EP0107562A1 - Concentration of ores by flotation and collector reagents used therefor - Google Patents
Concentration of ores by flotation and collector reagents used therefor Download PDFInfo
- Publication number
- EP0107562A1 EP0107562A1 EP83401957A EP83401957A EP0107562A1 EP 0107562 A1 EP0107562 A1 EP 0107562A1 EP 83401957 A EP83401957 A EP 83401957A EP 83401957 A EP83401957 A EP 83401957A EP 0107562 A1 EP0107562 A1 EP 0107562A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- flotation
- ores
- polysulfide
- concentration
- reagents used
- 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
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
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/001—Flotation agents
- B03D1/004—Organic compounds
- B03D1/012—Organic compounds containing sulfur
-
- 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
- B03D2201/00—Specified effects produced by the flotation agents
- B03D2201/02—Collectors
-
- 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
- B03D2203/00—Specified materials treated by the flotation agents; specified applications
- B03D2203/02—Ores
Definitions
- the present invention relates to the enrichment of ores by flotation with organic collectors, constituted by thio compounds. More specifically, it targets the processing of ores based on heavy metal oxides and sulphides.
- the present invention is based on the discovery that the collecting properties of a thio compound can be intensified by a certain accumulation of sulfur atoms in the molecules of these compounds.
- dialkyl polysulfides can give better results than the corresponding mercaptan; this is surprising theoretically, since polysulfides have a molecular structure with two lipophilic chains. This fact is all the more unexpected since the alkyl polysulfides with more C a are even less soluble in water than the mercaptans.
- the process according to the invention consists in carrying out the flotation of ores or minerals in the general manner, known per se, but with at least one dihydro-carbyl polysulfide as collector, or jointly with a collector of known type, this or these polysulphides being represented by the formula where R and R ', similar or different, are alkyls or alkenyls which can carry substituents and x is a number with an average value of 2 to 8.
- the substituents of the hydrocarbon groups R or / and R ' can be other aliphatic, cycloaliphatic or aryl radicals, halogens, nitriles or functional groups, for example OH, -COOH, NO 2 , NH 2 , CONH 2 , esters, carbonyls, etc.
- Functional substituents, providing affinity for water, are particularly favorable.
- the groups R and / and R ' are generally in C 1 to C18 linear or branched, and especially in C4 to C 1 2 "
- a method of preparing such polysulphides which consists in treating, for example, the corresponding mercaptan with sulfur, in the presence of an amine as catalyst, according to the reaction:
- This process actually provides a mixture of polysulfides of different numbers of S atoms, where x is actually an average of these numbers.
- the polysulfides according to the invention are practically insoluble in water, they can be introduced into the ore pulp to be treated in the form of a solution in a solvent, in that of emulsion or extremely fine dispersion.
- a solvent in that of emulsion or extremely fine dispersion.
- the emulsion can be produced by mixing with a surface-active liquid such as polyethoxylated polyol or alkylphenol, petroleum sulfonate, polyalkoxylated mercaptan, a fatty acid ester of polyoxyalkylene or sorbitan, etc.
- the aqueous or other dispersion it can be obtained by wet micronization.
- the molar proportions of the new collectors, according to the invention, to be used in flotation are the same as those of the known technique, that is to say in general about 0.05 to 0.5, and more often of 0.1 to 0.25 moles per tonne of ore.
- a series of flotation tests is carried out on copper sulphide ore from the South African mine at Palabora, with a Cu content of 0.45 to 0.48%. 600 g of this ore are ground to a fineness such that 76% of the powder passes through a 148 micron mesh sieve.
- the product After adding the necessary adjuvants, the product is subjected to flotation for 20 minutes at pH 7.5, in a 2.5-liter laboratory cell of the MINEMET M 130 type, in the presence of methyl-isobutyl carbinol as a foaming agent. , added at a rate of 25 g per tonne of ore.
