Multi-branched cationic phosphonium salt, forward osmosis extract employing the same and forward osmosis seawater desalination process
US-2018346496-A1 · Dec 6, 2018 · US
US11273410B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11273410-B2 |
| Application number | US-201916731435-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 31, 2019 |
| Priority date | Dec 31, 2019 |
| Publication date | Mar 15, 2022 |
| Grant date | Mar 15, 2022 |
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An extracted material for forward osmosis is provided. The extracted material includes a first ionic compound, a second ionic compound and a third ionic compound, which are represented by formula {K[A + (R 1 )(R 2 )(R 3 )] p }(X − ) c (Y − ) d . X − is the same as Y − in the first ionic compound. X − is the same as Y − in the second ionic compound. X − in the first ionic compound is different from X − in the second ionic compound. X − differs from Y − in the third ionic compound. X − in the third ionic compound is the same as X − in the first ionic compound or X − in the second ionic compound. Y − in the third ionic compound is the same as Y − in the first ionic compound or Y − in the second ionic compound. A method for preparing an extracted material and a forward-osmosis water desalination system using the same are also provided.
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What is claimed is: 1. An ionic composition for forward osmosis, comprising: a first ionic compound; a second ionic compound; and a third ionic compound, wherein the first ionic compound, the second ionic compound and the third ionic compound are represented by formula (I): {K[A + (R 1 )(R 2 )(R 3 )] p }(X − ) c (Y − ) d (I), wherein R 1 , R 2 and R 3 independently comprise straight or branched C1-12 alkyl, A comprises phosphorus or nitrogen, K comprises C1-15 alkyl and both ends thereof are connected to [A + (R 1 )(R 2 )(R 3 )], p=2, c and d are integers, c+d=2, and X − and Y − comprise CH 3 SO 3 − , I − , CF 3 COO − , SCN − , BF 4 − , CF 3 SO 3 − , PF 6 − , FeCl 4 − , wherein R 4 is —CH 2 COOH or —(CH 2 ) 4 —NH 2 , R 5 and R 6 are H or CH 3 , R 7 is —CH(CH 3 ) 2 , —(CH 2 ) 2 —CH(CH 3 ) 2 , —CH(CH 3 )—CH 2 —CH 3 or —CH 2 —C 6 H 5 , and R 8 is CH 3 or H, wherein the group X − is the same as the group Y − in the first ionic compound, the group X − is the same as the group Y − in the second ionic compound, and the group X − in the first ionic compound is different from the group X − in the second ionic compound, and the group X − differs from the group Y − in the third ionic compound, the group X − in the third ionic compound is the same as the group X − in the first ionic compound or the group X − in the second ionic compound, and the group Y − in the third ionic compound is the same as the group Y − in the first ionic compound or the group Y − in the second ionic compound. 2. The ionic composition for forward osmosis as claimed in claim 1 , wherein the first ionic compound and the second ionic compound comprise 3. The ionic composition for forward osmosis as claimed in claim 1 , wherein the third ionic compound comprises 4. The ionic composition for forward osmosis as claimed in claim 1 , further comprising a fourth ionic compound which is represented by formula (II): [A + (R 1 )(R 2 )(R 3 )(R 4 )] n (X − ) a (II), wherein R 1 , R 2 , R 3 and R 4 independently comprise straight or branched C1-12 alkyl, A comprises phosphorus or nitrogen, n=1, a=1, and X − comprises CH 3 SO 3 − , I − , CF 3 COO − , SCN − , BF 4 − , CF 3 SO 3 − , PF 6 − , FeCl 4 − , wherein R 4 is —CH 2 COOH or —(CH 2 ) 4 —NH 2 , R 5 and R 6 are H or CH 3 , R 7 is —CH(CH 3 ) 2 , —(CH 2 ) 2 —CH(CH 3 ) 2 , —CH(CH 3 )—CH 2 —CH 3 or —CH 2 —C 6 H 5 , and R 8 is CH 3 or H. 5. The ionic composition for forward osmosis as claimed in claim 4 , wherein the fourth ionic compound comprises 6. The ionic composition for forward osmosis as claimed in claim 1 , further comprising a fifth ionic compound which is represented by formula (III): wherein R 1 , R 2 , R 3 , R 4 and R 5 independently comprise straight or branched C1-12 alkyl, X − and Y − independently comprise organic or inorganic anions, e and f are zero or an integer and e+f=1. 