WO1987000088A1 - Process for the selective separation of a copper molybdenum ore - Google Patents
Process for the selective separation of a copper molybdenum ore Download PDFInfo
- Publication number
- WO1987000088A1 WO1987000088A1 PCT/US1986/001467 US8601467W WO8700088A1 WO 1987000088 A1 WO1987000088 A1 WO 1987000088A1 US 8601467 W US8601467 W US 8601467W WO 8700088 A1 WO8700088 A1 WO 8700088A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- copper
- molybdenum
- ore
- primary
- concentrate
- Prior art date
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03B—SEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
- B03B1/00—Conditioning for facilitating separation by altering physical properties of the matter to be treated
- B03B1/04—Conditioning for facilitating separation by altering physical properties of the matter to be treated by additives
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/02—Froth-flotation processes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/02—Froth-flotation processes
- B03D1/06—Froth-flotation processes differential
Definitions
- the present invention relates to an improved process for the selective separation of the components of a copper molybdenum (Mo--Cu) ore by flotation. More particularly, the present invention relates to a process for such separation conducted at a natural pH (i.e. without addition of alkalies (such as lime) or.acids in amounts sufficient to substantially modify the pH) and without the addition of a copper collector in the primary flotation circuit, which leads to the recovery of a primary Mo-Cu concentrate.
- a natural pH i.e. without addition of alkalies (such as lime) or.acids in amounts sufficient to substantially modify the pH
- alkalies such as lime
- acids in amounts sufficient to substantially modify the pH
- One object of the present invention is to provide a process for the separation by flotation of the components of a copper ore (with molybdenum as a by-product) by flotation. This process affords a convenient, inexpensive, and efficient method of molybdenum recovery at an acceptable grade.
- Another object of this invention is to provide a pro ⁇ cess for such separation, which can be conducted at a natural pH and avoids use of lime and other pH modifiers.
- Another object of this invention is to provide a pro ⁇ cess for such separation which avoids use of substantial amounts of depressant for copper minerals.
- Another object of this invention is to provide a pro ⁇ cess or such separation that avoids use of a copper collector i_ * the primary flotation circuit.
- Another object of this invention is to achieve the recovery in the primary flotation circuit of a concentrate substantially enriched in molybdenum which, because of its enhanced molybdenum content, can be further separated into a molybdenum concentrate with less reagents and in a substantial ⁇ ly smaller number of cleaning stages, and which affords sub ⁇ stantially enhanced recovery of the molybdenum mineral initial ⁇ ly contained in the ore.
- the copper content of this primary flotation circuit after the cleaning stages, can be diverted to the copper circuits. Hence, the overall copper recovery of the system is not jeopardized.
- the present invention is directed to a process for th separation of the mineral components of an ore, said ore com ⁇ prising minerals selected from the group consisting of base metal sulfides, including copper and molybdenum sulfides as well as pyrite, said process comprising:
- Fig. 1 is a flowsheet of a copper-molybdenum ore sep ration scheme by flotation in accordance with the present in vention.
- Fig. 2 is a water-balance flowsheet for a copper- molybdenum flotation process, as it is typically practiced in the Southwestern United States where water is in short supply. Detailed Description of the Invention
- copper ore with associated molybdenum values from a mine is crushed and ground to the required particle size to form the flotation fee and ore pulp.
- Preflotation conditioning of the ore may be conducted during or after the wet grinding stage and is comple ted before the first flotation stage. Preconditioning is marked as 1 in Fig. 1. According to the present invention, t only preconditioning that may be necessary at this stage woul require addition of very small amounts of redox agents, such a sodium sulfide, hydrogen peroxide, etc. , or aeration. Combine contributions from ore mineralization, degree of surface oj .da tion and water chemistry (unless modified) can result in vary ⁇ ing degrees of copper and iron sulfide mineral recovery along with the molybdenite, in the primary molybdenum rougher stage.
- redox agents such as sodium sulfide, hydrogen peroxide, etc.
