DE3415323A1 - METHOD FOR PRODUCING SINTERABLE POWDER FROM LITHIUM METASILICATE LI (DOWN ARROW) 2 (DOWN ARROW) SIO (DOWN ARROW) 3 (DOWN ARROW) AND THE USE THEREOF - Google Patents
METHOD FOR PRODUCING SINTERABLE POWDER FROM LITHIUM METASILICATE LI (DOWN ARROW) 2 (DOWN ARROW) SIO (DOWN ARROW) 3 (DOWN ARROW) AND THE USE THEREOFInfo
- Publication number
- DE3415323A1 DE3415323A1 DE19843415323 DE3415323A DE3415323A1 DE 3415323 A1 DE3415323 A1 DE 3415323A1 DE 19843415323 DE19843415323 DE 19843415323 DE 3415323 A DE3415323 A DE 3415323A DE 3415323 A1 DE3415323 A1 DE 3415323A1
- Authority
- DE
- Germany
- Prior art keywords
- sio
- down arrow
- sinterable powder
- suspension
- lithium metasilicate
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
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Classifications
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- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/01—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics
- C04B35/16—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics based on silicates other than clay
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B33/00—Silicon; Compounds thereof
- C01B33/20—Silicates
- C01B33/32—Alkali metal silicates
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B4/00—Hydrogen isotopes; Inorganic compounds thereof prepared by isotope exchange, e.g. NH3 + D2 → NH2D + HD
-
- G—PHYSICS
- G21—NUCLEAR PHYSICS; NUCLEAR ENGINEERING
- G21B—FUSION REACTORS
- G21B1/00—Thermonuclear fusion reactors
- G21B1/11—Details
- G21B1/13—First wall; Blanket; Divertor
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E30/00—Energy generation of nuclear origin
- Y02E30/10—Nuclear fusion reactors
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Ceramic Engineering (AREA)
- Inorganic Chemistry (AREA)
- Physics & Mathematics (AREA)
- General Engineering & Computer Science (AREA)
- Plasma & Fusion (AREA)
- Health & Medical Sciences (AREA)
- High Energy & Nuclear Physics (AREA)
- Manufacturing & Machinery (AREA)
- General Health & Medical Sciences (AREA)
- Materials Engineering (AREA)
- Structural Engineering (AREA)
- Silicates, Zeolites, And Molecular Sieves (AREA)
- Battery Electrode And Active Subsutance (AREA)
- Secondary Cells (AREA)
Description
Kernforschungszentrum ti/-> Karlsruhe, 19.04.1984 Karlsruhe GmbH PLA 8422 Gl/hrNuclear Research Center ti / -> Karlsruhe, April 19, 1984 Karlsruhe GmbH PLA 8422 Gl / hr
ANR 1 002 597ANR 1 002 597
Verfahren zur Herstellung von sinterfähigem Pulver aus Lithiuminetasilikat Li3SiO3 und dessen Verwendung.Process for the production of sinterable powder from lithium etasilicate Li 3 SiO 3 and its use.
Verfahren zur Herstellung von sinterfähigem Pulver aus Lithiummetasilikat Li3SiO und dessen Verwendung.Process for the production of sinterable powder from lithium metasilicate Li 3 SiO and its use.
Die Erfindung betrifft ein Verfahren zur Herstellung von sinterfähigem Pulver aus Litiummetasilikat Li SiO., mit einer Phasenreinheit von größenordnungsmäßig 99 %, bei welchem amorphes SiO2 in eine wäßrige Lithiumhydroxid-Lösung eingebracht und die entstehende Suspension einer erhöhten Temperatur ausgesetzt wird.The invention relates to a method for producing sinterable powder from lithium metasilicate Li SiO., With a phase purity of the order of 99 %, in which amorphous SiO 2 is introduced into an aqueous lithium hydroxide solution and the resulting suspension is exposed to an elevated temperature.
