序号 专利名 申请号 申请日 公开(公告)号 公开(公告)日 发明人
221 Process for the production of thermodynamically stable solid ion conductor materials US145638 1980-05-01 US4386020A 1983-05-31 Peter Hartwig; Werner Weppner; Winfried Wichelhaus
The present invention provides a process for the production of solid ion ductor materials (electrolytes) based on lithium or sodium compounds which stand in thermodynamic equilibrium with their alkali metal and have a high decomposition voltage, wherein two or more binary lithium or sodium compounds with an anion which is formed from one or more elements of the group consisting of nitrogen, phosphorus, arsenic, oxygen, sulphur, selenium, tellurium, hydrogen, fluorine, chlorine, bromine and iodine and which stand in thermodynamic equilibrium with their alkali metal are reacted together in such amounts and for such a period of time that a radiographically phase-pure product is formed.The present invention also provides ion conductor materials based on lithium or sodium compounds, which have the general formula:A.sub.3u+2v+w X.sub.u Y.sub.v Z.sub.wwherein A is lithium or sodium, X is nitrogen, phosphorus and/or arsenic, Y is nitrogen, sulphur, tellurium and/or selenium, Z is hydrogen and/or halogen and u, v and w each represent a number of from 0 to 1 inclusive, with the proviso that only one of u, v and w can assume the value of 0. Furthermore, the present invention provides galvanic cells comprising at least one of these ion conductor materials.
222 Crystalline lithium aluminates US217611 1980-12-18 US4348296A 1982-09-07 William C. Bauman; John M. Lee; John L. Burba, III
Porous substrates containing seeds of hydrous crystalline alumina are contacted with an aqueous solution of alkaline aluminate, thereby causing additional crystalline hydrous alumina to grow on the seeds within the pores of the substrate.
223 Transition metal aluminates US183908 1980-09-04 US4333846A 1982-06-08 John M. Lee; William C. Bauman
Crystalline transition metal aluminates conforming generally to the formulaMA.sub.a.sup.v Z.sub.b.sup.v.nAl(OH).sub.3.mH.sub.2 Owhere M is a transition metal having a valence charge of +2 selected from the group consisting of Cu, Zn, Mn, Fe, Co, and Ni, where AZ represents negative valence ions or radicals, v is a negative valence of 1, 2, or 3, n is a value to provide a mol ratio of Al/M of at least 1/1, preferably at least 1.5/1, and m is an integer of from zero to the maximum for waters of hydration, with (va)+(vb) equal to 2, are prepared in alkaline aqueous medium wherein transition metal compounds are caused to form adducts with amorphous hydrous alumina, Al(OH).sub.3, said adducts forming crystals when heated, said aluminates being useful, e.g., as ion exchangers and as spinel precursors among other things.
224 Recovery of lithium from brines US939545 1978-09-05 US4221767A 1980-09-09 John M. Lee; William C. Bauman
An anion exchange resin, containing Al(OH).sub.3 suspended therein, is reacted with aq. LiOH to form microcrystalline LiOH.2Al(OH).sub.3 which is then reacted with a halogen acid or halide salt to form microcrystalline LiX.2Al(OH).sub.3. The resin, after having a portion of the LiX eluted by using an aqueous wash, is used to recover Li.sup.+ values from aqueous brines.
225 Recovery of lithium from brines US939546 1978-09-05 US4159311A 1979-06-26 John M. Lee; William C. Bauman
Lithium is preferentially extracted from brine containing Li salts along with salts of other metals, e.g. Na, Ca, Mg, K, and/or B, by contacting the brine with a particulate anion exchange resin having suspended therein a microcrystalline form of LiX.sup.. 2A1 (OH).sub.3, where X=halide.
226 Method of purifying and concentrating lithium ions US29358772 1972-09-29 US3851040A 1974-11-26 ALBERTI G; MASSUCCI M
1. A METHOD OF PURIFYING AND CONCENTRATING LITHIUM IONS FROM AN AQUEOUS SOLUTION WHEREIN THEY ARE CONTAINED TOGETHER WITH OTHER IONS WHICH METHOD COMPRISES ADDING TO SAID SOLUTION A CAUSTIC SOLUTION TO OBTAIN A SOLUTION WHEREIN THE CONCENTRATION OF HYDROXYL IONS IS EQUAL AT LEAST TO THE LITHIUM ION CONCENTRATION; PERCOLATING THE SOLUTION SO OBTAINED THROUGH A BED CONSISTING OF CRYSTALLINE THORIUM ACID ARSENATE HAVING THE FORMULA TH(HASO4)2 AND AN ION EXCHANGE CAPACITY RANGING BETWEEN 1.40 ND 3.55 ME./G. TOWARD THE LITHIUM ION TO THEREBY OBTAIN THORIUM AND LITHIUM ARSENATE; WASHING SAID THORIUM AND LITHIUM ARSENATE WITH WATER PREVVIOUSLY ALKALIZED AT A PH FROM 9 TO 10; PERCOLATING A HYDROCHLORIC ACID SOLUTION THROUGH SAID THORIUM AND LITHIUM ARSENATE TO ELUTE THE LITHIUM IONS THEREFRM WHEREBY A CONCENTRATED AND PURIFIED LITHIUM SOLUTION IS OBTAINED AND THE THORIUM ARSENATE IS RESTORED TO ITS INITIAL FORM.
