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US 10,695,694B2 34 lesthan80um,lesthan10um,fromabout1umtoabout oxyfluoride,afluorophosphate,orcombinationsthereof.In 10um,fromabout5umtoabout75um,orfromabout10 someembodiments,theionexchangematerialofthe um toabout50um. uncoated ion exchange particle is selected LiMn 012, Insomeembodiments,theporousstructureformsa LiTiz012 Li,TiO3,Li,MnO3,Li,SnO3,LiMn204, porousmembrane,porousbead,otherporousstructure,5LiMn1.604, LiA102, LiCuO2, LiTiO2, LiTi04, densemembrane,densebead,scafold,awovenmembrane, LiTi1024,LizV04,Li2Si307,LiFePO4,LiMnPO4, awoundmembrane,aspiralwoundmembrane,orcombi Li-CuP,01, Al(OH)3, LiCl.xAl(OH)3.yH,O, nationsthereof.Insomeembodiments,theporousstructure SnO2.xSb2O3.yH,O,TiO2.xSb2O3.yH2O,solidsolutions formsaporousmembrane,aporousbead,orcombinations thereof,andcombinationsthereof.Insomeembodiment,x thereof. Insomeembodiments,thecoatedionexchangeparticles 2,3,4,5,6,7,8,9,and10.Insomeembodiments,yis compriseanionexchangematerialandacoatingmaterial.In selectedfrom0.1,0.2,0.3,0.4,0.5,0.6,0.7,0.8,0.9,1,2, someembodiments,thecoatingmaterialofthecoatedion 3,4,5,6,7,8,9,and10.Insomeembodiments,xandyis exchangeparticlespreventsdisolutionoftheionexchange independentlyselectedfrom0.1,0.2,0.3,0.4,0.5,0.6,0.7, material.Insomeembodiments,thecoatingmaterialofthe 15 0.8,0.9,1,2,3,4,5,6,7,8,9,and 10.Insomeembodi coatedionexchangeparticlesalowsdifusionoflithium ments,theionexchangematerialoftheuncoatedion ionsandhydrogenionstoandfromtheionexchange exchangeparticleisselectedfromLi2SnO3,LiMnOz, material. Insomeembodiments,thecoatingmaterialofthecoated nationsthereof. 10 isselected from 0.1,0.2,0.3,0.4,0.5,0.6,0.7,0.8,0.9,1, ionexchangeparticlescomprisesacarbide,anitride,an20 Insomeembodiments,theuncoatedionexchangeparticle oxide,aphosphate,afluoride,apolymer,carbon,acarbo hasanaveragediameteroflesthan10um.Insome naceousmaterial,orcombinationsthereof.Insomeembodi embodiments,theuncoatedionexchangeparticlehasan ments,thecoatingmaterialofthecoatedionexchange averagediameteroflesthan10um.Insomeembodiments, particlescomprisesTiO2,ZrO2,Mo02,SnO2,Nb05, theuncoatedionexchangeparticlehasanaveragediameter TaOs,LizTiO3,SiO2,LizZrO3,LizM003,LiNbO3,LiTaOz,25oflesthan1,0nm.Insomeembodiments,theuncoated AlPO4,LaPO4,ZrSi04,ZrP,07,MoP207,Mo2P3012, ionexchangeparticlehasanaveragediameteroflesthan BaSO4,AlF3,SiC,TiC,Zrc,SizN4,ZrN,BN,carbon, 100nm. graphiticcarbon,amorphouscarbon,hardcarbon,diamond Insomeembodiments,theporousstructureisintheform likecarbon,solidsolutionsthereof,orcombinationthereof. ofaporousbead.Insomeembodiments,theporousbeadis Insomeembodiments,thecoatingmaterialofthecoatedion 30aproximatelyspherical.Insomeembodiments,theporous exchangeparticlescomprisesTiO2.Insomeembodiments, beadhasanaveragediameteroflesthan10cm.Insome thecoatingmaterialofthecoatedionexchangeparticles embodiments,theporousbeadhasanaveragediameterof comprisesSiO2.Insomeembodiments,thecoatingmaterial lesthan1cm.Insomeembonents,theporousbeadhas ofthecoatedionexchangeparticlescomprisesZrO2. anaveragediameteroflesthan1mm.Insomeembodi Insomeembodiments,theionexchangematerialofthe35ments,theporousbeadhadanaveragediameteroflesthan coatedionexchangeparticlecomprisesanoxide,aphos 10um.Insomeembodiments,theporousbeadhasan phate,anoxyfluoride,afluorophosphate,orcombinations averagediameteroflesthan10um.Insomeembodiments, thereof.Insomeembodiments,theionexchangematerialof theporousbeadisaproximatelysphericalwithanaverage thecoatedionexchangeparticleisselectedfrom diameteroffromabout1umtoabout10um,fromabout Li.Mn3012,LiTi3012,Li,TiO3,Li,MnOz,Li,SnO3,401mmtoabout10mm,fromabout1mmtoabout80mm, LiMn04,Li1.6Mn.604,LiAl,LiCuO2,LiTiO2,Li_Ti04, fromabout1mmtoabout60mm,fromabout1toabout40 Li,Ti,1024) Li,VO4, Li,Si20, LiFePO4 LiMnPO4, mm,fromabout1toabout20mm,fromabout1toabout10 LiCuP207, Al(OH), LiCl.xAl(OH)3.yH2O, mm,fromabout1cmtoabout10cm,fromabout1cmto SnO2.xSb2Os.yH2O,TiO2.xSb2O3.yH,O,solidsolutions about8cm,fromabout1cmtoabout6cm,orfromabout thereof,andcombinationsthereof.Insomeembodiment,x45 1cmtoabout4cm. isselectedfrom 0.1,0.2,0.3,0.4,0.5,0.6,0.7,0.8,0.9,1, Insomeembodiments,theporousbeadistablet-shaped. 