Lithiumhaltige, oxidische Keramik-Materialien, beispielsweise Lithiummetasilikat, wurden als Brutstoffe für Fusionsreaktoren zur Gewinnung von Tritium bereits vorgeschlagen. Zur Herstellung von Li2SiO3 wurden meist feste Pulver von Li2CO3 und SiO2 oder H3SiO3 · nH 20 auf hohe Temperaturen erhitzt bzw. geschmolzen. Die zur Reaktion verwendeten Temperaturen lagen im Bereich von mehr als 700°c bis 1500°c und die Wärmebehandlungsdauer zwischen 3 bis 5 Stunden bei 1400°C bis 1500°C bis 8 Tage bei 700°C, wonach 3 Tage bei 800°C und 4 Tage bei 900°C weiter erhitzt wurde. Über die Reinheit der Produkte und über ihre Partikelgröße wurde nichts bekannt. Im allgemeinen aber müssen die Verfahrensprodukte vor ihrer Weiterverarbeitung gemahlen werden. Bei den Feststoffreaktionen der bekannten Herstellungsverfahren bei den hohen Temperaturen oder in der Schmelze ist mit Verunreinigungen zu rechnen, sodaß nur ein Anteil von 90 bis 95 % der gewünschten Phase im Endprodukt vorhanden ist.Oxidic ceramic materials containing lithium, for example lithium metasilicate, have already been proposed as breeding materials for fusion reactors for the extraction of tritium. To produce Li 2 SiO 3 , solid powders of Li 2 CO 3 and SiO 2 or H 3 SiO 3 · nH 2 0 were usually heated or melted to high temperatures. The temperatures used for the reaction were in the range from more than 700 ° C to 1500 ° C and the heat treatment time between 3 to 5 hours at 1400 ° C to 1500 ° C to 8 days at 700 ° C, followed by 3 days at 800 ° C and 4 days at 900 ° C was further heated. Nothing was known about the purity of the products or their particle size. In general, however, the process products have to be ground before they can be further processed. In the solids reactions of the known manufacturing processes at high temperatures or in the melt, impurities are to be expected, so that only 90 to 95 % of the desired phase is present in the end product.
Es wurde als wünschenwert erachtet, ein Verfahren zur Herstellung von Li2SiO-, zu schaffen, mit welchem die Verunreingungen im Endprodukt sowie der große AufwandIt was considered desirable to create a process for the production of Li 2 SiO-, with which the impurities in the end product as well as the great expense
an Zeit und Energie bei den bekannten Verfahren vermieden werden können. Gleichzeitig sollte das Verfahren wirtschaftlicher sein als die bisher bekannten Herstellungsverfahren. Aus "Gmelin's Handbuch der Anorganischen Chemie", System Nr. 20, Lithium, (1927) Seite 241 ist bekannt, daß amorphe, bei 100°C getrocknete Kieselsäure in warmerLiOH-Lösung sehr wenig löslich ist, in kalter, etwa 2N LiOH-Lösung jedoch 1 Mol Li2O wenigstens 3,4 Mol SiO2 lösen kann. Beim Erhitzen soll aus dieser Lösung Li„SiO-, · Hn ausfallen. Die Herstellung von sinterfähigem Pulver aus Li9SiO wird dort nicht ange-time and energy can be avoided with the known methods. At the same time, the process should be more economical than the previously known manufacturing processes. From "Gmelin's Handbuch der Anorganischen Chemie", System No. 20, Lithium, (1927) page 241 it is known that amorphous silica, dried at 100 ° C., is very sparingly soluble in warm LiOH solution, in cold, approximately 2N LiOH solution however, 1 mol of Li 2 O can dissolve at least 3.4 mol of SiO 2 . When heated, Li, SiO-, · Hn should precipitate from this solution. The production of sinterable powder from Li 9 SiO is not indicated there.
^ 3^ 3
sprochen.spoke.
