Patent Application
20190194387
This disclosure relates to a method of preparing glycolide.
Conventional synthesis of glycolide includes catalytic depolymerization performed with a high temperature (220-250° C.) or in a high boiling solvent. However, it is difficult to separate the high boiling solvent from the product and to recycle it. In addition, conventional catalysts for the synthesis of glycolide are metal compounds, such as Sn(Oct)2, SnCl2, Sb2O3. They are cytotoxic and difficult to recycle.
Disclosed is a method of preparing glycolide which is safe, environmentally friendly; the glycolide is prepared in a high yield and is of high purity.
Disclosed is a method of preparing glycolide, the method comprising dehydrative oligomerization and catalytic depolymerization, the dehydrative oligomerization comprising:
the catalytic depolymerization comprising:
e2) heating the reactant mixture from the temperature of between 270 and 275° C. to a temperature of between 280 and 285° C. at a heating rate of 1.0-1.5° C./min, and maintaining the temperature for 60-70 minutes, to yield a white or yellowish crude glycolide having a purity greater than or equal to 99.9%, and a yield greater than or equal to 98.0%.
The binary complex catalytic system can comprise a cyclic guanidine compound and a linear guanidine compound; the cyclic guanidine compound can be selected from bicyclic guanidine, guanine, and benzimidazole; the linear guanidine compound can be selected from glycocyamine, creatine, and phosphocreatine, and an addition amount of each of the cyclic guanidine compound and the linear guanidine compound can account for 0.05-0.10 wt. % of that of the oligoglycolic acid.
The oligoglycolic acid obtained in e1) can have a weight-average molecular weight (Mw) of 5.0-6.0×103, and is prepared in a yield of 100%.
The crude glycolide obtained in e2) can be white or yellowish and can have a purity greater than or equal to 99.9%, and is prepared in a yield greater than or equal to 98.0%.
Advantages of the method of preparing glycolide as described in the disclosure are summarized as follows.
1. The binary complex catalytic system is a non-cytotoxic guanidine compound with relatively high catalytic efficiency and relatively low addition amount.
2. The glycolide is prepared in high yield (≥98.0%) and is of high purity (≥99.9%).
3. The method is an efficient, environmentally friendly, closed cycle process.
To further illustrate, embodiments detailing a method of preparing glycolide are described below. It should be noted that the following embodiments are intended to describe and not to limit the disclosure.
50 kg of a 70 wt. % glycolic acid aqueous solution was added to a reactor for dehydrative oligomerization. First, the glycolic acid aqueous solution was heated from room temperature to 100° C. at a heating rate of 1.0° C./min, and then dehydrated under atmosphere for 1.0 hour. Second, the glycolic acid aqueous solution was heated from 100° C. to 140° C. at a heating rate of 1.0° C./min, and then dehydrated under atmosphere for 1.0 hour. Third, the glycolic acid aqueous solution was further heated from 140° C. to 155° C. at a heating rate of 1.0° C./min, and then dehydrated under atmosphere for 1.0 hour. Fourth, the glycolic acid aqueous solution was further heated from 155° C. to 200° C. at a heating rate of 1.0° C./min, and the absolute pressure of the glycolic acid aqueous solution was reduced from atmosphere to 90.0 torr at a decompression rate of 1.0 torr/min. Hold the temperature and the pressure for an hour. Thereafter, the absolute pressure of the glycolic acid aqueous solution was reduced from 90.0 torr to 10.0 torr at a decompression rate of 1.0 torr/min for an hour. A product of oligoglycolic acid having a weight-average molecular weight (Mw) of 5.0×103 was obtained, and a yield thereof was 100%.
25.0 g of bicyclic guanidine and 25.0 g of glycocyamine were added to the product of oligoglycolic acid. The absolute pressure of the reactant mixture was reduced from atmosphere to 3.0 torr at a decompression rate of 1.0 torr/min. Under the pressure, the reactant mixture was heated to 250° C. at a heating rate of 10° C./min, and the temperature was held for 20 minutes. Thereafter, the reactant mixture was heated from 250° C. to 270° C. at a heating rate of 1.0° C./min, and the temperature was held for 20 minutes. Next, the reactant mixture was further heated from 270° C. to 280° C. at a heating rate of 1.0° C./min, and the temperature was held for 60 minutes, to yield a white or yellowish crude glycolide.
