logo

P507 TBP Carriers for Lithium Extraction from Brines

PDF Publication Title:

P507 TBP Carriers for Lithium Extraction from Brines ( p507-tbp-carriers-lithium-extraction-from-brines )

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

Text from PDF Page: 003

Membranes 2022, 12, x FOR PEER REVIEW 3 of 13 Membranes 2022, 12, 839 used for the experiment without further purification. The deionized water with a conduc- tivity of less than 5 μS/cm was used as the medium to prepare the salt solutions. 2.2. Preparation of PIMs The PIMs using CTA as the polymer matrix and P507-TBP as extraction carrier were The PIMs using CTA as the polymer matrix and P507-TBP as extraction carrier were synthesized by the casting method according to the procedures in Figure 1. Specifically, synthesized by the casting method according to the procedures in Figure 1. Specifically, 0.2 g 0.2 g of CTA was dissolved into 5 mL of DCM. The TBP and P507 were mixed uniformly of CTA was dissolved into 5 mL of DCM. The TBP and P507 were mixed uniformly with with the volume ratio of 3:1 to prepare the extraction carrier [35]. Then the P507-TBP mix- 3 of 13 2.2. Preparation of PIMs the volume ratio of 3:1 to prepare the extraction carrier [35]. Then the P507-TBP mixture ture was added to the CTA solution, and the homogeneous casting solution was obtained was added to the CTA solution, and the homogeneous casting solution was obtained after after stirring for 1 h. Finally, the casting solution was transferred onto a 5 cm × 5 cm flat stirring for 1 h. Finally, the casting solution was transferred onto a 5 cm × 5 cm flat glass glass and placed at room temperature for 12 h to evaporate the solvent. The resulting and placed at room temperature for 12 h to evaporate the solvent. The resulting membrane membrane was peeled and marked as CTA/P507-TBPX, where X refers to the mass frac- was peeled and marked as CTA/P507-TBPX, where X refers to the mass fraction of P507- tion of P507-TBP in the membrane (X = 20 wt.%, 30 wt.%, 40 wt.%, 50 wt.%, 60 wt.% and TBP in the membrane (X = 20 wt.%, 30 wt.%, 40 wt.%, 50 wt.%, 60 wt.% and 70 wt.%). The 70 wt.%). The composition and thickness of PIMs are listed in Table 1. composition and thickness of PIMs are listed in Table 1. Figure 1. Schematic diagram of preparing CTA/P507-TBP membranes. Figure 1. Schematic diagram of preparing CTA/P507-TBP membranes. Table 1. The compositions and thicknesses of PIMs. Table 1. The compositions and thicknesses of PIMs. Membraneess CTA/P507-TBP2200%% CTA 0.2g P507-TBP((v/v/v: :33/1/1) ) 0.05 Thickness((μμm) ) 72± 3 81 ± 6 81 ± 6 CTA/P507-TBP30% 0.2 g 0.086 CTA/P507-TBP30% 0.2 g 0.086 97 ± 4 97 ± 4 CTA/P507-TBP40% 0.2 g 0.133 CTA/P507-TBP40% 0.2 g 0.133 112 ± 3 112 ± 3 CTA/P507-TBP50% 0.2 g 0.2 CTA/P507-TBP50% 0.2 g 0.2 132 ± 4 CTA/P507-TBP60% 0.2 g 0.3 CTA/P507-TBP60% 0.2 g 0.3 132 ± 4 CTA/P507-TBP70% 0.2 g 0.467 165 ± 3 165 ± 3 CTA/P507-TBP70% 2.3. Characterization of PIMs 2.3. Characterization of PIMs 0.2 g 0.467 The surface and cross-sectional morphologies of CTA/P507-TBP membranes were The surface and cross-sectional morphologies of CTA/P507-TBP membranes were observed by scanning electron microscopy (SEM, Hitachi S4800, Tokyo, Japan), and the observed by scanning electron microscopy (SEM, Hitachi S4800, Tokyo, Japan), and the element distribution of the membrane was investigated by energy dispersive X-ray spec- element distribution of the membrane was investigated by energy dispersive X-ray spec- troscopy (EDX, Tokyo, Japan). Fourier transform infrared spectroscopy (FTIR, Nicolet 6700, −1 Mtroascsoacphyu(sEetDtsX,,ATmoekryioca,)Jawpiathn)t.hFeosucarinenrintrganrasnfogremofin80fr0a–r2e0d00spcemctroswcaospayp(pFlTieIdR,toNsitcuodleyt −1 t6h7e00st,rMucatsusraecohfufsuenttcst,ioAnmalergircoau)pwsiitnhPthIMesc.aTnhneinwgartaenrgcoenotfac8t0a0n–2g0le00ofcmthemweamsabprapnliedsutro- fsatcuedwyathsetesstrteudctbuyreaonfofupntictailocnoanltgarcotuapnsgilnePmIeMasu.Trihnegwanataelryzcoernt(aOcCtaAnHg2le0o0)f.thFievmeedmiffberaenet siuterfsaocfe mweams tbersatnede sbaymapnleopwtiecrael sceolnectatecdt afnogr ltehemmeaesausruinregmaennatlyozfecro(nOtaCcAt Han2g0l0e)s.,Fainvde dthife- afevreernatgseitveasluofemweams dbreatenremsainmedplaeswthereefisnealelcrtesduflto.r the measurement of contact angles, and the average value was determined as the final result. 2.4. Transport Experiments The transport experiments were performed in a two-compartment permeation cell to study the Li+ separation performance of the CTA/P507-TBP membrane. As shown in Figure 2, the feed side was filled with 150 mL of a mixed solution containing 0.1 mol/L of

PDF Image | P507 TBP Carriers for Lithium Extraction from Brines

p507-tbp-carriers-lithium-extraction-from-brines-003

PDF Search Title:

P507 TBP Carriers for Lithium Extraction from Brines

Original File Name Searched:

membranes-12-00839.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