7. The ionic composition for forward osmosis as claimed in claim 6 , wherein, in formula (III), X − and Y − comprise CH 3 SO 3 − , I − , CF 3 COO − , SCN − , BF 4 − , CF 3 SO 3 − , PF 6 − , FeCl 4 − , wherein R 4 is —CH 2 COOH or —(CH 2 ) 4 —NH 2 , R 5 and R 6 are H or CH 3 , R 7 is —CH(CH 3 ) 2 , —(CH 2 ) 2 —CH(CH 3 ) 2 , —CH(CH 3 )—CH 2 —CH 3 or —CH 2 —C 6 H 5 , and R 8 is CH 3 or H. 8. The ionic composition for forward osmosis as claimed in claim 1 , wherein the extracted material has a phase-transition temperature which is in a range from 20° C. to 50° C. 9. A forward-osmosis water desalination system, comprising: a feeding unit comprising a feeding end and a draw-solution end separated from the feeding end by a semi-permeable membrane, wherein the feeding end comprises raw water, and the draw-solution end comprises the extracted material as claimed in claim 1 ; a phase-separation unit connected to the feeding unit, the phase-separation unit comprising an aqueous layer and an ionic liquid layer, wherein the extracted material has a concentration in the ionic liquid layer which is greater than that in the aqueous layer; and a recovery unit connected to the phase-separation unit and filtering the aqueous layer to recover pure water. 10. The forward-osmosis water desalination system as claimed in claim 9 , wherein the concentration of the extracted material is less than 10% in the aqueous layer in the phase-separation unit. 11. The forward-osmosis water desalination system as claimed in claim 9 , wherein the concentration of the extracted material is in a range from 10% to 70% in the ionic liquid layer in the phase-separation unit. 12. The forward-osmosis water desalination system as claimed in claim 9 , wherein the phase-separation unit has an operating temperature which is in a range from 20° C. to 50° C. 13. The forward-osmosis water desalination system as claimed in claim 9 , wherein the recovery unit further comprises a thin film to filter the aqueous layer introduced from the phase-separation unit. 14. A method for preparing an extracted material, comprising: providing a first ionic compound and a second ionic compound, wherein the first ionic compound and the second ionic compound are represented by formula (I): {K[A + (R 1 )(R 2 )(R 3 )] p }(X − ) c (Y − ) d (I), wherein R 1 , R 2 and R 3 independently comprise straight or branched C1-12 alkyl, A comprises phosphorus or nitrogen, K comprises C1-15 alkyl and both ends thereof are connected to [A + (R 1 )(R 2 )(R 3 )], p=2, c and d are integers, c+d=2, and X − and Y − comprise CH 3 SO 3 − , I − , CF 3 COO − , SCN − , BF 4 − , CF 3 SO 3 − , PF 6 − , FeCl 4 − , wherein R 4 is —CH 2 COOH or —(CH 2 ) 4 —NH 2 , R 5 and R 6 are H or CH 3 , R 7 is —CH(CH 3 ) 2 , —(CH 2 ) 2 —CH(CH 3 ) 2 , —CH(CH 3 )—CH 2 —CH 3 or —CH 2 —C 6 H 5 , and R 8 is CH 3 or H, wherein the group X − is the same as the group Y − in the first ionic compound, the group X − is the same as the group Y − in the second ionic compound, and the group X − in the first ionic compound is different from the group X − in the second ionic compound; and blending the first ionic compound and the second ionic compound to prepare an extraction material, wherein the first ionic compound and the second ionic compound have a molar ratio which is in a range from 0.05:0.95 to 0.95:0.05. 15. The method for preparing an extracted material as claimed in claim 14 , wherein the molar ratio of the first ionic compound to the second ionic compound is in a range from 0.15:0.85 to 0.85:0.15. 16. The method for preparing an extracted material as claimed in claim 14 , further comprising blending a fourth ionic compound which is represented by formula (II
comprising multiple forward osmosis steps · CPC title
Osmotic agents; Draw solutions · CPC title
by forward osmosis · CPC title
Reverse-osmosis · CPC title
Seawater, e.g. for desalination · CPC title
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