14 research outputs found
Optimal current quality of a single-phase multilevel inverter with a staircase modulation
The authors address the problem of optimal current quality for a single-phase
multilevel inverter with a staircase modulation (Fig.1). The current quality is characterized by current
ripple Normalized Mean Square (NMSc). The goal is to find theoretically optimal switching angles and
respective minimal NMSc values. The previous research didn't provide comprehensive solutions for
arbitrary modulation indices and level counts
ΠΠΈΠ΄ΡΠΎΡΠ΅ΡΠΌΠ°Π»ΡΠ½ΡΠΉ ΡΠΈΠ½ΡΠ΅Π· ΠΌΠΎΠ½ΠΎΡΡΡΡΠΊΡΡΡΠ½ΠΎΠ³ΠΎ LaPO4: ΠΌΠΎΡΡΠΎΠ»ΠΎΠ³ΠΈΡ ΠΈ ΡΡΡΡΠΊΡΡΡΠ°
ΠΠ±Π»Π°ΡΡΡ ΠΏΡΠΈΠΌΠ΅Π½Π΅Π½ΠΈΡ ΠΌΠ°ΡΠ΅ΡΠΈΠ°Π»ΠΎΠ² Π½Π° ΠΎΡΠ½ΠΎΠ²Π΅ ΠΎΡΡΠΎΡΠΎΡΡΠ°ΡΠ° Π»Π°Π½ΡΠ°Π½Π° (LaPO4), Π² ΡΠΎΠΌ ΡΠΈΡΠ»Π΅ Π½Π°Π½ΠΎΠΌΠ°ΡΠ΅ΡΠΈΠ°Π»ΠΎΠ², Π² ΠΏΠΎΡΠ»Π΅Π΄Π½Π΅Π΅ Π²ΡΠ΅ΠΌΡ ΠΏΠΎΡΡΠΎΡΠ½Π½ΠΎ ΡΠ°ΡΡΠΈΡΡΠ΅ΡΡΡ. ΠΡΡΠΎΠΊΠΈΠΉ ΡΡΠΎΠ²Π΅Π½Ρ ΠΌΠ΅Ρ
Π°Π½ΠΈΡΠ΅ΡΠΊΠΈΡ
ΡΠ²ΠΎΠΉΡΡΠ² ΠΈ ΡΠΎΠ²ΠΌΠ΅ΡΡΠΈΠΌΠΎΡΡΡ ΡΠΎ ΠΌΠ½ΠΎΠ³ΠΈΠΌΠΈ ΠΎΠΊΡΠΈΠ΄Π°ΠΌΠΈ ΠΏΠΎΠ·Π²ΠΎΠ»ΡΡΡ ΡΠ°ΡΡΠΌΠ°ΡΡΠΈΠ²Π°ΡΡ Π²ΠΎΠ·ΠΌΠΎΠΆΠ½ΠΎΡΡΡ ΠΈΡΒΠΏΠΎΠ»ΡΠ·ΠΎΠ²Π°Π½ΠΈΡ ΠΎΡΡΠΎΡΠΎΡΡΠ°ΡΠ° Π»Π°Π½ΡΠ°Π½Π° Π² ΠΊΠ°ΡΠ΅ΡΡΠ²Π΅ ΠΊΠΎΠΌΠΏΠΎΠ½Π΅Π½ΡΠ° ΠΊΠΎΠΌΠΏΠΎΠ·ΠΈΡΠΈΠΎΠ½Π½ΠΎΠ³ΠΎ ΠΌΠ°ΡΠ΅ΡΠΈΠ°Π»Π° ΠΊΠΎΠ½ΒΡΡΡΡΠΊΡΠΈΠΎΠ½Π½ΠΎΠ³ΠΎ Π½Π°Π·Π½Π°ΡΠ΅Π½ΠΈΡ. Π’Π°ΠΊΠΎΠ΅ ΠΏΡΠΈΠΌΠ΅Π½Π΅Π½ΠΈΠ΅ ΠΎΡΠΎΠ±Π΅Π½Π½ΠΎ ΠΏΠ΅ΡΡΠΏΠ΅ΠΊΡΠΈΠ²Π½ΠΎ ΠΏΡΠΈ ΠΈΡΠΏΠΎΠ»ΡΠ·ΠΎΠ²Π°Π½ΠΈΠΈ Π½Π°Π½ΠΎΡΠ°ΡΡΠΈΡ Ρ ΠΊΠ²Π°Π·ΠΈΠΎΠ΄Π½ΠΎΠΌΠ΅ΡΠ½ΠΎΠΉ ΠΌΠΎΡΡΠΎΠ»ΠΎΠ³ΠΈΠ΅ΠΉ (Π½Π°Π½ΠΎΡΡΠ΅ΡΠΆΠ½Π΅ΠΉ). ΠΠΎΠ»ΡΡΠ°Ρ ΠΈΠ·ΠΎΠΌΠΎΡΡΠ½Π°Ρ ΡΠΌΠΊΠΎΡΡΡ ΡΠ°Π·Ρ Π½Π° ΠΎΡΠ½ΠΎΠ²Π΅ LaPO4 ΠΏΠΎ ΠΎΡΠ½ΠΎΡΠ΅Π½ΠΈΡ ΠΊ ΡΡΠ»ΠΎΡΠ½ΠΎΠ·Π΅ΠΌΠ΅Π»ΡΠ½ΡΠΌ ΠΈΠΎΠ½Π°ΠΌ, ΠΈΠΎΠ½Π°ΠΌ Π»Π°Π½ΡΠ°Π½ΠΎΠΈΠ΄ΠΎΠ² ΠΈ Π°ΠΊΡΠΈΒΠ½ΠΎΠΈΠ΄ΠΎΠ², Π²ΡΡΠΎΠΊΠ°Ρ Ρ
ΠΈΠΌΠΈΡΠ΅ΡΠΊΠ°Ρ ΠΈ ΡΠ°Π΄ΠΈΠ°ΡΠΈΠΎΠ½Π½Π°Ρ ΡΡΠΎΠΉΠΊΠΎΡΡΡ Π΄Π΅Π»Π°ΡΡ ΠΏΠ΅ΡΡΠΏΠ΅ΠΊΡΠΈΠ²Π½ΡΠΌ ΠΈΡΠΏΠΎΠ»ΡΠ·ΠΎΠ²Π°ΒΠ½ΠΈΠ΅ ΡΡΠΎΠ³ΠΎ ΡΠΎΠ΅Π΄ΠΈΠ½Π΅Π½ΠΈΡ Π² ΠΊΠ°ΡΠ΅ΡΡΠ²Π΅ ΠΌΠ°ΡΡΠΈΡΡ Π΄Π»Ρ ΠΈΠΌΠΌΠΎΠ±ΠΈΠ»ΠΈΠ·Π°ΡΠΈΠΈ ΡΠ°Π΄ΠΈΠΎΠ°ΠΊΡΠΈΠ²Π½ΡΡ
ΠΎΡΡ
ΠΎΠ΄ΠΎΠ².
