Selective water temperature component for use with water treatment systems
US-9523514-B2 · Dec 20, 2016 · US
US9827602B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9827602-B2 |
| Application number | US-201514867604-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 28, 2015 |
| Priority date | Sep 28, 2015 |
| Publication date | Nov 28, 2017 |
| Grant date | Nov 28, 2017 |
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A method of thermally servicing a solvent-refining column comprises: running a closed-loop water-steam system past a top and bottom of a first column, the first column containing at least a solvent and impurities; boiling pressurized water in the closed-loop water-steam system to steam using first heat from the top of the first column; compressing the steam in the closed-loop water-steam system to a higher temperature; and providing second heat to the first column by condensing the steam at the bottom of the first column after compression.
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What is claimed is: 1. A system that thermally services a solvent-refining column, the system comprising: a column wherein impurities are removed from a solvent, the column having a top and a bottom; a first heat exchanger; a second heat exchanger; a compressor; an expansion valve; a closed-loop water-steam system having water-steam therein and connecting the first heat exchanger, the second heat exchanger, the compressor, and the expansion valve wherein: the compressor is arranged between the first heat exchanger and the second heat exchanger; the expansion value is arranged between the second heat exchanger and the first heat exchanger; the first heat exchanger transfers heat to the water-steam from the top of the column; the compressor increases a temperature of the water-steam received from the first heat exchanger; the second heat exchanger transfers heat from the water-steam to the bottom of the column; and the expansion valve reduces the temperature of the water-steam. 2. The system of claim 1 , further comprising another column including the solvent, the impurities and water wherein the water is separated from the solvent and the impurities and a third heat exchanger arranged between the compressor and the second heat exchanger, wherein the third heat exchanger transfers heat from the water-steam to the bottom of the another column. 3. The system of claim 1 , further comprising a first bypass in the closed-loop water-steam system for selectively bypassing, at least partially, the first heat exchanger. 4. The system of claim 1 , further comprising a heater positioned between the compressor and the second heat exchanger wherein the heater heats the water-steam. 5. The system of claim 1 , further comprising a second bypass in the closed-loop water-steam system wherein the second bypass selectively bypasses, at least partially, the second heat exchanger. 6. The system of claim 2 , further comprising a heater positioned between the compressor and the third heat exchanger wherein the heater heats the water-steam. 7. The system of claim 1 , wherein the impurities have a boiling point that is less than about 2% lower or higher than a boiling point of the solvent. 8. The system of claim 7 , wherein the solvent is n-methyl pyrrolidone and wherein the impurities are partial oxides of the n-methyl pyrrolidone. 9. The system of claim 2 , further comprising a third bypass in the closed-loop water-steam system wherein the third bypass selectively bypasses, at least partially, the third heat exchanger.
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