- the collectors are introduced in the form of mixtures of 57.5% by weight of thio compounds with 42.5% of tensio-ac tif, nonyl phenol polyoxyethylene, known commercially under the trademark "SIMULSOL 730". These are, on the one hand, (examples 1 and 2) usual mercaptans in flotation and, on the other hand,. (Examples 3 to 6) of the polysulfides according to the invention; their proportion, in millimoles per tonne of ore, is indicated in the Table of results, which follows.
- the Cu concentrations obtained are always higher, with the polysulphides, than those given by conventional collectors.
- the pentasulfides allow a copper recovery comparable or superior to that of the mercaptans.
Abstract
Procédé d'enrichissement de minerais par flottation à l'aide d'un collecteur constitué par un thio composé, ce thio composé étant un polysulfure de dialkyle ou de dialkényle, linéaires ou ramifiés.Process for the enrichment of ores by flotation using a collector consisting of a compound thio, this compound thio being a dialkyl or dialkenyl polysulfide, linear or branched.
Description
La présente invention se rapporte à l'enrichissement de minerais par flottation avec des collecteurs organiques, constitués par des thio composés. Elle vise plus spécialement le traitement de minerais à base d'oxydes et de sulfures de métaux lourds.The present invention relates to the enrichment of ores by flotation with organic collectors, constituted by thio compounds. More specifically, it targets the processing of ores based on heavy metal oxides and sulphides.
Des composés renfermant du soufre dans leur molécule sont employés avec succès dans la technique de flottation : c'est notamment le cas des alkyl xanthates alcalins qui comptent parmi les meilleurs collecteurs connus jusqu'à présent. De même, considère-t-on comme bons collecteurs les mercaptans d'alkyles, surtout en C12 à C16' qui - malgré leur peu de solubilité dans l'eau - ont pu être avantageusement utilisés, émulsionnés avec des composés tensio-actifs.Compounds containing sulfur in their molecule are used with success in the technique of flotation: it is in particular the case of alkaline alkyl xanthates which count among the best collectors known until now. Similarly, do we consider as good collectors the alkyl mercaptans, especially in C 12 to C 16 ' which - despite their little solubility in water - could be advantageously used, emulsified with surfactant compounds .
La présente invention est basée sur la découverte que les propriétés collectrices d'un thio composé peuvent être intensifiées par une certaine accumulation d'atomes de soufre dans les molécules de ces composés. Ainsi a-t-on trouvé que des polysulfures de dialkyles peuvent donner des résultats meilleurs que le mercaptan correspondant ; c'est surprenant théoriquement, puisque les polysulfures présentent une structure moléculaire à deux chaînes lipophiles. Ce fait est d'ailleurs d'autant plus inattendu que les polysulfures d'alkyles à plus de Ca sont encore moins solubles dans l'eau que les mercaptans.The present invention is based on the discovery that the collecting properties of a thio compound can be intensified by a certain accumulation of sulfur atoms in the molecules of these compounds. Thus it has been found that dialkyl polysulfides can give better results than the corresponding mercaptan; this is surprising theoretically, since polysulfides have a molecular structure with two lipophilic chains. This fact is all the more unexpected since the alkyl polysulfides with more C a are even less soluble in water than the mercaptans.
Le procédé suivant l'invention consiste à effectuer la flottation de minerais ou de minéraux à la manière générale, connue en soi, mais avec au moins un polysulfure de dihydro- carbyle en tant que collecteur, ou conjointement avec un collecteur de type connu, ce ou ces polysulfures étant représentés par la formule
Les substituants des groupes hydrocarbonés R ou/et R' peuvent être d'autres radicaux aliphatiques, cycloalipha- tiques ou aryliques, des halogènes, nitriles ou de groupes fonctionnels, par exemple des OH, -COOH, N02, NH2, CONH2, esters, carbonyles, etc. Des substituants fonctionnels, procurant de l'affinité pour l'eau, sont particulièrement favorables.The substituents of the hydrocarbon groups R or / and R 'can be other aliphatic, cycloaliphatic or aryl radicals, halogens, nitriles or functional groups, for example OH, -COOH, NO 2 , NH 2 , CONH 2 , esters, carbonyls, etc. Functional substituents, providing affinity for water, are particularly favorable.