Der Erfindung liegt die Aufgabe zugrunde, ein einfaches und verbessertes Verfahren zur Herstellung von Li-SiO-, zu schaffen,bei welchem ein möglichst großer Anteil des Verfahrens in einer wäßrigen Lösung abläuft und bei geringem Zeitaufwand und bei verhältnismäßig geringem Energieaufwand ein gut sinterfähiges Pulver des ge- ■ wünschten Li3SiO praktisch phasenrein erhalten wird.The invention is based on the object of creating a simple and improved process for the production of Li-SiO-, in which the largest possible proportion of the process takes place in an aqueous solution and a well sinterable powder of the with little time and relatively little energy desired Li 3 SiO is obtained practically in pure phase.
Die Aufgabe wird erfindungsgemäß dadurch gelöst, daßThe object is achieved according to the invention in that
a) eine stöchiometrische Menge an SiO zur Bildung der Suspension vewendet wird, bezogen auf das gelöste LiOH,a) a stoichiometric amount of SiO to form the Suspension is used, based on the dissolved LiOH,
b) die Suspension ohne weitere Zwischenbehandlung direkt mit Hilfe von Luft bei einer Temperatur zwischen 2000C und 45O°C sprühgetrocknet wird undb, the suspension without further intermediate treatment and is) directly by means of air at a temperature between 200 0 C and 45O ° C spray-dried
c) anschließend der pulverförmige Trockenrückstand bei einer Temperatur im Bereich von 500 C bis iOÖt> C erhitzt und kalziniert wird.c) then the powdery dry residue at a temperature in the range from 500 C to iOÖt> C is heated and calcined.
In der Lithiumhydroxid-Lösung findet folgende Reaktion statt:The following reaction takes place in the lithium hydroxide solution instead of:
2 LiOH + aq + SiO2 (amorph) =^ Li3SiO3 · xH 0 + aq2 LiOH + aq + SiO 2 (amorphous) = ^ Li 3 SiO 3 · xH 0 + aq
Die entstehende Suspension wird ohne weitere Zwischenbehandlung durch Sprühtrocknen in ein· Pulver umgearbeitet. Das sprühgetrocknete Pulver wurde durch eine Kalzinationsglühung bei vorzugsweise 600PC innerhalb von 2 Stunden in das gewünschte Li2SiO3 übergeführt. Bei geeigneten Sinterbedingungen kann eine Dichte von 95 % TD erreicht werden.The resulting suspension is converted into a powder by spray drying without any further intermediate treatment. The spray-dried powder was converted into the desired Li 2 SiO 3 within 2 hours by calcination annealing at preferably 600 P C. With suitable sintering conditions, a density of 95% TD can be achieved.
Das nach dem erfindungsgemäßen Verfahren hergestellte Lithiummetasilikat ist wegen seiner hohen Reinheit als Brutstoff für Fusionsreaktoren zur Gewinnung von Tritium besonders gut geeignet.The lithium metasilicate produced by the process according to the invention is because of its high purity as Breeding material for fusion reactors for the extraction of tritium particularly well suited.
Im folgenden wird die Erfindung anhand eines Durchführungsbeispiels näher erläutert. The invention is explained in more detail below with the aid of an implementation example.
Entsprechend der ReaktionsgleichungAccording to the reaction equation
2 LiOH + SiO-, + aa —*- Li0SiO0 · xH„0 + aa2 LiOH + SiO-, + aa - * - Li 0 SiO 0 · xH "0 + aa
wurde eine wäßrige Suspension von amorphem SiO,, (AEROSIL der Fa. DEGUSSSA) unter ständigem Rühren in eine wäßrige Lösung von Lithiumhydroxid eingebracht. Unter weiterem ständigem Rühren bei Zimmertemperatur (etwa 1 Stunde) wurde dabei in der Suspension das Lithiummetasilikatan aqueous suspension of amorphous SiO ,, (AEROSIL from DEGUSSSA) is introduced into an aqueous solution of lithium hydroxide with constant stirring. Among other things Constant stirring at room temperature (about 1 hour) was the lithium metasilicate in the suspension
gebildet. Es wurde angenommen, daß das Li9SiO- zum Teil als Monohydrat vorlag und zum Teil gelöst war.educated. It was assumed that the Li 9 SiO- was partly present as a monohydrate and partly dissolved.
