Method and apparatus for purifying aqueous streams contaminated with organic materials

• US 4,000,065 A
• Filed: 11/18/1974
• Issued: 12/28/1976
• Est. Priority Date: 11/18/1974
• Status: Expired due to Term

• Current Assignee: BASF Corporation (BASF SE)
• Original Assignee: BASF Wyandotte Corporation
• Inventors: Louvar, Joseph F., Herring, William M., Ladha, Kamal K.
• Primary Examiner(s): Spear, Jr., Frank A.
• Application Number:
  US05/524,806
• Time in Patent Office: 771 Days
• Field of Search: 210/22, 210/23, 210/321, 210/500 M
• US Class Current: 210/652
• CPC Class Codes: B01D 61/025 Reverse osmosis; Hyperfiltration
• CPC Class Codes: B01D 61/145 Ultrafiltration
• CPC Class Codes: B01D 61/58 Multistep processes
• CPC Class Codes: C02F 1/441 by reverse osmosis
• CPC Class Codes: C02F 1/444 by ultrafiltration or microfiltration

Abstract

Aqueous streams contaminated with minor amounts of organic materials are separated into an aqueous fraction which is concentrated with respect to the organic contaminants and a water fraction relatively free of the organic contaminants by a method which includes a unique combination of reverse osmosis (RO) and ultrafiltration (UF). The organic contaminants include substances having molecular weights of less than 10,000 which are soluble in the aqueous stream initially but have limited solubility ranges and are precipitated therefrom upon concentration. The contaminated aqueous stream is circulated from the high pressure compartment of a RO unit to the high pressure compartment of an UF unit, then to the low pressure compartment of the UF unit, and then back to the high pressure compartment of the RO unit. The contaminants are concentrated in the high pressure compartment of the RO unit, and a portion thereof is precipitated or otherwise rendered amenable to removal along with the UF concentrate upon passing the RO concentrate from the high pressure compartment of the RO unit to the high pressure compartment of the UF unit. Soluble organic contaminants remaining in the aqueous stream are removed in the UF permeate and are recycled back to the high pressure compartment of the RO unit for further concentration and precipitation, followed by recycling to the high pressure compartment of the UF unit for removal.

Claims

1. Apparatus for separating an aqueous medium contaminated with minor amounts of organic materials into an aqueous fraction relatively concentrated with respect to the organic contaminants and a water fraction relatively free of organic contaminants comprising

a reverse osmosis unit including a high pressure compartment and a low pressure compartment separated by a reverse osmosis membrane,

an ultrafiltration unit including a high pressure compartment and a low pressure compartment separated by an ultrafiltration membrane,

the high pressure compartment of the reverse osmosis unit being adapted to operate at a substantially higher pressure than the high pressure compartment of the ultrafiltration unit,

first conduit means including fluid pressure reducing means for withdrawing a concentrate fraction under a relatively high pressure from the high pressure compartment of the reverse osmosis unit and introducing it into the high pressure compartment of the ultrafiltration unit under a relatively low pressure,

second conduit means including fluid pressure increasing means for withdrawing a permeate fraction from the low pressure compartment of the ultrafiltration unit under a relatively low pressure and introducing it into the high pressure compartment of the reverse osmosis unit under a relatively high pressure,

the said high pressure compartment of the reverse osmosis unit, the said first conduit means, the said high pressure compartment of the ultrafiltration unit, the said low pressure compartment of the ultrafiltration unit, and the said second conduit means comprising a circuit for substantially continuously recirculating liquid and at least a portion of the contaminated aqueous medium being recirculated therein,

a source of aqueous medium contaminated with minor amounts of organic contaminants to be separated into an aqueous fraction which is relatively concentrated with respect to the organic contaminants and a water fraction which is relatively free of the organic contaminants, the said aqueous medium including organic contaminants having molecular weights of less than 10,000 which are soluble therein initially but have a limited solubility range and are precipitated therefrom upon concentration of the contaminated aqueous medium in the high pressure compartment of the reverse osmosis unit,

means including third conduit means for withdrawing contaminated aqueous medium from the said source and introducing it at a substantial rate of flow into the said circuit for recirculating liquid,

