Abstract:Analysis of contemporary cyclone gas purification apparatus was carried out in this article Calculation of the characteristics of the counterflow cyclone in application of pressurization system of the LV fuel tanks with gas pressure accumulator has been executed. 3D-model of the counter-flow cyclone was built. Numerical modeling of soot-cleaning process in countercurrent cyclone has been performed using ANSYS Fluent.
“…From the result of the research [5], the number of particles which pass through the apparatus per 200 seconds is equal to 629677. 78,3% of them (492893) were delivered to a soot-catching storage, 21,3% (134209) of them were still inside the flow channel and 0,4% (2575) were not separated from the flow and left the cyclone with cleaned gas.…”
Section: Formulation Of the Problemmentioning
confidence: 99%
“…For this purpose, a numerical modeling of a different configuration of cyclones was carried out in the ANSYS Fluent software. [3,4] The opposite-flow cyclone, presented in [5], was selected as a prototype.…”
Abstract. This article deals with a cyclone cleaner which separates solid particles from the gas. The influence of the input duct angle and the relation of the conical part of the apparatus to a cylindrical one on the cleaning degree were investigated. 3-d models of the flow channel of the opposite-flow cyclone with input duct angles varied from 0 to 40° and conical and cylindrical parts relation from 2:3 to 4:1 were considered. Numerical modelling of a soot clearing process in the opposite-flow cyclone was carried out in the ANSYS Fluent software. The results of 25 different models are presented.
“…From the result of the research [5], the number of particles which pass through the apparatus per 200 seconds is equal to 629677. 78,3% of them (492893) were delivered to a soot-catching storage, 21,3% (134209) of them were still inside the flow channel and 0,4% (2575) were not separated from the flow and left the cyclone with cleaned gas.…”
Section: Formulation Of the Problemmentioning
confidence: 99%
“…For this purpose, a numerical modeling of a different configuration of cyclones was carried out in the ANSYS Fluent software. [3,4] The opposite-flow cyclone, presented in [5], was selected as a prototype.…”
Abstract. This article deals with a cyclone cleaner which separates solid particles from the gas. The influence of the input duct angle and the relation of the conical part of the apparatus to a cylindrical one on the cleaning degree were investigated. 3-d models of the flow channel of the opposite-flow cyclone with input duct angles varied from 0 to 40° and conical and cylindrical parts relation from 2:3 to 4:1 were considered. Numerical modelling of a soot clearing process in the opposite-flow cyclone was carried out in the ANSYS Fluent software. The results of 25 different models are presented.
“…Another factor affecting the results of the chromatographic analysis is temperature fields distribution in the gas chromatograph detector. Output channels configuration in the gas chromatograph detector should provide uniform temperature fields distribution at constant gas-flow rate [7].…”
Section: The Resistance-temperature Dependence Of the Sensitive Ementioning
Thermal conductivity detector for use in gas dynamic express-analyzers and high-speed chromatography systems is being developed by chemistry department in cooperation with other Samara University departments. This article is devoted to investigating the effect of temperature on detector sensitivity. Silicon underlying with resistive chromium layer was used as a sensitive element of the detector. The temperature dependence of the sensitive element resistance was defined for different chromium film thicknesses. The film thickness which provides the highest sensitivity of the detector was found. Also optimal output channels configuration in the gas chromatograph detector was determined. It provides uniform temperature fields distribution at constant gas-flow rate.
“…For this purpose it is sufficient to investigate the generalized polytropic cycle (Figure 2), which is limited by the following assumptions: 1) processes are reversible; 2) the specific heat, and hence the polytropic indices are constant values; 3) working body -ideal gas; 4) heat supply is carried out during II, removal -during IV; 5) heat transfer in the process I is absent, although the process is considered as a polytropic (a consequence of the IPOA specificity, in which energy components are supplied either liquid, or in a precompressed state); 6) Process III is considered to be adiabatic [7]. The equation ߟ ௧ .о of polytropic cycle should include the maximum-to-minimum cycle temperature ratio ܶ ଷ /ܶ ଵ cycle and the pressure at point 4 -p 4 .…”
Abstract. The problems of high energy loss exists in many industries and in many technological processes. The problem of not effective use of the energy potential of the refrigerants is the main problem, because the refrigerant loses its potential and the potential energy at the regasification upon receipt of the liquefied natural gas. Solution of this problem is using low-grade heat of the refrigerant. This investigation describes the creation of a design procedure of the installation of the cycle that uses low-grade heat of the refrigerant. The cycle that uses low-grade heat of the refrigerant has been described and calculation method has been developed.
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