of plutonium per year. Reactors designed for sustained operation at significant power levels, regardless of their capacity for plutonium production, are not considered as ‘zero energy reactors’.

1.2. Reactor pressure vessels

Metal vessels, as complete units or as major shop-fabricated parts therefor, which are especially designed or prepared to contain the core of a nuclear reactor as defined in paragraph 1.1 and are capable of withstanding the operating pressure of the primary coolant.

Explanatory note

A top plate for a reactor pressure vessel is covered by item 1.2 as a major shop-fabricated part of a pressure vessel.

Reactor internals (e.g. support columns and plates for the core and other vessel internals, control rod guide tubes, thermal shields, baffles, core grid plates, diffuser plates, etc.) are normally supplied by the reactor supplier. In some cases, certain internal support components are included in the fabrication of the pressure vessel. These items are sufficiently critical to the safety and reliability of the operation of the reactor (and, therefore, to the guarantees and liability of the reactor supplier), so that their supply, outside the basic supply arrangement for the reactor itself, would not be common practice. Therefore, although the separate supply of these unique, especially designed and prepared, critical, large and expensive items would not necessarily be considered as falling outside the area of concern, such a mode of supply is considered unlikely.

1.3. Reactor fuel charging and discharging machines

Manipulative equipment especially designed or prepared for inserting or removing fuel in a nuclear reactor as defined in paragraph 1.1 capable of on-load operation or employing technically sophisticated positioning or alignment features to allow complex off-load fuelling operations such as those in which direct viewing of or access to the fuel is not normally available.

1.4. Reactor control rods

Rods especially designed or prepared for the control of the reaction rate in a nuclear reactor as defined in paragraph 1.1.

Explanatory note

This item includes, in addition to the neutron absorbing part, the support or suspension structures therefor is supplied separately.

1.5. Reactor pressure tubes

Tubes which are especially designed or prepared to contain fuel elements and the primary coolant in a reactor as defined in paragraph 1.1 at an operating pressure in excess of 5,1 MPa (740 psi).

1.6. Zirconium tubes

Zirconium metal and alloys in the form of tubes or assemblies of tubes, and in quantities exceeding 500 kg in any period of 12 months, especially designed or prepared for use in a reactor as defined in paragraph 1.1, and in which the relation of hafnium to zirconium is less than 1:500 parts by weight.

1.7. Primary coolant pumps

Pumps especially designed or prepared for circulating the primary coolant for nuclear reactors as defined in paragraph 1.1.

Explanatory note

Especially designed or prepared pumps may include elaborate sealed or multisealed systems to prevent leakage of primary coolant, canned-driven pumps, and pumps with inertial mass systems. This definition encompasses pumps certified to NC-1 or equivalent standards.

2. NON-NUCLEAR MATERIALS FOR REACTORS

2.1. Deuterium and heavy water

Deuterium, heavy water (deuterium oxide) and any other deuterium compound in which the ratio of deuterium to hydrogen atoms exceeds 1:5000 for use in a nuclear reactor as defined in paragraph 1.1 in quantities exceeding 200 kg of deuterium atoms for any one recipient country in any period of 12 months.

2.2. Nuclear grade graphite

Graphite having a purity level better than 5 parts per million boron equivalent and with a density greater than 1,50 g/cm

for use in a nuclear reactor as defined in paragraph 1.1 in quantities exceeding 3 x 10

kg (30 tonnes) for any one recipient country in any period of 12 months.

Note

For the purpose of reporting, the government will determine whether or not the exports of graphite meeting the above specifications are for nuclear reactor use.

3. PLANTS FOR THE REPROCESSING OF IRRADIATED FUEL ELEMENTS, AND EQUIPMENT ESPECIALLY DESIGNED OR PREPARED THEREFOR

Introductory note

Reprocessing irradiated nuclear fuel separates plutonium and uranium from intensely radioactive fission products and other transuranic elements. Different technical processes can accomplish this separation. However, over the years purex has become the most commonly used and accepted process. Purex involves the dissolution of irradiated nuclear fuel in nitric acid, followed by separation of the uranium, plutonium, and fission products by solvent extraction using a mixture of tributyl phosphate in an organic diluent.

Purex facilities have process functions similar to each other, including: irradiated fuel element chopping, fuel dissolution, solvent extraction, and process liquor storage. There may also be equipment for thermal denitration of uranium nitrate, conversion of plutonium nitrate to oxide or metal, and treatment of fission product waste liquor to a form suitable for long term storage or disposal. However, the specific type and configuration of the equipment performing these functions may differ between purex facilities for several reasons, including the type and quantity of irradiated nuclear fuel to be reprocessed and the intended disposition of the recovered materials, and the safety and maintenance philosophy incorporated into the design of the facility.

A ‘plant for the reprocessing of irradiated fuel elements’ included the equipment and components which normally come in direct contact with and directly control the irradiated fuel and the major nuclear material and fission product processing streams.

These processes, including the complete systems for plutonium conversion and plutonium metal production, may be identified by the measures taken to avoid criticality (e.g. by geometry), radiation exposure (e.g. by shielding), and toxicity hazards (e.g. by containment).

Items of equipment that are considered to fall within the meaning of the phrase ‘and equipment especially designed or prepared’ for the reprocessing of irradiated fuel elements include:

3.1. Irradiated fuel element chopping machines

Introductory note

This equipment breaches the cladding of the fuel to expose the irradiated nuclear material to dissolution. Especially designed metal cutting shears are the most commonly employed, although advanced equipment, such as lasers, may be used.

Remotely operated equipment especially designed or prepared for use in a reprocessing plant as identified above and intended to cut, chop or shear irradiated nuclear fuel assemblies, bundles or rods.

3.2. Dissolvers

Introductory note

Dissolvers normally receive the chopped-up spent fuel. In these critically safe vessels, the irradiated nuclear material is dissolved in nitric acid and the remaining hulls removed from the process stream.

Critically safe tanks (e.g. small diameter, annular or slab tanks) especially designed or prepared for use in a reprocessing plant as identified above, intended for dissolution of irradiated nuclear fuel and which are capable of withstanding hot, highly corrosive liquid, and which can be remotely loaded and maintained.

3.3. Solvent extractors and solvent extraction equipment

Introductory note

Solvent extractors both receive the solution of irradiated fuel from the dissolvers and the organic solution which separates the uranium, plutonium, and fission products. Solvent extraction equipment is normally designed to meet strict operating parameters, such as long operating lifetimes with no maintenance requirements or adaptability to easy replacement, simplicity of operation and control, and flexibility for variations in process conditions.

Especially designed or prepared solvent extractors such as packed or pulse columns, mixer settlers or centrifugal contactors for use in a plant for the reprocessing of irradiated fuel. Solvent extractors must be resistant to the corrosive effect of nitric acid. Solvent extractors are normally fabricated to extremely high standards (including special welding and inspection and quality assurance and quality control techniques) out of low carbon stainless steels, titanium, zirconium, or other high quality materials.

3.4. Chemical holding or storage vessels

Introductory note

Three main process liquor streams result from the solvent extraction step. Holding or storage vessels are used in the further processing of all three streams, as follows:

(a) the pure uranium nitrate solution is concentrated by evaporation and passed to a denitration process where it is converted to uranium oxide. This oxide is reused in the nuclear fuel cycle;

(b) the intensely radioactive fission products solution is normally concentrated by evaporation and stored as a liquor concentrate. This concentrate may be subsequently evaporated and converted to a form suitable for storage or disposal;

(c) the pure plutonium nitrate solution is concentrated and stored pending its transfer to further process steps. In particular, holding or storage vessels for plutonium solutions are designed to avoid criticality problems resulting from changes in concentration and form of this stream.