the high pressure compartment of the reverse osmosis unit being adapted to operate at a pressure in excess of the osmotic pressure of the aqueous medium and at a sufficiently elevated pressure to produce a permeate fraction which passes through the reverse osmosis membrane into the said low pressure compartment and a concentrate fraction in the said high pressure compartment which contains the said organic contaminants in sufficiently high concentration to cause precipitation of at least a portion of the organic contaminants therefrom,

the high pressure compartment of the ultrafiltration unit being adapted to operate at a pressure less than 200 pounds per square inch and at a sufficiently elevated pressure to produce a permeate fraction which passes through the ultrafiltration membrane into the said low pressure compartment

means including fourth conduit means for withdrawing a permeate fraction which is relatively free of organic contaminants from the low pressure compartment of the reverse osmosis unit, and

means including fifth conduit means for withdrawing a concentrate fraction which is relatively concentrated with respect to the organic contaminants from the high pressure compartment of the ultrafiltration unit.

2. The apparatus of claim 1 wherein the said fluid pressure reducing means includes a pressure reducing valve effective to reduce the pressure on the reverse osmosis concentrate fraction from substantially the relatively high operating presssure of the high pressure compartment of the reverse osmosis unit to approximately the relatively low operating pressure of the high pressure compartment of the ultrafiltration unit.

3. The apparatus of claim 1 wherein the said fluid pressure increasing means includes a pump effective to increase the pressure on the ultrafiltration unit permeate fraction from substantially the relatively low operating pressure of the low pressure compartment of the ultrafiltration unit to approximately the relatively high operating pressure of the high pressure compartment of the reverse osmosis unit.

4. The apparatus of claim 1 wherein the said fifth conduit means includes a pressure regulating means whereby the pressure of the withdrawn concentrate fraction may be reduced without adversely affecting the operating pressure within the high pressure compartment of the ultrafiltration unit.

5. The apparatus of claim 1 wherein the said fluid pressure reducing means includes a pressure reducing valve effective to reduce the pressure on the reverse osmosis concentrate fraction from substantially the relatively high operating pressure of the high pressure compartment of the reverse osmosis unit to approximately the relatively low operating pressure of the high pressure compartment of the ultrafiltration unit, the said fluid pressure increasing means includes a pump effective to increase the pressure on the ultrafiltration unit permeate fraction from substantially the relatively low operating pressure of the low pressure compartment of the ultrafiltration unit to approximately the relatively high operating pressure of the high pressure compartment of the reverse osmosis unit, and the said fifth conduit means includes a presssure regulating means whereby the pressure of the withdrawn concentrate fraction may be reduced without adversely affecting the operating pressure within the high pressure compartment of the ultrafiltration unit.

6. The apparatus of claim 1 wherein the said third conduit means includes means for introducing the contaminated aqueous medium withdrawn from the said source into the circuit for recirculating liquid at a point whereby it is passed through the reverse osmosis unit prior to passing through the ultrafiltration unit.

7. The apparatus of claim 6 wherein the said fluid pressure reducing means includes a pressure reducing valve effective to reduce the pressure on the reverse osmosis concentrate fraction from substantially the relatively high operating pressure of the high pressure compartment of the reverse osmosis unit to approximately the relatively low operating pressure of the high pressure compartment of the ultrafiltration unit, the said fluid pressure increasing means includes a pump effective to increase the pressure on the ultrafiltration unit permeate fraction from substantially the relatively low operating pressure of the low pressure compartment of the ultrafiltration unit to approximately the relatively high operating pressure of the high pressure compartment of the reverse osmosis unit, and the said fifth conduit means includes a pressure regulating means whereby the pressure of the withdrawn concentrate fraction may be reduced without adversely affecting the operating pressure within the high pressure compartment of the ultrafiltration unit.

8. The apparatus of claim 1 wherein the said third conduit means includes means for introducing the contaminated aqueous medium withdrawn from the said source into the circuit for recirculating liquid at a point whereby it is passed through the ultrafiltration unit prior to passing through the reverse osmosis unit.

