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Validation data for a hybrid smoothed dissipative particle dynamics (SDPD) spatial stochastic simulation algorithm (sSSA) method.
We present the validation of the hybrid sSSA-SDPD method for advection-diffusion-reaction problems coupled to discrete biochemical systems, as presented in the publication "A hybrid smoothed dissipative particle dynamics (SDPD) spatial stochastic simulation algorithm (sSSA) for advection-diffusion-reaction problems" (Drawert et al., 2019). We validate 1D diffusion, and 2D diffusion cases against their analytical solutions. We present graphs and tables of data showing the error in the simulation method
Validation data for a hybrid smoothed dissipative particle dynamics (SDPD) spatial stochastic simulation algorithm (sSSA) method
We present the validation of the hybrid sSSA-SDPD method for advection-diffusion-reaction problems coupled to discrete biochemical systems, as presented in the publication βA hybrid smoothed dissipative particle dynamics (SDPD) spatial stochastic simulation algorithm (sSSA) for advection-diffusion-reaction problemsβ (Drawert et al., 2019). We validate 1D diffusion, and 2D diffusion cases against their analytical solutions. We present graphs and tables of data showing the error in the simulation method
Multiscale analyses of cellular signaling and regulation in response to multiple stress conditions
Understanding the relationship between signaling and its corresponding cellular response is critical to combating stress responses, especially responses related antibiotic resistance and non-genetic phenotypic transitions to antibiotic tolerance. However, bacterial signal responses are notoriously noisy and difficult to predict. This work first develops a multiscale cell cycle-aware signal modeling framework to explore the energetics and dynamics of the phosphate starvation stress response two-component system, PhoBR, to better understand the relationship between stress response proteins and the bounds of cellular memory in stress response. I found that the transcription factor responsible for stress response remains nominally βactiveβ for 2-4 generations after the stress response is relieved due to sequestration effects, with differential memory in offspring cells dictated by stochastic protein inheritance. Next, I studied a novel antibiotic persister phenotype that arises in non-canonical conditions. This phenotype exhibited a previously unknown stress response that resulted in growth arrest, granting it antibiotic tolerance. The tolerance seems to be imparted by a global stress response arising from toxic excessive lactose import, seemingly opposite of the starvation response that induces canonical persister cell formation. Finally, I improved the PhoBR stress response model to measure stochastic fluctuations of proteins within the two-component system to identify the principles of signal fluctuations and how they drive variability in the bacterial cell cycle (i.e., growth rate). The downstream regulon of the PhoB response regulator is the main driver of the growth rate, but the transcriptionally active dimerized PhoB acts as the link between fast molecular fluctuations and slower gene expression fluctuations within the system. Finally, I present a vision for future developments of this style of modeling to include spatial information
ΠΠ΅ΡΠΎΠ΄ΠΎΠ»ΠΎΠ³ΠΈΡΠ° Π·Π° ΡΠΈΠ½ΡΠ΅Π·Ρ ΡΠ΅Π°ΠΊΡΠΎΡΠ° Π·Π°ΡΠ½ΠΎΠ²Π°Π½Π° Π½Π° ΠΊΠΎΠ½ΡΠ΅ΠΏΡΠΈΠΌΠ° ΠΈΠ½ΡΠ΅Π½Π·ΠΈΡΠΈΠΊΠ°ΡΠΈΡΠ΅ ΠΏΡΠΎΡΠ΅ΡΠ° ΠΈ ΠΏΡΠΈΠΌΠ΅Π½ΠΈ ΠΌΠ΅ΡΠΎΠ΄Π° ΠΎΠΏΡΠΈΠΌΠΈΠ·Π°ΡΠΈΡΠ΅
In this Ph.D. thesis, a new methodology for Reactor Synthesis Based on Process
Intensification Concepts and Application of Optimization Methods (ReSyPIO) is
presented and applied to two different cases.
