Results 101 to 110 of about 15,522 (156)
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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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Higher hydrates of lithium chloride, lithium bromide and lithium iodide
Acta Crystallographica Section C Structural Chemistry, 2018For 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, 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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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
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Journal of Chemical & Engineering Data, 2002
The differential enthalpies of dilution of the LiBr + 1,3-propanediol + water [LiBr/HO(CH2)3OH mass ratio = 3.5:1] and LiBr + LiI + LiCl + LiNO3 + water (mole ratio = 5:1:1:0.5) systems were determined at the four temperatures of 293.15, 303.15, 313.15, and 323.15 K and in the absorbent concentration ranges of 24.3−65.6 and 44.4−64.5%, respectively ...
Ki-Sub Kim, Huen Lee
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The differential enthalpies of dilution of the LiBr + 1,3-propanediol + water [LiBr/HO(CH2)3OH mass ratio = 3.5:1] and LiBr + LiI + LiCl + LiNO3 + water (mole ratio = 5:1:1:0.5) systems were determined at the four temperatures of 293.15, 303.15, 313.15, and 323.15 K and in the absorbent concentration ranges of 24.3−65.6 and 44.4−64.5%, respectively ...
Ki-Sub Kim, Huen Lee
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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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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).
Mahsa Arabi, Mohammad Reza Dehghani
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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).
Mahsa Arabi, Mohammad Reza Dehghani
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Cesium Lead Bromide Perovskite-Based Lithium–Oxygen Batteries
Nano Letters, 2021The main challenge for lithium-oxygen (Li-O2) batteries is their sluggish oxygen evolution reaction (OER) kinetics and high charge overpotentials caused by the poorly conductive discharge products of lithium peroxide (Li2O2). In this contribution, the cesium lead bromide perovskite (CsPbBr3) nanocrystals were first employed as a high-performance ...
Yin Zhou +7 more
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Journal of Chemical & Engineering Data, 1997
Heat capacities of the water + lithium bromide + ethanolamine (LiBr/H2N(CH2)2OH mass ratio = 3.5) and water + lithium bromide + 1,3-propanediol (LiBr/HO(CH2)3OH mass ratio = 3.5) systems were measured by using an isoperibol solution calorimeter at four temperatures (283.15, 298.15, 313.15, and 333.15 K) and absorbent (LiBr + H2N(CH2)2OH and LiBr + HO ...
Jin-Soo Kim +3 more
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Heat capacities of the water + lithium bromide + ethanolamine (LiBr/H2N(CH2)2OH mass ratio = 3.5) and water + lithium bromide + 1,3-propanediol (LiBr/HO(CH2)3OH mass ratio = 3.5) systems were measured by using an isoperibol solution calorimeter at four temperatures (283.15, 298.15, 313.15, and 333.15 K) and absorbent (LiBr + H2N(CH2)2OH and LiBr + HO ...
Jin-Soo Kim +3 more
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