Rejection of organic compounds by ultra-low pressure reverse osmosis membrane.

The introduction of ultra-low pressure reverse osmosis (ULPRO) membrane has widened the horizon of reverse osmosis (RO) in purification of surface water and wastewater as well as desalination of brackish water. The ULPRO membrane chemistry can provide a high water flux at low operating pressure, while maintaining a very good salt and organics rejection. This paper deals with the investigation on the rejection of low molecular weight organic compounds by ULPRO membrane. Laboratory scale experiments were carried out at a pressure of 3 kg/cm2 with a feed flow rate of 1.20 l/min. The rejection of undissociated organic compounds did not show a close relationship with the feed pH. The percentage removal of undissociated organic compounds increased linearly with the molecular weight as well as with the molecular width. The removal efficiency can be predicted by these relationships. But neither molecular weight nor molecular width can be considered as an absolute factor for rejection. The feed pH also influenced the removal efficiency of dissociated organic compounds. The efficiency decreased linearly with the increase in the dissociation constant.

[1]  Victor H. Edwards,et al.  Organic Molecules From Water Supplies by Reverse Osmosis , 1974 .

[2]  W. A. Duvel,et al.  Removal of wastewater organics by reverse osmosis. , 1975, Journal - Water Pollution Control Federation.

[3]  Y. Kiso Rejection properties of alkyl phthalates with nanofiltration membranes , 2001 .

[4]  H. Ruiz,et al.  Selecting membranes for removing NOM and DBP precursors , 1994 .

[5]  Masahiko Hirose,et al.  New membrane developments expanding the horizon for the application of reverse osmosis technology , 1998 .

[6]  James S. Taylor,et al.  SOC Removal in a Membrane Softening Process , 1992 .

[7]  Y. Kiso,et al.  The effects of molecular width on permeation of organic solute through cellulose acetate reverse osmosis membranes , 1992 .

[8]  Herman Koren Handbook of environmental health and safety : principles and practices / Herman Koren , 1980 .

[9]  W. P. Ball,et al.  NANOFILTRATION OF NATURAL ORGANIC MATTER: pH AND IONIC STRENGTH EFFECTS , 1997 .

[10]  Nandakishore Rajagopalan,et al.  Consider nanofiltration for membrane separations , 1994 .

[11]  Takane Kitao,et al.  Rejection properties of non-phenylic pesticides with nanofiltration membranes , 2000 .

[12]  G. Laufenberg,et al.  Waste water treatment using reverse osmosis: real osmotic pressure and chemical functionality as influencing parameters on the retention of carboxylic acids in multi-component systems , 1997 .

[13]  V. Dananić,et al.  FT30 membranes of characterized porosities in the reverse osmosis organics removal from aqueous solutions , 1997 .

[14]  J. Hofman,et al.  Removal of pesticides and other organic micropollutants with membrane filtration , 1993 .

[15]  E. Chian,et al.  Reverse osmosis separation of polar organic compounds in aqueous solution , 1976 .