Especially designed or prepared holding or storage vessels for use in a plant for the reprocessing of irradiated fuel. The holding or storage vessels must be resistant to the corrosive effect of nitric acid. The holding or storage vessels are normally fabricated of materials such as low carbon stainless steels, titanium or zirconium, or other high quality materials. Holding or storage vessels may be designed for remote operation and maintenance and may have the following features for control of nuclear criticality:

(1) walls or internal structures with a boron equivalent of at least 2 %, or

(2) a maximum diameter of 175 mm (7") for cylindrical vessels, or

(3) a maximum width of 75 mm (3") for either a slab or annular vessel.

3.5. Plutonium nitrate to oxide conversion system

Introductory note

In most reprocessing facilities, this final process involves the conversion of the plutonium nitrate solution to plutonium dioxide. The main functions involved in this process are: process feed storage and adjustment, precipitation and solid/liquor separation, calcination, product handling, ventilation, waste management, and process control.

Complete systems especially designed or prepared for the conversion of plutonium nitrate to plutonium oxide, in particular adapted so as to avoid criticality and radiation effects and to minimise toxicity hazards.

3.6. Plutonium oxide to metal production system

Introductory note

This process, which could be related to a reprocessing facility, involves the fluorination of plutonium dioxide, normally with highly corrosive hydrogen fluoride, to produce plutonium fluoride which is subsequently reduced using high purity calcium metal to produce metallic plutonium and a calcium fluoride slag. The main functions involved in this process are: fluorination (e.g. involving equipment fabricated or lined with a precious metal), metal reduction (e.g. employing ceramic crucibles), slag recovery, product handling, ventilation, waste management and process control.

Complete systems especially designed or prepared for the production of plutonium metal, in particular adapted so as to avoid criticality and radiation effects and to minimise toxicity hazards.

4. PLANTS FOR THE FABRICATION OF FUEL ELEMENTS

A ‘plant for the fabrication of fuel elements’ includes the equipment:

(a) which normally comes in direct contact with, or directly processes, or controls, the production flow of nuclear material, or

(b) which seals the nuclear material within the cladding.

5. PLANTS FOR THE SEPARATION OF ISOTOPES OF URANIUM AND EQUIPMENT, OTHER THAN ANALYTICAL INSTRUMENTS, ESPECIALLY DESIGNED OR PREPARED THEREFOR

Items of equipment that are considered to fall within the meaning of the phrase ‘equipment, other than analytical instruments, especially designed or prepared’ for the separation of isotopes of uranium include:

5.1. Gas centrifuges and assemblies and components especially designed or prepared for use in gas centrifuges

Introductory note

The gas centrifuge normally consists of a thin-walled cylinder(s) of between 75 mm (3") and 400 mm (16") diameter contained in a vacuum environment and spun at high peripheral speed of the order of 300 m/s or more with its central axis vertical. In order to achieve high speed the materials of construction for the rotating components have to be of a high strength to density ratio and the rotor assembly, and hence its individual components, have to be manufactured to very close tolerances in order to minimise the imbalance. In contrast to other centrifuges, the gas centrifuge for uranium enrichment is characterised by having within the rotor chamber a rotating disc-shaped baffle(s) and a stationary tube arrangement for feeding and extracting to UF

gas and featuring at least three separate channels, of which two are connected to scoops extending from the rotor axis towards the periphery of the rotor chamber. Also contained within the vacuum environment are a number of critical items which do not rotate and which although they are especially designed are not difficult to fabricate nor are they fabricated out of unique materials. A centrifuge facility however requires a large number of these components, so that quantities can provide an important indication of end use.

5.1.1. Rotating components

(a) Complete rotor assemblies

Thin-walled cylinders, or a number of interconnected thin-walled cylinders, manufactured from one or more of the high strength to density ratio materials described in the explanatory note to this section. If interconnected, the cylinders are joined together by flexible bellows or rings as described in Section 5.1.1.(c) following. The rotor is fitted with an internal baffle(s) and end caps, as described in Section 5.1.1.(d) and (e) following, if in final form. However the complete assembly may be delivered only partly assembled.

(b) Rotor tubes

Especially designed or prepared thin-walled cylinders with thickness of 12 mm (0,5") or less, a diameter of between 75 mm (3") and 400 mm (16"), and manufactured from one or more of the high strength to density ratio materials described in the explanatory note to this section.

(c) Rings or bellows

Components especially designed or prepared to give localised support to the rotor tube or to join together a number of rotor tubes. The bellows is a short cylinder of wall thickness 3 mm (0,12") or less, a diameter of between 75 mm (3") and 400 m (16"), having a convolute, and manufactured from one of the high strength to density ratio materials described in the explanatory note to this section.

(d) Baffles

Disc-shaped components of between 75 mm (3") and 400 m (16") diameter especially designed or prepared to be mounted inside the centrifuge rotor tube, in order to isolate the take-off chamber from the main separation chamber and, in some cases, to assist the UF

gas circulation within the main separation chamber of the rotor tube, and manufactured from one of the high strength to density ratio materials described in the explanatory note to this section.

(e) Top caps/bottom caps

Disc-shaped components of between 75 mm (3") and 400 (16") diameter especially designed or prepared to fit to the ends of the rotor tube, and so contain the UF

within the rotor tube, and in some cases to support, retain or contain as an integrated part an element of the upper bearing (top cap) or to carry the rotating elements of the motor and lower bearing (bottom cap), and manufactured from one of the high strength to density ratio materials described in the explanatory note to this section.

Explanatory note

The materials used for centrifuge rotating components are:

(a) maraging steel capable of an ultimate tensile strength of 2,05 x 10

N/m

(300 000 psi) or more,

(b) aluminium alloys capable of an ultimate tensile strength of 0,46 x 10

N/m

(67 000 psi) or more,

m or greater and a specific ultimate tensile strength of 0,3 x 10

m or greater (‘Specific Modulus’ is the Young's Modulus in N/m

divided by the specific weight in N/m

; ‘Specific Ultimate Tensile Strength’ is the ultimate tensile strength in N/m

divided by the specific weight in N/m

5.1.2. Static components

(a) Magnetic suspension bearings

Especially designed or prepared bearing assemblies consisting of an annular magnet suspended within a housing containing a damping medium. The housing will be manufactured from a UF

-resistant material (see explanatory note to Section 5.2). The magnet couples with a pole piece or a second magnet fitted to the top cap described in Section 5.1.1.(e). The magnet may be ring-shaped with a relation between outer and inner diameter smaller or equal to 1,6:1. The magnet may be in a form having an initial permeability of 0,15 H/m (120 000 in CGS units) or more, or a remanence of 98,5 % or more, or an energy product of greater than 80 kj/m

(10

gauss-oersteds). In addition to the usual material properties, it is a prerequisite that the deviation of the magnetic axes from the geometrical axes is limited to very small tolerances (lower than 0,1 mm or 0,004 in) or that homogeneity of the material of the magnet is specially called for.

(b) Bearings/dampers

Especially designed or prepared bearings comprising a pivot/cup assembly mounted on a damper. The pivot is normally a hardened steel shaft with a hemisphere at one end with a means of attachment to the bottom cap described in section 5.1.1.(e) at the other. The shaft may however have a hydrodynamic bearing attached. The cup is pellet-shaped with a hemispherical indentation in one surface. These components are often supplied separately to the damper.

(c) Molecular pumps

Especially designed or prepared cylinders having internally machined or extruded helical grooves and internally machines bores. Typical dimensions are as follows: 75 mm (3") to 400 mm (16") internal diameter, 10 mm (0,4") or more wall thickness, with the length equal to or greater than the diameter. The grooves are typically rectangular in cross-section and 2 mm (0,08") or more in depth.

(d) Motor stators

Especially designed or prepared ring-shaped stators for high speed multiphase AC hysteresis (or reluctance) motors for synchronous operation within a vacuufn in the frequency range of 600-2 000 Hz and a power range of 50-1 000 VA. The stators consist of multiphase windings on a laminated low loss iron core comprised of thin layers typically 2,0 mm (0,08") thick or less.

