Stanislaw Sosnowski
Current Organizations / Institutes
The organizations/institutes from the scholar's latest article
Previous Organizations / Institutes
The organizations / institutes from the scholar's other articles in the past ten years
Stanislaw Sosnowski has a total of 18 co-authors. Here are the top co-authors by number of shared publications:
- Ryszard Szymanski
Centre of Molecular and Macromolecular Studies, Polish Academy of Sciences, Sienkiewicza 112, 90-363 Lodz, Poland
14 shared publications - Alexander Penlidis
Department of Chemical Engineering, Institute for Polymer Research (IPR)
1 shared publication Alison J. Scott
1 shared publicationAndrzej Duda
Centre of Molecular and Macromolecular Studies, Polish Academy of Sciences, 90-363 Lodz, Sienkiewicza 112, Poland
1 shared publication- Jing Lyu
Charles Institute of Dermatology, School of Medicine, University College Dublin, Dublin, Ireland
1 shared publication Krzysztof Matyjaszewski
1 shared publication
Latest Publications
- 13 September 2025
- Published by Elsevier in Chemical Engineering Science
- Vol. 320
On determination of reactivity ratios for living/quasi-living copolymerization with slow initiation
- 13 September 2025
- Published by Elsevier in Chemical Engineering Science
- Vol. 320
On determination of reactivity ratios for living/quasi-living copolymerization with slow initiation
- Open Access
- 22 August 2023
- Published by Elsevier in Chemical Engineering Journal
- Vol. 474
Active kinetic chain length: Guide for control in atom transfer radical polymerization
- 22 August 2023
- Published by Elsevier in Chemical Engineering Journal
- Vol. 474
Open AccessActive kinetic chain length: Guide for control in atom transfer radical polymerization
- Open Access
- 7 November 2019
- Published by AIP Publishing in The Journal of Chemical Physics
- Vol. 151 (17) , 174113
Stochasticity of the transfer of reactant molecules between nano-reactors affecting the reversible association A + B ⇆ C
Theoretical analysis and computer simulations (Monte Carlo and numerical integration of differential equations) indicate that the statistical effect of a small number of reacting molecules is affected by transfer of reagent molecules between nanoreactors (droplets in this study). As a model reaction, a simple reversible association A + B ⇆ C was chosen, which was studied previously without reagent transfer processes. For sufficiently fast exchange of reactant molecules and a sufficiently high number of nanoreactors, the studied systems virtually do not differ from large volume systems if overall kinetics and thermodynamics of the chemical process are concerned. However, if either reagent molecule exchange is not fast or the number of exchanging nanoreactors is low, then the stochastic effect is clearly visible, influencing the kinetics of reaching reaction equilibrium. In systems with a low number of nanoreactors, the apparent (average) equilibrium constant is affected as well. The distribution of reactant molecules in the nanoreactors is governed by stochastic processes, dependent on stochastic rate constants of all processes, chemical as well as physical (transfer of molecules outside and into droplets). When accumulation of reactant molecules in the continuous phase cannot be neglected, then the partition coefficients of reactants between the continuous and dispersed phases have to be taken into account. Distributions of reactant molecules described in the paper for systems composed of few nanoreactors can be especially important for some biochemical processes in living cells or devised corresponding artificial reactors. If the reactant molecules predominate in a continuous phase, then the kinetics and overall conversion of reversible association may be significantly affected by the presence of the dispersed phase and its catalytic behavior can be observed. It has been shown that Monte Carlo simulations, applying a devised simple algorithm, give reliable results, allowing theoretical studies of nanoscale-droplet systems.
- 7 November 2019
- Published by AIP Publishing in The Journal of Chemical Physics
- Vol. 151 (17) , 174113
Open AccessStochasticity of the transfer of reactant molecules between nano-reactors affecting the reversible association A + B ⇆ C
Theoretical analysis and computer simulations (Monte Carlo and numerical integration of differential equations) indicate that the statistical effect of a small number of reacting molecules is affected by transfer of reagent molecules between nanoreactors (droplets in this study). As a model reaction, a simple reversible association A + B ⇆ C was chosen, which was studied previously without reagent transfer processes. For sufficiently fast exchange of reactant molecules and a sufficiently high number of nanoreactors, the studied systems virtually do not differ from large volume systems if overall kinetics and thermodynamics of the chemical process are concerned. However, if either reagent molecule exchange is not fast or the number of exchanging nanoreactors is low, then the stochastic effect is clearly visible, influencing the kinetics of reaching reaction equilibrium. In systems with a low number of nanoreactors, the apparent (average) equilibrium constant is affected as well. The distribution of reactant molecules in the nanoreactors is governed by stochastic processes, dependent on stochastic rate constants of all processes, chemical as well as physical (transfer of molecules outside and into droplets). When accumulation of reactant molecules in the continuous phase cannot be neglected, then the partition coefficients of reactants between the continuous and dispersed phases have to be taken into account. Distributions of reactant molecules described in the paper for systems composed of few nanoreactors can be especially important for some biochemical processes in living cells or devised corresponding artificial reactors. If the reactant molecules predominate in a continuous phase, then the kinetics and overall conversion of reversible association may be significantly affected by the presence of the dispersed phase and its catalytic behavior can be observed. It has been shown that Monte Carlo simulations, applying a devised simple algorithm, give reliable results, allowing theoretical studies of nanoscale-droplet systems.
