10 research outputs found
Influence of a binder on the electrochemical behaviour of Si/RGO composite as negative electrode material for Li-ion batteries
Received: 02.12.2020. Accepted: 21.12.2020. Published:30.12.2020.A composite consisting of silicon nanoparticles and reduced graphene oxide nanosheets (Si/RGO) was studied as a promising material for the negative electrode of lithium-ion batteries. Commonly used polyvinylidene fluoride (PVdF) and carboxymethyl cellulose (CMC) served as a binder. To reveal the influence of the binder on the electrochemical behaviour of the Si/RGO composite, binder-free electrodes were also prepared and examined. Anode half-cells with composites comprising CMC as a binder demonstrated the best properties: capacity over 1200 mAhΒ·gβ1, excellent cycling performance and good rate capability up to 1.0C.This work was performed with financial support from the Ministry of Science and Higher Education of Russian Federation, project ID RFMEFI60419X0235
Temperature Dependence of Initial Permeability of NixCo1-xFe2O4 Ferrite System
The aim of this work was to create and study of ferrite nickel-cobalt powders, using sol-gel technology with participation of auto-combustion. Dependence of the initial permeability from the degree of substitution of cobalt cations on nickel cations is obtained. It is revealed that the crystallite size has a significant influence on the magnetic properties of the samples. With decreasing of crystallite size of nickel-cobalt ferrite Curie temperature decreases. It is shown that the smaller the particle size, the greater the thickness of the surface layer with significant violations of magnetic structure. Keywords: sol-gel technology, nickel-cobalt ferrite, initial permeability, Curie temperature