Pratiquement, les groupes R ou/et R' sont en général en C1 à C18 linéaires ou ramifiés, et surtout en C4 à C12"In practice, the groups R and / and R 'are generally in C 1 to C18 linear or branched, and especially in C4 to C 1 2 "
On connait un mode de préparation de tels polysulfures, qui consiste à traiter par exemple le mercaptan correspondant par du soufre, en présence d'une amine comme catalyseur, suivant la réaction :
Ce procédé fournit en réalité un mélange de polysulfures de différents nombres d'atomes de S, x étant en fait une moyenne de ces nombres.This process actually provides a mixture of polysulfides of different numbers of S atoms, where x is actually an average of these numbers.
Bien qu'à partir de C8, les polysulfures suivant l'invention soient pratiquement insolubles dans l'eau, ils peuvent être introduits dans la pulpe de minerai à traiter sous la forme de solution dans un solvant, sous celle d'émulsion ou de dispersion extrêmement fine. Ainsi, peut-on employer le polysulfure en solution dans de l'alcool, du sulfure de carbone, du diméthyl sulfoxide, du benzène, du kérosène, de l'huile ou autre solvant approprié. L'émulsion peut être produite par mélange avec un liquide tensio-actif tel que polyol ou alkyl-phénol polyéthoxylé, un sulfonate de pétrole, un mercaptan polyalkoxylé, un ester d'acide gras de polyoxyalkylène ou de sorbitan, etc.Although from C 8 , the polysulfides according to the invention are practically insoluble in water, they can be introduced into the ore pulp to be treated in the form of a solution in a solvent, in that of emulsion or extremely fine dispersion. Thus, can we use polysulfide dissolved in alcohol, carbon sulfide, dimethyl sulfoxide, benzene, kerosene, oil or other suitable solvent. The emulsion can be produced by mixing with a surface-active liquid such as polyethoxylated polyol or alkylphenol, petroleum sulfonate, polyalkoxylated mercaptan, a fatty acid ester of polyoxyalkylene or sorbitan, etc.
Quant à la dispersion aqueuse ou autre, elle peut s'obtenir par la micronisation humide.As for the aqueous or other dispersion, it can be obtained by wet micronization.
Les proportions molaires des nouveaux collecteurs, suivant l'invention, à employer dans la flottation, sont les mêmes que celles de la technique connue, c'est-à-dire en général environ 0,05 à 0,5, et plus souvent de 0,1 à 0,25 mole par tonne de minerai.The molar proportions of the new collectors, according to the invention, to be used in flotation, are the same as those of the known technique, that is to say in general about 0.05 to 0.5, and more often of 0.1 to 0.25 moles per tonne of ore.
Les exemples qui suivent illustrent l'invention non limitativement.The examples which follow illustrate the invention without limitation.
Une série d'essais de flottation est effectuée sur un minerai sulfuré de cuivre provenant de la mine Sud Africaine de Palabora, à teneur en Cu de 0,45 à 0,48%. 600 g de ce minerai sont broyés à une finesse telle que 76% de la poudre traversent un tamis à mailles de 148 microns.A series of flotation tests is carried out on copper sulphide ore from the South African mine at Palabora, with a Cu content of 0.45 to 0.48%. 600 g of this ore are ground to a fineness such that 76% of the powder passes through a 148 micron mesh sieve.
Après l'adjonction des adjuvants nécessaires, le produit est soumis à la flottation pendant 20 minutes à pH 7,5, dans une cellule de laboratoire de 2,5 litres du type MINEMET M 130, en présence de méthyl-isobutyl carbinol comme agent moussant, ajouté à raison de 25 g par tonne de minerai.After adding the necessary adjuvants, the product is subjected to flotation for 20 minutes at pH 7.5, in a 2.5-liter laboratory cell of the MINEMET M 130 type, in the presence of methyl-isobutyl carbinol as a foaming agent. , added at a rate of 25 g per tonne of ore.