In Chapter 1: Introduction β Motivation and Objectives, the motive for the
research is presented, and Hypotheses are formulated. The ReSyPIO methodology
that rests upon these Hypotheses and consists of three consecutive stages is briefly
described in this Chapter. The first stage encapsulates all present phases and
phenomena inside the reactor functional building block, called module. Modules
come as a direct result of a conceptual representation of the analyzed system. In the
second stage, modules are further segmented if needed and interconnected, creating
a reactor superstructure that is mathematically described for all desirable operating
regimes. In the last stage of the ReSyPIO methodology, the optimal structure,
operating conditions, and the operational regime are determined with the use of
rigorous optimization. All three stages of the ReSyPIO methodology have a backflow,
meaning that if analysis leads to impractical, nonfunctional or inefficient results,
modifications in reactor superstructure and modules can be made. The objective is
to conceptually and numerically derive the most efficient reactor structure and a set
of operating conditions that would be used as a starting point in the future reactor
design.
Chapter 2: Literature Review is used to cover and review the most important
research published in the area of Process Intensification and different Process
System Engineering techniques. Different approaches and studies present in
academia are highlighted and their elements compared with the presented ReSyPIO
methodology with the accent on its advantages and contribution to the engineering
science community.Also, in this Chapter, an array of well researched analytical and numerical
approaches is presented that could be used in the future to strengthen the ReSyPIO
methodology further and facilitate its easier application.
In Chapter 3: Description of the ReSyPIO Methodology Reactor Synthesis based
on Process Intensification and Optimization of Superstructure is explained in detail,
with a graphical representation of the main building block, called Phenomenological
Module. A general explanation is given on how to form a reactor superstructure and
mathematically describe it with sets of material and energy balance equations that
correspond to a number of present phases and components in the system.
The ReSyPIO methodology is first applied to a generic case of two parallel reactions
in Chapter 4, called Application of the ReSyPIO Methodology on a Generic
Reaction Case. The case corresponds to two parallel reactions that could be found
in the fine chemical industry. The reactions are endothermic and slow with the
undesired product. After the application of the ReSyPIO methodology, an optimal
reactor structure consisting of a segmented module with 17 side inlets for the
reactant and heat source is obtained. It is recommended for the reactor to work in a
continuous steady-state mode as the dynamic operation would not lead to a
sufficient increase in reactor efficiency...Π£ ΠΎΠ²ΠΎΡ Π΄ΠΎΠΊΡΠΎΡΡΠΊΠΎΡ Π΄ΠΈΡΠ΅ΡΡΠ°ΡΠΈΡΠΈ ΡΠ΅ ΠΏΡΠ΅Π΄ΡΡΠ°Π²ΡΠ΅Π½Π° ΠΈ ΠΏΡΠΈΠΌΠ΅ΡΠ΅Π½Π° Π½ΠΎΠ²Π°
ΠΌΠ΅ΡΠΎΠ΄ΠΎΠ»ΠΎΠ³ΠΈΡΠ° Π·Π° ΡΠΈΠ½ΡΠ΅Π·Ρ ΡΠ΅Π°ΠΊΡΠΎΡΠ° Π·Π°ΡΠ½ΠΎΠ²Π°Π½Π° Π½Π° ΠΊΠΎΠ½ΡΠ΅ΠΏΡΠΈΠΌΠ° ΠΈΠ½ΡΠ΅Π½Π·ΠΈΡΠΈΠΊΠ°ΡΠΈΡΠ΅
ΠΏΡΠΎΡΠ΅ΡΠ° ΠΈ ΠΏΡΠΈΠΌΠ΅Π½ΠΈ ΡΠ°Π·Π»ΠΈΡΠΈΡΠΈΡ
ΠΎΠΏΡΠΈΠΌΠΈΠ·Π°ΡΠΈΠΎΠ½ΠΈΡ
ΡΠ΅Ρ
Π½ΠΈΠΊΠ° (Reactor Synthesis
Based on Process Intensification Concepts and Application of Optimization Methods β
ReSyPIO).