(e) Centrifuge housing/recipients

Components especially designed designed or prepared to contain the rotor tube assembly of a gas centrifuge. The housing consists of a rigid cylinder of wall thickness up to 30 mm (1,2") with precision machined ends to locate the bearings and with one or more flanges for mounting. The machined ends are parallel to each other and perpendicular to the cylinder's longitudinal axis to within 0,05

or less. The housing may also be a honeycomb type structure to accommodate several rotor tubes. The housings are made of or protected by materials resistant to corrosion by UF

(f) Scoops

Especially designed or prepared tubes up to 12 mm (0,5") internal diameter for the extraction of UF

gas from within the rotor tube by a pilot tube action (that is, with an aperture facing into the circumferential gas flow within the rotor tube, for example by bending the end of a radially disposed tube) and capable of being fixed to the central gas extraction system. The tubes are made of or protected by materials resistant to corrosion by UF

5.2. Especially designed or prepared auxiliary systems, equipment and components for gas centrifuge enrichment plants

Introductory note

The auxiliary systems, equipment and components for a gas centrifuge enrichment plant are the systems of plant needed to feed UF

to the centrifuges, to link the individual centrifuges to each other to form cascades (or stages) to allow for progressively higher enrichments and to extract the ‘product’ and ‘tails’ UF

from the centrifuges, together with the equipment required to drive the centrifuges or to control the plant.

Normally UF

is evaporated from the solid using heated autoclaves and is distributed in gaseous form to the centrifuges by way of cascade header pipework. The ‘product’ and ‘tails’ UF

gaseous streams flowing from the centrifuges are also passed by way of cascade header pipework to cold traps (operating at about 203 K (-70

C)) where they are condensed prior to onward transfer into suitable containers for transportation or storage. Because an enrichment plant consists of many thousands of centrifuges arranged in cascades there are many kilometres of cascade header pipework, incorporating thousands of welds with a substantial amount of repetition of layout. The equipment, components and piping systems are fabricated to very high vacuum and cleanliness standards.

5.2.1. Feed systems/product and tails withdrawal systems

Especially designed or prepared process systems including:

— feed autoclaves (or stations), used for passing UFg to the centrifuge cascades at up to 100 kPa (15 psi) and at a rate of 1 kg/h or more,

— desublimers (or cold traps) used to remove UF

from the cascades at up to 3 kPa (0,5 psi) pressure. The desublimers are capable of being chilled to 203 K (-70

C) and heated to 343 K (70

C),

— ‘product’ and ‘tails’ stations used for trapping UF

into containers.

This plant, equipment and pipework is wholly made of or lined with UF

-resistant materials (see explanatory note to this section) and is fabricated to very high vacuum and cleanliness standards.

5.2.2. Machine header piping systems

Especially designed or prepared piping systems and header systems for handling UF

within the centrifuge cascades. The piping network is normally of the ‘triple’ header system with each centrifuge connected to each of the headers. There is thus a substantial amount of repetition in its form. It is wholly made of UF

-resistant materials (see explanatory note to this section) and is fabricated to very high vacuum and cleanliness standards.

5.2.3. UF

6 mass spectrometers/ion sources

Especially designed designed or prepared magnetic or quadrupole mass spectrometers capable of taking ‘on-line’ samples of feed, product or tails, from UF

gas streams and having all of the following characteristics:

unit resolution for atomic mass unit greater than 320;

ion sources constructed of or lined with nichrome or monel or nickel plated;

electron bombardment ionisation sources;

having a collector system suitable for isotopic analysis.

5.2.4. Frequency changers

Frequency changers (also known as converters or invertors) especially designed or prepared to supply motor stators as defined under 5.1.2(d), or parts, components and subassemblies of such frequency changers having all of the following characteristics:

a multiphase output of 600 to 2 000 Hz;

high stability (with frequency control better than 0,1 %);

low harmonic distortion (less than 2 %), and

an efficiency of greater than 80 %.

Explanatory note

The items listed above either come into direct contact with the UF

process gas or directly control the centrifuges and the passage of the gas from centrifuge to centrifuge and cascade to cascade.

Materials resistant to corrosion by UF

include stainless steel, aluminium, aluminium alloys, nickel or alloys containing 60 % or more nickel.

5.3. Especially designed or prepared assemblies and components for use in gaseous diffusion enrichment

Introductory note

In the gaseous diffusion method of uranium isotope separation, the main technological assembly is a special porous gaseous diffusion barrier, heat exchanger for cooling the gas (which is heated by the process of compression), seal valves and control valves, and pipelines. Inasmuch as gaseous diffusion technology uses uranium hexafluoride (UF

), all equipment, pipeline and instrumentation surfaces (that come in contact with the gas) must be made of materials that remain stable in contact with UF

. A gaseous diffusion facility requires a number of these assemblies, so that quantities can provide an important indication of end use.

5.3.1. Gaseous diffusion barriers

(a) Especially designed or prepared thin, porous filters, with a pore size of 100-1 000 A (angstroms), a thickness of 5 mm (0,2") or less, and for tubular forms, a diameter of 25 mm (1") or less, made of metallic, polymer or ceramic materials resistant to corrosion by UF

, and

(b) especially prepared compounds or powders for the manufacture of such filters. Such compounds and powders include nickel or alloys containing 60 % or more nickel, aluminium oxide, or UF

-resistant fully fluorinated hydrocarbon polymers having a purity of 99,9 % or more, a particle size less than 10 microns, and a high degree of particle size uniformity, which are especially prepared for the manufacture of gaseous diffusion barriers.

5.3.2. Diffuser housings

Especially designed or prepared hermetically sealed cylindrical vessels greater than 300 mm (12") in diameter and greater than 900 mm (35") in length, or rectangular vessels of comparable dimensions, which have an inlet connection and two outlet connections all of which are greater than 50 mm (2") in diameter, for containing the gaseous diffusion barrier, made of or lined with UF

-resistant materials and designed for horizontal or vertical installation.

5.3.3. Compressors and gas blowers

Especially designed or prepared axial, centrifugal, or positive displacement compressors, or gas blowers with a suction volume capacity of 1 m

/min. or more of UF

and with a discharge pressure of up to several hundred kPa (100 psi), designed for long-term operation in the UF

environment with or without an electrical motor of appropriate power, as well as separate assemblies of such compressors and gas blowers. These compressors and gas blowers have a pressure ratio between 2:1 and 6:1 and are made of, or lined with, materials resistant to UF

5.3.4. Rotary shaft seals

Especially designed or prepared vacuum seals, with seal feed and seal exhaust connections, for sealing the shaft connecting the compressor or the gas blower rotor with the driver motor so as to ensure a reliable seal against in-leaking of air into the inner chamber of the compressor or gas blower which is filled with UF

Such seals are normally designed for a buffer gas in-leakage rate of less than 1 000 cm

/min (60 in

/min).

5.3.5. Heat exchangers for cooling UF

6

Especially designed or prepared heat exchangers made of or lined with UF

-resistant materials (except stainless steel) or with copper or any combination of those metals, and intended for a leakage pressure change rate of less than 10 Pa (0,0015 psi) per hour under a pressure difference of 100 kPa (15 psi).

5.4. Especially designed or prepared auxiliary systems, equipment and components for use in gaseous diffusion enrichment

Introductory note

The auxiliary systems, equipment and components for gaseous diffusion enrichment plants are the systems of plant needed to feed UF

to the gaseous diffusion assembly, to link the individual assemblies to each other to form cascades (or stages) to allow for progressively higher enrichments and to extract the ‘product’ and ‘tails’ UF

from the diffusion cascades. Because of the high inertial properties of diffusion cascades, any interruption in their operation, and especially their shutdown, leads to serious consequences. Therefore, a strict and constant maintenance of vacuum in all technological systems, automatic protection from accidents, and precise automated regulation of the gas flow is of importance in a gaseous diffusion plant. All this leads to a need to equip the plant with a large number of special measuring, regulating and controlling systems.

