197 research outputs found
Calculation of the Operation Parameters of the Catalytic Converters of the Harmful Gas Impurities
There are theoretically founded principles of catalytic converters designing of harmful gas emissions of various heat devices. Experimental investigations have shown that the smallest aerodynamic losses in the constructions of gas neutralizers are achieved at the using of profiled ceramic blades as working units - carriers of catalysts. To ensure intensive mixing of the flow inside the converter the input edges of the blades grids of the future stages should be located between the output edges of the blades of the grids of the preceding stages
PdO impact on the activity of hydrocarbon oxidation with oxide catalysts
The palladium component influence on the catalytic activity of a catalyst was investigated based on transition-metal oxides deposited on Ξ±-Al2O3 carrier in the process of hydrocarbon catalytic thermal destruction. It has been determined that the value of surface concentrations of PdO deposited on Co3O4 doesnβt effect on the achievable conversion degree when using the obtained catalytic converter. It is suggested that PdO facilitates the interfacial diffusion of atomic oxygen on the catalyst oxide component due to support it in an oxidized state. Adsorbed on palladium oxygen migrates on cobalt oxide in the composition of this catalyst. At the expense of this process oxygen passivation of Pd-Co3O4/Ξ³-Al2O3 catalyst is overcome and its high reaction activity is ensured. Our research is evidence that Co3O4 performs the role of active centers on a corundum carrier in the reaction of catalytic thermal hydrocarbon oxidation. Additionally injected PdO into the catalyst composition promotes to the cobalt phase enrichment by oxygen
Determining Energy Cost for Milling Solid Matter in a Ball Mill