Π ΡΠ°Π±ΠΎΡΠ΅ ΡΠ°ΡΡΠΌΠ°ΡΡΠΈΠ²Π°Π΅ΡΡΡ Π²ΠΎΠ·ΠΌΠΎΠΆΠ½ΠΎΡΡΡ ΠΏΠΎΠ»ΡΡΠ΅Π½ΠΈΡ ΠΎΡΡΠΎΡΠΎΡΡΠ°ΡΠ° Π»Π°Π½ΡΠ°Π½Π° (LaPO4) Π³ΠΈΠ΄ΡΠΎΒΡΠ΅ΡΠΌΠ°Π»ΡΠ½ΡΠΌ ΠΌΠ΅ΡΠΎΠ΄ΠΎΠΌ. ΠΡΠΈΠ²Π΅Π΄Π΅Π½Ρ ΡΠ΅Π·ΡΠ»ΡΡΠ°ΡΡ ΠΈΡΡΠ»Π΅Π΄ΠΎΠ²Π°Π½ΠΈΡ Π²Π»ΠΈΡΠ½ΠΈΡ ΡΠ, ΡΠ΅ΠΌΠΏΠ΅ΡΠ°ΡΡΡΡ ΠΈ Π²ΡΠ΅ΒΠΌΠ΅Π½ΠΈ ΠΎΠ±ΡΠ°Π±ΠΎΡΠΊΠΈ ΠΈ Π³ΠΈΠ΄ΡΠΎΡΠ΅ΡΠΌΠ°Π»ΡΠ½ΠΎΠ³ΠΎ ΡΠΈΠ½ΡΠ΅Π·Π° Π½Π° ΠΌΠΎΡΡΠΎΠ»ΠΎΠ³ΠΈΡ ΠΈ ΡΡΡΡΠΊΡΡΡΡ ΠΌΠΎΠ½ΠΎΡΡΡΡΠΊΡΡΡΠ½ΠΎΠ³ΠΎ ΡΠΎΡΡΠ°ΡΠ° Π»Π°Π½ΡΠ°Π½Π°. Π£ΡΡΠ°Π½ΠΎΠ²Π»Π΅Π½ΠΎ, ΡΡΠΎ Ρ ΡΠΎΡΡΠΎΠΌ ΡΠ ΠΌΠ΅Π½ΡΠ΅ΡΡΡ ΠΌΠΎΡΡΠΎΠ»ΠΎΠ³ΠΈΡ ΡΠΎΡΡΠ°ΡΠ° ΠΈ ΡΠ°Π·ΠΌΠ΅ΡΡ ΠΊΡΠΈΡΡΠ°Π»Π»ΠΈΡΠΎΠ², ΠΏΡΠΈ ΡΡΠΎΠΌ Π½Π°Π±Π»ΡΠ΄Π°Π΅ΡΡΡ ΠΏΠ΅ΡΠ΅Ρ
ΠΎΠ΄ ΠΊΡΠΈΡΡΠ°Π»Π»ΠΈΡΠ΅ΡΠΊΠΎΠΉ ΡΡΡΡΠΊΡΡΡΡ Ρ Π³Π΅ΠΊΡΠ°Π³ΠΎΠ½Π°Π»ΡΠ½ΠΎΠΉ Π² ΠΌΠΎΠ½ΠΎΠΊΠ»ΠΈΠ½Π½ΡΡ
Substantiation of Parameters for the Inertial Mixer in A Biodiesel Production Reactor
This paper reports results of the theoretical and experimental studies into the processes of transesterification of oils with methyl alcohol, which determined the material balance and established the molecular weight of the components involved in the process of transesterification as input and output products. The theoretical and experimental studies were carried out to calculate the indicators of the process of transesterification of fat-containing wastes depending on a change in the reaction duration and diameter of the inertial mixer of the reactor to accelerate the process of transesterification of oils with methyl alcohol.
The process of transesterification is one of the basic methods for modifying the molecular composition of fat raw materials. With transesterification, the composition of fat fatty acids does not change, their statistical redistribution occurs in a mixture of triacylglycerols, which leads to a change in the physicochemical properties of fat mixtures as a result of changes in molecular composition. Transesterification of high-melting animal and vegetable fats with methyl alcohol improves the conversion of oils for the production of biodiesel from fat-containing waste.