Tabelle: Ansätze zum Sprühtrocknen von Lithiummetasilikat Table : Approaches for the spray drying of lithium metasilicate
(cm )3
(cm)
Bei den Ansätzen Nr. 1 wurde wasserfreies Lithiumhydroxid, bei den Ansätzen der Nr. 2 kristallwasserhaltiges Lithiumhydroxid (LiOH · H9O) zur Herstellung der LiOH-Lösungen eingesetzt. Das Sprühtrocknen der Suspensionen erfolgte im Temperaturbereich von 200 - 37O°C. Die Ausbeute an sprühgetrocknetem Li9SiO., · xH2° t)etru5 jeweils mehr als 90 %. Der Feuchtigkeitsgehalt der Pulver war unterschiedlich und hing von der Temperatur des Sprühtrocknens ab. Höhere Sprühtemperaturen führten zu etwas geringeren Feuchtegehalten (etwa 2 %). Durch die Handhabung der Lithiumhydroxid-Lösungen und der Suspensionen an Luft enthielten die Pulver bis zu 6 Gew.-% Karbonatanteile, die während des Kalzinierungsschrxttes entfernt wurden.For batches no. 1, anhydrous lithium hydroxide was used, for batches of no. 2 lithium hydroxide containing water of crystallization (LiOH · H 9 O) was used to prepare the LiOH solutions. The suspensions were spray-dried in a temperature range of 200-370 ° C. The yield of spray-dried Li 9 SiO., · XH 2 ° t) etru 5 is more than 90% in each case. The moisture content of the powders varied and was dependent on the temperature of the spray drying. Higher spray temperatures led to slightly lower moisture contents (around 2%). As a result of the handling of the lithium hydroxide solutions and the suspensions in air, the powders contained up to 6% by weight of carbonate components, which were removed during the calcination step.
Die Pulverteilchen hatten die Form kleiner Hohlkügelchen mit einer durchschnittlichen Größe zwischen 3 und 5 ,um.The powder particles were in the form of small hollow spheres with an average size between 3 and 5 μm.
Nach dem Kalzinieren bei 600°C ließen sich die PulverAfter calcining at 600 ° C, the powders could be
:n bei
- 6 -: n at
- 6 -
durch Pressen und Sintern bei 1100°C/6Stunden bis zu 95 %by pressing and sintering at 1100 ° C / 6 hours up to 95%
•f'• f '
der theoretischen Dichte verdichten. Die Sinterproben ergaben jeweils einphasiges Li3SiO3.compress the theoretical density. The sintered samples each resulted in single-phase Li 3 SiO 3 .
Claims (2)
erhitzt und kalziniert wird.c) then the powdery dry residue at a temperature in the range from 500 ° C to 1000 ° C
is heated and calcined.
