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List of Figures Fig. 1. (a) Distribution of global lithium end-uses in various applications in the year of 2016, and (b) global lithium production in the years from 2010 to 2025. Part (a) and Part (b) of the figure were obtained from references [3–4], respectively, with copyright permissions from Elsevier. Fig. 2. Schematic diagram of separation principle of a supported liquid membrane. Figure obtained from reference [31] with copyright permission from Elsevier Fig. 3. Schematic diagram of the procedure for the preparation of IIMs for selective adsorption of Li+: (i) fabrication of the PVDF/GO hybrid membranes; (ii) PDA coating on PVDF/GO substrate as the anchor for loading imprinted sites; (iii) immobilization of 12-Crown-4-ether on the membrane surface. Figure obtained from reference [53] with copyright permission from the Royal Society of Chemistry. Fig. 4. Schematic illustration of the PSf based mixed matrix nanofibers membrane with lithium ion sieves: (i) preparation of lithium ion sieves particles; (ii) preparation of mixed LMO/PSf electrospun nanofibers; (iii) activation of mixed LMO/PSf membrane. Figure obtained from reference [63] with copyright permission from Elsevier. Fig. 5. Schematic diagram of the MDC system. Figure obtained from reference [67] with copyright permission from Elsevier. Fig. 6. Schematic illustration of (a) conventional ED stack and (b) BMED stack for recovering lithium. Figure obtained from reference [81] with copyright permission from ACS Publications. Fig. 7. Schematic illustration of PSMCDI lithium recovery system of (a) adsorption and (b) desorption processes. Figure obtained from reference [100] with copyright permission from Elsevier Publications. Fig. 8. Illustrations of the relationships between energy consumption and feed salinity in S-ED, PSMCDI, MDC, NF, SLM, IIM and LISM. 47PDF Image | Membrane based technologies for lithium recovery from water lithium
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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)