The article provides findings of analytical research into the process of milling friable matter in a ball mill. We have received an expression to determine energy cost of milling with the account of the method of milling and the characteristics of the material to be ground. In the paper, the analytical results of bulk materials grinding process in a ball mill are presented. The differential equation is obtained whose solution determines the value of the grinding mode coefficient, corresponding to the maximum value of grinding process efficiency. The use of the introduced ball mill modes allows reducing the time spent on grinding by 28.9 % for cement clinker, 18.4 % for black coal, 28.9 % for marble and 19.6 % for rock salt compared to the traditionally recommended ones
Electrodeposition of iron-molybdenum coatings from citrate electrolyte
Specifi c features of the electrodeposition of ironβmolybdenum coatings from a citrate electrolyte based on iron(III) sulfate and sodium molybdate in dc and unipolar pulsed modes were studied. It was demonstrated that bright compact coatings with varied content of molybdenum can be produced by varying the relative concentrations of salts of the alloy-forming components and the solution pH. The current density ranges providing the high efficiency of the galvanostastic electrolysis were determined and it was shown that using the pulsed mode makes smaller the amount of nonmetallic impurities in a coating, diminishes its roughness and leads to formation of surface layers with a more uniform composition, The ironβmolybdenum coatings exhibit a high corrosion resistance in corrosive media and physicomechanical properties improved as compared with the base metal, which makes it possible to recommend these coatings for protection from corrosive-mechanical disintegration and restoration of the surface of worn articles
The Longitudinal Flow of Oil and Petroleum Products in the Channels and Pipes. Part II