SOLID ELECTROLYTE AND ELECTRODE-ACTIVATED MEMBRANE WITH ITS EMPLOYMENT
FIELD: solid polymer ion conductors, namely, ion-conducting polymer electrolytes which can be used in electrochemical devices, specifically, in electrode-activated membranes. SUBSTANCE: given solid electrolyte contains copolymer based on acrylonitrile and butadiene carrying over 17.0 per cent by mass bonds of acrylonitrile or copolymer based on acrylonitrile and butadiene containing over 17.0 per cent by mass bonds of acrylonitrile and additionally under 5.0 per cent by mass of monomer residue of unsaturated carbonic acid. Solid electrolyte contains cobalt chloride (II) in the capacity of inorganic salt of metal with following proportion of components, molecular per cent,: copolymer of acrylonitrile and butadiene 99.00- 99.80; cobalt chloride (II) 0.20-1.00. Electrode-activated membrane includes layer of solid polymer electrolyte and metal current tap in which layer of solid polymer electrolyte has composition in mole per cent: copolymer of acrylonitrile and butadiene containing over 17.0 per cent by mass bonds of acrylonitrile or copolymer based on acrylonitrile and butadiene containing over 17 per cent by mass bonds of acrylonitrile and additionally containing under 5.0 per cent by mass monomeric residue of unsaturated carbonic acid - 99.00-99.80 and cobalt chloride (II) -0.20-1.00 and is 10- 150 mcm thick. Solid polymer electrolyte of proposed composition has conductance of the order of 10-8Ohm-1cm-1 and cobalt (II) detection limit 10-6mole/l. Proposed solid polymer electrolyte can be utilized in electrode-activated membrane showing good operational characteristics and simple design. EFFECT: development of solid polymer electrolyte to detect ions of cobalt and of electrode-activated membrane with its use. 2 cl, 2 dwg.