9. The apparatus of claim 8 wherein the said fluid pressure reducing means includes a pressure reducing valve effective to reduce the pressure on the reverse osmosis concentrate fraction from substantially the relatively high operating pressure of the high pressure compartment of the reverse osmosis unit to approximately the relatively low operating pressure of the high pressure compartment of the ultrafiltration unit, the said fluid pressure increasing means includes a pump effective to increase the pressure on the ultrafiltration unit permeate fraction from substantially the relatively low operating pressure of the low pressure compartment of the ultrafiltration unit to approximately the relatively high operating pressure of the high pressure compartment of the reverse osmosis unit, and the said fifth conduit means includes a pressure regulating means whereby the pressure of the withdrawn concentrate fraction may be reduced without adversely affecting the operating pressure within the high pressure compartment of the ultrafiltration unit.

10. The apparatus of claim 8 wherein a second ultrafiltration unit is provided including a high pressure compartment and a low pressure compartment separated by an ultrafiltration membrane, the concentrate fraction withdrawn via the said fifth conduit means is introduced into the high pressure compartment of the second ultrafiltration unit, means including sixth conduit means is provided for withdrawing a permeate fraction from the low pressure compartment of the second ultrafiltration unit and introducing it into the said third conduit means, and means including seventh conduit means is provided for withdrawing a concentrate fraction which is relatively concentrated with respect to the organic contaminants from the high pressure compartment of the second ultrafiltration unit.

11. The apparatus of claim 10 wherein the said fluid pressure reducing means includes a pressure reducing valve effective to reduce the pressure on the reverse osmosis concentrate fraction from substantially the relatively high operating pressure of the high pressure compartment of the reverse osmosis unit to approximately the relatively low operating pressure of the high pressure compartment of the ultrafiltration unit, the said fluid pressure increasing means includes a pump effective to increase the pressure on the ultrafiltration unit permeate fraction from substantially the relatively low operating pressure of the low pressure compartment of the ultrafiltration unit to approximately the relatively high operating pressure of the high pressure compartment of the reverse osmosis unit, and the said fifth and seventh conduit means include a pressure regulating means whereby the pressure of the withdrawn concentrate fraction may be reduced without adversely affecting the operating pressure within the high pressure compartments of the ultrafiltration units.

12. The apparatus of claim 1 where the said source of aqueous medium contains at least one hydroxyl terminated polyether polyol as an organic contaminant and at least a portion thereof is initially soluble in the aqueous medium.

13. The apparatus of claim 12 wherein the said source of aqueous medium contains about 100-10,000 parts per million of the hydroxyl terminated polyether polyol and about 1-100 parts per million of water soluble inorganic contaminants.

14. The apparatus of claim 12 wherein the said hydroxyl terminated polyether polyol has a molecular weight of about 300-7000 and is the condensation product of monomeric material selected from the group consisting of ethylene oxide, propylene oxide, butylene oxide and admixtures thereof with at least one compound condensable therewith containing active hydrogen.

15. The apparatus of claim 12 wherein means is provided for heating aqueous medium contaminated with the said hydroxyl terminated polyether polyol at a temperature which is sufficiently high to promote the precipitation thereof from the reverse osmosis concentrate.

16. The apparatus of claim 15 wherein the said heating means is adapted to heat the contaminated aqueous medium at a temperature of about 40°

-100°

C.

17. The apparatus of claim 16 wherein the said source of contaminated aqueous medium contains about 100-10,000 parts per million of the hydroxyl terminated polyether polyol as an organic contaminant and about 1-100 parts per million of water soluble inorganic contaminants, and the hydroxyl terminated polyether polyol has a molecular weight of about 400-4000 and is the condensation product of monomeric material selected from the group consisting of ethylene oxide, propylene oxide, butylene oxide and admixtures thereof with at least one compound condensable therewith containing active hydrogen.