A model associated fluid flow and heat transfer of longitudinal flows of oil in pipes and channels is considered. The model is an extended version of the Bingham flow on the case of flow with one or two solid cores. The fluid part is a two-phase medium, wherein the disperse phase may consist of solid particles, droplets and gas bubbles. The sliding on the borders of pipes and channels, thermal conductivity and viscosity of such systems and their impact on the characteristics of the solid core are discussed. The flow with a yield point dependence on the temperature is also considered
Mixed alumina and cobalt containing plasma electrolytic oxide coatings
Principles of plasma electrolytic oxidation of the AL25 aluminum alloy in diphosphate alkali solutions containing cobalt(2+) cations are discussed. It has been established that a variation in the concentration of the electrolyte components provides the formation of mixed-oxide coatings consisting of the basic matrix materials and the cobalt oxides of different content. An increase in the cobalt oxide content in the coating is achieved by the variation in electrolysis current density as well as the treatment time due to both the electrochemical and thermo-chemical reactions at substrate surface and in spark region. Current density intervals that provide micro-globular surface formation and uniform cobalt distribution in the coating are determined. The composition and morphology of the surface causes high catalytic properties of synthesized materials, which confirmed the results of testing in model reaction CO and benzene oxidation as well as fuel combustion for various modes of engine operation
Π€ΠΎΡΠΌΠΈΡΠΎΠ²Π°Π½ΠΈΠ΅ ΠΏΠΎΠΊΡΡΡΠΈΠΉ ΡΠΌΠ΅ΡΠ°Π½Π½ΡΠΌΠΈ ΠΎΠΊΡΠΈΠ΄Π°ΠΌΠΈ Π°Π»ΡΠΌΠΈΠ½ΠΈΡ ΠΈ ΠΌΠ°ΡΠ³Π°Π½ΡΠ° Π½Π° ΡΠΏΠ»Π°Π²Π΅ ΠΠ25
Features of plasma electrolytic oxidation of the AL25 cast complex-alloyed aluminum alloy are discussed. It has been shown that a variation in the nature and concentration ratio of the electrolyte components provides the formation of mixed-oxide coatings containing the materials of the basic matrix and the dopant. An increase in the coating thickness and