ΠΠ·ΠΎΠ±ΡΠ΅ΡΠ΅Π½ΠΈΠ΅ ΠΎΡΠ½ΠΎΡΠΈΡΡΡ ΠΊ ΠΎΠ±Π»Π°ΡΡΠΈ ΡΠ²Π΅ΡΠ΄ΠΎΡΠ΅Π»ΡΠ½ΡΡ
ΠΏΠΎΠ»ΠΈΠΌΠ΅ΡΠ½ΡΡ
ΠΈΠΎΠ½Π½ΡΡ
ΠΏΡΠΎΠ²ΠΎΠ΄Π½ΠΈΠΊΠΎΠ², Π° ΠΈΠΌΠ΅Π½Π½ΠΎ ΠΊ ΠΈΠΎΠ½-ΠΏΡΠΎΠ²ΠΎΠ΄ΡΡΠΈΠΌ ΠΏΠΎΠ»ΠΈΠΌΠ΅ΡΠ½ΡΠΌ ΡΠ»Π΅ΠΊΡΡΠΎΠ»ΠΈΡΠ°ΠΌ, ΠΊΠΎΡΠΎΡΡΠ΅ ΠΌΠΎΠ³ΡΡ Π±ΡΡΡ ΠΈΡΠΏΠΎΠ»ΡΠ·ΠΎΠ²Π°Π½Ρ Π² ΡΠ»Π΅ΠΊΡΡΠΎΡ
ΠΈΠΌΠΈΡΠ΅ΡΠΊΠΈΡ
ΡΡΡΡΠΎΠΉΡΡΠ²Π°Ρ
, Π² ΡΠ°ΡΡΠ½ΠΎΡΡΠΈ Π² ΡΠ»Π΅ΠΊΡΡΠΎΠ΄Π½ΠΎ-Π°ΠΊΡΠΈΠ²Π½ΡΡ
ΠΌΠ΅ΠΌΠ±ΡΠ°Π½Π°Ρ
. Π’Π²Π΅ΡΠ΄ΡΠΉ ΡΠ»Π΅ΠΊΡΡΠΎΠ»ΠΈΡ ΡΠΎΠ΄Π΅ΡΠΆΠΈΡ ΡΠΎΠΏΠΎΠ»ΠΈΠΌΠ΅Ρ Π½Π° ΠΎΡΠ½ΠΎΠ²Π΅ Π°ΠΊΡΠΈΠ»ΠΎΠ½ΠΈΡΡΠΈΠ»Π° ΠΈ Π±ΡΡΠ°Π΄ΠΈΠ΅Π½Π°, ΡΠΎΠ΄Π΅ΡΠΆΠ°ΡΠΈΠΉ Π½Π΅ ΠΌΠ΅Π½Π΅Π΅ 17 ΠΌΠ°Ρ.% Π·Π²Π΅Π½ΡΠ΅Π² Π°ΠΊΡΠΈΠ»ΠΎΠ½ΠΈΡΡΠΈΠ»Π°, ΠΈΠ»ΠΈ ΡΠΎΠΏΠΎΠ»ΠΈΠΌΠ΅Ρ Π½Π° ΠΎΡΠ½ΠΎΠ²Π΅ Π°ΠΊΡΠΈΠ»ΠΎΠ½ΠΈΡΡΠΈΠ»Π° ΠΈ Π±ΡΡΠ°Π΄ΠΈΠ΅Π½Π°, ΡΠΎΠ΄Π΅ΡΠΆΠ°ΡΠΈΠΉ Π½Π΅ ΠΌΠ΅Π½Π΅Π΅ 17 ΠΌΠ°Ρ.% Π·Π²Π΅Π½ΡΠ΅Π² Π°ΠΊΡΠΈΠ»ΠΎΠ½ΠΈΡΡΠΈΠ»Π°, ΠΈ Π΄ΠΎΠΏΠΎΠ»Π½ΠΈΡΠ΅Π»ΡΠ½ΠΎ Π½Π΅ Π±ΠΎΠ»Π΅Π΅ 5 ΠΌΠ°Ρ.% ΠΌΠΎΠ½ΠΎΠΌΠ΅ΡΠ½ΡΡ
ΠΎΡΡΠ°ΡΠΊΠΎΠ² Π½Π΅ΠΏΡΠ΅Π΄Π΅Π»ΡΠ½ΡΡ
ΠΊΠ°ΡΠ±ΠΎΠ½ΠΎΠ²ΡΡ
ΠΊΠΈΡΠ»ΠΎΡ, Π² ΠΊΠ°ΡΠ΅ΡΡΠ²Π΅ Π½Π΅ΠΎΡΠ³Π°Π½ΠΈΡΠ΅ΡΠΊΠΎΠΉ ΡΠΎΠ»ΠΈ ΠΌΠ΅ΡΠ°Π»Π»Π° - Ρ
Π»ΠΎΡΠΈΠ΄ ΠΊΠΎΠ±Π°Π»ΡΡΠ° II ΠΏΡΠΈ ΡΠ»Π΅Π΄ΡΡΡΠ΅ΠΌ ΡΠΎΠΎΡΠ½ΠΎΡΠ΅Π½ΠΈΠΈ ΠΊΠΎΠΌΠΏΠΎΠ½Π΅Π½ΡΠΎΠ², ΠΌΠΎΠ».%: ΡΠΎΠΏΠΎΠ»ΠΈΠΌΠ΅Ρ Π°ΠΊΡΠΈΠ»ΠΎΠ½ΠΈΡΡΠΈΠ»Π° ΠΈ Π±ΡΡΠ°Π΄ΠΈΠ΅Π½Π° 99,00-99,80, Ρ
Π»ΠΎΡΠΈΠ΄ ΠΊΠΎΠ±Π°Π»ΡΡΠ° II 0,20-1,00. ΠΠ»Π΅ΠΊΡΡΠΎΠ΄Π½ΠΎ-Π°ΠΊΡΠΈΠ²Π½Π°Ρ ΠΌΠ΅ΠΌΠ±ΡΠ°Π½Π° ΡΠΎΠ΄Π΅ΡΠΆΠΈΡ ΡΠ»ΠΎΠΉ ΡΠ²Π΅ΡΠ΄ΠΎΠ³ΠΎ ΠΏΠΎΠ»ΠΈΠΌΠ΅ΡΠ½ΠΎΠ³ΠΎ ΡΠ»Π΅ΠΊΡΡΠΎΠ»ΠΈΡΠ° ΠΈ ΠΌΠ΅ΡΠ°Π»Π»ΠΈΡΠ΅ΡΠΊΠΈΠΉ ΡΠΎΠΊΠΎΠΎΡΠ²ΠΎΠ΄, Π² ΠΊΠΎΡΠΎΡΠΎΠΉ ΡΠ»ΠΎΠΉ ΡΠ²Π΅ΡΠ΄ΠΎΠ³ΠΎ ΠΏΠΎΠ»ΠΈΠΌΠ΅ΡΠ½ΠΎΠ³ΠΎ ΡΠ»Π΅ΠΊΡΡΠΎΠ»ΠΈΡΠ° ΠΈΠΌΠ΅Π΅Ρ ΡΠΎΡΡΠ°Π², ΠΌΠΎΠ»Ρ.