Π£ ΠΏΠΎΠ³Π»Π°Π²ΡΡ Π£Π²ΠΎΠ΄ β ΠΠΎΡΠΈΠ²Π°ΡΠΈΡΠ° ΠΈ ΡΠΈΡΠ΅Π²ΠΈ, ΡΠΎΡΠΌΠΈΡΠ°Π½Π΅ ΡΡ Ρ
ΠΈΠΏΠΎΡΠ΅Π·Π΅ Π½Π° ΠΊΠΎΡΠΈΠΌΠ°
ΠΏΠΎΡΠΈΠ²Π° ReSyPIO ΠΌΠ΅ΡΠΎΠ΄ΠΎΠ»ΠΎΠ³ΠΈΡΠ° ΠΈ Π΄Π°ΡΠ° ΡΠ΅ ΠΌΠΎΡΠΈΠ²Π°ΡΠΈΡΠ° Π·Π° ΠΈΡΡΡΠ°ΠΆΠΈΠ²Π°ΡΠ΅. ReSyPIO
ΠΌΠ΅ΡΠΎΠ΄ΠΎΠ»ΠΎΠ³ΠΈΡΠ° ΡΠ΅ ΡΠΊΡΠ°ΡΠΊΠΎ ΠΏΡΠ΅Π΄ΡΡΠ°Π²ΡΠ΅Π½Π° ΠΈ ΠΎΠΏΠΈΡΠ°Π½Π° ΠΊΡΠΎΠ· ΡΡΠΈ ΡΠ·Π°ΡΡΠΎΠΏΠ½Π΅ Π΅ΡΠ°ΠΏΠ΅.
ΠΡΠ²Π° Π΅ΡΠ°ΠΏΠ° ΡΠΎΠΊΠ²ΠΈΡΠ°Π²Π° ΡΠ²Π΅ ΠΏΡΠΈΡΡΡΠ½Π΅ ΡΠ°Π·Π΅ ΠΈ ΡΠ΅Π½ΠΎΠΌΠ΅Π½Π΅ Ρ ΡΠ΅Π°ΠΊΡΠΎΡΡ ΡΠ½ΡΡΠ°Ρ
ΡΡΠ½ΠΊΡΠΈΠΎΠ½Π°Π»Π½ΠΈΡ
Π³ΡΠ°Π΄ΠΈΠ²Π½ΠΈΡ
ΡΠ΅Π΄ΠΈΠ½ΠΈΡΠ°, Π½Π°Π·Π²Π°Π½ΠΈΡ
ΠΌΠΎΠ΄ΡΠ»ΠΈ. ΠΠΎΠ΄ΡΠ»ΠΈ ΠΏΡΠ΅Π΄ΡΡΠ°Π²ΡΠ°ΡΡ
ΡΠ΅Π·ΡΠ»ΡΠ°Ρ ΠΊΠΎΠ½ΡΠ΅ΠΏΡΡΠ°Π»Π½ΠΎΠ³ ΠΏΡΠΈΠΊΠ°Π·Π° Π°Π½Π°Π»ΠΈΠ·ΠΈΡΠ°Π½ΠΎΠ³ ΡΠΈΡΡΠ΅ΠΌΠ°. Π£ Π΄ΡΡΠ³ΠΎΡ Π΅ΡΠ°ΠΏΠΈ,
ΠΌΠΎΠ΄ΡΠ»ΠΈ ΡΠ΅ ΠΏΠΎ ΠΏΠΎΡΡΠ΅Π±ΠΈ ΠΌΠΎΠ³Ρ Π΄Π°ΡΠ΅ ΠΏΠΎΠ΄Π΅Π»ΠΈΡΠΈ Ρ ΡΠ΅Π³ΠΌΠ΅Π½ΡΠ΅ ΠΈ ΠΌΠ΅ΡΡΡΠΎΠ±Π½ΠΎ ΠΏΠΎΠ²Π΅Π·Π°ΡΠΈ,