the manganese oxide content in the coating is achieved by the homogenization of the treated surface owing to the simultaneous formation of oxides and the removal of alloying components of the alloy from the surface layers. Current density intervals that provide a uniform distribution of elements in the coating and a high efficiency of the Faraday and thermochemical reactions are determined. It is found that the stoichiometric oxygen index in MnOx oxides is x = 1.71β1.87. Testing of the synthesized oxide systems in the model oxidation of carbon (II) oxide to COβ shows that the ignition and complete conversion temperatures are at the level of values characteristic of platinum catalysts.Π Π°ΡΡΠΌΠΎΡΡΠ΅Π½Ρ ΠΎΡΠΎΠ±Π΅Π½Π½ΠΎΡΡΠΈ ΠΏΠ»Π°Π·ΠΌΠ΅Π½Π½ΠΎ-ΡΠ»Π΅ΠΊΡΡΠΎΠ»ΠΈΡΠΈΡΠ΅ΡΠΊΠΎΠ³ΠΎ ΠΎΠΊΡΠΈΠ΄ΠΈΡΠΎΠ²Π°Π½ΠΈΡ Π»ΠΈΡΠ΅ΠΉΠ½ΠΎΠ³ΠΎ ΡΠ»ΠΎΠΆΠ½ΠΎΠ»Π΅Π³ΠΈΡΠΎΠ²Π°Π½Π½ΠΎΠ³ΠΎ ΡΠΏΠ»Π°Π²Π° Π°Π»ΡΠΌΠΈΠ½ΠΈΡ ΠΠ25. ΠΠΎΠΊΠ°Π·Π°Π½ΠΎ, ΡΡΠΎ Π²Π°ΡΡΠΈΡΠΎΠ²Π°Π½ΠΈΠ΅ ΠΏΡΠΈΡΠΎΠ΄Ρ ΠΈ ΡΠΎΠΎΡΠ½ΠΎΡΠ΅Π½ΠΈΡ ΠΊΠΎΠ½ΡΠ΅Π½ΡΡΠ°ΡΠΈΠΉ ΠΊΠΎΠΌΠΏΠΎΠ½Π΅Π½ΡΠΎΠ² ΡΠ»Π΅ΠΊΡΡΠΎΠ»ΠΈΡΠ° ΠΏΠΎΠ·Π²ΠΎΠ»ΡΠ΅Ρ ΡΠΎΡΠΌΠΈΡΠΎΠ²Π°ΡΡ ΠΏΠΎΠΊΡΡΡΠΈΡ ΡΠΌΠ΅ΡΠ°Π½Π½ΡΠΌΠΈ ΠΎΠΊΡΠΈΠ΄Π°ΠΌΠΈ, Π² ΡΠΎΡΡΠ°Π² ΠΊΠΎΡΠΎΡΡΡ
Π²Ρ
ΠΎΠ΄ΠΈΡ ΠΌΠ°ΡΠ΅ΡΠΈΠ°Π» ΠΎΡΠ½ΠΎΠ²Π½ΠΎΠΉ ΠΌΠ°ΡΡΠΈΡΡ ΠΈ Π΄ΠΎΠΏΠ°Π½ΡΠ°. ΠΠΎΠ²ΡΡΠ΅Π½ΠΈΠ΅ ΡΠΎΠ»ΡΠΈΠ½Ρ ΠΏΠΎΠΊΡΡΡΠΈΡ ΠΈ ΡΠΎΠ΄Π΅ΡΠΆΠ°Π½ΠΈΡ Π² Π½Π΅ΠΌ ΠΎΠΊΡΠΈΠ΄Π° ΠΌΠ°ΡΠ³Π°Π½ΡΠ° Π΄ΠΎΡΡΠΈΠ³Π°Π΅ΡΡΡ Π³ΠΎΠΌΠΎΠ³Π΅Π½ΠΈΠ·Π°ΡΠΈΠ΅ΠΉ ΠΎΠ±ΡΠ°Π±Π°ΡΡΠ²Π°Π΅ΠΌΠΎΠΉ ΠΏΠΎΠ²Π΅ΡΡ
Π½ΠΎΡΡΠΈ Π·Π° ΡΡΠ΅Ρ ΠΎΠ΄Π½ΠΎΠ²ΡΠ΅ΠΌΠ΅Π½Π½ΠΎΠ³ΠΎ ΡΠΎΡΠΌΠΈΡΠΎΠ²Π°Π½ΠΈΡ ΠΎΠΊΡΠΈΠ΄ΠΎΠ² ΠΈ ΡΠ΄Π°Π»Π΅Π½ΠΈΡ Π»Π΅Π³ΠΈΡΡΡΡΠΈΡ
ΠΊΠΎΠΌΠΏΠΎΠ½Π΅Π½ΡΠΎΠ² ΡΠΏΠ»Π°Π²Π° ΠΈΠ· ΠΏΠΎΠ²Π΅ΡΡ
Π½ΠΎΡΡΠ½ΡΡ
ΡΠ»ΠΎΠ΅Π². Π£ΡΡΠ°Π½ΠΎΠ²Π»Π΅Π½Ρ ΠΈΠ½ΡΠ΅ΡΠ²Π°Π»Ρ ΠΏΠ»ΠΎΡΠ½ΠΎΡΡΠΈ ΡΠΎΠΊΠ°, ΠΎΠ±Π΅ΡΠΏΠ΅ΡΠΈΠ²Π°ΡΡΠΈΠ΅ ΡΠ°Π²Π½ΠΎΠΌΠ΅ΡΠ½ΠΎΠ΅ ΡΠ°ΡΠΏΡΠ΅Π΄Π΅Π»Π΅Π½ΠΈΠ΅ ΡΠ»Π΅ΠΌΠ΅Π½ΡΠΎΠ² Π² ΠΏΠΎΠΊΡΡΡΠΈΠΈ ΠΈ Π²ΡΡΠΎΠΊΡΡ ΡΡΡΠ΅ΠΊΡΠΈΠ²Π½ΠΎΡΡΡ ΡΠ°ΡΠ°Π΄Π΅Π΅Π²ΡΠΊΠΈΡ
ΠΈ ΡΠ΅ΡΠΌΠΎΡ
ΠΈΠΌΠΈΡΠ΅ΡΠΊΠΈΡ
ΡΠ΅Π°ΠΊΡΠΈΠΉ. ΠΠΎΠΊΠ°Π·Π°Π½ΠΎ, ΡΡΠΎ ΡΡΠ΅Ρ
ΠΈΠΎΠΌΠ΅ΡΡΠΈΡΠ΅ΡΠΊΠΈΠΉ ΠΈΠ½Π΄Π΅ΠΊΡ ΠΏΠΎ ΠΊΠΈΡΠ»ΠΎΡΠΎΠ΄Ρ Π² ΠΎΠΊΡΠΈΠ΄Π°Ρ
MnOx ΡΠΎΡΡΠ°Π²Π»ΡΠ΅Ρ x = 1,71β1,87. Π’Π΅ΡΡΠΈΡΠΎΠ²Π°Π½ΠΈΠ΅ ΡΠΈΠ½ΡΠ΅Π·ΠΈΡΠΎΠ²Π°Π½Π½ΡΡ
