DESALINATION, TRENDS AND TECHNOLOGIES Phần 2 docx
DESALINATION, TRENDS AND TECHNOLOGIES Phần 2 docx
... system, Desalination, Vol. 42, No.1 (January 20 02) 79–88, ISSN 0011-9164 Gryta, M. (20 04). Water membrane distiller, Inż. Chem. Proc., Vol. 25 , No .2 (April 20 04), 381– 391, ISSN 020 8-6 425 Desalination, ... al., 20 05; Teoh et al., 20 08). 0 50 100 150 20 0 25 0 0 2 4 6 8 10 12 Time of MD, t [h] 0 0.5 1 1.5 2 2.5 C Feed [g TDS/dm 3 ] κ permeate [μS/cm...
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DESALINATION, TRENDS AND TECHNOLOGIES Phần 4 potx
... Desalination, Trends and Technologies 128 Parameter Metric US Capacity 165,000 m3/day (330,000 m3/day) 44 MGD (88 MGD) CAPITAL TOTAL $ 21 2 M $ 21 2 M Capital cost for 20 yrs at 6% $ ... large sizes were more Desalination, Trends and Technologies 122 MGD / 166,000 m3/day, which was expanded to 88 MGD / 330,000 m3/day at the end of 20 05. When different...
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DESALINATION, TRENDS AND TECHNOLOGIES Phần 7 pdf
... 11. 72 7 56 45.3 1.78 1.85 27 0 0.744 21 6.3 80.67 1150 11.87 13 .28 8 56 43.3 1.81 2 300 0.831 20 2 75.3 1016.8 12. 7 14.57 9 57 42. 8 1.77 2. 2 307 0.9 02 187 69. 82 9 82 13.7 15.8 10 59 42. 8 ... kJ/kg At d m 2 /kg/s SESM SQP 4 56 45.8 3.4 1.95 26 3 0.7 92 3 12. 8 116.9 450.8 8.18 8 .24 5 56 45.8 2. 55 1.87 26 3 0.756 24 9.6 93.15 699.8 10 .27 10 .26 6 56...
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DESALINATION, TRENDS AND TECHNOLOGIES Phần 9 doc
... 30º 18- 32 1.08 3.03 - 45º 18- 32 1.61 2. 82 - Cipollina et al (20 09) Convencional techniques 60º 18- 32 2. 32 2 .25 - 30º 27 -50 1.07 3.18 1.51 45º 27 -50 1.71 3.3 32 1.71 Kikkert et al (20 07) (LA) ... 25 -60 1.04F 3.48 - 45º 25 -60 1.56F 3.33 - Zeitoun et al (1970) Conventional techniques 60º 25 -60 2. 13F 3.19 1.12F Roberts et al, (1997) Optical techniques 60...
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DESALINATION, TRENDS AND TECHNOLOGIES Phần 10 ppsx
... ro1 ro1 ro2 ro2 ro2 hpp hpp ( - ) 1.01 325 24 ( - ) 1.01 325 24 PP W PP W eff eff ++ b f Rbdw RM b f Rbdw RM ers ro1 ro1 ro1 ro1 ers ro2 ro2 ro2 ro2 1.01 325 (2 - ) 24 ( ) 1.01 325 (2 - ) 24 ( )eff ... 1957.8 A t , m 2 - - - - 11858.9195 52. 9 27 100.3 34308.4 40568.8 46406 .2 525 94.8 Δt, K - - - - 7 .24 6.75 6.48 6.34 6.30 6 .28 6 .25 Δt f , K - - - - 3.54 2. 95 2. 63 2...
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