![]() Method for ore flotation
专利摘要:
The invention relates to the field of mineral processing and allows for increasing the efficiency of flotation by increasing the dissolution of the collecting agent (PC) in water. A PC consisting of three components is preliminarily introduced into the aqueous pulp: a yew compound, a surfactant, and an alcoholic component containing from 3 to 12 carbon atoms. Their ratio is as follows (wt.%): TI-compound 30-60 j surfactant 20-55; alcohol containing from 3 to 12 carbon atoms 5-30. The thio compound is selected from the series: mercaptans containing from 8 to 18 carbon atoms, polysulfide alkyls containing from 16 to 36 carbon atoms and from 3 to 8 sulfur atoms. As a mercaptan, m. p-dodecyl mercaptan or tertiary dodecyl mercaptan was used. As polysulfide alkyl, polyalkyl sulfides of the formula RS are chosen, (- R, where R, R are the same or different hydrocarbon radicals containing from 1 to 14 carbon atoms, x is an integer from 3 to 5, in particular, tri- or penta disulfides of di-tertiary nonyl or di-tertiary dodecyl. The composition of the PC ensures the formation of a PC microemulsion after its introduction into the mineral pulp. This allows the use of practically water-insoluble thio compounds, 3 3.pf files. (O CO with oo -4 00 cm 公开号:SU1304737A3 申请号:SU833657073 申请日:1983-10-12 公开日:1987-04-15 发明作者:Делурм Раймон;Детьенн Жан-Луи;Каморниски Жак;Теллье Жак 申请人:Сосьете Насьональ Елф Акитэн (Продюксьон) (Фирма); IPC主号:
专利说明:
SUBSTANCE: invention relates to (god of minerals fi1otane, oi, and in particular to C1 :: esters of mineralization of ores5 containing copper 5 lead, zinc, and molyb). The aim of the invention is to improve the efficiency of spores: | re geita-collector in the 1zod. According to the proposed method, a collector consisting of three components is introduced into the aqueous pulp: a mixture of compounds, a surface of an active substance and an alcoholic agent containing 3–12 carbon atoms, in the following ratios of components, May. %; Thio Compound 30-60 Surface-active substance 20-L5 Spi; st containing 3-12 atoms carbon-30 Tyosoed1 nepie selected from a number of yes; mercaptans containing 8-18 carbon atoms, hydrogen sulfides alkyl; cc oxidants 3-8 sulfur atoms. one At the same time, 1 to; 1ep, ilmer kaptap njn-i tertiary can be used as a measure of ghana:; LL iio iciiH. 1-and-one}, l i-catrecTBe polysch.chgyrmdalkil.; 1: sulfide1 ;; R-S forms, - l; where R 5 I am the same or uglevo.i..orodpye radikgy Y. soda zhagcie 1-1A ach omo-carbon, x is a number from 3 to 5, in particular, three- or ne: yyad1-; sulfide-1-dct1:; cnogo drank or dithiticho i o to, / 1edil. , Collect the indicated composition:: provides for the formation of microm o Tmulsi1-reagent after its addition, it should be valued. mineral plume makes it possible to use the ped pedals, residual - (-} 1o or practically insoluble in water with obtaining a high technological indicator: 7th flotation Practically non-existent i-e-t-junction1-; I such as dodep: 1mer: an-; m-pp or polysulfide; ierno; ai a.1: and terdodecyl can give excellent results in the formation of a microemulsion compared to the -1 them in the case of the usual emul iro: ai i or somobilizatsii. The peculiarity of the compositions for 31 pots according to the proposed method is concluded in that the liquid phase, connected to the collector itself, is formed by a liquid surfactant or at least measures: - races:) orim | | in a small amount of cooTBCTCTj yiuiiierc; dissolved t. The preferred; 1: YAKs are non-. soy; 1 penny, ko can be a choice) from the ichves of gypsy passages, for example, n (h1x:; eny ,, t corresponding to the total frmule R- (0-R i.