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A biodegradable methylcellulose‐based solid polymer electrolyte doped with calcium nitrate exhibits enhanced amorphous structure, strong polymer–salt complexation, and improved ionic conductivity, reaching 1.29 × 10−6 S/cm. The system demonstrates a 2.58 V stability window and promising EDLC performance, highlighting its potential for sustainable ...
Mahesh Vinay Kulkarni, Ismayil
wiley +1 more source
Solvate ionic liquids lubrication reduced the coefficient of friction by ∼60% compared to dry sliding, reaching steady‐state values as low as 0.04–0.05. Corrosion weight‐loss measurements in 1 M HCl further demonstrated significant inhibition behavior, with only 100 ppm of [Li(G3)][TFSI] (∼68.5 μL/L) reducing corrosion‐product weight loss by 63 ...
Sameh Dabees +6 more
wiley +1 more source
Higher hydrates of lithium chloride, lithium bromide and lithium iodide
For lithium halides, LiX (X = Cl, Br and I), hydrates with a water content of 1, 2, 3 and 5 moles of water per formula unit are known as phases in aqueous solid–liquid equilibria. The crystal structures of the monohydrates of LiCl and LiBr are known, but no crystal structures have been reported so far for the higher hydrates, apart from LiI·3H2O.
Julia Sohr +2 more
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International Journal of Refrigeration, 2015
Abstract Solubility of aqueous solutions containing lithium bromide + lithium chloride and lithium bromide + sodium formate were measured (LiBr/NaHCO 2 = 2 and LiBr/LiCl = 2 by mass ratio) at different temperatures. Visual polythermal method was used in the temperature range of (283.15–340.15) K and mass fraction range of (0.4–0.8).
Mohammad Reza Dehghani Sanij +1 more
exaly +2 more sources
Abstract Solubility of aqueous solutions containing lithium bromide + lithium chloride and lithium bromide + sodium formate were measured (LiBr/NaHCO 2 = 2 and LiBr/LiCl = 2 by mass ratio) at different temperatures. Visual polythermal method was used in the temperature range of (283.15–340.15) K and mass fraction range of (0.4–0.8).
Mohammad Reza Dehghani Sanij +1 more
exaly +2 more sources
International Journal of Refrigeration, 1989
Abstract The heat capacities of the water-lithium bromide system were measured in the temperature range 313.15–433.15 K. Those of the water-lithium bromide-zinc bromide-lithium chloride system wer also measured in the temperature range 373.15–433.15 K.
S. Iyoki, T. Uemura
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Abstract The heat capacities of the water-lithium bromide system were measured in the temperature range 313.15–433.15 K. Those of the water-lithium bromide-zinc bromide-lithium chloride system wer also measured in the temperature range 373.15–433.15 K.
S. Iyoki, T. Uemura
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The Journal of Chemical Thermodynamics, 1986
Abstract Molar enthalpies of solution of LiBr, LiBr·H 2 O, and LiBr·2H 2 O, in water at 298.15 K were determined in an LKB calorimeter. The molar enthalpies of solution extrapolated to infinite dilution are Δ sol H m o (LiBr, 298.15 K) = −(48760±128) J·mol −1 , Δ sol H m ∞ (LiBr·H 2 O, 298.15 K) = −(22581±337) J·mol −1 , and Δ sol H m ∞
Alexander Apelblat, Abraham Tamir
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Abstract Molar enthalpies of solution of LiBr, LiBr·H 2 O, and LiBr·2H 2 O, in water at 298.15 K were determined in an LKB calorimeter. The molar enthalpies of solution extrapolated to infinite dilution are Δ sol H m o (LiBr, 298.15 K) = −(48760±128) J·mol −1 , Δ sol H m ∞ (LiBr·H 2 O, 298.15 K) = −(22581±337) J·mol −1 , and Δ sol H m ∞
Alexander Apelblat, Abraham Tamir
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International Journal of Refrigeration, 1989
Abstract The vapour pressures (10.74–281.36 kPa) of the water-lithium bromide system were measured in the range of temperatures from 367.05 to 454.85 K and absorbent concentrations from 38.9 to 70.3 wt%. Furthermore, the vapour pressures (62.16–259.15 kPa) of the water-lithium bromide-zinc bromide-lithium chloride system were also measured in the ...
S Iyoki, T Uemura
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Abstract The vapour pressures (10.74–281.36 kPa) of the water-lithium bromide system were measured in the range of temperatures from 367.05 to 454.85 K and absorbent concentrations from 38.9 to 70.3 wt%. Furthermore, the vapour pressures (62.16–259.15 kPa) of the water-lithium bromide-zinc bromide-lithium chloride system were also measured in the ...
S Iyoki, T Uemura
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Lithium Carbonate-Lithium Bromide
2001(Li2CO3) [554-13-2] CLi2O3 (MW 73.89) InChI = 1S/CH2O3.2Li/c2-1(3)4;;/h(H2,2,3,4);;/q;2*+1/p-2 InChIKey = XGZVUEUWXADBQD-UHFFFAOYSA-L (LiBr) [7550-38-8] BrLi (MW 86.85) InChI = 1S/BrH.Li/h1H;/q;+1/p-1 InChIKey = AMXOYNBUYSYVKV-UHFFFAOYSA-M (reagent for dehydrohalogenation of α-halo ketones) Physical Data: see ...
Dennis Wright, Mark C. McMills
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Crystal Structure of the Monohydrates of Lithium Chloride and Lithium Bromide.
ChemInform, 2003AbstractFor Abstract see ChemInform Abstract in Full Text.
Andreas Hoennerscheid +3 more
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Industrial & Engineering Chemistry Research, 1990
Performance data have been obtained on a small absorption heat transformer operating with the following working fluid/absorbent paris : (i) water-lithium bromide, (ii) water-mixture of lithium chloride and lithium bromide (1:1 by weight), and (iii) water-lithium chloride. It is possible to deliver heat at temperatures beyond 100 ° C. It is demonstrated
Suryakant G. Pataskar +3 more
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Performance data have been obtained on a small absorption heat transformer operating with the following working fluid/absorbent paris : (i) water-lithium bromide, (ii) water-mixture of lithium chloride and lithium bromide (1:1 by weight), and (iii) water-lithium chloride. It is possible to deliver heat at temperatures beyond 100 ° C. It is demonstrated
Suryakant G. Pataskar +3 more
openaire +1 more source