Normally UF

is evaporated from cylinders placed within autoclaves and is distributed in gaseous form to the entry point by way of cascade header pipework. The ‘product’ and ‘tails’ UF

gaseous streams flowing from exit points are passed by way of cascade header pipework to either cold traps or to compression stations where the UF

gas is liquefied prior to onward transfer into suitable containers for transportation or storage. Because a gaseous diffusion enrichment plant consists of a large number of gaseous diffusion assemblies arranged in cascades, there are many kilometres of cascade header pipework, incorporating thousands of welds with substantial amounts of repetition of layout. The equipment, components and piping systems are fabricated to very high vacuum and cleanliness standards.

5.4.1. Feed systems/product and tails withdrawal systems

Especially designed or prepared process systems, capable of operating at pressures of 300 kPa (45 psi) or less, including:

— feed autoclaves (or systems), used for passing UF

to the gaseous diffusion cascades,

— desublimers (or cold traps) used to remove UF

from diffusion cascades,

— liquefaction stations where UF

gas from the cascade is compressed and cooled to form liquid UF

— ‘product’ or ‘tails’ stations used for transferring UF

into containers.

5.4.2. Header piping systems

Especially designed or prepared piping systems and header systems for handling UF

within the gaseous diffusion cascades. This piping network is normally of the ‘double’ header system with each cell connected to each of the headers.

5.4.3. Vacuum systems

(a) Especially designed or prepared large vacuum manifolds, vacuum headers and vacuum pumps having a suction capacity of 5 m

/min. (175 ft

/min.) or more.

(b) Vacuum pumps especially designed for service in UF

-bearing atmospheres made of, or lined with, aluminium, nickel, or alloys bearing more than 60 % nickel. These pumps may be either rotary or positive, may have displacement and fluorocarbon seals, and may have special working fluids present.

5.4.4. Special shut-off and control valves

Especially designed or prepared manual or automated shut-off and control bellows valves made of UF

-resistant materials with a diameter of 40 to 1 500 mm (1,5 to 59") for installation in main and auxiliary systems of gaseous diffusion enrichment plants.

5.4.5. UF

6 mass spectrometers/ion sources

Especially designed or prepared magnetic or quadrupole mass spectrometers capable of taking on-line samples of feed, product or tails, from UF

gas streams and having all of the following characteristics:

unit resolution for atomic mass unit greater than 320;

ion sources constructed of or lined with nichrome or monel or nickel plated;

Electron bombardment ionisation sources;

collector system suitable for isotopic analysis.

Explanatory note

The items listed above either come into direct contact with the UF

process gas or directly control the flow within the cascade. All surfaces which come into contact with the process gas are wholly made of, or lined with, UF

-resistant materials. For the purposes of the sections relating to gaseous diffusion items the materials resistant to corrosion by UF

include stainless steel, aluminium, aluminium alloys, aluminium oxide, nickel or alloys containing 60 % or more nickel and UF

-resistant fully fluorinated hydrocarbon polymers.

5.5. Especially designed or prepared systems, equipment and components for use in aerodynamic enrichment plants

Introductory note

In aerodynamic enrichment processes, a mixture of gaseous UF

and light gas (hydrogen of helium) is compressed and then passed through separating elements wherein isotopic separation is accomplished by the generation of high centrifugal forces over a curved-wall geometry. Two processes of this type have been successfully developed: the separation nozzle process and the vortex tube process. For both processes the main components of a separation stage include cylindrical vessels housing the special separation elements (nozzles or vortex tubes), gas compressors and heat exchangers to remove the heat of compression. An aerodynamic plant requires a number of these stages, so that quantities can provide an important indication of end use. Since aerodynamic processes use UF

all equipment, pipeline and instrumentation surfaces (that come in contact with the gas) must be made of materials that remain stable in contact with UF

Explanatory note

The items listed in this section either come into direct contact with the UF

process gas or directly control the flow within the cascade. All surfaces which come into contact with the process gas are wholly made of or protected by UF

-resistant materials. For the purpose of the section relating to aerodynamic enrichments items, the materials resistant to corrosion by UF

include copper, stainless steel, aluminium, aluminium alloys, nickel or alloys containing 60 % or more nickel and UF

-resistant fully fluorinated hydrocarbon polymers.

5.5.1. Separation nozzles

Especially designed or prepared separation nozzles and assemblies thereof. The separation nozzles consist of slit-shaped, curved channels having a radius of curvature less than 1 mm (typically 0,1 to 0,05 mm), resistant to corrosion by UF

and having a knife-edge within the nozzle that separates the gas flowing through the nozzle into two fractions.

5.5.2. Vortex tubes

Especially designed or prepared vortex tubes and assemblies thereof. The vortex tubes are cylindrical or tapered, made of or protected by materials resistant to corrosion by UF

, having a diameter of between 0,5 cm and 4 cm, a length to diameter ratio of 20:1 or less and with one or more tangential inlets. The tubes may be equipped with nozzle-type appendages at either or both ends.

Explanatory note

The feed gas enters the vortex tube tangentially at one end or through swirl vanes or at numerous tangential positions along the periphery of the tube.

5.5.3. Compressors and gas blowers

Especially designed or prepared axial, centrifugal or positive displacement compressors or gas blowers made of or protected by materials resistant to corrosion by UF

and with a suction volume capacity of 2 m

/min. or more of UF

/carrier gas (hydrogen or helium) mixture.

Explanatory note

These compressors and gas blowers typically have a pressure ratio between 1.2:1 and 6:1.

5.5.4. Rotary shaft seals

Especially designed or prepared rotary shaft seals, with seal feed and seal exhaust connections, for sealing the shaft connecting the compressor rotor or the gas blower rotor with the driver motor so as to ensure a reliable seal against out-leakage of process gas or in-leakage of air or seal gas into the inner chamber of the compressor or gas blower which is filled with a UF

/carrier gas mixture.

5.5.5. Heat exchangers for gas cooling

Especially designed or prepared heat exchangers made of or protected by materials resistant to corrosion by UF

5.5.6. Separation element housings

Especially designed or prepared separation element housings, made of or protected by materials resistant to corrosion by UF

, for containing vortex tubes or separation nozzles.

Explanatory note

These housings may be cylindrical vessels greater than 300 mm in diameter and greater than 900 mm in length, or may be rectangular vessels of comparable dimensions, and may be designed for horizontal or vertical installation.

5.5.7. Feed systems/product and tails withdrawal systems

Especially designed or prepared process systems or equipment for enrichment plants made of or protected by materials resistant to corrosion by UF

, including:

(a) feed autoclaves, ovens, or systems used for passing UF

to the enrichment process;

(b) desublimers (or cold traps) used to remove UF

from the enrichment process for subsequent transfer upon heating;

from the enrichment process by compressing and converting UF

to a liquid or solid form;

(d) ‘product’ or ‘tails’ stations used for transferring UF

into containers.

5.5.8. Header piping systems

Especially designed or prepared header piping systems, made of or protected by materials resistant to corrosion by UF

for handling UF

within the aerodynamic cascades. This piping network is normally of the ‘double’ header design with each stage or group of stages connected to each of the headers.

5.5.9. Vacuum systems and pumps

(a) Especially designed or prepared vacuum systems having a suction capacity of 5 m

/min or more, consisting of vacuum manifolds, vacuum headers and vacuum pumps, and designed for service in UF

-bearing atmospheres.

(b) Vacuum pumps especially designed or prepared for service in UF

-bearing atmospheres and made of or protected by materials resistant to corrosion by UF

. These pumps may use fluorocarbon seals and special working fluids.