ΠΊΡΠ΅ΠΈΡΠ°ΡΡΡΠΈ ΡΡΠΏΠ΅ΡΡΡΡΡΠΊΡΡΡΡ ΡΠ΅Π°ΠΊΡΠΎΡΠ°. Π‘ΡΠΏΠ΅ΡΡΡΡΡΠΊΡΡΡΠ° ΡΠ΅ ΠΌΠ°ΡΠ΅ΠΌΠ°ΡΠΈΡΠΊΠΈ
ΠΎΠΏΠΈΡΠ°Π½Π° Π·Π° ΡΠ²Π΅ ΡΠ΅ΠΆΠΈΠΌΠ΅ ΡΠ°Π΄Π° ΡΠ΅Π°ΠΊΡΠΎΡΠ° ΠΎΠ΄ ΠΈΠ½ΡΠ΅ΡΠ΅ΡΠ°. Π£ ΠΏΠΎΡΠ»Π΅Π΄ΡΠΎΡ Π΅ΡΠ°ΠΏΠΈ ReSyPIO
ΠΌΠ΅ΡΠΎΠ΄ΠΎΠ»ΠΎΠ³ΠΈΡΠ΅, ΠΎΠΏΡΠΈΠΌΠ°Π»Π½Π° ΡΡΡΡΠΊΡΡΡΠ°, ΡΡΠ»ΠΎΠ²ΠΈ ΠΈ ΡΠ΅ΠΆΠΈΠΌ ΡΠ°Π΄Π° ΡΠ΅Π°ΠΊΡΠΎΡΠ° ΡΡ
ΠΎΠ΄ΡΠ΅ΡΠ΅Π½ΠΈ ΠΏΡΠΈΠΌΠ΅Π½ΠΎΠΌ ΡΠΈΠ³ΠΎΡΠΎΠ·Π½Π΅ ΠΎΠΏΡΠΈΠΌΠΈΠ·Π°ΡΠΈΡΠ΅. Π‘Π²Π΅ ΡΡΠΈ Π΅ΡΠ°ΠΏΠ΅ ReSyPIO
ΠΌΠ΅ΡΠΎΠ΄ΠΎΠ»ΠΎΠ³ΠΈΡΠ΅ ΠΈΠΌΠ°ΡΡ ΠΏΠΎΠ²ΡΠ°ΡΠ½ΠΈ ΡΠΎΠΊ, ΡΡΠΎ Π·Π½Π°ΡΠΈ Π΄Π° ΡΠΊΠΎΠ»ΠΈΠΊΠΎ Π°Π½Π°Π»ΠΈΠ·Π° Π²ΠΎΠ΄ΠΈ ΠΊΠ°
Π½Π΅ΠΏΡΠ°ΠΊΡΠΈΡΠ½ΠΈΠΌ, Π½Π΅ΡΡΠ½ΠΊΡΠΈΠΎΠ½Π°Π»Π½ΠΈΠΌ ΠΈΠ»ΠΈ Π½Π΅Π΅ΡΠΈΠΊΠ°ΡΠ½ΠΈΠΌ ΡΠ΅ΡΠ΅ΡΠΈΠΌΠ°,
ΠΌΠΎΠ΄ΠΈΡΠΈΠΊΠ°ΡΠΈΡΠ° ΠΌΠ°ΡΠ΅ΠΌΠ°ΡΠΈΡΠΊΠΎΠ³ ΠΌΠΎΠ΄Π΅Π»Π°, ΡΡΠΏΠ΅ΡΡΡΡΡΠΊΡΡΡΠ΅ ΠΈ/ΠΈΠ»ΠΈ ΠΌΠΎΠ΄ΡΠ»Π° ΡΠ΅ ΠΌΠΎΠ³ΡΡΠ°.