- Preflotation conditioning of the ore, with specific reagents, conducted during or after the grinding stage, may be necessar to prevent or minimize this recovery of copper and iron sul ⁇ fides.
- the reagents used may be of reducing characteristics, such as hypochlorites, peroxides or atmospheric air. The amounts required are just sufficient to prevent or minimi _ ** t aforesaid recovery of copper and iron sulfides along with' he molybdenite during the primary molybdenite flotation stage.
- the amount of the redox reagent, or the extei-t o aeration is preferably just sufficient to prevent or minimiz copper sulfide and pyrite flotation, without affecting molyb ⁇ denite flotation, and does not affect the pH.
- no lime or other pH modifiers are adde (or, if added, lime is in extremely small amounts compared wi the conventional lime circuits and only for protective alkali nity, i.e. to prevent equipment corrosion) .
- No copper collector is added in the primary molybdenite flotation circuit.
- a small amount of a hydrocarbon oil is added as a moly-collector, at 2 in Fig. 1, along with a frother.
- Suitable hydrocarbon oils include vapor oil, diesel oil, fuel oil, etc.
- the hydrocarbon will contain as little wax fraction as possible.
- the primary flotation circuit produces a rougher molyb ⁇ denum concentrate containing some copper and a non-float.
- This concentrate which is substantially enriched in moly as compared to conventional circuits, is then reground if necessary and directed to cleaner stages which lead to the production of a final molybdenum concentrate.
- the cleaner stage simplification and cost savings achieved by the present invention are also substantial.
- the non-float of the primary circuit is directed to a copper flotation circuit.
- the non-float contains some of the copper and the remaining non-floating minerals. Copper col ⁇ lector is added at 3 in Fig. 1.
- Whether an oxidation/reduction agent is added or not depends in large measure on the natu ⁇ ral oxidation/reduction conditions of the ore and the water used in the flotation process.
- the copper rougher concentrate is typically directed to regrind and cleaner operations, resulting in production of a final copper concentrate, a final tailings product, and possi ⁇ bly a secondary molybdenum concentr?te.
- This latter concen ⁇ trate when produced, represents a small proportion of the total moly content of the original ore, because of the effi ⁇ ciency of the present primary flotation circuit in recovering molybdenite.
- This secondary molybdenum concentrate may be recycled to the primary molybdenum circuit, or to the molyb ⁇ denum cleaner circuit, depending on the molybdenum assay.
- Further separation of the scavenger concentrate may require addition of a small amount of an oxidation/reduction agent sufficient to minimize pyrite flotation.
- the process of the present invention does not need to employ cyanide.
- Aeration is advantageously used instead of (or in addi tion to) a redox additive to control the redox potential of th pulp.
- Aeration can be used at 1 in the primary flotation cir ⁇ cuit, or at 4 in the first scavenger circuit.
- Advantages of the present process include simplifica ⁇ tion of the flotation scheme and savings in all reagents, in ⁇ cluding those resulting from the omission of lime and the mini mal — if any — addition of a redox agent, and also in frothe and collector consumption.
- Suitable molybdenum-copper ores for practice of the present process include-copper-molybdenum sulfide ores which contain chalcopyrite and chalcocite.
- the present process is particularly suited for ore separation in plants where the water is recycled.
- t present process can be advantageously introduced in separatio plants where a major portion of the water is reclaimed as il ⁇ lustrated in Fig. 2 (Prio ' r Art) . This is so because the addi tion of reagents (including- collector and redox reagent, if any) is so minimal the? ⁇ ⁇ "-_they do not accumulate in the reclaim water.
- Fig. 2 app oximately 60% of the water in the syst is reclaimed after flotation of a rougher concentrate, 4. Additional water is reclaimed from the non-float scavenger circuit, 2. All reclaimed water is combined at 3.
- Example 1 The invention is further illustrated below by referen to specific examples. However, the scope of the present inve tion is not limited to these examples.
- Example 1 The invention is further illustrated below by referen to specific examples. However, the scope of the present inve tion is not limited to these examples.