Priority Applications (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE19843415323 DE3415323A1 (en) | 1984-04-25 | 1984-04-25 | METHOD FOR PRODUCING SINTERABLE POWDER FROM LITHIUM METASILICATE LI (DOWN ARROW) 2 (DOWN ARROW) SIO (DOWN ARROW) 3 (DOWN ARROW) AND THE USE THEREOF |
| FR8505316A FR2563510B1 (en) | 1984-04-25 | 1985-04-09 | PROCESS FOR THE MANUFACTURE OF SINTERABLE LITHIUM METASILICATE LI2SIO3 POWDER, AND USE THEREOF |
| GB08509433A GB2159807B (en) | 1984-04-25 | 1985-04-12 | Method of producing a sinterable lithium metasilicate li2si03 powder |
| BE1/11236A BE902192A (en) | 1984-04-25 | 1985-04-15 | PROCESS FOR THE MANUFACTURE OF SINTERABLE LITHIUM METASILICATE LI2SIO3 POWDER AND USE THEREOF. |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE19843415323 DE3415323A1 (en) | 1984-04-25 | 1984-04-25 | METHOD FOR PRODUCING SINTERABLE POWDER FROM LITHIUM METASILICATE LI (DOWN ARROW) 2 (DOWN ARROW) SIO (DOWN ARROW) 3 (DOWN ARROW) AND THE USE THEREOF |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| DE3415323A1 true DE3415323A1 (en) | 1985-10-31 |
| DE3415323C2 DE3415323C2 (en) | 1988-10-06 |
Family
ID=6234299
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| DE19843415323 Granted DE3415323A1 (en) | 1984-04-25 | 1984-04-25 | METHOD FOR PRODUCING SINTERABLE POWDER FROM LITHIUM METASILICATE LI (DOWN ARROW) 2 (DOWN ARROW) SIO (DOWN ARROW) 3 (DOWN ARROW) AND THE USE THEREOF |
Country Status (4)
| Country | Link |
|---|---|
| BE (1) | BE902192A (en) |
| DE (1) | DE3415323A1 (en) |
| FR (1) | FR2563510B1 (en) |
| GB (1) | GB2159807B (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3725740A1 (en) * | 1987-08-04 | 1989-02-16 | Kernforschungsz Karlsruhe | METHOD FOR THE PRODUCTION OF SINTERABLE POWDER FOR BINARY AND MULTINERAL, CERAMIC OXIDE MATERIALS |
| CN100395183C (en) * | 2006-06-02 | 2008-06-18 | 东莞市黑马化工有限公司 | Method for preparing high-modulus water-soluble lithium silicate and application of high-modulus water-soluble lithium silicate in wood processing |
| CN103159222B (en) * | 2011-12-09 | 2014-10-01 | 核工业西南物理研究院 | A kind of method for compacting lithium orthosilicate pellets for tritium propagation |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3121919A1 (en) * | 1980-06-24 | 1982-04-29 | Steirische Magnesit-Industrie AG, 1130 Wien | HYDROTHERMAL DIRECT SYNTHESIS OF ALKALISILICATES |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR1546127A (en) * | 1966-11-30 | 1968-11-15 | Henkel & Cie Gmbh | Process for preparing lithium silicate solutions |
| US3838192A (en) * | 1971-10-28 | 1974-09-24 | Huber Corp J M | Production of alkali metal polysilicates |
-
1984
- 1984-04-25 DE DE19843415323 patent/DE3415323A1/en active Granted
-
1985
- 1985-04-09 FR FR8505316A patent/FR2563510B1/en not_active Expired
- 1985-04-12 GB GB08509433A patent/GB2159807B/en not_active Expired
- 1985-04-15 BE BE1/11236A patent/BE902192A/en not_active IP Right Cessation
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3121919A1 (en) * | 1980-06-24 | 1982-04-29 | Steirische Magnesit-Industrie AG, 1130 Wien | HYDROTHERMAL DIRECT SYNTHESIS OF ALKALISILICATES |
Also Published As
| Publication number | Publication date |
|---|---|
| BE902192A (en) | 1985-07-31 |
| GB2159807A (en) | 1985-12-11 |
| DE3415323C2 (en) | 1988-10-06 |
| GB8509433D0 (en) | 1985-06-19 |
| GB2159807B (en) | 1988-02-24 |
| FR2563510B1 (en) | 1987-01-23 |
| FR2563510A1 (en) | 1985-10-31 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| 8110 | Request for examination paragraph 44 | ||
| D2 | Grant after examination | ||
| 8364 | No opposition during term of opposition | ||
| 8339 | Ceased/non-payment of the annual fee |