Whitewater recovery processes, and associated systems and components, are generally described. Certain embodiments relate to whitewater recovery processes in which ion exchange is used to remove dissolved ions from the whitewater, which can reduce the degree to which chemical additives are used in t
Whitewater recovery processes, and associated systems and components, are generally described. Certain embodiments relate to whitewater recovery processes in which ion exchange is used to remove dissolved ions from the whitewater, which can reduce the degree to which chemical additives are used in the process. In certain embodiments, flocculation and/or filter components can be employed to aid in the removal of suspended solids from the whitewater.
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1. A method of treating whitewater, comprising: exposing a liquid input stream comprising whitewater or derived from whitewater and containing cations and suspended solids to a flocculent such that agglomerations of flocculent and suspended solids are formed;removing at least a portion of the agglom
1. A method of treating whitewater, comprising: exposing a liquid input stream comprising whitewater or derived from whitewater and containing cations and suspended solids to a flocculent such that agglomerations of flocculent and suspended solids are formed;removing at least a portion of the agglomerations from the liquid input stream to produce a supernatant stream containing a lower quantity of suspended solids than the liquid input stream;filtering the supernatant stream to produce a retentate stream and a filtrate stream containing a lower quantity of suspended solids than the retentate stream; andremoving at least a portion of the cations from the filtrate stream using an ion exchange medium. 2. The method of claim 1, comprising introducing gas into the liquid input stream. 3. The method of claim 2, wherein the gas is introduced into the liquid input within a dissolved gas flotation separation apparatus. 4. The method of claim 1, wherein the ion exchange medium comprises a weak acid cation resin. 5. The method of claim 1, wherein the ion exchange medium comprises a strong acid cation resin. 6. The method of claim 1, comprising reducing the total dissolved solids of the filtrate stream after exposure of the filtrate stream to the ion exchange medium. 7. The method of claim 6, wherein reducing the total dissolved solids of the filtrate stream comprises removing anions from the filtrate stream. 8. The method of claim 1, comprising exposing the filtrate stream to ultraviolet electromagnetic radiation. 9. The method of claim 1, wherein removing at least a portion of the cations from the filtrate stream using an ion exchange medium is performed at a pH of between about 5.5 and about 8.5. 10. The method of claim 1, wherein the suspended solids comprise colloidal solids and/or organic solids. 11. The method of claim 1, wherein the liquid input stream comprises calcium carbonate. 12. The method of claim 11, comprising adjusting or maintaining the pH of the filtrate stream at or below about 7.5 such that at least a portion of the calcium carbonate is dissolved within the filtrate stream prior to removing at least a portion of the cations from the filtrate stream using the ion exchange medium. 13. A method of treating whitewater, comprising: flowing a liquid input stream comprising whitewater or derived from whitewater and containing cations through an ion exchange vessel containing an ion exchange medium; andremoving at least a portion of the cations from the liquid input stream using the ion exchange medium to produce an ion exchanged effluent stream. 14. The method of claim 13, wherein the cations comprise multivalent cations. 15. The method of claim 14, wherein the multivalent cations comprise Mg2+, Ca2+, Sr2+, Ba2+, Fe2+, Mn2+, and/or A13+. 16. The method of claim 13, wherein the amount of cations within the ion exchanged effluent stream is at least about 70% lower than the amount of cations within the liquid input stream. 17. The method of claim 13, wherein the ion exchange medium comprises a weak acid cation resin. 18. The method of claim 13, wherein removing at least a portion of the cations from the liquid stream using the ion exchange medium is performed at a pH of between about 5.5 and about 8.5. 19. The method of claim 13, wherein the liquid input stream comprises calcium carbonate. 20. The method of claim 19, comprising adjusting or maintaining the pH of the liquid input stream at or below about 7.5 such that at least a portion of the calcium carbonate is dissolved within the liquid input stream during and/or prior to being flowed through the ion exchange vessel. 21. The method of claim 20, wherein adjusting or maintaining the pH of the liquid input stream comprises allowing the liquid input stream to contact the ion exchange medium, and allowing the operating pH of the ion exchange medium to reduce the pH of the liquid input stream. 22. A method of treating whitewater, comprising: exposing a liquid input stream comprising whitewater or derived from whitewater and containing cations and suspended solids to a flocculent and a magnetically responsive material such that agglomerations of flocculent, magnetically responsive material, and suspended solids are formed;removing at least a portion of the agglomerations from the liquid input stream using a magnet to produce a supernatant stream containing less suspended solids than the liquid input stream; andremoving at least a portion of the cations from the supernatant stream using an ion exchange medium.
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