The crude glycolide was washed using a 0.1 wt. % alkali solution and deionized water to be neutral, and then vacuum dried at 20° C. for 24 hours. The obtained glycolide has a yield of 98.5% and a purity of 99.9%.
The preparation method is basically the same as that in Example 1 except that only 25.0 g of bicyclic guanidine was added in the catalytic depolymerization, and the obtained glycolide has a yield of 41.1% and a purity of 82.5%.
The preparation method is basically the same as that in Example 1 except that only 25.0 g of glycocyamine was added in the catalytic depolymerization, and the obtained glycolide has a yield of 34.5% and a purity of 85.3%.
50 kg of a 70 wt. % glycolic acid aqueous solution was added to a reactor for dehydrative oligomerization. First, the glycolic acid aqueous solution was heated from room temperature to 100° C. at a heating rate of 1.0° C./min, and then dehydrated under atmosphere for 1.0 hour. Second, the glycolic acid aqueous solution was heated from 100° C. to 140° C. at a heating rate of 1.0° C./min, and then dehydrated under atmosphere for 1.0 hour. Third, the glycolic acid aqueous solution was further heated from 140° C. to 155° C. at a heating rate of 1.0° C./min, and then dehydrated under atmosphere for 1.0 hour. Fourth, the glycolic acid aqueous solution was further heated from 155° C. to 200° C. at a heating rate of 1.0° C./min, and the absolute pressure of the glycolic acid aqueous solution was reduced from atmosphere to 90.0 torr at a decompression rate of 1.0 torr/min. Hold the temperature and the pressure for an hour. Thereafter, the absolute pressure of the glycolic acid aqueous solution was reduced from 90.0 torr to 10.0 torr at a decompression rate of 1.0 torr/min for an hour. A product of oligoglycolic acid having a weight-average molecular weight (Mw) of 5.0×103 was obtained, and a yield thereof was 100%.
50.0 g of bicyclic guanidine and 35.0 g of creatine were added to the product of oligoglycolic acid. The absolute pressure of the reactant mixture was reduced from atmosphere to 3.0 torr at a decompression rate of 1.0 torr/min. Under the pressure, the reactant mixture was heated to 250° C. at a heating rate of 10° C./min, and the temperature was held for 20 minutes. Thereafter, the reactant mixture was heated from 250° C. to 270° C. at a heating rate of 1.0° C./min, and the temperature was held for 20 minutes. Next, the reactant mixture was further heated from 270° C. to 280° C. at a heating rate of 1.0° C./min, and the temperature was held for 60 minutes, to yield a white or yellowish crude glycolide.
The crude glycolide was washed using a 0.1 wt. % alkali solution and deionized water to be neutral, and then vacuum dried at 20° C. for 24 hours. The obtained glycolide has a yield of 98.2% and a purity of 99.9%.
50 kg of a 70 wt. % glycolic acid aqueous solution was added to a reactor for dehydrative oligomerization. First, the glycolic acid aqueous solution was heated from room temperature to 100° C. at a heating rate of 1.0° C./min, and then dehydrated under atmosphere for 1.0 hour. Second, the glycolic acid aqueous solution was heated from 100° C. to 140° C. at a heating rate of 1.0° C./min, and then dehydrated under atmosphere for 1.0 hour. Third, the glycolic acid aqueous solution was further heated from 140° C. to 155° C. at a heating rate of 1.0° C./min, and then dehydrated under atmosphere for 1.0 hour. Fourth, the glycolic acid aqueous solution was further heated from 155° C. to 200° C. at a heating rate of 1.0° C./min, and the absolute pressure of the glycolic acid aqueous solution was reduced from atmosphere to 90.0 torr at a decompression rate of 1.0 torr/min. Hold the temperature and the pressure for an hour. Thereafter, the absolute pressure of the glycolic acid aqueous solution was reduced from 90.0 torr to 10.0 torr at a decompression rate of 1.0 torr/min for an hour. A product of oligoglycolic acid having a weight-average molecular weight (Mw) of 5.0×103 was obtained, and a yield thereof was 100%.