227 Removal of dissolved lead from alkali metal chloride containing solutions US3671187D 1970-07-13 US3671187A 1972-06-20 CUEVAS EPHRAIM A
A PROCESS IS DESCRIBED FOR THE REMOVAL OF LEAD FROM ALKALI METAL CHLORIDE CONTAINING SOLUTIONS BY PRECIPITATION OF THE LEAD IONS AS LEAD SULFIDE. THE METHOD INVOLVES UTILIZING AN ALKALI METAL SULFIDE AS THE PRECIPITATING AGENT IN LIEU OF HYDROGEN SULFIDE. THE USE OF ALKALI METAL SULFIDE AS THE PRECIPITATING AGENT PRECIPITATES THE LEAD IN LARGE PARTICLE SIZES RENDERING FILTRATION EASY. THE QUANTITY OF SULFIDE IONS IN THE SOLUTIONS NECESSARY IN ACCOMPLISH PRECIPITATION OF DISSOLVED LEAD IS ALSO MINIMIZED. TREATMENTS OF SOLUTIONS BY THE PROPOSED SCHEME SHOW REDUCTIONS OF THE LEAD CONTENT OF SOLUTIONS TREATED FROM QUANTITIES OF 0.6 PERCENT BY WEIGHT IN 18 PARTS PER MILLION OR LESS LEAD. THE PROCESS IS DESCRIBED IN PARTICULAR IN CONNECTION WITH THE TREATMENT OF LITHIUM CHLORIDE-LITHIUM HYDROXIDE SOLUTIONS CONTAINING CONTAMINATING LEAD IONS AND UTILIZING LITHIUM SULFIDE AS THE PRECIPITATING AGENT.
228 Process for removal of salts from aqueous solutions with solid methylenedianiline US3433583D 1967-06-28 US3433583A 1969-03-18 HESS HOWARD V; MCCOY FREDERIC C
229 Method of lithium recovery US35012364 1964-03-06 US3306700A 1967-02-28 NEIPERT MARSHALL P; BON CHARLES K
230 Separation of lithium isotopes US65444657 1957-04-23 US3085852A 1963-04-16 KURT PETERS
231 Purifying lithium salts US76694058 1958-10-13 US3000699A 1961-09-19 ROLAND GAUGUIN; JACQUES CLAUS
232 Process of recovering lithium values from dilithium sodium phosphate US66618746 1946-04-30 US2548037A 1951-04-10 JOHN MINNICK LEONARD; RAYMOND BROWN CHARLES
233 Production of pure lithium compounds from impure solutions US70761734 1934-01-20 US2021986A 1935-11-26 SEYMOUR COLTON HENRY
234 LITHIUM-RICH ANTIPEROVSKITE-COATED LCO-BASED LITHIUM COMPOSITE, METHOD FOR PREPARING SAME, AND POSITIVE ELECTRODE ACTIVE MATERIAL AND LITHIUM SECONDARY BATTERY COMPRISING SAME EP17853364.2 2017-09-15 EP3444880A1 2019-02-20 PARK, Se Ho; SUNG, Da Young; JANG, Minchul; SON, Byoungkuk; CHOI, Junghun

The present invention relates to a Li-rich antiperovskite-coated LCO-based lithium complex, a method of preparing the same, and a positive electrode active material and a lithium secondary battery, both of which include the LCO-based lithium complex. When a lithium complex in which a coating layer of a compound having a lithium-rich antiperovskite (LiRAP) crystal structure is formed on surfaces of LCO-based particles is applied as the positive electrode active material, the lithium complex is favorable for batteries which are operated at a high voltage, has high lithium ion conductivity, and can be applied to lithium secondary batteries which are driven at a high temperature due to high thermal stability.

235 LITHIUM REAGENT POROUS METAL OXIDE COMPOSITIONS EP07814783.2 2007-09-10 EP2081682B1 2018-05-30 LEFENFELD, Michael; DYE, James L.; NANDI, Partha; JACKSON, James
The invention relates to lithium metal/porous metal oxide compositions. These lithium metal compositions are prepared by mixing liquid lithium metal with a porous metal oxide in an inert atmosphere under exothermic conditions sufficient to absorb the liquid lithium metal into the porous metal oxide pores. The lithium metal/porous metal oxide compositions of the invention are preferably loaded with lithium metal up to about 40% by weight, with about 20% to 40% by weight being the most preferred loading. The invention also relates to lithium reagent-porous metal oxide compositions having RLi absorbed into a porous oxide. The preparation and use of these compositions are also described.