5.5.10. Special shut-off and control valves

Especially designed or prepared manual or automated shut-off and control bellows valves made of or protected by materials resistant to corrosion by UF

with a diameter of 40 to 1 500 mm for installation in main and auxiliary systems of aerodynamic enrichment plants.

5.5.11. UF

6 mass spectrometers/ion sources

Especially designed or prepared magnetic or quadrupole mass spectrometers capable of taking ‘on-line’ samples of feed, ‘product’ or ‘tails’, from UF

gas streams and having all of the following characteristics:

unit resolution for mass greater than 320;

ion sources constructed of or lined with nichrome or monel or nickel plated;

electron bombardment ionisation sources;

collector system suitable for isotopic analysis.

5.5.12. UF

6 / carrier gas separation systems

Especially designed or prepared systems for separating UF

from carrier gas (hydrogen or helium).

Explanatory note

These systems are designed to reduce the UF

content in the carrier gas to 1 ppm or less and many incorporate equipment such as:

(a) cryogenic heat exchangers and cryoseparators capable of temperatures of -120

c or less, or

(b) cryogenic refrigeration units capable of temperatures of -120

C or less, or

from carrier gas, or

(d) UF

cold traps capable of temperatures of -20

C or less.

5.6. Especially designed or prepared systems, equipment and components for use in chemical exchange or ion exchange enrichment plants

Introductory note

The slight difference in mass between the isotopes of uranium causes small changes in chemical reaction equilibria that can be used as a basis for separation of the isotopes. Two processes have been successfully developed: liquid-liquid chemical exchange and solid-liquid ion exchange.

In the liquid-liquid chemical exchange process, immiscible liquid phases (aqueous and organic) are countercurrently contacted to give the cascading effect of thousands of separation stages. The aqueous phase consists of uranium chloride in hydrochloric acid solution; the organic phase consists of an extractant containing uranium chloride in an organic solvent. The contactors employed in the separation cascade can be liquid-liquid exchange columns (such as pulsed columns with sieve plates) or liquid centrifugal contactors. Chemical conversions (oxidation and reduction) are required at both ends of the separation cascade in order to provide for the reflux requirements at each end. A major design concern is to avoid contamination of the process streams with certain metal ions. Plastic, plastic-lined (including use of fluorocarbon polymers) and/or glass-lined columns and piping are therefore used.

In the solid-liquid ion-exchange process, enrichment is accomplished by uranium adsorption/desorption on a special, very fast-acting, ion-exchange resin or adsorbent. A solution of uranium in hydrochloric acid and other chemical agents is passed through cylindrical enrichment columns containing packed beds of the adsorbent. For a continuous process, a reflux system is necessary to release the uranium from the adsorbent back into the liquid flow so that ‘product’ and ‘tails’ can be collected. This is accomplished with the use of suitable reduction/oxidation chemical agents that are fully regenerated in separate external circuits and that may be partially regenerated within the isotopic separation columns themselves. The presence of hot concentrated hydrochloric acid solutions in the process requires that the equipment be made of or protected by special corrosion-resistant materials.

5.6.1. Liquid-liquid exchange columns (chemical exchange)

Countercurrent liquid-liquid exchange columns having mechanical power input (i.e., pulsed columns with sieve plates, reciprocating plate columns, and columns with internal turbine mixers), especially designed or prepared for uranium enrichment using the chemical exchange process. For corrosion resistance to concentrated hydrochloric acid solutions, these columns and their internals are made of or protected by suitable plastic materials (such as fluorocarbon polymers) or glass. The stage residence time of the columns is designed to be short (30 seconds or less).

5.6.2. Liquid-liquid centrifugal contactors (chemical exchange)

Liquid-liquid centrifugal contactors especially designed or prepared for uranium enrichment using the chemical exchange process. Such contactors use rotation to achieve dispersion of the organic and aqueous streams and then centrifugal force to separate the phases. For corrosion resistance to concentrated hydrochloric acid solutions, the contactors are made of or are lined with suitable plastic materials (such as fluorocarbon polymers) or are lined with glass. The stage residence time of the centrifugal contactors is designed to be short (30 seconds or less).

5.6.3. Uranium reduction systems and equipment (chemical exchange)

(a) Especially designed or prepared electrochemical reduction cells to reduce uranium from one valence state to another for uranium enrichment using the chemical exchange process. The cell materials in contact with process solutions must be corrosion resistant to concentrated hydrochloric acid solutions.

Explanatory note

The cell cathodic compartment must be designed to prevent reoxidation of uranium to its higher valence state. To keep the uranium in the cathodic compartment, the cell may have an impervious diaphragm membrane constructed of special cation exchange material. The cathode consists of a suitable solid conductor such as graphite.

(b) Especially designed or prepared systems at the product end of the cascade for taking the U

out of the organic stream, adjusting the acid concentration and feeding to the electrochemical reduction cells.

Explanatory note

These systems consist of solvent extraction equipment for stripping the U

from the organic stream into an aqueous solution, evaporation and/or other equipment to accomplish solution pH adjustment and control, and pumps or other transfer devices for feeding to the electrochemical reduction cells. A major design concern is to avoid contamination of the aqueous stream with certain metal ions. Consequently, for those parts in contact with the process stream, the system is constructed of equipment made of or protected by suitable materials (such as glass, fluorocarbon polymers, polyphenyl sulfate, polyether sulfone, and resin-impregnated graphite).

5.6.4. Feed preparation systems (chemical exchange)

Especially designed or prepared systems for producing high-purity uranium chloride feed solutions for chemical exchange uranium isotope separation plants.

Explanatory note

These systems consist of dissolution, solvent extraction and/or ion exchange equipment for purification and electrolytic cells for reducing the uranium U

or U

to U

. These systems produce uranium chloride solutions having only a few parts per million of metallic impurities such as chromium, iron, vanadium, molybdenum and other bivalent or higher multi-valent cations. Materials of construction for portions of the systems processing high-purity U

include glass, fluorocarbon polymers, polyphenyl sulfate or polyether sulfone plastic-lined and resin-impregnated graphite.

5.6.5. Uranium oxidation systems (chemical exchange)

Especially designed or prepared systems for oxidation of U

to U

for return to the uranium isotope separation cascade in the chemical exchange enrichment process.

Explanatory note

These systems may incorporate equipment such as:

(a) equipment for contacting chlorine and oxygen with the aqueous effluent from the isotope separation equipment and extracting the resultant U

into the stripped organic stream returning from the product end of the cascade,

(b) equipment that separates water from hydrochloric acid so that the water and the concentrated hydrochloric acid may be reintroduced to the process at the proper locations.

5.6.6. Fast-reacting ion exchange resins/adsorbents (ion exchange)

Fast-reacting ion-exchange resins or adsorbents especially designed or prepared for uranium enrichment using the ion exchange process, including porous macroreticular resins, and/or pellicular structures in which the active chemical exchange groups are limited to a coating on the surface of an inactive porous support structure, and other composite structures in any suitable form including particles or fibres. These ion exchange resins/adsorbents have diameters of 0,2 mm or less and must be chemically resistant to concentrated hydrochloric acid solutions as well as physically strong enough so as not to degrade in the exchange columns. The resins/adsorbents are especially designed to achieve very fast uranium isotope exchange kinetics (exchange rate half-time of less than 10 seconds) and are capable of operating at a temperature in the range of 100

C to 200

5.6.7. Ion exchange columns (ion exchange)

Cylindrical columns greater than 1 000 mm in diameter for containing and supporting packed beds of ion exchange resin/adsorbent, especially designed or prepared for uranium enrichment using the ion exchange process. These columns are made of or protected by materials (such as titanium or fluorocarbon plastics) resistant to corrosion by concentrated hydrochloric acid solutions and are capable of operating at a temperature in the range of 100

C to 200

C and pressures above 0,7 MPa (102 psia).