35.0 g of bicyclic guanidine and 50.0 g of phosphocreatine were added to the product of oligoglycolic acid. The absolute pressure of the reactant mixture was reduced from atmosphere to 3.0 torr at a decompression rate of 1.0 torr/min. Under the pressure, the reactant mixture was heated to 250° C. at a heating rate of 10° C./min, and the temperature was held for 20 minutes. Thereafter, the reactant mixture was heated from 250° C. to 270° C. at a heating rate of 1.0° C./min, and the temperature was held for 20 minutes. Next, the reactant mixture was further heated from 270° C. to 280° C. at a heating rate of 1.0° C./min, and the temperature was held for 60 minutes, to yield a white or yellowish crude glycolide.
The crude glycolide was washed using a 0.1 wt. % alkali solution and deionized water to be neutral, and then vacuum dried at 20° C. for 24 hours. The obtained glycolide has a yield of 98.7% and a purity of 99.9%.
Example 4
100 kg of a 70 wt. % glycolic acid aqueous solution was added to a reactor for dehydrative oligomerization. First, the glycolic acid aqueous solution was heated from room temperature to 105° C. at a heating rate of 1.2° C./min, and then dehydrated under atmosphere for 1.2 hour. Second, the glycolic acid aqueous solution was heated from 105° C. to 145° C. at a heating rate of 1.2° C./min, and then dehydrated under atmosphere for 1.2 hour. Third, the glycolic acid aqueous solution was further heated from 145° C. to 160° C. at a heating rate of 1.0° C./min, and then dehydrated under atmosphere for 1.2 hour. Fourth, the glycolic acid aqueous solution was further heated from 160° C. to 205° C. at a heating rate of 1.2° C./min, and the absolute pressure of the glycolic acid aqueous solution was reduced from atmosphere to 92.0 torr at a decompression rate of 1.2 torr/min. Hold the temperature and the pressure for 1.2 hour. Thereafter, the absolute pressure of the glycolic acid aqueous solution was reduced from 92.0 torr to 15.0 torr at a decompression rate of 1.2 torr/min for 1.5 hour. A product of oligoglycolic acid having a weight-average molecular weight (Mw) of 5.5×103 was obtained, and a yield thereof was 100%.
100.0 g of guanine and 70.0 g of glycocyamine were added to the product of oligoglycolic acid. The absolute pressure of the reactant mixture was reduced from atmosphere to 4.0 torr at a decompression rate of 1.2 torr/min. Under the pressure, the reactant mixture was heated to 255° C. at a heating rate of 12° C./min, and the temperature was held for 25 minutes. Thereafter, the reactant mixture was heated from 255° C. to 272° C. at a heating rate of 1.2° C./min, and the temperature was held for 25 minutes. Next, the reactant mixture was further heated from 272° C. to 282° C. at a heating rate of 1.2° C./min, and the temperature was held for 65 minutes, to yield a white or yellowish crude glycolide.
The crude glycolide was washed using a 0.1 wt. % alkali solution and deionized water to be neutral, and then vacuum dried at 20° C. for 24 hours. The obtained glycolide has a yield of 98.6% and a purity of 99.9%.
100 kg of a 70 wt. % glycolic acid aqueous solution was added to a reactor for dehydrative oligomerization. First, the glycolic acid aqueous solution was heated from room temperature to 105° C. at a heating rate of 1.2° C./min, and then dehydrated under atmosphere for 1.2 hour. Second, the glycolic acid aqueous solution was heated from 105° C. to 145° C. at a heating rate of 1.2° C./min, and then dehydrated under atmosphere for 1.2 hour. Third, the glycolic acid aqueous solution was further heated from 145° C. to 160° C. at a heating rate of 1.0° C./min, and then dehydrated under atmosphere for 1.2 hour. Fourth, the glycolic acid aqueous solution was further heated from 160° C. to 205° C. at a heating rate of 1.2° C./min, and the absolute pressure of the glycolic acid aqueous solution was reduced from atmosphere to 92.0 torr at a decompression rate of 1.2 torr/min. Hold the temperature and the pressure for 1.2 hour. Thereafter, the absolute pressure of the glycolic acid aqueous solution was reduced from 92.0 torr to 15.0 torr at a decompression rate of 1.2 torr/min for 1.5 hour. A product of oligoglycolic acid having a weight-average molecular weight (Mw) of 5.5×103 was obtained, and a yield thereof was 100%.