-Oli, where R is aj-kil s C; | -C:. (., G p D1K1; tite; id1o with HS of teropyklicha-ska i ruppa, cycloalkyl i.; And hydrogen atom, R-a.akile, C) (1) p 1, from 1 ds: 12. Can also be used thioether poli-T1-: sia, gkilets ,, t, k. BeiiiecTBa, in ks) - TC pi.ix iiepisbif: 1sys, r; oG Od in the index oh (:: pyvJIe in gray. It is possible to use ani-g: ny or ka: ION; 1Ы. , if it is 1: 1, TreS)) 1) | p the pH of the pulp, on the Hj-UMep petrogene zgh so l lononates, alcoholic sulphates. fatty acids, alkyl amides, amkpo} fatty acids, or the fourth or fourth ammonia; When it is, and PLV is bent or viscous, you can create an environment by adding a small amount of water or a homogenizer, the bottom: rimar. The third xcm; one of the mixtures is a real body, which is an organic molecule, having a lipo- (r part and at least one - noj; Hpi io (r) upg: y, these are alcohols, co; ; with szhaltsie 3 - 12 atsmov carbon, Ra-C; vimosti:; togs; compounds in water he is grateful ii P i m e; “0.6 KI - copper sulbium, ore, 13, t; to the size of /), i Cl;:; ss minus I i.8 microns. Flotation, dip in a laboratory flotation unit: Minat miniature with a capacity of 0.025 m in the presence of methyl 7 Puffy carbinol in the form of t C L: with rP 7.5, Flotation time 20 mip, AT; Eating with: Obir 1-ate into pulp was administered by the four method EI: aj in the form of a coagulum according to the image of shadow O (microglobulating mixture) containing,%; e. P. IL is a measure of r-a and 52 Pocilfenoj g SP taek Si etyl 38.4 O pi r t isopropyl 4,3 2-ethylhexanol 4,8 J) in the form of a classical 3NryjibCHH composition,%: n-dodecyl mercaptan 80 Nonylphenolgene aoxy-ethylene 20 E)) as a classic p-dodecyl mercaptan emulsion 80 Polyol decaoxy ethylene 20 2.) emulsion composition,%: E-dodecyl mercaptan n-90 0 Experimental data show that copper extraction in variant a (50.8–79.5%) is significantly higher than in other variants (15.5–50.8). EXAMPLE 2 Experimental conditions are similar to those of Example 1, but instead of p-dodecyl mercaptan, tertiary dodecyl mercaptan, tertiary dodecyl penta sulphide, tertiary nonyl penta sulphide, and tertiary nonyl trisulfide are used. The best results were obtained using the composition according to the invention (75.8 and 73.7%, 65.2%, 59.9%). I EXAMPLE 3 Experimental conditions are similar to those of Example 2, but tertiary dodecyl trisulfide was used as a thio-compound, and the ratio of alcohols: isopropanol — 6.25%, 2-ethylhexanol, 3.35% The best results are also obtained with the introduction of the mixture corresponding to the invention (58.1%). EXAMPLE 4 Experimental conditions are analogous to example 1, but amyl xanthate sodium potassium is added as a collector in the form of an aqueous solution. Copper recovery was 56.7-80%. Xanthate provides a higher recovery of copper, but dramatically reduces the quality of the concentrate from 14.6 to 16.4% (examples 3-6) to 10.4%, i.e. practically 50% of the required metal content in the flotation product Example5. 0.5 kg of lead ore was crushed to a particle size of 90% of the class of 100 μm and floated at pH 10 for 15 minutes. The flow rate of the blowing agent was 310 kg / kg. As collectors, the composition was introduced corresponding to the variant a of example 1 of the following composition.