Π¦ΠΈΡ ΠΏΡΠΈΠΌΠ΅Π½Π΅ ReSyPIO ΠΌΠ΅ΡΠΎΠ΄ΠΎΠ»ΠΎΠ³ΠΈΡΠ΅ ΡΠ΅ Π΄Π° ΡΠ΅ ΠΊΠΎΠ½ΡΠ΅ΠΏΡΡΠ°Π»Π½ΠΈΠΌ ΠΈ Π½ΡΠΌΠ΅ΡΠΈΡΠΊΠΈΠΌ
ΠΏΡΠΈΡΡΡΠΏΠΎΠΌ Π΄ΠΎΡΠ΅ Π΄ΠΎ ΠΎΠΏΡΠΈΠΌΠ°Π»Π½Π΅ ΠΏΡΠ΅ΠΏΠΎΡΡΠΊΠ΅ Π·Π° ΡΡΡΡΠΊΡΡΡΡ ΡΠ΅Π°ΠΊΡΠΎΡΠ°, ΠΎΠΏΠ΅ΡΠ°ΡΠΈΠ²Π½Π΅
ΡΡΠ»ΠΎΠ²Π΅ ΠΈ ΡΠ΅ΠΆΠΈΠΌ ΡΠ°Π΄Π°, ΠΊΠΎΡΠ° Π±ΠΈ Π±ΠΈΠ»Π° ΠΏΠΎΡΠ΅ΡΠ½Π° ΠΏΡΠ΅ΡΠΏΠΎΡΡΠ°Π²ΠΊΠ° Ρ Π±ΡΠ΄ΡΡΠ΅ΠΌ Π΄ΠΈΠ·Π°ΡΠ½Ρ
ΡΡΠ΅ΡΠ°ΡΠ°.
ΠΡΠ΅Π³Π»Π΅Π΄ Π»ΠΈΡΠ΅ΡΠ°ΡΡΡΠ΅ Π΄Π°ΡΠ΅ ΠΎΠΏΠΈΡ ΠΈ ΠΏΡΠΈΠΊΠ°Π· ΡΠ²ΠΈΡ
ΠΈΡΡΡΠ°ΠΆΠΈΠ²Π°ΡΠ° ΠΎΠ΄ ΠΈΠ½ΡΠ΅ΡΠ΅ΡΠ°, ΠΈΠ·
ΠΎΠ±Π»Π°ΡΡΠΈ ΠΠ½ΡΠ΅Π½Π·ΠΈΡΠΈΠΊΠ°ΡΠΈΡΠ΅ ΠΏΡΠΎΡΠ΅ΡΠ° ΠΈ Π’Π΅ΠΎΡΠΈΡΠ΅ ΠΈ Π°Π½Π°Π»ΠΈΠ·Π΅ ΠΏΡΠΎΡΠ΅ΡΠ½ΠΈΡ
ΡΠΈΡΡΠ΅ΠΌΠ°.