- 1 August 2019
- Published by Elsevier in Chemical Engineering Journal
- Vol. 370, 432-443
Cumulative steady state Monte Carlo method for processes with exchange between reactive species. Case of controlled radical copolymerization
- 1 August 2019
- Published by Elsevier in Chemical Engineering Journal
- Vol. 370, 432-443
Cumulative steady state Monte Carlo method for processes with exchange between reactive species. Case of controlled radical copolymerization
- 1 February 2019
- Published by Elsevier in Chemical Engineering Journal
- Vol. 358, 197-210
A novel efficient hybrid algorithm for Monte Carlo simulation of controlled radical polymerization: The method integrating reactive and deactivated species
- 1 February 2019
- Published by Elsevier in Chemical Engineering Journal
- Vol. 358, 197-210
A novel efficient hybrid algorithm for Monte Carlo simulation of controlled radical polymerization: The method integrating reactive and deactivated species
- 14 May 2018
- Published by Wiley in Macromolecular Theory and Simulations
- Vol. 27 (5)
Evolution of Chain Length Distribution and Microstructure of Macromolecules in Irreversible Copolymerization Proceeding with Segmental Exchange Investigated with a New Monte Carlo Algorithm
A process of irreversible copolymerization with segmental exchange reactions is simulated using a Monte Carlo algorithm. The terminal (dyad) model is assumed for eight considered reactions: propagations and attacks of active centers on monomeric units in chains with subsequent chain scissions. It is established that microstructure of macromolecules at any given moment depends on the values of reaction rate constants and evolves from the beginning one, defined mainly by propagation rates, to the final one, determined by chain transfer rates. Dispersity and randomization degree of unit sequences in macromolecules can change nonmonotonically with progress of the process. Equilibration of the microstructure needs usually significantly longer time than needed for attaining the equilibrium chain lengths distribution. The proposed new Monte Carlo algorithm allows to more efficiently investigate the studied process.
- 14 May 2018
- Published by Wiley in Macromolecular Theory and Simulations
- Vol. 27 (5)
Evolution of Chain Length Distribution and Microstructure of Macromolecules in Irreversible Copolymerization Proceeding with Segmental Exchange Investigated with a New Monte Carlo Algorithm
A process of irreversible copolymerization with segmental exchange reactions is simulated using a Monte Carlo algorithm. The terminal (dyad) model is assumed for eight considered reactions: propagations and attacks of active centers on monomeric units in chains with subsequent chain scissions. It is established that microstructure of macromolecules at any given moment depends on the values of reaction rate constants and evolves from the beginning one, defined mainly by propagation rates, to the final one, determined by chain transfer rates. Dispersity and randomization degree of unit sequences in macromolecules can change nonmonotonically with progress of the process. Equilibration of the microstructure needs usually significantly longer time than needed for attaining the equilibrium chain lengths distribution. The proposed new Monte Carlo algorithm allows to more efficiently investigate the studied process.
- Open Access
Effect of the Configuration of a Bulky Aluminum Initiator on the Structure of Copolymers of l,l-Lactide with Symmetric Comonomer Trimethylene Carbonate
The effect of configuration of an asymmetric bulky initiator 2,2′-[1,1′-binaphtyl-2,2′-diyl- bis-(nitrylomethilidyne)]diphenoxy aluminum isopropoxide (Ini) on structure of copolymer of asymmetric monomer l,l-lactide (Lac) with symmetric comonomer trimethylene carbonate (Tmc) was studied using polarimetry, dilatometry, Size Exclusion Chromatography (SEC), and Carbon Nuclear Magnetic Resonance (13C NMR). When the S-enantiomer of Ini was used the distribution in copolymer chains at the beginning of polymerization is statistical, with alternacy tendency, changing next through a gradient region to homoblocks of Tmc. However, when R-Ini was used, the product formed was a gradient oligoblock one, with Tmc blocks prevailing at the beginning, changing to Lac blocks dominating at the end part of chains. Initiation of copolymerization with the mixture of both initiator enantiomers (S:R = 6:94) gave a multiblock copolymer of similar features but shorter blocks. Analysis of copolymerization progress required complex analysis of dilatometric data, assuming different molar volume contraction coefficients for units located in different triads. Comonomer reactivity ratios of studied copolymerizations were determined.