%: O five five p-Dodecyl mercaptan 55 NONILPhenolheptaoxyethylenene 33.75 Methylisobutylcarbinol 4.5 Ethyl 2-hexanol 6.75. In addition, a collector was used, containing:% p-Dodecyl mercaptan 90 Nonylphenoldecoxy-ethylene10 The extraction of lead and zinc was 91.5 and 98.2% in the case of the composition according to the invention and 68.5 and 54.3% in the case of using the known emulsion collector + surfactant. Limer 6. According to example 1, a series of experiments was carried out with a collector consumption of 35-10 kg / kg for various 0 ratios of the components of the mixture. From the data obtained it can be seen that when the surfactant content is less than 20% or more than 54%, the yield of copper decreases rapidly. Example 7. Various polysulfide and mercaptans were tested as thiosoate; Mercaptans containing less than 8 carbon atoms, Provide the same results as known emulsions. Mercaptans containing more than 18 carbon atoms reduce the yield of copper. The best are mercaptans containing 8-18 carbon atoms. Polysulfide alkyls are less than Cg, i.e. containing only 16 carbon atoms, do not provide an advantage over the known method. Outside C, d, copper output is sharply reduced. Optimal are polysulfides C, | j-Cjg (in total), containing 3-8 sulfur atoms. EXAMPLE 8 The conditions of the experiment are similar to those of example 2, but alcohols with different numbers of carbon atoms were used as the alcohol. Best results were obtained using alcohols. WITH.. Thus, the use of the proposed method allows to increase the extraction and copper content by 25.8-30% and 3-5%, the extraction of zinc by 34.9%, lead by 35.2%, i.e. improve flotation efficiency. 0 five 0 five 0 five C, (2 So
权利要求:
Claims (3) [1] 1. The method of flotation of ores, including the preliminary introduction of water5 Collecting reagent-containing slurry containing a thio compound and a liquid surfactant, 5 in order 5 to increase flotation efficiency by increasing the dissolving reagent-collector in water, alcohol coenzide 5 containing 3-12 carbon atoms is added to the collector, and the thio compound is selected from the following series: mercaptans containing 8–18 carbon atoms, polysulfide alkyls containing 16–36 carbon atoms and 3–8 sulfur atoms, with the following ratio of components, wt%: Tisson Connection 30-60 Patented substance 20-55 alcohol, containing five 6 carbon [2] 2. The method according to p. 3-I 5-30 About tl and h and ush, and with the fact that p; the quality of the mercaptan is chosen p-dodecylmercaptan or tertiary dodecium. mercaptan. [3] 3. The method according to claim 1, about tl and h and y and so, with polysulfide alkyl, choose the polyalkyl sulfide of the formula R-Sj-Bl, where R, R are the same or different hydrocarbon radicals containing 1-14 carbon atoms -: hydrograph, where x is an integer from 3 to 5 4, The method according to p. 3, is also distinguished by the fact that as a polis. Sfidalkyl f1Ormules choose tri- or pentadisulfides of dithitic nonyl or dithitic dedecyl,
类似技术:
公开号 | 公开日 | 专利标题 SU1304737A3|1987-04-15|Method for ore flotation CN104874488B|2017-05-24|Collecting agent and preparation method and application thereof US2266954A|1941-12-23|Wetting agent in settling of oe pulps DE4133063A1|1993-04-08|PROCESS FOR PRODUCING IRON ORE CONCENTRATES BY FLOTATION US5962828A|1999-10-05|Enhanced flotation reagents for beneficiation of phosphate ores US4584097A|1986-04-22|Neutral hydrocarboxycarbonyl thionocarbamate sulfide collectors US4595493A|1986-06-17|Process for the flotation of base metal sulfide minerals in acid, neutral or mildly alkaline circuits US4587013A|1986-05-06|Monothiophosphinates as acid, neutral, or mildly alkaline circuit sulfide collectors and process for using same SU837310A3|1981-06-07|Method of separating sulfide copper-molybdenum products US4459237A|1984-07-10|Trithiocarbonates SU1433396A3|1988-10-23|Method of foam flotation of oxidized and salt-like ores US2251217A|1941-07-29|Ore flotation US4102781A|1978-07-25|Flotation process US2410021A|1946-10-29|Flotation process US4561984A|1985-12-31|Trithiocarbonate flotation reagents US4098688A|1978-07-04|Brightening