logo

Patent Lithium Extraction with coated ion exchange particles

PDF Publication Title:

Patent Lithium Extraction with coated ion exchange particles ( patent-lithium-extraction-with-coated-ion-exchange-particles )

Previous Page View | Next Page View | Return to Search List

Text from PDF Page: 009

US 10,695,694B2 78 LiSiO3,Li,Si,Os,LiMnOz,ZrSiO4,AIPO4,LaPO4, oxidants,reductants,acids,bases,orcombinationsthereof. ZrP,O,MOP,0%,Mo,P,0,2,BaSO4,AlF3,Sic,Tic,Zrc, Insomeembodiments,thereagentsareadedinthepres SizN4,ZrN,BN,carbon,graphiticcarbon,amorphouscar enceofcatalystssuchasacids,bases,orcombinations bon,hardcarbon,diamond-likecarbon,solidsolutions thereof.Insomeembodiments,thereagentsareaded thereof,orcombinationsthereof.Insomeembodiments,the 5 duringatimeperiodoflesthan1minute,lesthan1hour, coatingmaterialcomprisespolyvinylidenedifluoride,poly lesthan1day,lesabout1week,morethan1minute,more vinylchloride,afluoro-polymer,achloro-polymer,ora than1hour,morethan1day,fromabout1minutetoabout fluoro-chloro-polymer.Insomeembodiments,thecoating 60minutes,fromabout1hourtoabout24hours,orfrom materialcomprisesTiO2,ZrO2,SiO2M002,LiTiO3, about1daytoabout7days.Insomeembodiments,the LiZr03,Li,MnO3,ZrSiO4,orLiNbO3,AlF3,Sic,SizN4,10reagentsaredripedintothereactorcontinuouslyorat graphiticcarbon,amorphouscarbon,diamond-likecarbon, intervals.Insomeembodiments,multiplereagentsareaded orcombinationsthereof.Insomeembodiments,thecoating tothereactoratdiferentrates.Insomeembodiments,some materialcomprisesTiO2,SiO2,orZrO2.Insomeembodi reagentsarecombinedseparatelyandreactedtoformagel ments,thecoatingmaterialcomprisesTiO2.Insome orpolymerpriortoaditiontothereactor. embodiments,thecoatingmaterialcomprisesSiO2.Insome15 Insomeembodiments,thefreshlycoatedionexchange embodiments,thecoatingmaterialcomprisesZroz. materialisheatedtooneormoretemperaturestoage,dry, Insomeembodiments,thecoatingcoatsprimaryion react,orcrystalizethecoating.Insomeembodiments,the exchangeparticlesorsecondaryionexchangeparticles.In freshlycoatedionexchangematerialisheatedtoatempera someembodiments,thecoatingcoatsboththeprimaryion tureoflesthanabout10°C.,lesthanabout20°C.,les exchangeparticlesandthesecondaryionexchangeparticles.20thanabout30°C.,lesthanabout40°C.,lesthanabout Insomeembodiments,theprimaryionexchangeparticles 50°C.,lesthanabout600°C.,lesthanabout70°C.,or haveafirstcoatingandthesecondaryionexchangeparticles lesthanabout800°C.Insomeembodiments,thefreshly haveasecondcoatingthatisidentical,similar,ordiferent coatedionexchangematerialisheatedtoatemperatureof in composition to the first coating. more than about 100° C.,more than about 200° C.,more Insomeembodiments,thecoatingmaterialhasathick-25 thanabout300°C.,morethanabout400°C.,morethan nessoflesthan1nm,lesthan10nm,lesthan100nm, about500°C.,morethanabout600°C.,morethanabout lesthan1,0nm,lesthan10,0nm,morethan1nm, 700°C.,ormorethanabout80°C.Insomeembodiments, morethan10nm,morethan10nm,morethan1,0nm, thefreshlycoatedionexchangematerialisheatedtoa morethan10,0nm,fromabout1nmtoabout10,0nm, temperaturefromabout100°C.toabout800°C.,fromabout fromabout10nm,toabout1,0nm,orfromabout10to3020°C.toabout80°C.,fromabout30°C.toabout70° about1,0nm.Insomeembodiments,thecoatingmaterial C.,fromabout400°C.toabout70°C.,fromabout500°C. hasathicknesoflesthan5nm,lesthan10nm,lesthan toabout700°C.,fromabout10°C.toabout300°C.,from 50nm,lesthan10nm,lesthan500nm,morethan1nm, about200°C.toabout400°C.,fromabout300°C.toabout morethan5nm,morethan10nm,morethan50nm,more 50°C.,fromabout400°C.toabout600°C.,fromabout