Open AccessEffect of the Configuration of a Bulky Aluminum Initiator on the Structure of Copolymers of l,l-Lactide with Symmetric Comonomer Trimethylene Carbonate
The effect of configuration of an asymmetric bulky initiator 2,2′-[1,1′-binaphtyl-2,2′-diyl- bis-(nitrylomethilidyne)]diphenoxy aluminum isopropoxide (Ini) on structure of copolymer of asymmetric monomer l,l-lactide (Lac) with symmetric comonomer trimethylene carbonate (Tmc) was studied using polarimetry, dilatometry, Size Exclusion Chromatography (SEC), and Carbon Nuclear Magnetic Resonance (13C NMR). When the S-enantiomer of Ini was used the distribution in copolymer chains at the beginning of polymerization is statistical, with alternacy tendency, changing next through a gradient region to homoblocks of Tmc. However, when R-Ini was used, the product formed was a gradient oligoblock one, with Tmc blocks prevailing at the beginning, changing to Lac blocks dominating at the end part of chains. Initiation of copolymerization with the mixture of both initiator enantiomers (S:R = 6:94) gave a multiblock copolymer of similar features but shorter blocks. Analysis of copolymerization progress required complex analysis of dilatometric data, assuming different molar volume contraction coefficients for units located in different triads. Comonomer reactivity ratios of studied copolymerizations were determined.
- 28 January 2017
- Published by AIP Publishing in The Journal of Chemical Physics
- Vol. 146 (4) , 044113
Chain length distributions in linear polyaddition proceeding in nano-scale small volumes without mass transfer
Computer simulations (Monte Carlo and numerical integration of differential equations) and theoretical analysis show that the statistical nature of polyaddition, both irreversible and reversible one, affects the way the macromolecules of different lengths are distributed among the small volume nano-reactors (droplets in this study) at any reaction time. The corresponding droplet distributions in respect to the number of reacting chains as well as the chain length distributions depend, for the given reaction time, on rate constants of polyaddition kp and depolymerization kd (reversible process), and the initial conditions: monomer concentration and the number of its molecules in a droplet. As a model reaction, a simple polyaddition process , was chosen, enabling to observe both kinetic and thermodynamic (apparent equilibrium constant) effects of a small number of reactant molecules in a droplet. The average rate constant of polymerization is lower than in a macroscopic system, depending on the average number of reactant molecules in a droplet. The apparent equilibrium constants of polymerization appear to depend on oligomer/polymer sizes as well as on the initial number of monomer molecules in a droplet. The corresponding equations, enabling prediction of the equilibrium conditions, were derived. All the analyzed effects are observed not only for ideally dispersed systems, i.e. with all droplets containing initially the same number of monomer (M)1 molecules, but also when initially the numbers of monomer molecules conform the Poisson distribution, expected for dispersions of reaction mixtures.- 28 January 2017
- Published by AIP Publishing in The Journal of Chemical Physics
- Vol. 146 (4) , 044113
Chain length distributions in linear polyaddition proceeding in nano-scale small volumes without mass transfer
Computer simulations (Monte Carlo and numerical integration of differential equations) and theoretical analysis show that the statistical nature of polyaddition, both irreversible and reversible one, affects the way the macromolecules of different lengths are distributed among the small volume nano-reactors (droplets in this study) at any reaction time. The corresponding droplet distributions in respect to the number of reacting chains as well as the chain length distributions depend, for the given reaction time, on rate constants of polyaddition kp and depolymerization kd (reversible process), and the initial conditions: monomer concentration and the number of its molecules in a droplet. As a model reaction, a simple polyaddition process , was chosen, enabling to observe both kinetic and thermodynamic (apparent equilibrium constant) effects of a small number of reactant molecules in a droplet. The average rate constant of polymerization is lower than in a macroscopic system, depending on the average number of reactant molecules in a droplet. The apparent equilibrium constants of polymerization appear to depend on oligomer/polymer sizes as well as on the initial number of monomer molecules in a droplet. The corresponding equations, enabling prediction of the equilibrium conditions, were derived. All the analyzed effects are observed not only for ideally dispersed systems, i.e. with all droplets containing initially the same number of monomer (M)1 molecules, but also when initially the numbers of monomer molecules conform the Poisson distribution, expected for dispersions of reaction mixtures.