Process for the preparation of perfluoroalkylcyano- or perfluoroalkylcyanofluoroborates
US-9175021-B2 · Nov 3, 2015 · US
US9556124B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9556124-B2 |
| Application number | US-201414471635-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 28, 2014 |
| Priority date | Oct 31, 2013 |
| Publication date | Jan 31, 2017 |
| Grant date | Jan 31, 2017 |
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Methods for removing 1,3,5-trimethylhexahydro-1,3,5-triazine and N-methylenemethanamine from a N-methylimidazole and methods for making oligonucleotides using N-methylimidazole are provided. In one embodiment, a method for removing 1,3,5-trimethylhexahydro-1,3,5-triazine and N-methylenemethanamine from a feedstock containing N-methylimidazole includes contacting the feedstock with small or medium pore molecular sieves. The small or medium pore molecular sieves adsorb 1,3,5-trimethylhexahydro-1,3,5-triazine and N-methylenemethanamine from the feedstock. The method further includes separating the small or medium pore molecular sieves from the feedstock.
Opening claim text (preview).
What is claimed is: 1. A method for removing 1,3,5-trimethylhexahydro-1,3,5-triazine and N-methylenemethanamine from a feedstock containing N-methylimidazole, the method comprising: contacting the feedstock with small or medium pore molecular sieves, wherein the small or medium pore molecular sieves adsorb 1,3,5-trimethylhexahydro-1,3,5-triazine and N-methylenemethanamine from the feedstock; and separating the small or medium pore molecular sieves from the feedstock. 2. The method of claim 1 wherein contacting the feedstock with small or medium pore molecular sieves comprises contacting the feedstock with synthetic molecular sieves having a pore aperture size of no more than about 0.6 nm. 3. The method of claim 2 wherein contacting the feedstock with small or medium pore molecular sieves comprises contacting the feedstock with silicoaluminophosphate (SAPO) molecular sieves. 4. The method of claim 3 wherein contacting the feedstock with small or medium pore molecular sieves comprises contacting the feedstock with SAPO-34 molecular sieves. 5. The method of claim 1 wherein contacting the feedstock with small or medium pore molecular sieves comprises: mixing the feedstock with the small or medium pore molecular sieves in a chamber, heating the chamber to form a reflux of condensed vapor, and returning the reflux to the chamber. 6. The method of claim 1 further comprising the step of heating the small or medium pore molecular sieves and the feedstock to the boiling point of the feedstock for at least about 3 minutes. 7. The method of claim 1 wherein separating the small or medium pore molecular sieves from the feedstock forms a supernatant containing the N-methylimidazole, and wherein the method further comprises fractionating the supernatant to obtain an N-methylimidazole product. 8. The method of claim 1 wherein the feedstock has a 1,3,5-trimethylhexahydro-1,3,5-triazine and N-methylenemethanamine concentration of about 200 parts per million (ppm) to about 1100 ppm, and wherein separating the small or medium pore molecular sieves from the feedstock comprises isolating a supernatant with a 1,3,5-trimethylhexahydro-1,3,5-triazine and N-methylenemethanamine concentration of about 0 ppm to about 20 ppm. 9. The method of claim 1 wherein contacting the feedstock with small or medium pore molecular sieves comprises contacting the small or medium pore molecular sieves with the feedstock in a ratio between about 0.5 grams (g) of the small or medium pore molecular sieves per 100 milliliters (ml) of feedstock to about 8 g of the small or medium pore molecular sieves per 100 ml of feedstock. 10. The method of claim 1 wherein contacting the feedstock with small or medium pore molecular sieves comprises contacting the small or medium pore molecular sieves with the feedstock in a ratio of about 2.5 grams (g) of the small or medium pore molecular sieves per 100 milliliters (ml) of feedstock.
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