than10nm,fromabout1nm toabout50nm,fromabout3550°C.toabout70°C.,orfrom about600°C.toabout 1nmtoabout10nm,fromabout1nmtoabout50nm, 800°C.Insomeembodiments,thefreshlycoatedion fromabout1nmtoabout10nm,fromabout1nmtoabout exchangematerialisheatedinanatmosphereofaircom 5nm,orfrom about5nm toabout10nm. prisingoxygen,nitrogen,hydrogen,argon,orcombinations Insomeembodiments,thecoatingmaterialisdeposited thereof.Insomeembodiments,thefreshlycoatedion byamethodsuchaschemicalvapordeposition,atomiclayer40exchangematerialisheatedforatimeperiodoflesthan deposition,physicalvapordeposition,hydrothermal,solvo about1hour,lesthanabout2hours,lesthanabout4hours, thermal,sol-gel,solidstate,moltensaltflux,ionexchange, lesthanabout8hours,lesthanabout24hours,morethan microwave,chemicalprecipitation,co-precipitation,bal 1hour,morethan2hours,morethan4hours,morethan8 miling,pyrolysis,orcombinationsthereof.Insome hours,fromabout0.5hourstoabout24hours,fromabout embodiments,thecoatingmaterialisdepositedbyamethod450.5hourstoabout8hours,fromabout0.5hourstoabout4 suchaschemicalvapordeposition,hydrothermal,solvother hours,fromabout0.5hourstoabout2hours,orfromabout mal,sol-gel,precipitation,microwavesol-gel,chemical 0.5hourstoabout1hour. precipitation,orcombinationsthereof.Insomeembodi Insomeembodiments,thecoatingmaterialisdeposited ments,thecoatingmaterialsisdepositedinareactorthatis withphysicalcharacteristicssuchascrystaline,amorphous, abatchtankreactor,acontinuoustankreactor,abatch 50fulcoverage,partialcoverage,uniform,non-uniform,or furnace,acontinuousfurnace,atubefurnace,arotarytube combinationsthereof.Insomeembodiments,multiplecoat furnace, or combinations thereof. ings are deposited on the ion exchange material in an Insomeembodiments,thecoatingmaterialisdepositedin arangementsuchasconcentric,patchwork,orcombinations areactorbysuspendingtheionexchangematerialina thereof. solventwithreagentsthatisadedalatonceoradedover5IonExchangeMaterialofCoatedIonExchangeParticle time.Insomeembodiments,thereagentsareadedina Insomeembodiments,theionexchangematerialissuit specifictimeseriestocontrolreactionratesandcoating ableforhighlithiumabsorptioncapacityandforlithium depositions.Insomeembodiments,thesolventisaqueousor ionsinaliquidresourcerelativetootherionssuchassodium non-aqueous.Insomeembodiments,thesolventisanalco ionsandmagnesiumions.Insomeembodiments,theion holsuchasethanol,propanol,butanol,pentanol,hexanol,60 exchangematerialissuitableforstronglithiumionuptakein septanol,oroctanol.Insomeembodiments,thereagents liquidresourcesincludingthosewithlowconcentrationsof includemetalchlorides,metaloxides,metalalkoxides, lithiumions,facileelutionoflithiumionswithasmal metaloxychlorides,metaloidoxides,metaloidalkoxides, excesofacid,andfastionicdifusion. metaloidchlorides,metaloidoxychlorides,orcombina Insomeembodiments,theionexchangematerialcom tionsthereof.Insomeembodiments,thereagentsinclude65prisesanoxide,aphosphate,anoxyfluoride,afluorophos monomers,oligomers,polymers,gels,orcombinations phate,orcombinationsthereof.Inafurtherembodiment,the thereof.Insomeembodiments,thereagentsincludewater, ionexchangematerialcomprisesLiFePO4,LiMnPO4,

PDF Image | Patent Lithium Extraction with coated ion exchange particles

patent-lithium-extraction-with-coated-ion-exchange-particles-009

PDF Search Title:

Patent Lithium Extraction with coated ion exchange particles

Original File Name Searched:

US10695694.pdf

DIY PDF Search: Google It | Yahoo | Bing

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 | RSS | AMP