Distillation desalination

Larbot A, Gazagnes L, Krajewski S, Bukowska M, and Kujawski W. Water desalination using ceramic membranes distillation. Desalination 2004 168 367-372. 

Khayet, M. and Mengual, J.I. Effect of salt concentration during the treatment of humic acid solutions by membrane distillation. Desalination, 168(1-3), 373, 2004. 

Andersson, S.I., Kjellander, N., and Rodesjo, B. Design and field tests of a new membrane distillation desalination process. 

Schofield, R.W., et al. Factors affecting flux in membrane distillation. Desalination, 77, 279, 1990. 

Ding, Z., Runyu, M., and Eane, A.G. A new model for mass transfer in direct contact membrane distillation. Desalination, 151, 217, 2002. 

Ohta, K. Experiments on seawater desalination by membrane distillation, Desalination, 78, 177, 1990. 

Basini, L., et al. Desalination process through sweeping gas membrane distillation. Desalination, 64, 245, 1987. 

Courel, M. The problem of membrane characterization for the process of osmotic distillation. Desalination, 140, 15, 2001. 

Celere, M. and Gostoli, C. The heat and mass transfer phenomena in osmotic membrane distillation. Desalination, 147, 133, 2002. 

Larbot, A., et al. Water desalination using ceramic membrane distillation. Desalination, 168, 367, 2004. 

Bandini, S. and Sarti, G.C. Concentration of must through vacuum membrane distillation. Desalination, 149, 253, 2002. 

AUdaibi, A.M. and Lior, N. Membrane-distillation desalination Status and potential. Desalination, 171, 111, 2004. 

Koschikowski, J., Wieghaus, M., and Rommel, M. Solar thermal-driven desalination plants based on membrane distillation, Desalination, 156, 295, 2003. 

M. Qtaishat, T. Matsuura, B. Kruczek, M. Khayet, Heat and mass transfer analysis in direct contact membrane distillation. Desalination 2008, 219, 272-292. 

Al-Asheh S., Banat E, Qtaishat M., Al-Khateeb M. (2006), Concentration of sucrose solutions via vacuum membrane distillation. Desalination, 195,60-68. 

Banat F.A., Simandl J. (1994),Theoretical and experimental study in membrane distillation, Desalination, 95,39-52. 

Boi C., Bandini S., Sarti G.C. (2005), Pollutants removal from wastewaters through membrane distillation, Desalination, 183,383-394. 

Gryta M., Tomaszewska M, Karakulski K. (2006), Wastewater treatment by membrane distillation. Desalination, 198,67-73. 

Martinez-Diez L., Florido-Diaz F. J. (2001), Desalination of brines by membrane distillation, Desalination, 137,1CI-TT5. 

Phattaranawik J., Pane A.G., Pasquier A.C.S., Bing W. (2008), A novel membrane bioreactor based on membrane distillation. Desalination, 223,386-395. 

Tomaszewska M. (1996), Preparation and properties of flat-sheet membranes from poly(vinyldene fluoride) for membrane distillation, Desalination, 104,1-11. 

The steam turbine plant (STP) is intended to provide electric energy to consumers and to transfer thermal energy from the NSSS to a distillation desalination plant (DDP). Each reactor plant operates together with its own STP. The secondary circuit of each STP includes 4 SGs, 2 turbo-generators (TGs) with condensate pumps, main and standby feed pumps, two process condensers with condensate plants, tanks, etc. 

A power and desalination complex (a cogeneration plant) based on a distillation desalinating plant (DDP) includes the reactor installation the extraction turbine the intermediate loop and the desalination plant (see Fig. IV-11). Heat and part of the electric power generated by the floating power unit are used for desalination the rest of the electric power is supplied to the consumers. 

Bottoming cycle Feed forward multi-effect distillation desalination. 

Farid Benyahia (immobilized nitrifiers in wastewater treatment membrane distillation desalination water quality and energy efficiency analysis airlift bioreactors low-grade heat in membrane distillation for freshwater production bioremediation of oil spills development, design and evaluation of advanced refinery wastewater treatment processes), College of Engineering, Department of Chemical Engineering, Qatar University (QU), Doha... 

The NDF RUTA could be a reliable, safe and ecologically friendly plant due to technical features of the reactor. Only the standard domestic distillation desalination plants (DDP) are applied for desalination. These plants have been modified to operate in the range of heat parameters provided by the reactor. The output of a NDF equipped with a single RUTA-70 reactor is about 30 000 mVday of distilled water. The estimated price of one cubic meter of fresh water varies from US 0.9 to US 1.3 depending on local economic conditions. The schematic flow diagram of the desalination plant with the RUTA reactor is given in Fig. XII-10. 

Lai, W.-C., Cheng, L.-T, 2014. Preparation and characterization of novel polyjvinylidene fluoride) membranes using self-assembled dibenzylidene sorbitol for membrane distillation. Desalination 332, 7-17. 

Banat, F., Al-Asheh, S., and Qtaishat, M. (2005). Treatment of waters colored with methylene blue dye by vacuum membrane distillation. Desalination 174, 87. 

Basini, L., D Angelo, G., Gobbi, M., Sard, G. C., and GostoU, C. (1987). A desalination process through sweeping gas membrane distillation. Desalination 64, 245. 

Couffin, N., Cabassud, C., and Lahoussine-Turcaud, V. (1998). A new process to remove halogenated VOCs for drinking water production Vacuum membrane distillation. Desalination 117, 233. CriscuoU, A., and DrioU, E. (1999). Energetic and exegetic analysis of an integrated membrane desa-Unation system. Desalination 124, 243. 

Khayet, M., and Matsuura, T. (2003a). Application of surface modifying macromolecules for the preparation of membranes for membrane distillation. Desalination 158, 51. 

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