PDF Publication Title:
Text from PDF Page: 014
Minerals 2021, 11, 1330 14 of 23 Minerals 2021, 11, 1330 15 of 24 5.2. Determination of the Starting and Stopping Temperatures of the Water–Rock Reaction The homogenization temperature range of gas–liquid two-phase inclusions in granite varies greatly, with a concentration range of 170–230 ◦C and an average homogenization temperature of 210.1 ◦C, indicating that the fluid temperature of the water–rock reaction is high, and the lowest temperature of mineralization is 210.1 ◦C [53]. Therefore, the initial temperature of the water–rock reaction in igneous rock was set at 150–200 ◦C, and the experimental temperature range was set at 150–400 ◦C to explore the effect of the water–rock reaction on brine mineralization. 5.3. Discussion on the Genesis of Lithium–Potassium-Rich Brine 5.3.1. Analysis of Static Immersion Experimental Results The contents of K in the five fluids were different, but the trend was similar. Most of the K content in the solution was the highest after soaking for 55 h after the seventh sampling. Moreover, weakly alkaline (pH = 8) solutions and 1 mol/L and 2 mol/L NaCl solutions were more conducive to K leaching (Figure 7). At room temperature, the content of K in the 2 mol/L NaCl was higher than that in the 1 mol/L NaCl solution, and the dissolution amount of K in the 1 mol/L of NaCl solution was 10.90 mg/L. However, its concentration increased with increasing salinity and soaking time. In the 2 mol/L NaCl solution, the maximum value was 14.86 mg/L. Basalt immersion was more conducive to potassium dissolution than granite, and the dissolution amount was one order of magnitude higher (Table 4). Figure 7. Variation diagram of K ion concentration in igneousrock static immersion experiment. Figure 7. Variation diagram of K ion concentration in igneousrock static immersion experiment. Caa,,Mg,,andSr showedaconssiisstteenntttrtreenndd,,wwitihthththeehihgihgehsetsetlemlemenetnctocnotenntetnint itnheth1e 1mool/lL/Lanadnd22mmolo/Ll/NLaNCalCsollsuotliountiso,nfso,llfowlloedwbedybthyetshoelustoilountiwonithwpitHhp=H5;=th5e;tlohweeloswtels-t eelemmeennttcoconntetnenttwwaassininththeeddisistitlileleddwaateterraannddththeessoolulutitoionnwitihthppH==88(F(Figiguureress88––1100),),inin whhicichhtthheecconttenttoffCawasthehighest, followedbyMg,,andthellowessttwaassSSrr..Witihth ininccrreeaassininggsosaokakininggtimtime,et,hethdeisdsoislsuotliuotnioanmaomunotuonftthoef threeethkrienedskionfdiosnosfiniocnresasinedcrselaoswedly. Astlorwoolym. Atetmropoemrattuerme,ptehreatCuar,eM, thge, aCnad, SMrgc,oanntednStsricno2ntmenotls/iLnN2amCollw/LerNeagCelnwerearlelygheingehre-r tahlalynhthigohserinth1anmtohlo/sLe iNna1Cml sool/lLutNioanC.lIsnotluhteio1nm. Ionl/thLeN1amColls/LolNutaiConl,sothluetmiona,xitmheumaCx-a diimssuomlutCioandaimssouluntiwonasa2m9o0u.4n0tmwga/sL2,9a0n.d40thmecgo/Ln,ceantdrathioencofnCceanintrcarteiaosnedofwCitahincreaseindg swalitnhitiynacrnedasiminmgesarslinointytimaned.Timhemmerasxioimnutimev.aTluheeomfCaxaiminutmhev2amluoel/oLfCNaCinlsthoelu2tiomnowl/Las 3N43a.C45lmsoglu/tLio.nInwthaes134m3o.4l5/LmNg/aLC.lIsnotluhteio1nm,tohle/LmNaxaiCmlusmoluMtigond,istshoelumtiaoxnimwuams18M.9g7dmisgs/oL-, wluhtiloeninwtahse182.9m7oml/gL/LN, waChlilseoilnuthioen2, mthoel/mLaNxaimClusmoluMtigond,isthsoelmutaioxinmwumas M22g.7d9isMsogl/utLio. nIn 1wmaosl2/2L.7N9aMCgl/sLo.luIntio1nm,othl/eLmNaxCimlsuomlutSirorne,ltehaesemwaaxsim1.u5m9mSgr/reLl,ewasheilweainst1h.5e92mgo/lL/,LwNhailCel sionluthtieon2 ,mthoel/mL aNxaimClusmoluStriorenl,etahse mwaxsim1.9u0mmSgr/rLele(Taaseblwe a4s).1.90 mg/L (Table 4). No concentration of lithium was detected in the five fluids. Br, I, and B were not detected in distilled water, pH = 5, and pH = 8 solutions but were detected in the 1 mol/L and 2 mol/L NaCl solutions. The changes in Br, I, and B in 1 mol/L and 2 mol/L NaCl solutions are discussed as follows:PDF Image | Origin of Lithium Potassium Rich Brines in the Jianghan
PDF Search Title:
Origin of Lithium Potassium Rich Brines in the JianghanOriginal File Name Searched:
minerals-11-01330-v2.pdfDIY 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 (Standard Web Page)