- T electrochemical potential was measured and found to be +40 in the first conditioning stage, during aeration, and in the rougher concentrate flotation step, and +50 in the first sca ⁇ venger flotation step.
- the pH was 7.5 during aeration, 7.8 during conditioning, 8.0 during flotation of the primary con ⁇ centrate and 8.2 during flotation of the secondary concentrat.
- the ore was ground for 6 min. and only frother (2 dro of MIBC) was added.
- Fuel oil (6 drops) was added in a first conditioning stage (1 min.) and the pulp was aerated for two min. No sodium sulfide or other redox reagent was added.
- T rougher concentrate was floated (3 min.) and the non-float w conditioned (2 min.) with the addition of 2 drops of copper collector.
- the first scavenger concentrate was floated (4 min.) and the non-float was conditioned for 2 minutes with 1 .
Abstract
Description
Claims
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
BR8606758A BR8606758A (en) | 1985-07-09 | 1986-07-09 | PROCESS TO SEPARATE MINERAL COMPONENTS FROM A MINERY |
DE8686905004T DE3688591T2 (en) | 1985-07-09 | 1986-07-09 | METHOD FOR SELECTIVELY SEPARATING COPPER MOLYBENE ORE. |
AT86905004T ATE90592T1 (en) | 1985-07-09 | 1986-07-09 | PROCESS FOR SELECTIVE SEPARATION OF COPPER-MOLYBIDIUM ORE. |
FI870999A FI80835C (en) | 1985-07-09 | 1987-03-06 | FOERFARANDE FOER SELEKTIV ANRIKNING AV KOPPARMOLYBDENMALM. |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US75318185A | 1985-07-09 | 1985-07-09 | |
US753,181 | 1985-07-09 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1987000088A1 true WO1987000088A1 (en) | 1987-01-15 |
Family
ID=25029518
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US1986/001467 WO1987000088A1 (en) | 1985-07-09 | 1986-07-09 | Process for the selective separation of a copper molybdenum ore |
Country Status (8)
Country | Link |
---|---|
EP (1) | EP0229835B1 (en) |
JP (1) | JPS63500577A (en) |
AT (1) | ATE90592T1 (en) |
AU (2) | AU6191386A (en) |
BR (1) | BR8606758A (en) |
DE (1) | DE3688591T2 (en) |
FI (1) | FI80835C (en) |
WO (1) | WO1987000088A1 (en) |
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5068028A (en) * | 1990-01-21 | 1991-11-26 | University Of Utah | Molybdenite flotation from copper sulfide/molybdenite containing materials by ozone conditioning |
US5110455A (en) * | 1990-12-13 | 1992-05-05 | Cyprus Minerals Company | Method for achieving enhanced copper flotation concentrate grade by oxidation and flotation |
CN102259050A (en) * | 2010-08-23 | 2011-11-30 | 鞍钢集团矿业公司 | Novel middling treatment process for reverse flotation operation |
CN102671769A (en) * | 2012-05-14 | 2012-09-19 | 长沙矿冶研究院有限责任公司 | Beneficiation method for flotation and recovery of molybdenum from easy-floating gangue refractory molybdenum ore |
CN102773152A (en) * | 2012-07-13 | 2012-11-14 | 四川领航石墨制品有限公司 | Fine flaky-cryptocrystalline mixed graphite separation technique |
US8413816B2 (en) | 2010-02-16 | 2013-04-09 | Nalco Company | Sulfide flotation aid |
CN103128004A (en) * | 2013-01-07 | 2013-06-05 | 湖南有色金属研究院 | Method for flotation and separation of copper molybdenum sulphide bulk concentrates |
CN103386356A (en) * | 2012-05-09 | 2013-11-13 | 中国瑞林工程技术有限公司 | Flotation method for copper sulphide ore |
CN106378262A (en) * | 2016-12-07 | 2017-02-08 | 广西大学 | Method for recycling powethite from molybdenite tailings |
