Process for dewatering an aqueous organic solution

Abstract

An energy-efficient process for dewatering an aqueous organic solution includes using freely available solar energy to concentrate a draw solution within a reservoir. The draw solution is used in conjunction with a membrane to remove water from the organic solution in a forward osmosis process. The draw solution is diluted by the osmosis process, and returned to the reservoir to be re-concentrated and reused in the osmosis process.

1 . A system for dewatering an aqueous organic solution, comprising:
 a) a source of feed solution comprising an organic liquid and water, the feed solution having a water activity;   b) a reservoir containing a draw solution comprising an osmotic agent and water, the draw solution having a water activity lower than the water activity of the feed solution, wherein solar energy concentrates the draw solution to a desired concentration within the reservoir;   c) a membrane having a water/organic selectivity greater than 1 and an osmotic agent rejection rate greater than 95%, the membrane having a draw solution side and a feed solution side;   d) a means for delivering the feed solution to the feed solution side of the membrane whereupon the feed solution is dewatered;   e) a means for delivering the draw solution from the reservoir to the draw solution side of the membrane whereupon the draw solution is diluted;   f) a means for delivering the diluted draw solution from the draw solution side of the membrane to the reservoir; and   g) a means for removing the dewatered organic solution from the feed solution side of the membrane.   
   
   
       2 . The system according to  claim 1  wherein the aqueous organic solution is an aqueous alcohol solution and wherein the membrane has a water/organic selectivity greater than 50. 
   
   
       3 . The system according to  claim 1  wherein the reservoir is a pond, an open tank or a closed tank. 
   
   
       4 . The system according to  claim 1  wherein the feed and draw solutions are delivered continuously to the feed and draw solution sides of the membrane, respectively, and the reservoir is sized such that the concentration of the draw solution in the reservoir is essentially constant. 
   
   
       5 . The system according to  claim 1  further comprising a means for removing solids from the feed solution prior to delivering to the membrane. 
   
   
       6 . The system according to  claim 5  wherein the means for removing solids is a filter, a centrifuge, a microporous membrane or a dense membrane. 
   
   
       7 . The system according to  claim 6  wherein the means for removing solids is an ethanol selective membrane. 
   
   
       8 . The system according to  claim 1  wherein the membrane is selected from the group consisting of hollow fiber membranes, flat asymmetric membranes, multicomponent membranes and dense film membranes and wherein the membrane comprises a material selected from the group consisting of polymeric materials, metal-organic complexes, inorganic materials and combinations thereof. 
   
   
       9 . The system according to  claim 1  wherein the means for delivering the feed solution to the membrane and the means for delivering the draw solution to the membrane comprise pumps or gravity. 
   
   
       10 . The system according to  claim 1  wherein the means for delivering the draw solution to the membrane and the means for delivering the diluted draw solution to the reservoir comprise non-corroding plastic piping. 
   
   
       11 . A process for dewatering an aqueous organic solution, comprising the steps of:
 a) providing a membrane having a water/organic selectivity greater than 1 and an osmotic agent rejection rate greater than 95%, the membrane having a draw solution side and a feed solution side;   b) delivering a feed solution comprising an organic liquid and water having a water activity to the feed solution side of the membrane;   c) delivering a draw solution comprising an osmotic agent having a water activity lower than the water activity of the feed solution and having a desired concentration from a reservoir to the draw solution side of the membrane whereupon water from the feed solution moves from the feed solution side of the membrane to the draw solution side of the membrane, thereby dewatering the feed solution and diluting the draw solution;   d) delivering the diluted draw solution from the membrane to the reservoir;   e) concentrating the draw solution in the reservoir by the use of solar energy to the desired concentration; and   f) removing the dewatered organic solution from the membrane.   
   
   
       12 . The process according to  claim 11  wherein the aqueous organic solution comprises at least one alcohol selected from the group consisting of alcohols having between 2 and 14 carbon atoms and isomers thereof. 
   
   
       13 . The process according to  claim 11  wherein the aqueous organic solution comprises ethanol. 
   
   
       14 . The process according to  claim 11  wherein the feed solution has a concentration between about 0.1% and about 50% by volume. 
   
   
       15 . The process according to  claim 11  wherein the feed solution has a concentration between about 0.1% and about 15% by volume. 
   
   
       16 . The process according to  claim 11  wherein the dewatered organic solution has a concentration of between about 1% and about 99% by volume. 
   
   
       17 . The process according to  claim 11  wherein the draw solution comprises a water-soluble component selected from the group consisting of halides, nitrates, phosphates, sulfates, acetates and sugars. 
   
   
       18 . The process according to  claim 11  wherein the draw solution comprises urea. 
   
   
       19 . The process according to  claim 11  wherein the membrane has a water/organic selectivity of at least about 50 and a flux of at least about 1 L/m 2 /hr. 
   
   
       20 . The process according to  claim 11  wherein the feed and draw solutions are delivered continuously to the feed and draw solution sides of the membrane, respectively and wherein the reservoir is sized such that the concentration of the draw solution in the reservoir is essentially constant. 
   
   
       21 . The process according to  claim 11  wherein the feed and draw solutions are delivered semi-continuously or batchwise to the feed and draw solution sides of the membrane, respectively. 
   
   
       22 . The process according to  claim 11  wherein the membrane is selected from the group consisting of hollow fiber membranes, flat asymmetric membranes, multicomponent membranes and dense membranes, and wherein the membrane comprises a material selected from the group consisting of polymeric materials, metal-organic complexes, inorganic materials and combinations thereof. 
   
   
       23 . The process according to  claim 11  further comprising removing solids from the feed solution prior to delivering the feed solution to the membrane. 
   
   
       24 . The process according to  claim 11  wherein the reservoir is open to the atmosphere and solar energy drives evaporation of the water in the draw solution. 
   
   
       25 . The process according to  claim 11  wherein solar energy is concentrated with the use of mirrors and/or lenses to heat the draw solution in the reservoir.