Advancements in osmotically driven membrane systems including multi-stage purification
An example water purification system for purifying high concentration feed solutions includes a high rejection forward osmosis module, one or more low rejection modules, and a high rejection reverse osmosis module. The low rejection modules may have different rejection levels. The system may be pressurized by one or more pumps. One or more of the low rejection modules may include one or more nanofiltration (NF) membranes. The draw solution may comprise a monovalent salt, a multivalent salt, or a combination of both.
1. An apparatus, comprising:
a forward osmosis module configured to receive a feed stream and a high concentration draw stream, wherein the forward osmosis module is further configured to produce a first stream comprising water from the feed stream and the high concentration draw stream via forward osmosis;
a pump configured to pressurize the first stream;
a low rejection membrane module configured to receive the pressurized first stream and to produce the high concentration draw stream and a low concentration stream via reverse osmosis, the low rejection membrane module having a low rejection membrane with a salt rejection rate of less than 90% at a first hydrostatic pressure; and
a reverse osmosis module configured to receive at least a portion of the low concentration stream and to produce a product stream and a reverse osmosis reject stream, wherein the reverse osmosis module has a reverse osmosis membrane with a higher salt rejection than the low rejection membrane module at the first hydrostatic pressure;
wherein the reverse osmosis reject stream is fluidly coupled to the high concentration draw stream prior to the forward osmosis module.
2. The apparatus of claim 1 , further comprising a second pump configured to pressurize the low concentration stream provided to the reverse osmosis module.
3. The apparatus of claim 1 , wherein the first stream is pressurized to less than 3000 psi.
4. The apparatus of claim 1 , further comprising an energy recovery device configured to reduce the pressure of the high concentration draw stream produced by the low rejection membrane module.
5. The apparatus of claim 1 , further comprising a feed pump configured to provide the feed stream to the forward osmosis module.
6. The apparatus of claim 1 , wherein the reverse osmosis reject stream is combined with the pressurized first stream provided to the low rejection membrane module prior to the low rejection membrane module.
7. The apparatus of claim 1 , wherein the low rejection membrane module has a salt rejection rate that is less than 80%.
8. The apparatus of claim 1 , wherein the low rejection membrane module comprises a membrane with a salt rejection rate that is less than 80%.
9. The apparatus of claim 1 , further comprising a dosing pump configured to provide a salt to the high concentration draw stream.
10. The apparatus of claim 9 , wherein the salt comprises a multivalent salt.
11. The apparatus of claim 9 , wherein the salt comprises a monovalent salt.
12. The apparatus of claim 1 , wherein the low concentration stream is provided to an additional low rejection membrane module configured to produce a dilute stream and a rejection stream, wherein the additional low rejection membrane module is disposed between the low rejection membrane module and the reverse osmosis module, and wherein the reverse osmosis module is configured to receive the dilute stream containing a portion of the low concentration stream.
13. The apparatus of claim 12 , wherein the reverse osmosis reject stream is combined with the pressurized first stream provided to the low rejection membrane module.
14. The apparatus of claim 12 , wherein the reverse osmosis reject stream is combined with the low concentration stream provided to the additional low rejection module.
15. The apparatus of claim 12 , further comprising a third pump configured to pressurize the dilute stream provided to the reverse osmosis module.
16. The apparatus of claim 1 , wherein the low rejection membrane module is configured to be operated at the first hydrostatic pressure and the reverse osmosis membrane module is configured to be operated at the first hydrostatic pressure.