5.6.8. Ion exchange reflux systems (ion exchange)

(a) Especially designed or prepared chemical or electrochemical reduction systems for regeneration of the chemical reducing agent(s) used in ion exchange uranium enrichment cascades.

(b) Especially designed or prepared chemical or electrochemical oxidation systems for regeneration of the chemical oxidising agent(s) used in ion exchange uranium enrichment cascades.

Explanatory note

The ion exchange enrichment process may use, for example, trivalent titanium (Ti

) as a reducing cation in which case the reduction system would regenerate Ti

by reducing Ti

. The process may use, for example, trivalent iron (Fe

) as an oxidant in which case the oxidation system would regenerate Fe

by oxidising Fe

5.7. Expecially designed or prepared systems, equipment and components for use in laser-based enrichment plants

Introductory note

Present systems for enrichment processes using lasers fall into two categories: those in which the process medium is atomic uranium vapour and those in which the process medium is the vapour of a uranium compound. Common nomenclature for such processes include: first category, atomic vapour laser isotope separation (AVLIS or SILVA); second category, molecular laser isotope separation (MLIS or MOLIS) and chemical reaction by isotope selective laser activation (CRISLA). The systems, equipment and components for laser enrichment plants embrace:

(a) devices to feed uranium-metal vapour (for selective photo-ionisation) or devices to feed the vapour of a uranium compound (for photo-dissociation or chemical activation);

(b) devices to collect enriched and depleted uranium metal as ‘product’ and ‘tails’ in the first category, and devices to collect dissociated or reacted compounds as ‘product’ and unaffected material as ‘tails’ in the second category;

(d) feed preparation and product conversion equipment. The complexity of the spectroscopy of uranium atoms and compounds may require incorporation of any of a number of available laser technologies.

Explanatory note

Many of the items listed in this section come into direct contact with uranium metal vapour or liquid or with process gas consisting of UF

or a mixture of UF

and other gases. All surfaces that come into contact with the uranium or UF

are wholly made of or protected by corrosion-resistant materials. For the purposes of the section relating to laser-based enrichment items, the materials resistant to corrosion by the vapour or liquid of uranium metal or uranium alloys include yttria-coated graphite and tantalum; and the materials resistant to corrosion by UF

include copper, stainless steel, aluminium, aluminium alloys, nickel or alloys containing 60 % or more nickel and UF

-resistant fully fluorinated hydrocarbon polymers.

5.7.1. Uranium vaporisation systems (AVLIS)

Especially designed or prepared uranium vaporisation systems which contain high-power strip or scanning electron beam guns with a delivered power on the target of more than 2,5 kW/cm.

5.7.2. Liquid uranium metal handling systems (AVLIS)

Especially designed or prepared liquid metal handling systems for molten uranium or uranium alloys, consisting of crucibles and cooling equipment for the crucibles.

Explanatory note

The crucibles and other parts of this system that come into contact with molten uranium and uranium alloys are made of or protected by materials of suitable corrosion and heat resistance. Suitable materials include tantalum, yttria-coated graphite, graphite coated with other rare earth oxides or mixtures thereof.

5.7.3. Uranium metal ‘product’ and ‘tails’ collector assemblies (AVLIS)

Especially designed or prepared ‘ product ’ and ‘ tails ’ collector assemblies for uranium metal in liquid or solid form.

Explanatory note

Components for these assemblies are made of or protected by materials resistant to the heat and corrosion of uranium metal vapour or liquid (such as yttria-coated graphite or tantalum) and may include pipes, valves, fittings, ‘gutters’, feed-throughs, heat exchangers and collector plates for magnetic, electrostatic or other separation methods.

5.7.4. Separator module housings (AVLIS)

Especially designed or prepared cylindrical or rectangular vessels for containing the uranium metal vapour source, the electron beam gun, and the ‘ product’ and ‘ tails’ collectors.

Explanatory note

These housings have multiplicity of ports for electrical and water feed-throughs, laser beam windows, vacuum pump connections and instrumentation diagnostics and monitoring. They have provisions for opening and closure to allow refurbishment of internal components.

5.7.5. Supersonic expansion nozzles (MLIS)

Especially designed or prepared supersonic expansion nozzles for cooling mixtures of UF

and carrier gas to 150 K or less and which are corrosion resistant to UF

5.7.6. Uranium pentafluoride product collectors (MLIS)

Especially designed or prepared uranium pentafluoride (UF

) solid product collectors consisting of filter, impact, or cyclone-type collectors, or combinations thereof, and which are corrosion resistant to the UF

/UF

environment.

5.7.7. UF

6 /carrier gas compressors (MLIS)

Especially designed or prepared compressors for UF

/carrier gas mixtures, designed for long term operation in a UF

environment. The components of these compressors that come into contact with process gas are made of or protected by materials resistant to corrosion by UF

5.7.8. Rotary shaft seals (MLIS)

Especially designed or prepared rotary shaft seals, with seal feed and seal exhaust connections, for sealing the shaft connecting the compressor rotor with the driver motor so as to ensure a reliable seal against out-leakage of process gas or in-leakage of air or seal gas into the inner chamber of the compressor which is filled with a UF

/carrier gas mixture.

5.7.9. Fluorination systems (MLIS)

Especially designed or prepared systems for fluorinating UF

(solid) to UF

(gas).

Explanatory note

These systems are designed to fluorinate the collected UF

powder to UF

for subsequent collection in product containers or for transfer as feed to MLIS units for additional enrichment. In one approach, the fluorination reaction may be accomplished within the isotope separation system to react and recover directly off the ‘product’ collectors. In another approach, the UF

powder may be removed/transferred from the ‘product’ collectors into a suitable reaction vessel (e.g., fluidised-bed reactor, screw reactor or flame tower) for fluorination. In both approaches, equipment for storage and transfer of fluorine (or other suitable fluorinating agents) and for collection and transfer of UF

are used.

5.7.10. UF

6 mass spectrometers/ion sources (MLIS)

Especially designed or prepared magnetic or quadrupole mass spectrometers capable of taking ‘on-line’ samples of feed, ‘product’ or ‘tails’, from UF

gas streams and having all of the following characteristics:

unit resolution for mass greater than 320;

ion sources constructed of or lined with nichrome or monel or nickel plated;

electron bombardment ionisation sources;

collector system suitable for isotopic analysis.

5.7.11. Feed systems/product and tails withdrawal systems (MLIS)

Especially designed or prepared process systems or equipment for enrichment plants made of or protected by materials resistant to corrosion by UF

, including:

(a) feed autoclaves, ovens, or systems used for passing UF

to the enrichment process;

(b) desublimers (or cold traps) used to remove UF

from the enrichment process for subsequent transfer upon heating;

from the enrichment process by compressing and converting UF

to a liquid or solid form;

(d) ‘product’ or ‘tails’ stations used for transferring UF

into containers.

5.7.12. UF

6 /carrier gas separation systems (MLIS)

Especially designed or prepared process systems for separating UF

from carrier gas. The carrier gas may be nitrogen, argon, or other as.

Explanatory note

These systems may incorporate equipment such as:

(a) cryogenic heat exchangers or cryoseparators capable of temperatures of -120

C or less, or

(b) cryogenic refrigeration units capable of temperatures of -120

C or less, or

cold traps capable of temperatures of -20

C or less.

5.7.13. Laser systems (AVLIS, MLIS and CRISLA)

Lasers or laser systems especially designed or prepared for the separation of uranium isotopes.

Explanatory note

The laser system for the AVLIS process usually consists of two lasers: a copper vapour laser and a dye laser. The laser system for MLIS usually consists of a CO

or excimer laser and a multipass optical cell with revolving mirrors at both ends. Lasers or laser systems for both processes require a spectrum frequency stabiliser for operation over extended periods of time.

