Methods and apparatus for the analysis of fatty acids
US-2015331001-A1 · Nov 19, 2015 · US
US10159913B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10159913-B2 |
| Application number | US-201615333876-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 25, 2016 |
| Priority date | Oct 26, 2015 |
| Publication date | Dec 25, 2018 |
| Grant date | Dec 25, 2018 |
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Methods, systems and apparatus are provided for degassing a supersaturated solution. An example degasser is described having a continuous body of gas-permeable tubing to remove an amount of a gas from the supersaturated solution below the gas's saturation point in the supersaturated solution. The degasser can be connected to at least one of a fraction collector or a detector. The example degasser is sized and/or positioned to cause a change in pressure (ΔP) across the degasser to drive removal of a dissolved gas from a supersaturated solution passing through the degasser. As a result of the reduction of gas, efficiencies in system flow and fraction collection are achieved.
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What is claimed: 1. A degasser for removing gas from a supersaturated solution, comprising: (i) a continuous body of gas-permeable tubing having an interior portion and an exterior portion and an inlet and an outlet for conducting the supersaturated solution through the continuous body of gas-permeable tubing; and (ii) a fraction collector in direct fluid communication with the outlet of the continuous body of gas-permeable tubing, wherein the degasser removes a portion of the gas below the saturation point of the gas in the supersaturated solution. 2. The degasser of claim 1 , wherein a partial pressure of a component of the supersaturated solution decreases between the inlet and the outlet of the continuous body of gas-permeable tubing. 3. The degasser of claim 1 , wherein the continuous body of gas-permeable tubing is comprised of a polymeric material. 4. The degasser of claim 3 , wherein the continuous body of gas-permeable tubing is formed from a material which expands upon intake of the supersaturated solution. 5. The degasser of claim 1 , wherein a change in pressure occurs between the interior portion and exterior portion of the continuous body of gas-permeable tubing. 6. The degasser of claim 1 , wherein the gas-permeable tubing is entangled. 7. The degasser of claim 1 , further comprising a vacuum source connected to the continuous body of gas-permeable tubing. 8. A method of degassing a solution within a system, the method comprising: (i) flowing a solution through a degasser, the degasser comprising a continuous body of tubing, having an interior portion and an exterior portion, comprised of a gas permeable material, the degasser having an inlet and an outlet; (ii) applying a change in pressure across at least a portion of the degasser to reduce a partial pressure of a component in the solution; and (iii) conducting the solution from the outlet of the degasser directly to an inlet of a fraction collector. 9. The method of claim 8 , wherein the partial pressure of a component in the solution will be below the supersaturation point of the solution at operative temperature and pressure conditions at or about an inlet of a detector or inlet of the fraction collector. 10. The method of claim 8 , wherein a detector or the fraction collector are at ambient pressure and temperature. 11. The method of claim 8 , wherein a change in pressure occurs between the outlet of the degasser and an inlet of a detector or the inlet of the fraction collector. 12. The method of claim 11 , wherein the pressure decreases between the outlet of the degasser and an inlet of a detector or the inlet of the fraction collector. 13. The method of claim 8 , wherein a change in temperature occurs between the outlet of the degasser and an inlet of a detector or the inlet of the fraction collector. 14. The method of claim 13 , wherein the temperature increases between the outlet of the degasser and an inlet of the of a detector or the inlet of the fraction collector. 15. A method of degassing a supersaturated solution within a mixed fluid system, comprising: (i) providing a gas-liquid separator fluidly connected to a degasser, the degasser comprising a continuous body of tubing, having an interior portion and an exterior portion, comprised of a gas permeable material, the degasser having an inlet connected to the gas-liquid separator and an outlet; (ii) separating at least a portion of the supersaturated solution into a gas and a first liquid eluent within the gas-liquid separator; (iii) introducing the first liquid eluent from the gas-liquid separator into the inlet of the degasser; (iv) applying a differential pressure gradient across the degasser; (v) separating an additional portion of the gas from the first liquid eluent, resulting in a second liquid eluent; and (vi) conducting the second liquid eluent from an outlet of the degasser directly to an inlet of a fraction collector. 16. The method of claim 15 , wherein the second liquid eluent comprises a greater liquid to gas ratio by weight than the first liquid eluent. 17. The degasser of claim 1 wherein the continuous body has a residence time (g) adapted to remove the portion of the gas below the saturation point of the gas in the supersaturated solution. 18. The method of claim 8 , wherein the solution introduced to the degasser is a supersaturated solution.
by filtration · CPC title
using supercritical fluid as mobile phase or eluent · CPC title
Preparation of the fraction to be distributed · CPC title
using permeable separator tubes · CPC title
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