аэродинамика воздухоочистных устройств с зернистым слоем

329
Sercu, B.; Núñez, D.; Van Langenhove, H.; Aroca, G.; Verstraete, W. 2005. Operational and
microbiological aspects of a bioaugmented two-stage biotrickling filter removing hydrogen
sulfide and dimethyl sulphide, Biotechnology and Bioengineering 90(2): 259–269.
Sercu, B.; Peixoto, J.; Demeestere, K.; Elst, T.; Langenhof, H. 2006. Odors treatment: biological
technologies, in Odors in the Food Industry, Chapter 8, Springer US, 125–158.
Seze, М.; Nishimura, Y.; Sakohara, S.; Shinagawa, H.; Kamamura, Y. 1977. The analysis of
flow of rarefied gases through packed beds by Monte-Carlo method, Journal Chemical
Engineering Japan 10(5): 360–365.
Shareefdeen, Z.; Herner, B.; Webb, D.; Wilson, S. 2003. Biofiltration eliminates nuisance
chemical odors from industrial air streams, Journal of Industrial Microbiology and Biotechnology
30: 168–174.
Sheridan, B. A.; Curran, T. P.; Dodd, V. A. 2002. Assessment of the influence of media
particle size on the biofiltration of odorous exhaust ventilation air from a piggery facility,
Bioresource Technology 84: 129–143.
Shim, E. H.; Kim, J.; Cho, K. S.; Wook Ryu, H. W. 2006. Biofiltration and inhibitory interactions
of gaseous benzene, toluene, xylene, and methyl tert-butyl ether, Environmental
Science & Technology 40(9): 3089–3094.
Solntsev, M. Ya.; Bobe, L. S.; Korotaeva, G. K. 1963. Determination of the Coefficients of
Heat Transfer from a Gas to a Bed of Free-Flowing Materials, International Chemical
Engineering 3(2): 215–219.
Sonntag, G. 1960. Einfluss des Lückenvolümen auf den Druckverlust in gasdurchströmten
Füllkörpersäule, Chemie-Ingenieur-Technik 32(Jabrgang 5): 317–329.
Specchia, V.; Baldi, G. 1977. Pressure drop and liquid holdup for two phase concurrent flow
in packed beds, Chemical Engineering Science 32(5): 515–523.
Srinivasan, S. K.; Mehata, К. М. 1972. A Markov Chain Model of a Packed Bed, American
Institute of Chemical Engineers Journal 18(13): 650–652.
Staneck, V.; Szekely, J. 1972. The Effect of Non-Uniform Porosity in Causing Flow Maldistributions
in Isothermal Packed Beds, The Canadian Journal of Chemical Engineering
50(1): 9–14.
Staneck, V.; Szekely, J. 1973. Flow Maldistribution in Two Dimensional Packed Beds. Part
II. The Behavior of Non-Isothermal Systems, The Canadian Journal of Chemical Engineering
51(1): 22–30.
Stroh, K. R.; Olson, H. G.; Jiacoletti, R. J. 1979. Comparison of Coolant Flow Predictions
with Those Measured on a Full-Scale Mackup of a Pebble Bed Reactor Core, Nuclear
Engineering and Design 52(2): 349–356.
Studer, M.; Rudof von Rohr, P. 2008. Novel membrane bioreactor: able to cope with fluctuating
loads, poorly water soluble VOCs, and biomass accumulation, Biotechnology and
Bioengineering 99(1): 38–48.
Syron, E.; Casey, E. 2008. Membrane-aerated biofilms for high rate biotreatment: performance
appraisal, engineering principles, scale-up, and development requirements, Environmental
Science & Technology 42(6): 1833–1844.
Szekely, J.; Poveromo, J. J. 1975. Flow Maldistribution in Packed Beds: A Comparison
of Measurements with Predictionse, American Institute of Chemical Engineers Journal
21(4): 769–775.