Les collecteurs sont introduits sous la forme de mélanges de 57,5% en poids de thio composés avec 42,5% de tensio-actif, nonyl phénol polyoxyéthylène, connu dans le commerce sous la marque "SIMULSOL 730".. Ce sont, d'une part, (exemples 1 et 2) des mercaptans usuels en flottation et,d'autre part,. (exemples 3 à 6) des polysulfures suivant l'invention ; leur proportion, en millimoles par tonne de minerai, est indiquée dans le Tableau des résultats, qui suit.The collectors are introduced in the form of mixtures of 57.5% by weight of thio compounds with 42.5% of tensio-ac tif, nonyl phenol polyoxyethylene, known commercially under the trademark "SIMULSOL 730". These are, on the one hand, (examples 1 and 2) usual mercaptans in flotation and, on the other hand,. (Examples 3 to 6) of the polysulfides according to the invention; their proportion, in millimoles per tonne of ore, is indicated in the Table of results, which follows.
Les deux dernières colonnes de ce Tableau indiquent la teneur pourcent en Cu dans le concentré obtenu, ainsi que les % de Cu récupéré.
Il en résulte que les concentrations en Cu, obtenues, sont toujours supérieures, avec les polysulfures, à celles que donnent les collecteurs classiques. En outre, à proportions molaires égales, les pentasulfures permettent une récupération en cuivre comparable ou supérieure à celles des mercaptans.As a result, the Cu concentrations obtained are always higher, with the polysulphides, than those given by conventional collectors. In addition, at equal molar proportions, the pentasulfides allow a copper recovery comparable or superior to that of the mercaptans.
Des essais de flottation sont effectués avec chacun des minéraux désignés dans le tableau des résultats par :
Dans une cellule, on introduit 265 ml d'eau, 1 g de poudre fine de minéral et 3x10-4 g de collecteur à essayer, par litre ; ce collecteur est utilisé sous la forme d'une solution à 1% dans de l'éthanol.265 ml of water, 1 g of fine mineral powder and 3 × 10 -4 g of collector to be tested are introduced into a cell per liter; this collector is used in the form of a 1% solution in ethanol.
Le tableau ci-après donne les % de chaque minéral recueilli comme produit de la flottation.
On peut constater que les polysulfures des exemples 8 à 13 donnent des résultats supérieurs à ceux du n-dodécyl mercaptan (exemple 14) couramment employé à l'heure actuelle.It can be seen that the polysulphides of Examples 8 to 13 give better results than those of n-dodecyl mercaptan (Example 14) commonly used at present.
Essais sur la chalcopyrite avec 3 x 10-4 g/1 de collecteur.Chalcopyrite tests with 3 x 10 -4 g / 1 of collector.
