Zobrazeno 1 - 10
of 13
pro vyhledávání: '"V. K. Maskaev"'
Autor:
V. K. Maskaev, A. I. Samoilenko
Publikováno v:
Automation and Remote Control. 71:2483-2490
Description and technical performances of standard test rig for measuring air flow speed in the range between 0.1 and 60 m/s are given. The test rig is designed for metrological analysis, verification tests and calibration of air flow speed meters.
Publikováno v:
Journal of Engineering Physics. 61:1368-1371
The authors present results of an experimental investigation of external heat transfer over the height of a circulation fluidized bed.
Publikováno v:
Journal of Engineering Physics. 59:1570-1574
Results are presented from an experimental study of external heat transfer in a circulating fluidized bed.
Publikováno v:
Journal of Engineering Physics. 59:1307-1310
Experimental results on the turbulent diffusion of passive impurity in a gas-suspension flow in a vertical cylindrical channel are outlined. On the basis of introducing simple approximations of spectral functions of the velocity pulsations, the influ
Publikováno v:
Measurement Techniques. 20:30-34
Autor:
V. K. Maskaev, A. P. Baskakov
Publikováno v:
Journal of Engineering Physics. 37:1423-1428
A method is given for calculating drying installations where an air suspension of finely dispersed particles is used as the drying agent.
Autor:
A. P. Baskakov, V. K. Maskaev
Publikováno v:
Journal of Engineering Physics. 43:894-900
A method is given for designing drying installations where a suspension of finely dispersed hygroscopic particles in air is used as the drying agent.
Publikováno v:
Journal of Engineering Physics. 57:1312-1317
The authors present results of an experimental determination of the aerodynamic drag, density, velocity and dwell time of disperse material in a circulating bed.
Publikováno v:
Measurement Techniques. 21:515-518
Autor:
V. S. Nosov, V. K. Maskaev
Publikováno v:
Journal of Engineering Physics. 21:1503-1506
The results of an experimental investigation of the effect of the degree of dust contamination of the air on the hydraulic resistance and velocity of the start of fluidization of a bed of spherical particles with an average diameter of 2.00–9.35 mm