of clay by froth flotation US4579651A|1986-04-01|Flotation reagents US1858007A|1932-05-10|Method and agent for recovery of oxidized ores US4556500A|1985-12-03|Flotation reagents FI74892B|1987-12-31|FOER REFRIGERATION FOR MALMER GENOM FLOTATION. SU1058136A1|1985-04-15|Collector for ore flotation RU2108167C1|1998-04-10|Method of selective flotation of pentlandite in alkali medium from materials containing pyrrhotine sulfides US3596838A|1971-08-03|Flotation of sulphide ores SU774602A1|1980-10-30|Lead/copper ore flotation modifier CA2144242A1|1995-09-11|Dewatering of alumina trihydrate
同族专利:
公开号 | 公开日 US4594151A|1986-06-10| FI74891B|1987-12-31| EP0107561A1|1984-05-02| FI74891C|1988-04-11| CA1222379A|1987-06-02| FR2534492A1|1984-04-20| ES8501252A1|1984-12-16| ZA837619B|1985-02-27| US4526696A|1985-07-02| DE107561T1|1984-09-13| AU2015383A|1984-04-19| FI833715A|1984-04-14| AU562922B2|1987-06-25| FI833715A0|1983-10-12| FR2534492B1|1984-12-28| EP0107561B1|1986-07-30| ES526760A0|1984-12-16| DE3364986D1|1986-09-04|
引用文献:
公开号 | 申请日 | 公开日 | 申请人 | 专利标题 RU2679765C2|2013-10-01|2019-02-12|ЭКОЛАБ ЮЭсЭй ИНК.|Method of improving collector performance during pulp separation by froth floatation | RU2685596C2|2013-10-01|2019-04-22|ЭКОЛАБ ЮЭсЭй ИНК.|Method for improving production characteristics of foaming agent in separating treatment of foamed suspension in medium | RU2715577C2|2015-12-28|2020-03-02|ШЕВРОН ФИЛЛИПС КЕМИКАЛ КОМПАНИ ЭлПи|Compositions of mixed decylmercaptans and their use for extraction of chemical substances during extraction of minerals|US2371292A|1945-03-13|Flotation reagent | US1659396A|1926-10-25|1928-02-14|Du Pont|Process of concentrating ores and minerals by flotation| US1774183A|1927-05-13|1930-08-26|Barrett Co|Concentration of minerals| US2027357A|1927-05-13|1936-01-07|Barrett Co|Flotation of minerals| US2128570A|1935-09-17|1938-08-30|Great Western Electro Chemical Co|Flotation material| US2163702A|1937-09-10|1939-06-27|Separation Process Company|Flotation process| CH203184A|1937-10-12|1939-02-28|Visura Treuhand Ges|Process for the concentration of usable minerals through foam swimming treatment.| US2302338A|1938-05-18|1942-11-17|Moeller August|Froth flotation| US2310240A|1939-10-02|1943-02-09|Walter E Keck|Flotation of ores| US2378552A|1943-03-03|1945-06-19|Edward H Hoag|Flotation process| US2610738A|1951-06-02|1952-09-16|Climax Molybdenum Co|Froth flotation of monazite from heavy gravity minerals| US2690259A|1951-11-14|1954-09-28|Bethlehem Steel Corp|Froth flotation of iron sulfide ore| IT522759A|1953-10-14|1900-01-01| US3309352A|1959-10-19|1967-03-14|Swift & Co|Alkylolamine phosphated alkylolamides prepared by heating a mixture of fat, protein, an alkylolamine and phosphoric acid| US3444090A|1967-03-01|1969-05-13|Grace W R & Co|Stabilizing filming amine emulsions| US3456791A|1967-04-17|1969-07-22|Jose L Ramirez|Separation of schoenite by flotation| US4012329A|1973-08-27|1977-03-15|Marathon Oil Company|Water-in-oil microemulsion drilling fluids| ZA767089B|1976-11-26|1978-05-30|Tekplex Ltd|Froth flotation process and collector composition| FI62006C|1978-06-22|1982-11-10|Outokumpu Oy|FOERFARANDE FOER SELEKTIV FLOTATION AV SULFIDISKA MINERALIER| SE436000B|1978-06-27|1984-11-05|Elf Aquitaine|PROCEDURE FOR FLOTATION OF MINERALS| FR2429617B1|1978-06-27|1982-02-12|Elf Aquitaine| US4251301A|1979-06-20|1981-02-17|The United States Of America As Represented By The Secretary Of The Army|Impact resistant pressable explosive composition of high energetic material content| US4256696A|1980-01-21|1981-03-17|Baxter Travenol Laboratories, Inc.