Claims (5)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR8217128 | 1982-10-13 | ||
FR8217128A FR2534493B1 (en) | 1982-10-13 | 1982-10-13 | ENRICHMENT OF ORES BY FLOTATION AND COLLECTING AGENTS EMPLOYED THEREFOR |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0107562A1 true EP0107562A1 (en) | 1984-05-02 |
EP0107562B1 EP0107562B1 (en) | 1987-08-12 |
Family
ID=9278233
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP83401957A Expired EP0107562B1 (en) | 1982-10-13 | 1983-10-07 | Concentration of ores by flotation and collector reagents used therefor |
Country Status (9)
Country | Link |
---|---|
US (1) | US4554137A (en) |
EP (1) | EP0107562B1 (en) |
AU (1) | AU562923B2 (en) |
CA (1) | CA1215547A (en) |
DE (1) | DE107562T1 (en) |
ES (1) | ES526758A0 (en) |
FI (1) | FI74892C (en) |
FR (1) | FR2534493B1 (en) |
ZA (1) | ZA837622B (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4735711A (en) * | 1985-05-31 | 1988-04-05 | The Dow Chemical Company | Novel collectors for the selective froth flotation of mineral sulfides |
US5338338A (en) * | 1992-09-22 | 1994-08-16 | Geobiotics, Inc. | Method for recovering gold and other precious metals from carbonaceous ores |
US5364453A (en) * | 1992-09-22 | 1994-11-15 | Geobiotics, Inc. | Method for recovering gold and other precious metals from carbonaceous ores |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1774183A (en) * | 1927-05-13 | 1930-08-26 | Barrett Co | Concentration of minerals |
GB362366A (en) * | 1929-09-04 | 1931-12-01 | Minerals Separation Ltd | Improvements in or relating to concentration by froth flotation |
US2027357A (en) * | 1927-05-13 | 1936-01-07 | Barrett Co | Flotation of minerals |
US3059774A (en) * | 1961-07-31 | 1962-10-23 | United States Borax Chem | Method and means for beneficiating ores |
FR2429617A1 (en) * | 1978-06-27 | 1980-01-25 | Elf Aquitaine | Flotation collectors esp. for sulphide minerals - comprise organic thio cpds. esp. alkyl thio ethanol(s) (SW 28.1.80) |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4341626A (en) * | 1980-12-22 | 1982-07-27 | American Cyanamid Company | Process for the flotation of sulfide minerals employing alkylaryl hydrocarbon compounds |
-
1982
- 1982-10-13 FR FR8217128A patent/FR2534493B1/en not_active Expired
-
1983
- 1983-10-07 DE DE198383401957T patent/DE107562T1/en active Pending
- 1983-10-07 EP EP83401957A patent/EP0107562B1/en not_active Expired
- 1983-10-12 CA CA000438865A patent/CA1215547A/en not_active Expired
- 1983-10-12 FI FI833716A patent/FI74892C/en not_active IP Right Cessation
- 1983-10-13 ES ES526758A patent/ES526758A0/en active Granted
- 1983-10-13 US US06/541,776 patent/US4554137A/en not_active Expired - Lifetime
- 1983-10-13 AU AU20154/83A patent/AU562923B2/en not_active Ceased
- 1983-10-13 ZA ZA837622A patent/ZA837622B/en unknown
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1774183A (en) * | 1927-05-13 | 1930-08-26 | Barrett Co | Concentration of minerals |
US2027357A (en) * | 1927-05-13 | 1936-01-07 | Barrett Co | Flotation of minerals |
GB362366A (en) * | 1929-09-04 | 1931-12-01 | Minerals Separation Ltd | Improvements in or relating to concentration by froth flotation |
US3059774A (en) * | 1961-07-31 | 1962-10-23 | United States Borax Chem | Method and means for beneficiating ores |
FR2429617A1 (en) * | 1978-06-27 | 1980-01-25 | Elf Aquitaine | Flotation collectors esp. for sulphide minerals - comprise organic thio cpds. esp. alkyl thio ethanol(s) (SW 28.1.80) |
Also Published As
Publication number | Publication date |
---|---|
DE107562T1 (en) | 1984-09-13 |
FI74892C (en) | 1988-04-11 |
EP0107562B1 (en) | 1987-08-12 |
ZA837622B (en) | 1984-06-27 |
CA1215547A (en) | 1986-12-23 |
FI833716A (en) | 1984-04-14 |
AU2015483A (en) | 1984-04-19 |
FI833716A0 (en) | 1983-10-12 |
FR2534493B1 (en) | 1986-05-30 |
AU562923B2 (en) | 1987-06-25 |
ES8501251A1 (en) | 1984-12-01 |
FR2534493A1 (en) | 1984-04-20 |
FI74892B (en) | 1987-12-31 |
ES526758A0 (en) | 1984-12-01 |
US4554137A (en) | 1985-11-19 |
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