5.8. Especially designed or prepared systems, equipment and components for use in plasma separation enrichment plants

Introductory note

In the plasma separation process, a plasma of uranium ions passes through an electric field tuned to the U-235 ion resonance frequency so that they preferentially absorb energy and increase the diameter of their corkscrew-like orbits. Ions with a large-diameter path are trapped to produce a product enriched in U-235. The plasma, which is made by ionising uranium vapour, is contained in a vacuum chamber with a high-strength magnetic field produced by a superconducting magnet. The main technological systems of the process include the uranium plasma generation system, the separator module with superconducting magnet and metal removal systems for the collection of ‘product’ and ‘tails’.

5.8.1. Microwave power sources and antennae

Especially designed or prepared microwave power sources and antennae for producing or accelerating ions and having the following characteristics: greater than 30 GHz frequency and greater than 50 kW mean power output for ion production.

5.8.2. Ion excitation coils

Especially designed or prepared radio frequency ion excitation coils for frequencies of more than 100 kHz and capable of handling more than 40 kW mean power.

5.8.3. Uranium plasma generation systems

Especially designed or prepared systems for the generation of uranium plasma, which may contain high-power strip or scanning electron beam guns with a delivered power on the target of more than 2,5 kW/cm.

5.8.4. Liquid uranium metal handling systems

Especially designed or prepared liquid metal handling systems for molten uranium or uranium alloys, consisting of crucibles and cooling equipment for the crucibles.

Explanatory note

The crucibles and other parts of this system that come into contact with molten uranium or uranium alloys are made of or protected by materials of suitable corrosion and heat resistance. Suitable materials include tantalum, yttria-coated graphite, graphite coated with other rare earth oxides or mixtures thereof.

5.8.5. Uranium metal ‘product’ and ‘tails’ collector assemblies

Especially designed or prepared ‘ product’ and ‘ tails’ collector assemblies for uranium metal in solid form. These collector assemblies are made of or protected by materials resistant to the heat and corrosion of uranium metal vapour, such as yttria-coated graphite or tantalum.

5.8.6. Separator module housings

Cylindrical vessels especially designed or prepared for use in plasma separation enrichment plants for containing the uranium plasma source, radio-frequency drive coil and the ‘product’ and ‘tail’ collectors.

Explanatory note

These housings have a multiplicity of ports for electrical feed-throughs, diffusion pump connections and instrumentation diagnostics and monitoring. They have provisions for opening and closure to allow for refurbishment of internal components and are constructed of a suitable non-magnetic material such as stainless steel.

5.9. Especially designed or prepared systems, equipment and components for use in electromagnetic enrichment plants

Introductory note

In the electromagnetic process, uranium metal ions produced by ionisation of a salt feed material (typically UCl

) are accelerated and passed through a magnetic field that has the effect of causing the ions of different isotopes to follow different paths. The major components of an electromagnetic isotope separator include: a magnetic field for ion-beam diversion/separation of the isotopes, an ion source with its acceleration system, and a collection system for the separated ions. Auxiliary systems for the process include the magnet power supply system, the ion source high-voltage power supply system, the vacuum system, and extensive chemical handling systems for recovery of product and cleaning/recycling of components.

5.9.1. Electromagnetic isotope separators

Electromagnetic isotope separators, especially designed or prepared for the separation of uranium isotopes, and equipment and components therefor, including:

(a) ion sources

Especially designed or prepared single or multiple uranium ion sources consisting of a vapour source, ioniser, and beam accelerator, constructed of suitable materials such as graphite, stainless steel, or copper, and capable of providing a total ion beam current of 50 mA or greater;

(b) ion collectors

Collector plates consisting of two or more slits and pockets especially designed or prepared for collection of enriched and depleted uranium ion beams and constructed of suitable materials such as graphite or stainless steel;

(c) vacuum housings

Especially designed or prepared vacuum housings for uranium electromagnetic separators, constructed of suitable non-magnetic materials such as stainless steel and designed for operation at pressures of 0,1 Pa or lower;

Explanatory note

The housings are specially designed to contain the ion sources, collector plates and water-cooled liners and have provision for diffusion pump connections and opening and closure for removal and reinstallation of these components.

(d) Magnet pole pieces

Especially designed or prepared magnet pole pieces having a diameter greater than 2 m used to maintain a constant magnetic field within a electromagnetic isotope separator and to transfer the magnetic field between adjoining separators.

5.9.2. High voltage power supplies

Especially designed or prepared high-voltage power supplies for ion sources, having all of the following characteristics: capable of continuous operation, output voltage of 20 000 V or greater, output current of 1 A or greater, and voltage regulation of better than 0,01 % over a period of eight hours.

5.9.3. Magnet power supplies

Especially designed or prepared high-power, direct current magnet power supplies having all of the following characteristics: capable of continuously producing a current output of 500 A or greater at a voltage of 100 V or greater and with a current or voltage regulation better than 0,01 % over a period of 8 hours.

6. PLANTS FOR THE PRODUCTION OF HEAVY WATER, DEUTERIUM AND DEUTERIUM COMPOUNDS AND EQUIPMENT ESPECIALLY DESIGNED OR PREPARED THEREFOR

Introductory note

Heavy water can be produced by a variety of processes. However, the two processes that have proven to be commercially viable are the water-hydrogen sulphide exchange process (GS process) and the ammonia-hydrogen exchange process.

The GS process is based upon the exchange of hydrogen an deuterium between water and hydrogen sulphide within a series of towers which are operated with the top section cold and the bottom section hot. Water flows down the towers while the hydrogen sulphide gas circulates from the bottom to the top of the towers. A series of perforated trays are used to promote mixing between the gas and the water. Deuterium migrates to the water at low temperatures and to the hydrogen sulphide at high temperatures. Gas or water, enriched in deuterium, is removed from the first stage towers at the junction of the hot and cold sections and the process is repeated in subsequent stage towers. The product of the last stage, water enriched up to 30 % in deuterium, is sent to a distillation unit to produce reactor grade heavy water, i.e., 99,75 % deuterium oxide.

The ammonia-hydrogen exchange process can extract deuterium from synthesis gas through contact with liquid ammonia in the presence of a catalyst. The synthesis gas is fed into exchange towers and to an ammonia converter. Inside the towers the gas flows from the bottom to the top while the liquid ammonia flows from the top to the bottom. The deuterium is stripped from the hydrogen in the synthesis gas and concentrated in the ammonia. The ammonia then flows into an ammonia cracker at the bottom of the tower while the gas flows into an ammonia converter at the top. Further enrichment takes place in subsequent stages and reactor grade heavy water is produced through final distillation. The synthesis gas feed can be provided by an ammonia plant that, in turn, can be constructed in association with a heavy water ammonia-hydrogen exchange plant. The ammonia-hydrogen exchange process can also use ordinary water as a feed source of deuterium.

Many of the key equipment items for heavy water production plants using GS or the ammonia-hydrogen exchange processes are common to several segments of the chemical and petroleum industries. This is particularly so for small plants using the GS process. However, few of the items are available ‘off-the shelf ’. The GS and ammonia-hydrogen processes require the handling of large quantities of flammable, corrosive and toxic fluids at elevated pressures. Accordingly, in establishing the design and operating standards for plants and equipment using these processes, careful attention to the materials selection and specifications is required to ensure long service life with high safety and reliability factors. The choice of scale is primarily a function of economics and need. Thus, most of the equipment items would be prepared according to the requirements of the customer.

Finally, it should be noted that, in both the GS and the ammonia-hydrogen exchange processes, items of equipment which individually are not especially designed or prepared for heavy water production can be assembled into systems which are especially designed or prepared for producing heavy water. The catalyst production system used in the ammonia-hydrogen exchange process and water distillation systems used for the final concentration of heavy water to reactor-grade in either process are examples of such systems.