%: ΡΠΎΠΏΠΎΠ»ΠΈΠΌΠ΅Ρ Π°ΠΊΡΠΈΠ»ΠΎΠ½ΠΈΡΡΠΈΠ»Π° ΠΈ Π±ΡΡΠ°Π΄ΠΈΠ΅Π½Π°, ΡΠΎΠ΄Π΅ΡΠΆΠ°ΡΠΈΠΉ Π½Π΅ ΠΌΠ΅Π½Π΅Π΅ 17 ΠΌΠ°Ρ.% Π·Π²Π΅Π½ΡΠ΅Π² Π°ΠΊΡΠΈΠ»ΠΎΠ½ΠΈΡΡΠΈΠ»Π°, ΠΈΠ»ΠΈ ΡΠΎΠΏΠΎΠ»ΠΈΠΌΠ΅Ρ Π½Π° ΠΎΡΠ½ΠΎΠ²Π΅ Π°ΠΊΡΠΈΠ»ΠΎΠ½ΠΈΡΡΠΈΠ»Π° ΠΈ Π±ΡΡΠ°Π΄ΠΈΠ΅Π½Π°, ΡΠΎΠ΄Π΅ΡΠΆΠ°ΡΠΈΠΉ Π½Π΅ ΠΌΠ΅Π½Π΅Π΅ 17 ΠΌΠ°Ρ.% Π·Π²Π΅Π½ΡΠ΅Π² Π°ΠΊΡΠΈΠ»ΠΎΠ½ΠΈΡΡΠΈΠ»Π° ΠΈ Π΄ΠΎΠΏΠΎΠ»Π½ΠΈΡΠ΅Π»ΡΠ½ΠΎ ΡΠΎΠ΄Π΅ΡΠΆΠ°ΡΠΈΠΉ Π½Π΅ Π±ΠΎΠ»Π΅Π΅ 5 ΠΌΠ°Ρ.% ΠΌΠΎΠ½ΠΎΠΌΠ΅ΡΠ½ΡΡ
ΠΎΡΡΠ°ΡΠΊΠΎΠ² Π½Π΅ΠΏΡΠ΅Π΄Π΅Π»ΡΠ½ΡΡ
ΠΊΠ°ΡΠ±ΠΎΠ½ΠΎΠ²ΡΡ
ΠΊΠΈΡΠ»ΠΎΡ, 99,00?99,80 ΠΈ Ρ
Π»ΠΎΡΠΈΠ΄ ΠΊΠΎΠ±Π°Π»ΡΡΠ° II - 0,20?1,00, ΠΈ ΠΈΠΌΠ΅Π΅Ρ ΡΠΎΠ»ΡΠΈΠ½Ρ 10-150 ΠΌΠΊΠΌ. Π’Π²Π΅ΡΠ΄ΡΠΉ ΠΏΠΎΠ»ΠΈΠΌΠ΅ΡΠ½ΡΠΉ ΡΠ»Π΅ΠΊΡΡΠΎΠ»ΠΈΡ ΠΏΡΠ΅Π΄Π»Π°Π³Π°Π΅ΠΌΠΎΠ³ΠΎ ΡΠΎΡΡΠ°Π²Π° ΠΈΠΌΠ΅Π΅Ρ ΠΏΡΠΎΠ²ΠΎΠ΄ΠΈΠΌΠΎΡΡΡ ΠΏΠΎΡΡΠ΄ΠΊΠ° 10-8 ΠΠΌ-1β’ΡΠΌ-1 ΠΈ ΠΏΡΠ΅Π΄Π΅Π» ΠΎΠ±Π½Π°ΡΡΠΆΠ΅Π½ΠΈΡ ΠΊΠΎΠ±Π°Π»ΡΡΠ° II 10-6 ΠΌΠΎΠ»Ρ/Π». ΠΡΠ΅Π΄Π»Π°Π³Π°Π΅ΠΌΡΠΉ ΡΠ»Π΅ΠΊΡΡΠΎΠ»ΠΈΡ ΠΌΠΎΠΆΠ΅Ρ Π±ΡΡΡ ΠΈΡΠΏΠΎΠ»ΡΠ·ΠΎΠ²Π°Π½ Π² ΡΠ»Π΅ΠΊΡΡΠΎΠ΄Π½ΠΎ-Π°ΠΊΡΠΈΠ²Π½ΠΎΠΉ ΠΌΠ΅ΠΌΠ±ΡΠ°Π½Π΅, ΠΎΠ±Π»Π°Π΄Π°ΡΡΠ΅ΠΉ Ρ
ΠΎΡΠΎΡΠΈΠΌΠΈ ΡΠ°Π±ΠΎΡΠΈΠΌΠΈ Ρ
Π°ΡΠ°ΠΊΡΠ΅ΡΠΈΡΡΠΈΠΊΠ°ΠΌΠΈ, ΠΏΡΠΎΡΡΠΎΠΉ ΠΊΠΎΠ½ΡΡΡΡΠΊΡΠΈΠΈ. Π’Π΅Ρ
Π½ΠΈΡΠ΅ΡΠΊΠΈΠΌ ΡΠ΅Π·ΡΠ»ΡΡΠ°ΡΠΎΠΌ ΠΏΡΠ΅Π΄Π»ΠΎΠΆΠ΅Π½Π½ΠΎΠ³ΠΎ ΠΈΠ·ΠΎΠ±ΡΠ΅ΡΠ΅Π½ΠΈΡ ΡΠ²Π»ΡΠ΅ΡΡΡ ΡΠ°Π·ΡΠ°Π±ΠΎΡΠΊΠ° ΡΠΎΡΡΠ°Π²Π° ΡΠ²Π΅ΡΠ΄ΠΎΠ³ΠΎ ΠΏΠΎΠ»ΠΈΠΌΠ΅ΡΠ½ΠΎΠ³ΠΎ ΡΠ»Π΅ΠΊΡΡΠΎΠ»ΠΈΡΠ° Π΄Π»Ρ ΠΎΠ±Π½Π°ΡΡΠΆΠ΅Π½ΠΈΡ ΠΈΠΎΠ½ΠΎΠ² ΠΊΠΎΠ±Π°Π»ΡΡΠ°, Π° ΡΠ°ΠΊΠΆΠ΅ ΡΠ»Π΅ΠΊΡΡΠΎΠ΄Π½ΠΎ-Π°ΠΊΡΠΈΠ²Π½ΠΎΠΉ ΠΌΠ΅ΠΌΠ±ΡΠ°Π½Ρ Ρ Π΅Π³ΠΎ ΠΈΡΠΏΠΎΠ»ΡΠ·ΠΎΠ²Π°Π½ΠΈΠ΅ΠΌ ΠΏΡΠΎΡΡΠΎΠΉ ΠΊΠΎΠ½ΡΡΡΡΠΊΡΠΈΠΈ. 2 Ρ. ΠΏ. Ρ-Π»Ρ, 2 ΠΈΠ»
Lithium conducting solid polymer electrolytes based on polyacrylonitrile copolymers: Ion solvation and transport properties
Polymer-in-Salt Electrolytes Based on Acrylonitrile/Butyl Acrylate Copolymers and Lithium Salts