18. A method of separating an aqueous medium contaminated with minor amounts of organic materials into an aqueous fraction relatively concentrated with respect to the organic contaminants and a water fraction relatively free of organic contaminants comprising

introducing aqueous medium contaminated with organic materials into a reverse osmosis unit including a first high pressure compartment and a first low pressure compartment separated by a reverse osmosis membrane,

the contaminated aqueous medium containing soluble organic contaminants and being introduced into the said first high pressure compartment and maintained therein under a pressure in excess of the osmotic pressure of the contaminated aqueous medium and under a sufficiently elevated pressure whereby reverse osmosis permeate is produced which passes through the reverse osmosis membrane into the said first low pressure compartment and reverse osmosis concentrate is produced which is retained in the said first high pressure compartment by the reverse osmosis membrane,

the reverse osmosis permeate being a water fraction which is relatively free of the organic contaminants and the reverse osmosis concentrate being an aqueous fraction which is sufficiently concentrated with respect to the organic contaminants to cause precipitation of at least a portion of the initially soluble organic contaminants therefrom,

withdrawing the reverse osmosis permeate from the said first low pressure compartment,

withdrawing the reverse osmosis concentrate from the said first high pressure compartment,

introducing the reverse osmosis concentrate into an ultrafiltration unit including a second high pressure compartment and a second low pressure compartment separated by an ultrafiltration membrane,

the reverse osmosis concentrate containing precipitated organic contaminants which are retained by the reverse osmosis membrane and being introduced into the said second high pressure compartment and maintained under a pressure which is substantially lower than the pressure existing in the said first high pressure compartment, the said pressure being less than 200 pounds per square inch but sufficiently elevated whereby ultrafiltration permeate is produced which passes through the ultrafilitration membrane into the said second low pressure compartment and ultrafiltration concentrate is produced which is retained in the said second high pressure compartment by the ultrafiltration membrane,

the ultrafiltration permeate being an aqueous medium contaminated with soluble organic materials which are not retained by the ultrafiltration membrane and the ultrafiltration concentrate being an aqueous fraction relatively concentrated with respect to the organic contaminants,

withdrawing the ultrafiltration concentrate from the said second high pressure compartment,

withdrawing ultrafiltration permeate from the said second low pressure compartment,

introducing the withdrawn ultrafiltration permeate into the said first high pressure compartment and producing therefrom reverse osmosis concentrate containing precipitated organic contaminants which are retained by the ultrafiltration membrane and additional reverse osmosis permeate,

at least a portion of the contaminated aqueous medium being substantially continuously recirculated in a circuit for recirculating liquid which includes the high pressure conpartment of the reverse osmosis unit, the high pressure compartment of the ultrafiltration unit and the low pressure compartment of the ultrafiltration unit, and

introducing into the said circuit for circulating liquid fresh contaminated aqueous medium to be separated into an aqueous fraction relatively concentrated with respect to the organic contaminants and a water fraction relatively free of the organic contaminants,

the said fresh contaminated aqueous medium being introduced at a substantial rate of flow and including at least one contaminating organic material having a molecular weight of less than 10,000 which is soluble therein initially but has a solubility range such that at least a portion thereof is precipitated from the reverse osmosis concentrate whereby the said precipitated contaminating organic material is retained by the ultrafiltration membrane in the said second high pressure compartment and is withdrawn in the ultrafiltration concentrate.

19. The method of claim 18 wherein the organic contaminants comprise organic compounds having molecular weights of about 300-7,000

20. The method of claim 18 wherein the organic contaminants comprise at least one polyol.

21. The method of claim 20 wherein the polyol has a molecular weight of about 300-7,000.

22. The method of claim 20 wherein at least a portion of the polyol is initially soluble in the aqueous medium, and the aqueous medium is heated to an elevated temperature which is sufficiently high to promote the precipitation of the initially soluble polyol from the reverse osmosis concentrate.

23. The method of claim 22 wherein the polyol has a molecular weight of about 400-4,000.

24. The method of claim 18 wherein the said fresh contaminated aqueous medium is introduced into the said circuit for recirculating liquid at a point whereby it is passed through the reverse osmosis unit prior to passing through the ultrafiltration unit.

25. The method of claim 24 wherein the organic contaminants comprise organic compounds having molecular weights of about 300-7,000.

26. The method of claim 24 wherein the organic contaminants comprise at least one polyol.

27. The method of claim 26 wherein the polyol has a molecular weight of about 300-7,000.

28. The method of claim 26 wherein at least a portion of the polyol is initially soluble in the aqueous medium, and the aqueous medium is heated to an elevated temperature which is sufficiently high to promote the precipitation of the initially soluble polyol from the reverse osmosis concentrate.