ΠΠ°Π³Π»Π°ΡΠ΅Π½ΠΈ ΡΡ ΡΠ°Π·Π»ΠΈΡΠΈΡΠΈ ΠΏΡΠΈΡΡΡΠΏΠΈ ΠΈ ΡΡΡΠ΄ΠΈΡΠ΅ ΠΏΡΠΈΡΡΡΠ½Π΅ Ρ ΠΈΡΡΡΠ°ΠΆΠΈΠ²Π°ΡΠΊΠΎΡΠ·Π°ΡΠ΅Π΄Π½ΠΈΡΠΈ, Π° ΡΠΈΡ
ΠΎΠ²ΠΈ Π΅Π»Π΅ΠΌΠ΅Π½ΡΠΈ ΡΠΏΠΎΡΠ΅ΡΠ΅Π½ΠΈ ΡΠ° ΠΏΡΠ΅Π΄ΡΡΠ°Π²ΡΠ΅Π½ΠΎΠΌ ReSyPIO
ΠΌΠ΅ΡΠΎΠ΄ΠΎΠ»ΠΎΠ³ΠΈΡΠΎΠΌ ΡΠ° Π°ΠΊΡΠ΅Π½ΡΠΎΠΌ Π½Π° ΠΏΡΠ΅Π΄Π½ΠΎΡΡΠΈΠΌΠ° ΠΈ Π½Π°ΡΡΠ½ΠΎΠΌ Π΄ΠΎΠΏΡΠΈΠ½ΠΎΡΡ. Π£ ΠΎΠ²ΠΎΠΌ
ΠΏΠΎΠ³Π»Π°Π²ΡΡ ΡΠ΅ Π΄Π°Ρ ΠΈ Π½ΠΈΠ· Π΄ΠΎΠ±ΡΠΎ ΠΈΡΡΡΠ°ΠΆΠ΅Π½ΠΈΡ
Π°Π½Π°Π»ΠΈΡΠΈΡΠΊΠΈΡ
ΠΈ Π½ΡΠΌΠ΅ΡΠΈΡΠΊΠΈΡ
ΠΏΡΠΈΡΡΡΠΏΠ°
ΠΊΠΎΡΠΈ Π±ΠΈ ΠΌΠΎΠ³Π»ΠΈ Π΄Π° Π±ΡΠ΄Ρ ΠΊΠΎΡΠΈΡΡΠ΅Π½ΠΈ Ρ ΠΎΠΊΠ²ΠΈΡΡ ReSyPIO ΠΌΠ΅ΡΠΎΠ΄ΠΎΠ»ΠΎΠ³ΠΈΡΠ΅ ΠΈ ΠΎΠ»Π°ΠΊΡΠ°ΡΡ
ΡΠ΅Π½Ρ ΠΏΡΠΈΠΌΠ΅Π½Ρ.
Π£ ΠΏΠΎΠ³Π»Π°Π²ΡΡ ΠΠΏΠΈΡ ReSyPIO ΠΌΠ΅ΡΠΎΠ΄ΠΎΠ»ΠΎΠ³ΠΈΡΠ΅, ΡΠ΅ Π΄Π΅ΡΠ°ΡΠ½ΠΎ ΠΎΠ±ΡΠ°ΡΡΠ΅Π½Π° ΡΠΈΠ½ΡΠ΅Π·Π°
ΡΠ΅Π°ΠΊΡΠΎΡΠ° Π·Π°ΡΠ½ΠΎΠ²Π°Π½Π° Π½Π° ΠΊΠΎΠ½ΡΠ΅ΠΏΡΠΈΠΌΠ° ΠΈΠ½ΡΠ΅Π½Π·ΠΈΡΠΈΠΊΠ°ΡΠΈΡΠ΅ ΠΏΡΠΎΡΠ΅ΡΠ° ΠΈ ΠΎΠΏΡΠΈΠΌΠΈΠ·Π°ΡΠΈΡΠΈ
ΡΡΠΏΠ΅ΡΡΡΡΡΠΊΡΡΡΠ΅. ΠΡΠ²ΠΎ ΡΠ΅ Π΄Π°ΡΠ° ΠΏΡΠΎΡΠ΅Π΄ΡΡΠ° Π·Π° Π³ΡΠ°ΡΠΈΡΠΊΡ ΠΈ ΠΊΠΎΠ½ΡΠ΅ΠΏΡΡΠ°Π»Π½Ρ