ΠΎΠΊΡΠΈΠ΄Π½ΡΡ
ΡΠΈΡΡΠ΅ΠΌ Π² ΠΌΠΎΠ΄Π΅Π»ΡΠ½ΠΎΠΉ ΡΠ΅Π°ΠΊΡΠΈΠΈ ΠΎΠΊΠΈΡΠ»Π΅Π½ΠΈΡ ΠΎΠΊΡΠΈΠ΄Π° ΡΠ³Π»Π΅ΡΠΎΠ΄Π° (II) Π΄ΠΎ COβ ΠΏΠΎΠΊΠ°Π·Π°Π»ΠΎ, ΡΡΠΎ ΡΠ΅ΠΌΠΏΠ΅ΡΠ°ΡΡΡΠ° Π·Π°ΠΆΠΈΠ³Π°Π½ΠΈΡ ΠΈ ΠΏΠΎΠ»Π½ΠΎΠΉ ΠΊΠΎΠ½Π²Π΅ΡΡΠΈΠΈ Π½Π°Ρ
ΠΎΠ΄ΠΈΡΡΡ Π½Π° ΡΡΠΎΠ²Π½Π΅ ΠΏΠ»Π°ΡΠΈΠ½ΠΎΠ²ΡΡ
ΠΊΠ°ΡΠ°Π»ΠΈΠ·Π°ΡΠΎΡΠΎΠ²
ΠΠ°Π»ΡΠ²Π°Π½ΠΎΡ ΡΠΌΡΡΠ½Π΅ ΡΠΎΡΠΌΡΠ²Π°Π½Π½Ρ Π±Π°Π³Π°ΡΠΎΠΊΠΎΠΌΠΏΠΎΠ½Π΅Π½ΡΠ½ΠΎΠ³ΠΎ ΡΠΏΠ»Π°Π²Ρ Π½Π° ΠΎΡΠ½ΠΎΠ²Ρ ΠΊΠΎΠ±Π°Π»ΡΡΠ° ΡΠ° ΡΡΠ³ΠΎΠΏΠ»Π°Π²ΠΊΠΈΡ ΠΌΠ΅ΡΠ°Π»ΡΠ²
Effects of major parameters of electrolysis on the composition and morphology of the cobalt-molybdenum-tungsten alloy from citrate- pyrophosphate and citrate-ammonium electrolytes have been analysed. It has been shown that the content of component metals in the Co-W-Mo alloy depends on the nature and composition of the electrolyte solution. The influence of electrolysis conditions and regime on the structure and morphology of cobalt alloys with refractory metals has been established. The elemental composition and morphology of the triple cobalt - molybdenum - tungsten coatings have been determined with a scanning electron microscope.ΠΡΠΎΠ°Π½Π°Π»ΡΠ·ΠΎΠ²Π°Π½ΠΎ Π²ΠΏΠ»ΠΈΠ² ΠΎΡΠ½ΠΎΠ²Π½ΠΈΡ
ΠΏΠ°ΡΠ°ΠΌΠ΅ΡΡΡΠ² Π΅Π»Π΅ΠΊΡΡΠΎΠ»ΡΠ·Ρ Π½Π° ΡΠΊΠ»Π°Π΄ ΡΠ° ΠΌΠΎΡΡΠΎΠ»ΠΎΠ³ΡΡ ΡΠΏΠ»Π°Π²Ρ ΠΊΠΎΠ±Π°Π»ΡΡ-ΠΌΠΎΠ»ΡΠ±Π΄Π΅Π½-Π²ΠΎΠ»ΡΡΡΠ°ΠΌ ΠΎΡΡΠΈΠΌΠ°Π½ΠΎΠ³ΠΎ Π· ΡΠΈΡΡΠ°ΡΠ½ΠΎ-Π΄ΠΈΡΠΎΡΡΠ°ΡΠ½ΠΎΠ³ΠΎ ΡΠ° ΡΠΈΡΡΠ°ΡΠ½ΠΎ-Π°ΠΌΠΎΠ½ΡΠ°ΡΠ½ΠΎΠ³ΠΎ Π΅Π»Π΅ΠΊΡΡΠΎΠ»ΡΡΡΠ². ΠΠ° Π΄ΠΎΠΏΠΎΠΌΠΎΠ³ΠΎΡ ΡΠΊΠ°Π½ΡΠ²Π½ΠΎΠ³ΠΎ Π΅Π»Π΅ΠΊΡΡΠΎΠ½Π½ΠΎΠ³ΠΎ ΠΌΡΠΊΡΠΎΡΠΊΠΎΠΏΡ Π΄ΠΎΡΠ»ΡΠ΄ΠΆΠ΅Π½ΠΎ ΡΠΊΠ»Π°Π΄ Ρ ΠΌΠΎΡΡΠΎΠ»ΠΎΠ³ΡΡ ΠΏΠΎΡΡΡΠΉΠ½ΠΈΡ
ΠΏΠΎΠΊΡΠΈΡΡΡΠ². ΠΡΠ»ΠΎ ΠΏΠΎΠΊΠ°Π·Π°Π½ΠΎ, ΡΠΎ Π²ΠΌΡΡΡ ΠΊΠΎΠΌΠΏΠΎΠ½Π΅Π½ΡΡΠ² Π² ΡΠΏΠ»Π°Π²Ρ Π‘ΠΎ-W-ΠΠΎ Π·Π°Π»Π΅ΠΆΠΈΡΡ Π²ΡΠ΄ ΠΏΡΠΈΡΠΎΠ΄ΠΈ Π»ΡΠ³Π°Π½Π΄Π° Ρ ΡΠΏΡΠ²Π²ΡΠ΄Π½ΠΎΡΠ΅Π½Π½Ρ ΠΊΠΎΠ½ΡΠ΅Π½ΡΡΠ°ΡΡΠΉ ΡΠΏΠ»Π°Π²ΠΎΡΠ²ΡΡΠ½ΠΈΡ
ΠΌΠ΅ΡΠ°Π»ΡΠ². ΠΡΡΠ°Π½ΠΎΠ²Π»Π΅Π½ΠΎ Π²ΠΏΠ»ΠΈΠ² Π³ΡΡΡΠΈΠ½ΠΈ ΡΡΡΡΠΌΡ, Π° ΡΠ°ΠΊΠΎΠΆ ΡΠ°ΡΡ ΡΠΌΠΏΡΠ»ΡΡΡ ΡΠ° ΠΏΠ°ΡΠ·ΠΈ Π½Π° ΡΡΡΡΠΊΡΡΡΡ Ρ ΠΌΠΎΡΡΠΎΠ»ΠΎΠ³ΡΡ ΠΏΠΎΠΊΡΠΈΡΡΡΠ²
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