US9839917B2 (en) | 2013-07-19 | 2017-12-12 | Evonik Degussa Gmbh | Method for recovering a copper sulfide concentrate from an ore containing an iron sulfide |
US10413914B2 (en) | 2012-01-27 | 2019-09-17 | Evonik Degussa Gmbh | Enrichment of metal sulfide ores by oxidant assisted froth flotation |
Families Citing this family (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101927213A (en) * | 2009-06-26 | 2010-12-29 | 西北有色金属研究院 | Flotation separation method for molybdenite and galena |
CN102228870B (en) * | 2011-05-26 | 2013-09-04 | 山东梁邹矿业集团有限公司 | Method for improving copper-molybdenum separating flotation index through combined use of chemical agents |
CN102302981B (en) * | 2011-09-21 | 2013-06-12 | 紫金矿业集团股份有限公司 | Beneficiation reagent and method for separating copper-molybdenum mixed concentrates |
CN104128263A (en) * | 2014-07-11 | 2014-11-05 | 北京矿冶研究总院 | Inhibitor for talc and serpentine and beneficiation method using inhibitor |
CN105665146B (en) * | 2016-03-04 | 2018-06-01 | 中南大学 | A kind of method for improving the Rutile Flotation rate of recovery |
CN106238214B (en) * | 2016-08-10 | 2018-05-15 | 金堆城钼业股份有限公司 | A kind of molybdenum concntrate decarbonization process |
CN106583026B (en) * | 2016-10-31 | 2019-11-26 | 江苏旌凯中科超导高技术有限公司 | A kind of floating magnetic joint separation of copper-molybdenum-separation method |
CN107790291B (en) * | 2017-09-30 | 2019-08-27 | 紫金矿业集团股份有限公司 | The floatation process of comprehensive recovery of gold sulphur from copper tailing |
Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2316743A (en) * | 1939-11-09 | 1943-04-13 | American Cyanamid Co | Flotation of molybdenite |
US2559104A (en) * | 1948-03-23 | 1951-07-03 | Phelps Dodge Corp | Flotation recovery of molybdenite |
US3426896A (en) * | 1965-08-20 | 1969-02-11 | Armour Ind Chem Co | Flotation of bulk concentrates of molybdenum and copper sulfide minerals and separation thereof |
US3788467A (en) * | 1972-04-27 | 1974-01-29 | American Cyanamid Co | Flotation process for recovering molybdenum |
US3811569A (en) * | 1971-06-07 | 1974-05-21 | Fmc Corp | Flotation recovery of molybdenite |
US4231859A (en) * | 1979-11-27 | 1980-11-04 | The United States Of America As Represented By The Secretary Of The Interior | Molybdenite flotation |
US4268380A (en) * | 1978-08-15 | 1981-05-19 | Pennwalt Corporation | Froth flotation process |
US4515688A (en) * | 1982-08-20 | 1985-05-07 | South American Placers, Inc. | Process for the selective separation of base metal sulfides and oxides contained in an ore |
US4587013A (en) * | 1984-11-28 | 1986-05-06 | American Cyanamid Company | Monothiophosphinates as acid, neutral, or mildly alkaline circuit sulfide collectors and process for using same |
-
1986
- 1986-07-09 WO PCT/US1986/001467 patent/WO1987000088A1/en active IP Right Grant
- 1986-07-09 AT AT86905004T patent/ATE90592T1/en active
- 1986-07-09 BR BR8606758A patent/BR8606758A/en not_active IP Right Cessation
- 1986-07-09 AU AU61913/86A patent/AU6191386A/en not_active Abandoned
- 1986-07-09 EP EP86905004A patent/EP0229835B1/en not_active Expired - Lifetime
- 1986-07-09 JP JP61504290A patent/JPS63500577A/en active Pending
- 1986-07-09 DE DE8686905004T patent/DE3688591T2/en not_active Expired - Fee Related
-
1987
- 1987-03-06 FI FI870999A patent/FI80835C/en not_active IP Right Cessation
-
1990
- 1990-06-05 AU AU56840/90A patent/AU629646B2/en not_active Ceased
