PDF Publication Title:
Text from PDF Page: 021
Figure 3.33 The breakthrough curves at different initial lithium concentrations. .....98 Figure 3.34 The breakthrough curves at different flow rates...................................100 Figure 3.35 The breakthrough curves for different bead sizes.................................101 Figure 3.36 The breakthrough curve for sodium chloride feed solution .................103 Figure 3.37 The breakthrough curve for potassium chloride feed solution ............. 104 Figure 3.38 The breakthrough curve for magnesium chloride feed solution...........105 Figure 3.39 The effluent lithium concentration in a column fed with artificially prepared brine solution.............................................................................................107 Figure 3.40 The effluent lithium concentration in a column fed with concentrated brine solution from Çamaltı Salina ..........................................................................108 Figure 3.41 The elution curve after Run 3...............................................................110 Figure 3.42 The change of ion concentrations in sweeping process applied after Run 12..............................................................................................................................112 Figure 3.43 The molar ratio of potassium and magnesium with respect to lithium during sweeping process ..........................................................................................113 Figure 3.44 The change of ion concentrations in sweeping process applied after Run 14..............................................................................................................................121 xxiPDF Image | SEPARATION OF LITHIUM FROM BRINES
PDF Search Title:
SEPARATION OF LITHIUM FROM BRINESOriginal File Name Searched:
separation-lithium-from-brine.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 | RSS | AMP |