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19 20 US 10,695,694B2 thanabout40um,morethanabout50um,morethanabout about1umtoabout2mm,fromabout1umtoabout20mm, 60um,morethanabout70um,morethanabout80um, orfromabout2mmtoabout20mm. morethanabout90um,morethanabout10um,morethan Tablet-ShapedBeads about1,0um,morethanabout10,0um,fromabout1 Insomeembodiments,theporousbeadistablet-shaped umtoabout10,0um,fromabout1umtoabout1,0um,5 withadiameteroflesthan1mm,lesthan2mm,lesthan fromabout1umtoabout10um,fromabout1umtoabout 4mm,lesthan8mm,lesthan20mm,morethan1mm, 80um,fromabout1umtoabout60um,fromabout1um morethan2mm,morethan4mm,morethan8mm,from toabout40um,orfromabout1umtoabout20um.Insome about0.5mmtoabout1mm,fromabout0.5mmtoabout embodiments,theuncoatedionexchangeparticleshavean 2mm,fromabout1mmtoabout4mm,fromabout1mm averagesizeoflesthanabout10um,lesthanabout1,010toabout8mm,fromabout1mm toabout20mm,andwith um,orlesthanabout10,0um.Insomeembodiments,the aheightoflesthan1mm,lesthan2mm,lesthan4mm, uncoatedionexchangeparticlesaresecondaryparticles lesthan8mm,lesthan20mm,morethan1mm,more comprisedofsmalerprimaryparticles,whereinthesecond than2mm,morethan4mm,morethan8mm,fromabout aryparticleshaveanaveragediameteroflesthanabout10 0.5mmtoabout1mm,fromabout0.5mmtoabout2mm, um,lesthanabout20um,lesthanabout30um,lesthan 15 fromabout1mm toabout4mm,fromabout1mm toabout about40um,lesthanabout50um,lesthanabout60um, 8mm,fromabout1mmtoabout20mm.Insomeembodi lesthanabout70um,lesthanabout80um,lesthanabout ments,theporousbeadhasadiameteroflesthan8mmand 90um,lesthanabout10um,lesthanabout1,0um, aheightoflesthan8mm.Insomeembodiments,the lesthanabout10,0um,lesthanabout10,0um,more porousbeadhasadiameteroflesthan4mmandaheight thanabout10um,morethanabout20um,morethanabout20oflesthan4mm.Insomeembodiments,theporousbead 30um,morethanabout40um,morethanabout50um, hasadiameteroflesthan2mmandaheightoflesthan morethanabout60um,morethanabout70um,morethan 2mm.Insomeembodiments,theporousbeadhasadiameter about80um,morethanabout90um,morethanabout10 oflesthan1mmandaheightoflesthan1mm. um,morethanabout1,0um,morethanabout10,0um, Methods fromabout1umtoabout10,0um,fromabout1um to25MethodsUsingCoatedIonExchangeParticles about1,0um,from about1um toabout10um,from Inanaspectdescribedhereinaremethodsofextracting about1umtoabout80um,fromabout1umtoabout60um, lithiumfromaliquidresource,comprisingcontactingthe fromabout1umtoabout40um,orfromabout1umto coatedionexchangeparticleswithaliquidresourceto about20um. producelithiatedcoatedionexchangeparticles;andtreating Inanembodiment,theaveragediameteroftheuncoated30thelithiatedcoatedionexchangeparticleswithanacid ionexchangeparticlesortheaveragediameterofthe solutiontoproduceasaltsolutioncomprisinglithiumions. uncoatedionexchangeparticleswhicharesecondarypar Here,thecoatedionexchangeparticlesareoptionalymixed ticlescomprisedofsmalerprimaryparticles,isdetermined withaliquidresourcetoabsorblithiumandthenrecovered bymeasuringtheparticlesizedistributionoftheuncoated throughfiltration,gravimetricseparation,orothermeans. ionexchangeparticlesortheuncoatedionexchangepar-35 Insomeembodiments,theliquidresourceisanatural ticleswhicharesecondaryparticlescomprisedofsmaler brine,adisolvedsaltflat,seawater,concentratedseawater, primaryparticles,anddeterminingthemeanparticlesize. desalinationefluent,aconcentratedbrine,aprocesed PorousBeads brine,liquidfromanionexchangeproces,liquidfroma Inanaspectdescribedherein,theporousstructureisinthe solventextractionproces,asyntheticbrine,leachatefrom form ofaporousbead. 40 ores,leachatefrom minerals,leachatefrom clays,leachate Insomeembodiments,theporousbeadisformedfrom fromrecycledproducts,leachatefromrecycledmaterials, drypowderusingamechanicalpres,apeletpres,atablet waterfromanoilfield,efluentfromachemicalproces,or pres,apilpres,arotarypres,orcombinationsthereof.In combinationsthereof.Insomeembodiments,aliquid someembodiments,theporousbeadisformedfroma resourceisanaturalbrine,adisolvedsaltflat,aconcen solventslurybydripingthesluryintoadiferentliquid45 tratedbrine,waterfrom anoilfield,aprocesedbrine,a solution.Thesolventsluryisformedusingasolventof syntheticbrine,liquidfromanionexchangeproces,liquid N-methyl-2-pyrolidone,dimethylsulfoxide,tetrahydro fromasolventextractionproces,leachatefromminerals, furan,dimethylformamide,dimethylacetamide,methylethyl leachatefromclays,leachatefromrecycledproducts, ketone,orcombinationsthereof.Thediferentliquidsolu leachatefromrecycledmaterials,orcombinationsthereof. tionscomprisewater,ethanol,iso-propylalcohol,acetone,50Insomeembodiments,thepHofthebrineisadjustedbefore orcombinationsthereof. orafterionexchangetoneutralizeacidicprotonsreleasedby SphericalBeads theionexchangematerialduringlithiumuptake. Insomeembodiments,theporousbeadisaproximately Insomeembodiments,theliquidresourcehasalithium sphericalwithanaveragediameteroflesthan10um,les ionconcentrationoflesthanabout10,0pm,lesthan than10um,lesthan1mm,lesthan1cm,lesthan10 5about10,0pm,lesthanabout1,0ppm,lesthan cm,morethan10um,morethan10um,morethan1mm, about10ppm,lesthanabout10pm,orcombinations morethan1cm,fromabout1umtoabout10um,from thereof.Insomeembodiments,theliquidresourcehasa about1mmtoabout10mm,fromabout1mmtoabout80 lithiumionconcentrationlesthanabout5,0ppm,les mm,fromabout1mmtoabout60mm,fromabout1to thanabout50pm,lesthanabout50pm,orcombina about40mm,from about1toabout20mm,from about160 tionsthereof.Insomeembodiments,theliquidresourcehas toabout10mm,fromabout1cmtoabout10cm,fromabout sodiumion,calciumion,magnesiumion,potasiumion,or 1cmtoabout8cm,fromabout1cmtoabout6cm,orfrom strontiumionconcentrationsgreaterthanabout100ppm, about1cmtoabout4cm.Insomeembodiments,theporous greaterthanabout1,0pm,greaterthanabout10,0 beadisaproximatelysphericalwithanaveragediameterof pm,orgreaterthanabout10,0pm.Insomeembodi lesthan20um,lesthan2mm,lesthan20mm,more 65ments,theliquidresourcehashydrocarbon,hydrogensul than20um,morethan2mm,morethan20mm,fromabout fide,surfactant,ormicrobeconcentrationsgreaterthanabout lutoabout10um,fromabout1umtoabout20um,from 1pb,1pm,10ppm,10pm,1,0pm,or10,0pm.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)