Filtration process for purifying liquid azole heteroaromatic compound-containing mixtures
IPC분류정보
국가/구분
United States(US) Patent
등록
국제특허분류(IPC7판)
C07D-249/16
C07D-249/18
출원번호
US-0064465
(2013-10-28)
등록번호
US-9309205
(2016-04-12)
발명자
/ 주소
Vogt, Peter F.
Milawski, James E.
Lees, Michael E.
Wessel, Alexander J.
출원인 / 주소
Wincom, Inc.
대리인 / 주소
Guttag, Eric W.
인용정보
피인용 횟수 :
1인용 특허 :
53
초록▼
A process for removing impurities from a liquid azole heteroaromatic compound-containing (e.g., triazole-containing) mixture by: (a) providing a liquid azole heteroaromatic compound-containing mixture having impurities; and (b) passing the azole heteroaromatic compound-containing mixture through at
A process for removing impurities from a liquid azole heteroaromatic compound-containing (e.g., triazole-containing) mixture by: (a) providing a liquid azole heteroaromatic compound-containing mixture having impurities; and (b) passing the azole heteroaromatic compound-containing mixture through at least one filtration membrane which is a nanofiltration membrane and/or ultrafiltration membrane having a molecular pore size in the range of from about 200 daltons to about 1 kilodaltons to provide a permeate that is an at least partially purified azole heteroaromatic compound-containing mixture and a retentate with at least some impurities.
대표청구항▼
1. A process for removing impurities from a liquid azole heteroaromatic compound-containing mixture, which comprises the following steps: (a) providing a liquid azole heteroaromatic compound-containing mixture comprising impurities; and having a PH of at least about 9; and(b) passing the azole heter
1. A process for removing impurities from a liquid azole heteroaromatic compound-containing mixture, which comprises the following steps: (a) providing a liquid azole heteroaromatic compound-containing mixture comprising impurities; and having a PH of at least about 9; and(b) passing the azole heteroaromatic compound-containing mixture of step (a) in a cross-flow manner through at least one filtration membrane selected from the group consisting of nanofiltration and ultrafiltration membranes and having a molecular pore size in the range of from about 200 daltons to about 1 kilodalton to provide a permeate comprising an at least partially purified azole heteroaromatic compound-containing mixture and a retentate comprising at least some impurities. 2. The process of claim 1, wherein the at least one filtration membrane of step (b) has a molecular pore size in the range of from about 250 daltons to about 600 daltons. 3. The process of claim 2, wherein the at least one filtration membrane of step (b) has a molecular pore size in the range of from about 350 daltons to about 500 daltons and wherein the permeate of step (b) comprises components having a molecular weight below about 500 daltons. 4. The process of claim 3, wherein the permeate of step (b) comprises components having a molecular weight below about 300 daltons. 5. The process of claim 1, wherein step (b) is carried out by passing the azole heteroaromatic compound-containing mixture of step (a) through a plurality of filtration membranes. 6. The process of claim 5, wherein the plurality of filtration membranes comprise spiral membrane structures, tubular membrane structures, or a combination of spiral membrane structures and tubular membrane structures. 7. The process of claim 6, wherein each of the plurality of filtration membranes comprise spiral membrane structures. 8. The process of claim 5, wherein the plurality of filtration membranes comprise a plurality of filtration units connected in sequence and in series, and wherein at least part of the retentate obtained from a filtration unit earlier in the sequence is used to provide the feed flow for the filtration unit next in the sequence. 9. The process of claim 1, wherein the azole heteroaromatic compound-containing mixture of step (a) is passed through the at least one filtration membrane at pressure of from about 1 to about 2500 psi during step (b). 10. The process of claim 9, wherein the azole heteroaromatic compound-containing mixture of step (a) is passed through the through at least one filtration membrane at pressure of from about 100 to about 500 psi during step (b). 11. The process of claim 1, wherein the azole heteroaromatic compound-containing mixture of step (a) comprises at least about 5% of one or more triazoles. 12. The process of claim 11, wherein the azole heteroaromatic compound-containing mixture of step (a) comprises at least about 40% of one or more of benzotriazole, toluyltriazole, or a water-soluble salt thereof and has a pH in the range of from about 10 to about 14. 13. The process of claim 1, wherein the azole heteroaromatic compound-containing mixture of step (a) comprises up about 10% impurities. 14. The process of claim 13, wherein the azole heteroaromatic compound-containing mixture of step (a) comprises from about 0.1 to about 8% impurities. 15. The process of claim 1, wherein the azole heteroaromatic compound-containing mixture of step (a) comprises a liquid carrier comprising one more of: water, methanol, ethanol, propanol, isopropanol, ethylene glycol, propylene glycol, or diethylene glycol. 16. The process of claim 11, wherein the azole heteroaromatic compound-containing mixture of step (a) comprises at least about 50% of the one or more triazoles.
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