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Leaching experiments were carried out by a leaching solution of 0.5 M HCl with a certain amount of product in a 250 ml erlenmeyer for 24 hour at room temperature, than the supernatant was taken for desired ion analysis in AAS. 2.2.8 LiMnO bead preparation In LiMnO bead preparation, two methods were employed, which were suspension polymerization technique and precipitation technique - Suspension polymerization technique First organic and aqueous phases were prepared separately. Organic phase consists of 0.57 g glycidyl methacrylate (GMA), 1.4 g methyl methacrylate, 0.4 g ethylene glycol dimethacrylate and 0.03 g azobisisobutyronitrile (AIBN) and 2.37 ml toluene. In aqueous phase, 0.57 g sodium sulfate, 0.08 g polyvinyl pyrrolidone were dissolved in 28.4 g of water. Lithium manganese oxide particles were added to organic phase and formed a slurry. After aqueous phase reached to 65 oC in a constant temperature bath by a temperature controlled heater, the organic slurry was dripped onto aqueous phase slowly. The organic drops split into individual droplets in aqueous phase and the process was completed in 4 hours. - Precipitation technique In precipitation technique, 3 grams of poly (styrene-maleic anhydride-glycidyl methacrylate) (PSMA) was mixed with 1.5 g N-methyl pyrrolidone (NMP) and 1 g of LiMnO. LiMnO was added in excess amount into the mixture to be sure that NMP-PSMA solution was saturated with LiMnO content. Tap water was put into another 1 L beaker and few drops of cetyl tert butyl ammonium bromide was added. The slurry was dripped into 1 L beaker by a 5 ml volume dropper while the water was mixing with a magnet on a magnetic stirrer. After dripping process, newly formed beads continued to be mixed by the stirrer for 24 hours. Then the beads were filtered by an ordinary filter paper, washed with plenty of deionized water and dried in room temperature for 24 h. 33PDF Image | SEPARATION OF LITHIUM FROM BRINES
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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 | RSS | AMP |