The results of the theoretical and experimental studies have helped determine the value of the flow rate of the reaction mixture, as well as the values of the geometric dimensions of the reactor, were determined (the diameter of the mixer, d=100Γ·500 mm; the length of the reactor is 1.5Γ·2.0 m). Processing of the reaction mixture made it possible to obtain a high degree of homogeneity in the concentration of components with large diameters of the inertial mixer β 300...500 mm at average rotational speeds. The oil conversion has been improved, as well as productivity, by using equipment to produce biodiesel from fat-containing waste. Optimal pump performance is also ensured with minimal power consumption and reactor operatio
Gravitino and Polonyi production in supergravity
International audienceWe study production of gravitino and Polonyi particles in the minimal Starobinsky-Polonyi supergravity with inflaton belonging to a massive vector supermultiplet. Our model has only one free parameter given by the scale of spontaneous SUSY breaking triggered by Polonyi chiral superfield. The vector supermultiplet generically enters the action non-minimally, via an arbitrary real function. This function is chosen to generate the inflaton scalar potential of the Starobinsky model. Our supergravity model can be reformulated as an abelian supersymmetric gauge theory with the vector gauge superfield coupled to two (Higgs and Polonyi) chiral superfields interacting with supergravity, where the U(1) gauge symmetry is spontaneously broken. We find that Polonyi and gravitino particles are efficiently produced during inflation, and estimate their masses and the reheating temperature. After inflation, perturbative decay of inflaton also produces Polonyi particles that rapidly decay into gravitinos. As a result, a coherent picture of inflation and dark matter emerges, where the abundance of produced gravitinos after inflation fits the CMB constraints as a Super Heavy Dark Matter (SHDM) candidate. Our scenario avoids the notorous gravitino and Polonyi problems with the Big Bang Nucleosynthesis (BBN) and DM overproduction