The items of equipment which are especially designed or prepared for the production of heavy water utilising either the water-hydrogen sulphide exchange process or the ammonia-hydrogen exchange process include the following:

6.1. Water — hydrogen sulphide exchange towers

Exchange towers fabricated from fine carbon steel (such as ASTM A516) with diameters of 6 m (20') to 9 m (39'), capable of operating at pressures greater than or equal to 2 MPa (300 psi) and with a corrosion allowance of 6 mm or greater, especially designed or prepared for heavy water production utilising the water-hydrogen sulphide exchange process.

6.2. Blowers and compressors

Single stage, low head (i.e., 0,2 MPa or 30 psi) centrifugal blowers or compressors for hydrogen-sulphide gas circulation (i.e., gas containing more than 70 % H

S) especially designed or prepared for heavy water production utilising the water-hydrogen sulphide exchange process. These blowers or compressors have a throughput capacity greater than or equal to 56 m

/second (120,000 SCFM) while operating at pressures greater than or equal to 1,8 MPa (260 psi) suction and have seals designed for wet H

S service.

6.3. Ammonia-hydrogen exchange towers

Ammonia-hydrogen exchange towers greater than or equal to 35 m (114,3' in height with diameters of 1,5 m (4,9' to 2,5 m (8,2') capable of operating at pressures greater than 15 MPa (2225 psi) especially designed or prepared for heavy water production utilising the ammonia-hydrogen exchange process. These towers also have at least one flanged axial opening of the same diameter as the cylindrical part through which the tower internals can be inserted or withdrawn.

6.4. Tower internals and stage pumps

Tower internals and stage pumps especially designed or prepared for towers for heavy water production utilising the ammonia-hydrogen exchange process. Tower internals include especially designed stage contactors which promote intimate gas/liquid contact. Stage pumps include especially designed submersible pumps for circulation of liquid ammonia within a contacting stage internal to the stage towers.

6.5. Ammonia crackers

Ammonia crackers with operating pressures greater than or equal to 3 MPa (450 psi) especially designed or prepared for heavy water production utilising the ammonia-hydrogen exchange process.

6.6. Infrared absorption analysers

Infrared absorption analysers capable of on-line hydrogen/deuterium ratio analysis where deuterium concentrations are equal to or greater than 90 %.

6.7. Catalytic burners

Catalytic burners for the conversion of enriched deuterium gas into heavy water especially designed or prepared for heavy water production utilising the ammonia-hydrogen exchange process.

7. PLANTS FOR THE CONVERSION OF URANIUM AND EQUIPMENT ESPECIALLY DESIGNED OR PREPARED THEREFOR

Introductory note

Uranium conversion plants and systems may perform one or more transformations from one uranium chemical species to another, including: conversion of uranium ore concentrates to UO

, conversion of UO

to UO

, conversion of uranium oxides to UF

or UF

, conversion of UF

to UF

, conversion of UF

to UF

, conversion of UF

to uranium metal, and conversion of uranium fluorides to UO

Many of the key equipment items for uranium conversion plants are common to several segments of the chemical process industry. For example, the types of equipment employed in these processes may include: furnaces, rotary kilns, fluidised bed reactors, flame tower reactors, liquid centrifuges, distillation columns and liquid-liquid extraction columns. However, few of the items are available ‘off-the-shelf ’, most would be prepared according to the requirements and specifications of the customer. In some instances, special design and construction considerations are required to address the corrosive properties of some of the chemicals handled (HF, F

, CIF

, and uranium fluorides). Finally, it should be noted that, in all of the uranium conversion processes, items of equipment which individually are not especially designed or prepared for uranium conversion can be assembled into systems which are especially designed or prepared for use in uranium conversion.

7.1. Especially designed or prepared systems for the conversion of uranium ore concentrates to UO

3

Explanatory note

Conversion of uranium ore concentrates to UO

can be performed by first dissolving the ore in nitric acid and extracting purified uranyl nitrate using a solvent such as tributyl phosphate. Next, the uranyl nitrate is converted to UO

either by concentration and denitration or by neutralization with gaseous ammonia to produce ammonium diuranate with subsequent filtering, drying, and calcining.

7.2. Especially designed or prepared systems for the conversion of UO

3 to UF

6

Explanatory note

Conversion of UO

to UF

can be performed directly by fluorination. The process requires a source of fluorine gas or chlorine trifluoride.

7.3. Especially designed or prepared systems for the conversion of UO

3 to UO

2

Explanatory note

Conversion of UO

to UO

can be performed through reduction of UO

with cracked ammonia gas or hydrogen.

7.4. Especially designed or prepared systems for the conversion of UO

2 to UF

4

Explanatory note

Conversion of UO

to UF

can be performed by reacting UO

with hydrogen fluoride gas (HF) at 300-500

7.5. Especially designed or prepared systems for the conversion of UF

4 to UF

6

Explanatory note

Conversion of UF

to UF

is performed by exothermic reaction with fluorine in a tower reactor. UF

is condensed from the hot effluent gases by passing the effluent stream through a cold trap cooled to -10

C. The process requires a source of fluorine gas.

7.6. Especially designed or prepared systems for the conversion of UF

4 to U metal

Explanatory note

Conversion UF

to U metal is performed by reduction with magnesium (large batches) or calcium (small batches). The reaction is carried out at temperatures above the melting point of uranium (1 130

C).

7.7. Especially designed or prepared systems for the conversion of UF

6 to UO

2

Explanatory note

Conversion of UF

to UO

can be performed by one of three processes. In the first, UF

is reduced and hydrolysed to UO

using hydrogen and steam. In the second, UF

is hydrolysed by solution in water, ammonia is added to precipitate ammonium diuranate, and the diuranate is reduced to UO

with hydrogen at 820

C. In the third process, gaseous UF

, CO

and NH

are combined in water, precipitating ammonium uranyl carbonate. The ammonium aranyl carbonate is combined with steam and hydrogen at 500-600

C to yield UO

to UO

conversion is often performed as the first stage of a fuel fabrication plant.

7.8. Especially designed or prepared systems for the conversion of UF

6 to UF

4

Explanatory note

Conversion of UF

to UF

is performed by reduction with hydrogen.

ANNEX III

To the extent that the measures in this Protocol involve nuclear material declared by the Community and without prejudice to Article 1 of this Protocol, the Agency and the Community shall cooperate to facilitate implementation of those measures and shall avoid unnecessary duplication of activities.

The Community shall provide the Agency with information relating to transfers, for both nuclear and non-nuclear purposes, from each State to another Member State of the Community and to such transfers to each State from another Member State of the Community that corresponds to the information to be provided under Article 2 (a)(vi)(b) and under Article 2(a)(vi)(c) in relation to exports and imports of source material which has not reached the composition and purity suitable for fuel fabrication or for being isotopically enriched.

Each State shall provide the Agency with information relating to transfers to or from another Member State of the Community that corresponds to the information on specified equipment and non-nuclear material listed in Annex II of this Protocol to be provided under Article 2(a)(ix)(a) in relation to exports and, on specific request of the Agency, under Article 2(a)(ix)(b) in relation to imports.

With regard to the Community's Joint Research Centre, the Community shall also implement the measures which this Protocol sets out for States, as appropriate in close collaboration with the State on whose territory an establishment of the centre is located.

The Liaison Committee, established under Article 25(a) of the Protocol referred to in Article 26 of the Safeguards Agreement, will be extended in order to allow for participation by representatives of the States and adjustment to the new circumstances resulting from this Protocol.

For the sole purposes of the implementation of this Protocol, and without prejudice to the respective competences and responsibilities of the Community and its Member States, each State which decides to entrust to the Commission of the European Communities implementation of certain provisions which under this Protocol are the responsibility of the States, shall so inform the other Parties to the Protocol through a side letter. The Commission of the European Communities shall inform the other Parties to the Protocol of its acceptance of any such decisions.