Ion chromatography system with eluent recycle
US-9322815-B2 · Apr 26, 2016 · US
US11285403B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11285403-B2 |
| Application number | US-201916426320-A |
| Country | US |
| Kind code | B2 |
| Filing date | May 30, 2019 |
| Priority date | May 31, 2018 |
| Publication date | Mar 29, 2022 |
| Grant date | Mar 29, 2022 |
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The disclosure relates to a recycling chromatography method that includes injecting a sample into a mobile phase flow stream of a chromatography system to create a combined flow stream. The sample includes an API and at least one impurity. The chromatography system includes a first column and a column in series, a first valve in fluid communication with the first and second chromatographic columns, a heater in communication with the first and second chromatographic columns, a fraction collector in fluid communication with the first and second chromatographic columns, and a second valve positioned before the fraction collector. The combined flow stream is recycled from the first chromatographic column to the second chromatographic column and vice versa by switching the first valve until a baseline resolution is achieved to separate the at least one impurity from the API. The at least one impurity is collected in the fraction collector.
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What is claimed is: 1. A recycling chromatography method comprising the steps of: (i) injecting a sample into a mobile phase flow stream of a chromatography system to create a combined flow stream, the sample comprising an active pharmaceutical ingredient and at least one impurity, wherein the selectivity factor of the active pharmaceutical ingredient and the at least one impurity is <1.2, and wherein the amount of the at least one impurity in the sample is less than 0.1% by weight, the chromatography system comprising: a first chromatographic column and a second chromatographic column positioned in series; a first valve in fluid communication with the first chromatographic column and the second chromatographic column; a heater in communication with the first chromatographic column and the second chromatographic column; a fraction collector in fluid communication with the first chromatographic column and the second chromatographic column; and a second valve positioned before the fraction collector; (ii) recycling the combined flow stream from the first chromatographic column to the second chromatographic column and from the second chromatographic column to the first chromatographic column by switching the first valve until a baseline resolution is achieved to separate the at least one impurity from the active pharmaceutical ingredient; and (iii) collecting the at least one impurity in the fraction collector; and (iv) repeating steps (i)-(iii) until at least about 1 mg of the at least one impurity is collected in the fraction collector. 2. The method of claim 1 , wherein the chromatography system is a liquid chromatography system, a gas chromatography system, a supercritical fluid chromatography system, or a capillary electrophoresis chromatography system. 3. The method of claim 2 , wherein the chromatography system is a semi-preparative chromatography system. 4. The method of claim 1 , wherein the chromatography system is a semi-preparative, high performance liquid chromatography system. 5. The method of claim 1 , wherein the first chromatographic column and the second chromatographic column are identical. 6. The method of claim 1 , wherein the first valve is a six-port or an eight-port valve. 7. The method of claim 1 , wherein the second valve is a four-port valve. 8. The method of claim 1 , wherein fraction collector collects about 1 mg of the at least one impurity at a purity level of at least 90%. 9. The method of claim 1 , further comprising determining the chemical structure of the at least one impurity. 10. The method of claim 9 , wherein the chemical structure of the at least one impurity is determined by nuclear magnetic resonance. 11. The method of claim 1 , further comprising pre-determining a number of valve switches to achieve the baseline resolution to separate the at least one impurity from the active pharmaceutical ingredient. 12. The method of claim 1 , wherein the heater maintains a column temperature between about 20° C. to about 100° C. 13. The method of claim 1 , wherein the combined flow stream has a flow rate between about 0.5 mL/min and about 2 mL/min and the first chromatographic column and the second chromatographic column each have an inner diameter of about 4.6 mm. 14. The method of claim 1 , wherein the combined flow stream has a flow rate between about 2 mL/min and about 10 mL/min and the first chromatographic column and the second chromatographic column each have an inner diameter of about 1 cm. 15. The method of claim 1 , wherein the chromatography system further comprises a detector positioned between the first chromatographic column and the second chromatographic column. 16. The method of claim 1 , wherein the chromatography system further comprises a detector positioned before the fraction collector. 17. The method of claim 1 , wherein the collected at least one impurity is about 90% pure. 18. The method of claim 1 , wherein the collected at least one impurity is about 95% pure. 19. The method of claim 1 , wherein the collected at least one impurity is about 99% pure.
Temperature conditioning · CPC title
placed in series · CPC title
using recycling of the fraction to be distributed · CPC title
Pressure or speed conditioning · CPC title
with serial coupling of separation columns · CPC title
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