ΡΠ΅ΠΏΡΠ΅Π·Π΅Π½ΡΠ°ΡΠΈΡΡ ΡΠΈΡΡΠ΅ΠΌΠ°, ΠΏΡΠ΅ΠΊΠΎ Π³Π»Π°Π²Π½ΠΈΡ
Π³ΡΠ°Π΄ΠΈΠ²Π½ΠΈΡ
ΡΠ΅Π΄ΠΈΠ½ΠΈΡΠ°,
ΡΠ΅Π½ΠΎΠΌΠ΅Π½ΠΎΠ»ΠΎΡΠΊΠΈΡ
ΠΌΠΎΠ΄ΡΠ»Π°. ΠΠΎΡΠΎΠΌ ΡΠ΅ ΠΎΠ±ΡΠ°ΡΡΠ΅Π½ΠΎ ΠΊΠ°ΠΊΠΎ ΡΠ΅ ΠΊΡΠ΅ΠΈΡΠ° ΡΡΠΏΠ΅ΡΡΡΡΡΠΊΡΡΡΠ°
ΡΠ΅Π°ΠΊΡΠΎΡΠ°. ΠΠ° ΠΊΡΠ°ΡΡ ΡΠ΅ Π΄Π°Ρ ΡΠΎΠΏΡΡΠ΅Π½ ΠΏΠΎΡΡΡΠΏΠ°ΠΊ Π·Π° ΠΌΠ°ΡΠ΅ΠΌΠ°ΡΠΈΡΠΊΠΈ ΠΎΠΏΠΈΡ
ΡΡΠΏΠ΅ΡΡΡΡΡΠΊΡΡΡΠ΅ ΠΏΡΠ΅ΠΊΠΎ ΡΠΊΡΠΏΠΎΠ²Π° ΡΠ΅Π΄Π½Π°ΡΠΈΠ½Π° ΠΌΠ°ΡΠ΅ΡΠΈΡΠ°Π»Π½ΠΎΠ³ ΠΈ Π΅Π½Π΅ΡΠ³Π΅ΡΡΠΊΠΎΠ³ Π±ΠΈΠ»Π°Π½ΡΠ°,
ΡΠΈΡΠΈ Π±ΡΠΎΡ Π·Π°Π²ΠΈΡΠΈ ΠΎΠ΄ Π±ΡΠΎΡΠ° ΠΏΡΠΈΡΡΡΠ½ΠΈΡ
ΡΠ°Π·Π° ΠΈ ΠΊΠΎΠΌΠΏΠΎΠ½Π΅Π½Π°ΡΠ° Ρ ΡΠΈΡΡΠ΅ΠΌΡ.
ReSyPIO ΠΌΠ΅ΡΠΎΠ΄ΠΎΠ»ΠΎΠ³ΠΈΡΠ° ΡΠ΅ ΠΏΡΠ²ΠΈ ΠΏΡΡ ΠΏΡΠΈΠΌΠ΅ΡΠ΅Π½Π° Π½Π° ΡΠ»ΡΡΠ°ΡΡ Π΄Π²Π΅ Π³Π΅Π½Π΅ΡΠΈΡΠΊΠ΅
ΠΏΠ°ΡΠ°Π»Π΅Π»Π½Π΅ ΡΠ΅Π°ΠΊΡΠΈΡΠ΅ Ρ ΠΏΠΎΠ³Π»Π°Π²ΡΡ ΠΏΠΎΠ΄ Π½Π°Π·ΠΈΠ²ΠΎΠΌ ΠΡΠΈΠΌΠ΅Π½Π° ReSyPIO ΠΌΠ΅ΡΠΎΠ΄ΠΎΠ»ΠΎΠ³ΠΈΡΠ΅
Π½Π° ΡΠ»ΡΡΠ°ΡΡ Π³Π΅Π½Π΅ΡΠΈΡΠΊΠ΅ ΡΠ΅Π°ΠΊΡΠΈΡΠ΅. ΠΠ²Π°Ρ ΡΠ»ΡΡΠ°Ρ ΠΎΠ΄Π³ΠΎΠ²Π°ΡΠ° ΡΠ΅Π°ΠΊΡΠΈΡΠ°ΠΌΠ° ΠΊΠΎΡΠ΅ ΡΠ΅ ΠΌΠΎΠ³Ρ