2,3,4,5,6,7,8,9,and10.Insomeembodiments,yis Insomeembodiments,theporousbeadhasadiameterof selectedfrom0.1,0.2,0.3,0.4,0.5,0.6,0.7,0.8,0.9,1,2, lesthan20mmandaheightoflesthan20mm.Insome 3,4,5,6,7,8,9,and10.Insomeembodiments,xandyis embodiments,theporousbeadhasadiameteroflesthan8 independentlyselectedfrom0.1,0.2,0.3,0.4,0.5,0.6,0.7,50mm andaheightoflesthan8mm.Insomeembodiments, 0.8,0.9,1,2,3,4,5,6,7,8,9,or10.Insomeembodiments, theporousbeadhasadiameteroflesthan4mmanda theionexchangematerialofthecoatedionexchange heightoflesthan4mm.Insomeembodiments,theporous particleisselectedfromLi,Sn03,LiMnO3,LiTi03, beadhasadiameteroflesthan2mmandaheightofles LiTis012,LiMn012,LiMn604,andcombinations than2mm.Insomeembodiments,theporousbeadhasa LiTiO3,LiTis012,LiMn012,Li1.6Mn1.604,andcombi 5diameteroflesthan1mm andaheightoflesthan1mm. thereof. In some embodiments, the coated ion exchange particle An aspect described herein is a method of extracting hasanaveragediameteroflesthan10um.Insome lithiumfromaliquidresource,comprising:contactingthe embodiments,thecoatedionexchangeparticlehasanaver coatedionexchangeparticlewithaliquidresourceto agediameteroflesthan10um.Insomeembodiments,the producelithiatedcoatedionexchangeparticles;andtreating coatedionexchangeparticlehasanaveragediameterofles60 thelithiatedcoated ionexchangeparticleswith anacid than1,0nm.Insomeembodiments,thecoatedion solutiontoproduceasaltsolutioncomprisinglithiumions. exchangeparticlehasanaveragediameteroflesthan10 Insomeembodiments,theliquidresourceisanaturalbrine, nm. adisolved saltflat,seawater,concentrated seawater,a Insomeembodiments,theuncoatedionexchangepar desalinationefluent,aconcentratedbrine,aprocesed ticlescompriseanionexchangematerial.Insomeembodi-65brine,anoilfieldbrine, liquidfrom anionexchange ments,theionexchangematerialoftheuncoatedion proces,aliquidfromasolventextractionproces,asyn exchangeparticlecomprisesanoxide,aphosphate,an theticbrine,aleachatefromanoreorcombinationofores,PDF Image | Patent Lithium Extraction with coated ion exchange particles
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Product and Development Focus for Infinity Turbine
ORC Waste Heat Turbine and ORC System Build Plans: All turbine plans are $10,000 each. This allows you to build a system and then consider licensing for production after you have completed and tested a unit.Redox Flow Battery Technology: With the advent of the new USA tax credits for producing and selling batteries ($35/kW) we are focussing on a simple flow battery using shipping containers as the modular electrolyte storage units with tax credits up to $140,000 per system. Our main focus is on the salt battery. This battery can be used for both thermal and electrical storage applications. We call it the Cogeneration Battery or Cogen Battery. One project is converting salt (brine) based water conditioners to simultaneously produce power. In addition, there are many opportunities to extract Lithium from brine (salt lakes, groundwater, and producer water).Salt water or brine are huge sources for lithium. Most of the worlds lithium is acquired from a brine source. It's even in seawater in a low concentration. Brine is also a byproduct of huge powerplants, which can now use that as an electrolyte and a huge flow battery (which allows storage at the source).We welcome any business and equipment inquiries, as well as licensing our turbines for manufacturing.CONTACT TEL: 608-238-6001 Email: greg@infinityturbine.com (Standard Web Page)