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Streat

K. For liquids, fixed and fluidized beds, Rahman and Streat correlation... [Pg.619]

Streat and Cloete, Ion Exchange, in Rousseau (ed.). Handbook of Sepa-lation Piocess Technology, Wiley, New York, 1987. [Pg.1496]

STREAT, M. Hydrotransport 10 (BHRA, Fluid Engineering, Innsbruck, Austria), (Oct. 1986). Paper Bl. Dense phase flow of solid-water mixtures in pipelines A state of the arl review. [Pg.227]

Cijoete, F. L. D, Miller, A. I., and Streat, M. Trans. Inst. Chem. Eng. 45 (1967) T392. Dense phase flow of solid-water mixtures through vertical pipes. [Pg.229]

M. Streat and D. Naden, eds., Ion Exchange and Sorption Processes in Hydrometallurgy, John Wiley Sons, 1987. [Pg.578]

Lloyd-Jones, P.J., Rangel-Mendez, J.R., and Streat, M., Mercury sorption from aqueous solution by chelating ion exchange resins, activated carbon and a biosorbent, Process Safety and Environmental Protection, 82 (4), 301-311, 2004. [Pg.406]

Fig. 2 Hypothetical fragment of an oxidized carbon arnface. The figure was taken from [10] with kind permission from Prof. M. Streat... Fig. 2 Hypothetical fragment of an oxidized carbon arnface. The figure was taken from [10] with kind permission from Prof. M. Streat...
Streat M, Malik DJ, Saha B (2004) Adsorption and ion-exchange properties of engineered activated carbons and carbonaceous materials. In SenGupta AK, Marcus Y, Marinsky JA (eds) Ion exchange and solvent extraction, chap 1. Dekker, New York... [Pg.33]

For 5 < Rep < 100, the following correlation, obtained by Rahman and Streat for mass transfer, is valid for conventional liquid fluidized beds (Rahman and Streat, 1981 Hausmann et al., 2000) ... [Pg.225]

Basic properties of common materials used in the manufacture of activated carbon (Dabrowski et al., 2005 Streat el al., 1995)... [Pg.244]

Ashm 226 Thomas Sharpe, (24 Dec. 1597), William Streate (24 Dec. 1597), Robert Steavens (29 Jan. 1597). Thomas Colman and an unnamed boy were also noted by Forman as having been part ofthe Skinner household. [Pg.147]

Green B. R., Jaskulla .//Ion Exchange Technology / D. Naden Streat. Chichester Ellis Horwood Limited, 1984. P. 490—499. [Pg.279]

Figure 15.22. A process for recovering uranium from mine waters. The absorption column is 2.16 m dia, water flow rate is 28.5 m/hr, resin transfer off the top of the absorption column is 87 L every 3 hr, inlet concentration 3-6mgU/L, outlet 0.002-0.009 mg U/L (Himsley and Bennett, in Naden and Streat, 1984, pp. 144-168 U.S. Pat. 4,018,677). Figure 15.22. A process for recovering uranium from mine waters. The absorption column is 2.16 m dia, water flow rate is 28.5 m/hr, resin transfer off the top of the absorption column is 87 L every 3 hr, inlet concentration 3-6mgU/L, outlet 0.002-0.009 mg U/L (Himsley and Bennett, in Naden and Streat, 1984, pp. 144-168 U.S. Pat. 4,018,677).
Performances of four fluidized bed ion exchange plants are described by Cloete (in Naden and Streat, 1984, pp. 661-667). One of the exchange columns is 4.85 m dia, has 12 stages each 1 m high, with perforated trays having holes 12 mm dia with a capacity of 640 m3/hr of uranium mine waters. [Pg.517]

D. Naden and M. Streat, Eds., Ion Exchange Technology, Horwood, Chichester, England, 1984. [Pg.522]

ADSORPTION AND ION-EXCHANGE PROPERTIES OF ENGINEERED ACTIVATED CARBONS AND CARBONACEOUS MATERIALS Michael Streat, Danish J. Malik, and Basudeb Saha... [Pg.670]

Barnes CD, da Silva Neves RD, Streat M (1974) J Appl Chem Biotechnol 24 787... [Pg.188]


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See also in sourсe #XX -- [ Pg.113 , Pg.197 , Pg.249 , Pg.271 ]

See also in sourсe #XX -- [ Pg.198 , Pg.210 , Pg.227 , Pg.229 ]




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