|Cuvette rotor assembly| US4521300A|1982-08-18|1985-06-04|Parlman Robert M|Ore flotation with combined collectors|US4789392A|1984-09-13|1988-12-06|The Dow Chemical Company|Froth flotation method| DE3517154A1|1985-05-11|1986-11-13|Henkel KGaA, 4000 Düsseldorf|USE OF SURFACTANT MIXTURES AS AUXILIARIES FOR THE FLOTATION OF NON-SULFIDIC ORES| ES8800077A1|1985-05-31|1987-10-16|Dow Chemical Co|Novel collectors for the selective froth flotation of sulfide minerals| US4735711A|1985-05-31|1988-04-05|The Dow Chemical Company|Novel collectors for the selective froth flotation of mineral sulfides| DE3536975A1|1985-10-17|1987-04-23|Henkel Kgaa|USE OF NON-ionic surfactants as aids for the flotation of non-sulphide ores| US4684459A|1985-11-29|1987-08-04|The Dow Chemical Company|Collector compositions for the froth flotation of mineral values| US4676890A|1985-11-29|1987-06-30|The Dow Chemical Company|Collector compositions for the froth flotation of mineral values| FI73899C|1986-04-01|1987-12-10|Kemira Oy|Process for flotation of a phosphate mineral and an agent intended to be used therein| DE3641447A1|1986-12-04|1988-06-09|Henkel Kgaa|TENSIDE MIXTURES AS COLLECTORS FOR THE FLOTATION OF NON-SULFIDIC ORES| DE3818482A1|1988-05-31|1989-12-07|Henkel Kgaa|TENSIDE MIXTURES AS COLLECTORS FOR THE FLOTATION OF NON-SULFIDIC ORES| US4883585A|1988-10-27|1989-11-28|Phillips Petroleum Company|Ore flotation and sulfenyl dithiocarbamates as agents for use therein| US5132008A|1991-09-30|1992-07-21|Phillips Petroleum Company|Preparation of bis alkanes or bis alkanes and use thereof| GB9600525D0|1996-01-11|1996-03-13|Allied Colloids Ltd|Process for recovering minerals and compositions for use in this| AU4458797A|1997-09-15|1999-04-05|Sofitech N.V.|Electrically conductive non-aqueous wellbore fluids| US6793025B2|1998-01-08|2004-09-21|M-I L. L. C.|Double emulsion based drilling fluids| US6405809B2|1998-01-08|2002-06-18|M-I Llc|Conductive medium for openhold logging and logging while drilling| FR2855987B1|2003-06-16|2005-11-04|Atofina|MERCAPTANS COMPOSITION FOR USE IN A FLOATING PROCESS OF ORES| FR2857278B1|2003-06-16|2005-08-26|Atofina|MERCAPTAN COMPOSITIONS FOR USE IN A METHOD FOR FLOATING ORES| CN101081378B|2007-05-23|2012-04-18|华锡集团车河选矿厂|Novel technics of rough-flotation high concentration high-efficient flotation| EP2017009B1|2007-07-20|2013-07-03|ClariantS.A.|Reverse iron ore flotation by collectors in aqueous nanoemulsion| US8950090B2|2011-02-22|2015-02-10|Nike, Inc.|Article of footwear with adjustable cleats| CN104148163B|2014-07-29|2016-08-31|广西金山铟锗冶金化工有限公司|A kind of beneficiation method processing low-grade tin-lead-zinc multi-metal oxygen ore deposit| US9447481B1|2015-10-07|2016-09-20|Chevron Phillips Chemical Company Lp|Dipentene dimercaptan compositions and use thereof as a mining chemical collector| US9512248B1|2015-12-28|2016-12-06|Chevron Phillips Chemical Company Lp|Mixed decyl mercaptans compositions and use thereof as chain transfer agents| US10040758B2|2015-12-28|2018-08-07|Chevron Phillips Chemical Company Lp|Mixed decyl mercaptans compositions and methods of making same| US10294200B2|2015-12-28|2019-05-21|Chevron Phillips Chemical Company, Lp|Mixed branched eicosyl polysulfide compositions and methods of making same| US10011564B2|2015-12-28|2018-07-03|Chevron Phillips Chemical Company Lp|Mixed decyl mercaptans compositions and methods of making same| US9512071B1|2015-12-28|2016-12-06|Chevron Phillips Chemical Company Lp|Mixed decyl mercaptans compositions and methods of making same| CN105903552B|2016-04-26|2021-03-12|中南大学|Beneficiation method for efficiently recovering micro-fine particle molybdenum ore|
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申请号 | 申请日 | 专利标题 FR8217127A|FR2534492B1|1982-10-13|1982-10-13| 相关专利
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