Π½Π°ΡΠΈ Ρ ΠΈΠ½Π΄ΡΡΡΡΠΈΡΠΈ ΡΠΈΠ½ΠΈΡ
Ρ
Π΅ΠΌΠΈΠΊΠ°Π»ΠΈΡΠ°. Π Π΅Π°ΠΊΡΠΈΡΠ΅ ΡΡ Π΅Π½Π΄ΠΎΡΠ΅ΡΠΌΠ½Π΅ ΠΈ ΡΠΏΠΎΡΠ΅, ΠΏΡΠΈ
ΡΠ΅ΠΌΡ ΡΠ΅ ΠΊΠΈΠ½Π΅ΡΠΈΡΠΊΠΈ ΡΠ°Π²ΠΎΡΠΈΠ·ΠΎΠ²Π°Π½ΠΎ ΠΊΡΠ΅ΠΈΡΠ°ΡΠ΅ Π½Π΅ΠΆΠ΅ΡΠ΅Π½ΠΎΠ³ ΠΏΡΠΎΠΈΠ·Π²ΠΎΠ΄Π°. ΠΠ°ΠΊΠΎΠ½
ΠΏΡΠΈΠΌΠ΅Π½Π΅ ReSyPIO ΠΌΠ΅ΡΠΎΠ΄ΠΎΠ»ΠΎΠ³ΠΈΡΠ΅, Π΄ΠΎΠ±ΠΈΡΠ΅Π½Π° ΡΠ΅ ΠΎΠΏΡΠΈΠΌΠ°Π»Π½Π° ΡΡΡΡΠΊΡΡΡΠ° ΡΠ΅Π°ΠΊΡΠΎΡΠ°
ΠΊΠΎΡΠ° ΡΠ΅ ΡΠ°ΡΡΠΎΡΠΈ ΠΎΠ΄ ΡΠ΅Π³ΠΌΠ΅Π½ΡΠΈΡΠ°Π½ΠΎΠ³ ΠΌΠΎΠ΄ΡΠ»Π° ΡΠ° 17 ΡΠ»Π°Π·Π° Π·Π° ΠΈΠ·Π²ΠΎΡ ΡΠΎΠΏΠ»ΠΎΡΠ΅ ΠΈ
ΡΠ΅Π°ΠΊΡΠ°Π½Ρ ΠΊΠΎΡΠΈ ΡΠ΅ Π΄ΠΎΠ·ΠΈΡΠ°. ΠΡΠ΅Π΄Π»ΠΎΠΆΠ΅Π½ΠΎ ΡΠ΅ Π΄Π° ΡΠ΅Π°ΠΊΡΠΎΡ ΡΠ°Π΄ΠΈ ΠΊΠΎΠ½ΡΠΈΠ½ΡΠ°Π»Π½ΠΎ, Ρ
ΡΡΠ°ΡΠΈΠΎΠ½Π°ΡΠ½ΠΎΠΌ ΡΠ΅ΠΆΠΈΠΌΡ ΡΠ°Π΄Π°, ΡΠ΅Ρ Π±ΠΈ Π΄ΠΈΠ½Π°ΠΌΠΈΡΠΊΠΈ ΡΠ΅ΠΆΠΈΠΌ ΡΠ°Π΄Π° ΡΠ΅Π·ΡΠ»ΡΠΎΠ²Π°ΠΎ
Π½Π΅Π΄ΠΎΠ²ΠΎΡΠ½ΠΈΠΌ ΠΏΠΎΠ²Π΅ΡΠ°ΡΠ΅ΠΌ Π΅ΡΠΈΠΊΠ°ΡΠ½ΠΎΡΡΠΈ ΡΠ΅Π°ΠΊΡΠΎΡΠ°..
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