236 COMPLEXOMETRIC PRECURSOR FORMULATION METHODOLOGY FOR INDUSTRIAL PRODUCTION OF HIGH PERFORMANCE FINE AND ULTRAFINE POWDERS AND NANOPOWDERS FOR SPECIALIZED APPLICATIONS EP14767613.4 2014-03-14 EP3245682A2 2017-11-22 FRIANEZA-KULLBERG, Teresita
A method of forming a powder MjXp wherein Mj is a positive ion or several positive ions selected from alkali metal, alkaline earth metal or transition metal; and Xp is a monoatomic or a polyatomic anion selected from Groups IIIA, IVA, VA, VIA or VIIA; called complexometric precursor formulation or CPF. The method includes the steps of: providing a first reactor vessel with a first gas diffuser and an first agitator; providing a second reactor vessel with a second gas diffuser and a second agitator; charging the first reactor vessel with a first solution comprising a first salt of Mj; introducing gas into the first solution through the first gas diffuser, charging the second reactor vessel with a second solution comprising a salt of Mp; adding the second solution to the first solution to form a complexcelle; drying the complexcelle, to obtain a dry powder; and calcining the dried powder of said MjXp.
237 LEITSALZ FÜR LITHIUM-BASIERTE ENERGIESPEICHER EP13706047.1 2013-02-27 EP2819951B1 2016-08-03 RÖSCHENTHALER, Gerd-Volker; WINTER, Martin; PASSERINI, Stefano; VLASOV, Katja; KALINOVICH, Nataliya; SCHREINER, Christian; SCHMITZ, Raphael Wilhelm; MÜLLER, Romek Ansgar; SCHMITZ, René; SCHEDLBAUER, Tanja; LEX-BALDUCCI, Alexandra; KUNZE, Miriam
238 METHOD FOR PREPARING LITHIUM METAL PHOSPHOR OXIDE EP13827963 2013-05-10 EP2883838A4 2016-03-30 SONG HYUN A; CHANG DONG GYU; YANG WOO YOUNG
The present invention relates to a method for preparing a lithium metal phosphor oxide, the method including: mixing an iron salt solution and a phosphate solution in a reactor; applying a shearing force to the mixed solution in the reactor during the mixing to form a suspension containing nano-sized iron phosphate precipitate particles; obtaining the nano-sized iron phosphate particles from the suspension; and mixing the iron phosphate with a lithium raw material and performing firing, and the lithium metal phosphor oxide according to the present invention has an Equation of LiM n FePO 4 . Herein, M is selected from the group consisting of Ni, Co, Mn, Cr, Zr, Nb, Cu, V, Ti, Zn, Al, Ga, and Mg, and n is in a range of 0 to 1. According to the present invention, since calcination is performed at a temperature that is lower than that of another existing method, there is an effect of reducing a process cost, and the obtained lithium metal phosphor oxide prepared according to the method of the present invention has an olivine structure type.
239 NONAQUEOUS ELECTROLYTE SOLUTION FOR BATTERIES, NOVEL COMPOUND, POLYMER ELECTROLYTE, AND LITHIUM SECONDARY BATTERY EP14788457.1 2014-04-21 EP2991154A1 2016-03-02 MIYASATO, Masataka; FUJIYAMA, Satoko; HAYASHI, Takashi; KOBAYASHI, Takeshi

A non-aqueous electrolyte solution for a battery, including a compound represented by formula (1), wherein each A represents P or P=O; each R represents H, a halogen, an alkyl, an aryl, an alkoxy or an aryloxy; each X represents H, an alkyl, an aryl, an alkali metal or formula (2); each Y represents H, a halogen, an alkyl, an aryl, an alkoxy, an aryloxy or formula (3); each Z represents H, an alkyl, an aryl or OZ1; Z1 represents H, an alkyl, an aryl, an alkali metal, formula (2), or formula (4); each M represents an alkali metal; n is 1 or more; m is 1 or more; I is 1 or more; a sum of n, m and I in one molecule is from 1 to 200; and each * represents a position of bonding:

240 STABILIZED LITHIUM COMPOSITE PARTICLES EP13789463.0 2013-11-01 EP2916982A1 2015-09-16 GADKAREE, Kishor Purushottam; LIU, Xiaorong
Stabilized lithium particles include a lithium-containing core and a coating of a complex lithium salt that surrounds and encapsulates the core. The coating, which is a barrier to oxygen and water, enables the particles to be handled in the open air and incorporated directly into electrochemical devices. The coating material is compatible, for example, with electrolytic materials that are used in electrochemical cells. The average coated particle size is less than 500 microns.
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