Evaluation of the main processing parameters influencing the performance of poly(vinylidene fluoride β trifluorethylene) lithium ion battery separators
Poly(vinylidene fluoride β trifluorethylene) membranes are evaluated for lithium ion battery separator applications. Some of the main parameters affecting separator performance such as porosity, dehydration of lithium ions and processing technique (Li-ion uptake versus composite formation) are investigated. The polymer characteristics, as determined by infrared spectroscopy, do not change as a function of porosity, dehydration of lithium ions in the electrolyte solution or processing technique. The electrochemical impedance spectroscopy represented through the Nyquist plot, Bode plot and the ionic conductivity as a function of temperature, strongly depends on the aforementioned paramenters. The membrane that exhibits the highest ionic conductivity is a porous membrane without dehydration of lithium ions and prepared by the uptake technique. The performance of the membrane for battery applications are therefore strongly influenced both by porosity and processing technique.This work is funded by FEDER funds through the "Programa Operacional Factores de Competitividade β COMPETE" and by national funds by FCT- Fundação para a CiΓͺncia e a Tecnologia, project references Projects PTDC/CTM/69316/2006, project nΒΊF-COMP-01-0124-FEDER-022716 (refΒͺ FCT PEst-C/QUI/UI0686/2011) and NANO/NMed-SD/0156/2007, and grants SFRH/BD/68499/2010 (C.M.C) and SFRH/BPD/63148/2009 (V.S.). The authors thank Celgard, LLC for kindly supplying their high quality membranes. The authors also thank support from the COST Action MP1003, 2010 βEuropean Scientific Network for Artificial Musclesβ