29. The method of claim 28 wherein the polyol has a molecular weight of about 400-4,000.

30. The method of claim 18 wherein the said fresh contaminated aqueous medium is introduced into the said circuit for recirculating liquid at a point whereby it is passed through the ultrafiltration unit prior to passing through the reverse osmosis unit.

31. The method of claim 30 wherein the organic contaminants comprise organic compounds having molecular weights of about 300-7,000.

32. The method of claim 30 wherein the organic contaminants comprise at least one polyol.

33. The method of claim 32 wherein the polyol has a molecular weight of about 300-7,000.

34. The method of claim 32 wherein at least a portion of the polyol is initially soluble in the aqueous medium, and the aqueous medium is heated to an elevated temperature which is sufficiently high to promote the precipitation of the initially soluble polyol from the reverse osmosis concentrate.

35. The method of claim 34 wherein the polyol has a molecular weight of about 400-4,000.

36. The method of claim 30 wherein the ultrafiltration concentrate withdrawn from the said second high pressure compartment is introduced into a second ultrafiltration unit including a third high pressure compartment and a third low pressure compartment separated by an ultrafiltration membrane.

the withdrawn ultrafiltration concentrate is introduced into the third high pressure compartment and maintained under a pressure which is sufficiently elevated whereby ultrafiltration permeate is produced and passes through the ultrafiltration membrane into the third low pressure compartment and ultrafiltration concentrate is produced which is retained by the ultrafiltration membrane in the said third high pressure compartment,

the ultrafiltration permeate in the third low pressure compartment contains soluble organic contaminants which are not retained by the ultrafiltration membrane and the ultrafiltration concentrate in the third high pressure compartment is an aqueous fraction relatively concentrated with respect to the organic contaminants,

the ultrafiltration concentrate is withdrawn from the third high pressure compartment, and

the ultrafiltration permeate is withdrawn from the third low pressure compartment and is introduced into the said circuit for recirculating liquid.

37. The method of claim 36 wherein the organic contaminants comprise organic compounds having molecular weights of about 300-7,000.

38. The method of claim 36 wherein the organic contaminants comprise at least one polyol.

39. The method of claim 38 wherein the polyol has a molecular weight of about 300-7,000.

40. The method of claim 38 wherein at least a portion of the polyol is initially soluble in the aqueous medium, and the aqueous medium is heated to an elevated temperature which is sufficiently high to promote the precipitation of the initially soluble polyol from the reverse osmosis concentrate.

41. The method of claim 40 wherein the polyol has a molecular weight of about 400-4,000.

42. The method of claim 18 wherein the said fresh contaminated aqueous medium contains at least one hydroxyl terminated polyether polyol as an organic contaminant and at least a portion thereof is initially soluble in the aqueous medium.

43. The method of claim 42 wherein the said fresh contaminated aqueous medium contains about 100-10,000 parts per million of the hydroxyl terminated polyether polyol and about 1-100 parts per million of water soluble inorganic contaminants.

44. The method of claim 42 wherein the said hydroxyl terminated polyether polyol has a molecular weight of about 300-7000 and is the condensation product of monomeric material selected from the group consisting of ethylene oxide, propylene oxide, butylene oxide and admixtures thereof with at least one compound condensable therewith containing active hydrogen.

45. The method of claim 42 wherein the said aqueous medium contaminated with the said hydroxyl terminated polyether polyol is heated at a temperature which is sufficiently high to promote the precipitation thereof from the reverse osmosis concentrate.

46. The method of claim 45 wherein the said contaminated aqueous medium is heated at a temperature of about 40°

-100°

C.

47. The method of claim 46 wherein the said fresh contaminated aqueous medium contains about 100-10,000 parts per million of the hydroxyl terminated polyether polyol as an organic contaminant and about 1-100 parts per million of water soluble inorganic contaminants, and the hydroxyl terminated polyether polyol has a molecular weight of about 400-4000 and is the condensation product of monomeric material selected from the group consisting of ethylene oxide, propylene oxide, butylene oxide and admixtures thereof with at least one compound condensable therewith containing active hydrogen.