Patent Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2316743A (en) * | 1939-11-09 | 1943-04-13 | American Cyanamid Co | Flotation of molybdenite |
US2559104A (en) * | 1948-03-23 | 1951-07-03 | Phelps Dodge Corp | Flotation recovery of molybdenite |
US3426896A (en) * | 1965-08-20 | 1969-02-11 | Armour Ind Chem Co | Flotation of bulk concentrates of molybdenum and copper sulfide minerals and separation thereof |
US3811569A (en) * | 1971-06-07 | 1974-05-21 | Fmc Corp | Flotation recovery of molybdenite |
US3788467A (en) * | 1972-04-27 | 1974-01-29 | American Cyanamid Co | Flotation process for recovering molybdenum |
US4268380A (en) * | 1978-08-15 | 1981-05-19 | Pennwalt Corporation | Froth flotation process |
US4231859A (en) * | 1979-11-27 | 1980-11-04 | The United States Of America As Represented By The Secretary Of The Interior | Molybdenite flotation |
US4515688A (en) * | 1982-08-20 | 1985-05-07 | South American Placers, Inc. | Process for the selective separation of base metal sulfides and oxides contained in an ore |
US4587013A (en) * | 1984-11-28 | 1986-05-06 | American Cyanamid Company | Monothiophosphinates as acid, neutral, or mildly alkaline circuit sulfide collectors and process for using same |
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5068028A (en) * | 1990-01-21 | 1991-11-26 | University Of Utah | Molybdenite flotation from copper sulfide/molybdenite containing materials by ozone conditioning |
US5110455A (en) * | 1990-12-13 | 1992-05-05 | Cyprus Minerals Company | Method for achieving enhanced copper flotation concentrate grade by oxidation and flotation |
US8413816B2 (en) | 2010-02-16 | 2013-04-09 | Nalco Company | Sulfide flotation aid |
CN102259050A (en) * | 2010-08-23 | 2011-11-30 | 鞍钢集团矿业公司 | Novel middling treatment process for reverse flotation operation |
US10413914B2 (en) | 2012-01-27 | 2019-09-17 | Evonik Degussa Gmbh | Enrichment of metal sulfide ores by oxidant assisted froth flotation |
CN103386356A (en) * | 2012-05-09 | 2013-11-13 | 中国瑞林工程技术有限公司 | Flotation method for copper sulphide ore |
CN102671769A (en) * | 2012-05-14 | 2012-09-19 | 长沙矿冶研究院有限责任公司 | Beneficiation method for flotation and recovery of molybdenum from easy-floating gangue refractory molybdenum ore |
CN102773152A (en) * | 2012-07-13 | 2012-11-14 | 四川领航石墨制品有限公司 | Fine flaky-cryptocrystalline mixed graphite separation technique |
CN103128004A (en) * | 2013-01-07 | 2013-06-05 | 湖南有色金属研究院 | Method for flotation and separation of copper molybdenum sulphide bulk concentrates |
US9839917B2 (en) | 2013-07-19 | 2017-12-12 | Evonik Degussa Gmbh | Method for recovering a copper sulfide concentrate from an ore containing an iron sulfide |
CN106378262A (en) * | 2016-12-07 | 2017-02-08 | 广西大学 | Method for recycling powethite from molybdenite tailings |
Also Published As
Publication number | Publication date |
---|---|
AU5684090A (en) | 1990-09-27 |
AU6191386A (en) | 1987-01-30 |
FI80835B (en) | 1990-04-30 |
EP0229835A1 (en) | 1987-07-29 |
FI80835C (en) | 1990-08-10 |
EP0229835A4 (en) | 1989-12-12 |
DE3688591D1 (en) | 1993-07-22 |
JPS63500577A (en) | 1988-03-03 |
FI870999A (en) | 1987-03-06 |
BR8606758A (en) | 1987-10-13 |
FI870999A0 (en) | 1987-03-06 |
DE3688591T2 (en) | 1993-09-23 |
AU629646B2 (en) | 1992-10-08 |
EP0229835B1 (en) | 1993-06-16 |
ATE90592T1 (en) | 1993-07-15 |
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