System and method for recovering nutrients from a high nitrogenous liquid waste
US-2024083791-A1 · Mar 14, 2024 · US
US10501344B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10501344-B2 |
| Application number | US-201916372683-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 2, 2019 |
| Priority date | Apr 23, 2014 |
| Publication date | Dec 10, 2019 |
| Grant date | Dec 10, 2019 |
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A method reuses produced water resulting from a fossil fuel extraction operation. The method includes providing the produced water as an input to an electrodialysis system. The method also includes running the electrodialysis system to produce a diluate and a concentrate. The diluate is contaminated so as to have a conductivity of no less than 0.1 Siemens/meter. The method also includes reformulating the diluate to produce fossil fuel extraction fluid. The method also includes using the produced fossil fuel extraction fluid in the fossil fuel extraction operation. An electrodialysis system includes first and second stacks. The electrodialysis system also includes first and second voltage sources, coupled to the first and second stacks, so as to apply a first voltage to the first stack lower by at least about 10% than a second voltage to the second stack.
Opening claim text (preview).
What is claimed is: 1. An electrodialysis system comprising: a first stack and a second stack, each stack having at least one pair of electrodes, between which is disposed at least one cell pair having an anion exchange membrane and a cation exchange membrane; each of the first and second stacks having a diluate input, a diluate output and a concentrate output, wherein the diluate output of the first stack is fluidly coupled to the diluate input of the second stack; and first and second voltage sources coupled to the at least one pair of electrodes of the first and second stacks, respectively, so as to apply a first voltage of less than about 0.2V per cell pair to the first stack and a second voltage to the second stack, wherein the first voltage is lower than the second voltage, by at least about 10%. 2. An electrodialysis system of claim 1 , wherein the first stack has a first electrical resistance and the second stack has a second electrical resistance, and a ratio of the first voltage to the second voltage is approximately equal to a square root of a ratio of the first electrical resistance to the second electrical resistance. 3. An electrodialysis system of claim 1 , wherein the first voltage is lower than the second voltage by at least about 20%. 4. An electrodialysis system of claim 1 , wherein the first voltage is lower than the second voltage by at least about 50%. 5. An electrodialysis system of claim 1 , wherein the first voltage is about 0.15 V per cell pair. 6. An electrodialysis system of claim 1 , wherein the first voltage is about 0.10 V per cell pair.
Voltage · CPC title
Viscosity · CPC title
Multistage treatment of water, waste water or sewage · CPC title
Current · CPC title
electrodialysis · CPC title
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