50.0 g of guanine and 50.0 g of creatine were added to the product of oligoglycolic acid. The absolute pressure of the reactant mixture was reduced from atmosphere to 4.0 torr at a decompression rate of 1.2 torr/min. Under the pressure, the reactant mixture was heated to 255° C. at a heating rate of 12° C./min, and the temperature was held for 25 minutes. Thereafter, the reactant mixture was heated from 255° C. to 272° C. at a heating rate of 1.2° C./min, and the temperature was held for 25 minutes. Next, the reactant mixture was further heated from 272° C. to 282° C. at a heating rate of 1.2° C./min, and the temperature was held for 65 minutes, to yield a white or yellowish crude glycolide.
The crude glycolide was washed using a 0.1 wt. % alkali solution and deionized water to be neutral, and then vacuum dried at 20° C. for 24 hours. The obtained glycolide has a yield of 98.3% and a purity of 99.9%.
100 kg of a 70 wt. % glycolic acid aqueous solution was added to a reactor for dehydrative oligomerization. First, the glycolic acid aqueous solution was heated from room temperature to 105° C. at a heating rate of 1.2° C./min, and then dehydrated under atmosphere for 1.2 hour. Second, the glycolic acid aqueous solution was heated from 105° C. to 145° C. at a heating rate of 1.2° C./min, and then dehydrated under atmosphere for 1.2 hour. Third, the glycolic acid aqueous solution was further heated from 145° C. to 160° C. at a heating rate of 1.0° C./min, and then dehydrated under atmosphere for 1.2 hour. Fourth, the glycolic acid aqueous solution was further heated from 160° C. to 205° C. at a heating rate of 1.2° C./min, and the absolute pressure of the glycolic acid aqueous solution was reduced from atmosphere to 92.0 torr at a decompression rate of 1.2 torr/min. Hold the temperature and the pressure for 1.2 hour. Thereafter, the absolute pressure of the glycolic acid aqueous solution was reduced from 92.0 torr to 15.0 torr at a decompression rate of 1.2 torr/min for 1.5 hour. A product of oligoglycolic acid having a weight-average molecular weight (Mw) of 5.5×103 was obtained, and a yield thereof was 100%.
70.0 g of guanine and 100.0 g of phosphocreatine were added to the product of oligoglycolic acid. The absolute pressure of the reactant mixture was reduced from atmosphere to 4.0 torr at a decompression rate of 1.2 torr/min. Under the pressure, the reactant mixture was heated to 255° C. at a heating rate of 12° C./min, and the temperature was held for 25 minutes. Thereafter, the reactant mixture was heated from 255° C. to 272° C. at a heating rate of 1.2° C./min, and the temperature was held for 25 minutes. Next, the reactant mixture was further heated from 272° C. to 282° C. at a heating rate of 1.2° C./min, and the temperature was held for 65 minutes, to yield a white or yellowish crude glycolide.
The crude glycolide was washed using a 0.1 wt. % alkali solution and deionized water to be neutral, and then vacuum dried at 20° C. for 24 hours. The obtained glycolide has a yield of 98.4% and a purity of 99.9%.
150 kg of a 70 wt. % glycolic acid aqueous solution was added to a reactor for dehydrative oligomerization. First, the glycolic acid aqueous solution was heated from room temperature to 110° C. at a heating rate of 1.5° C./min, and then dehydrated under atmosphere for 1.5 hour. Second, the glycolic acid aqueous solution was heated from 110° C. to 150° C. at a heating rate of 1.5° C./min, and then dehydrated under atmosphere for 1.5 hour. Third, the glycolic acid aqueous solution was further heated from 150° C. to 165° C. at a heating rate of 1.5° C./min, and then dehydrated under atmosphere for 1.5 hour. Fourth, the glycolic acid aqueous solution was further heated from 165° C. to 210° C. at a heating rate of 1.5° C./min, and the absolute pressure of the glycolic acid aqueous solution was reduced from atmosphere to 95.0 torr at a decompression rate of 1.5 torr/min. Hold the temperature and the pressure for 1.5 hour. Thereafter, the absolute pressure of the glycolic acid aqueous solution was reduced from 95.0 torr to 20.0 torr at a decompression rate of 1.5 torr/min for 2.0 hour. A product of oligoglycolic acid having a weight-average molecular weight (Mw) of 6.0×103 was obtained, and a yield thereof was 100%.
150.0 g of benzimidazole and 75.0 g of glycocyamine were added to the product of oligoglycolic acid. The absolute pressure of the reactant mixture was reduced from atmosphere to 5.0 torr at a decompression rate of 1.5 torr/min. Under the pressure, the reactant mixture was heated to 260° C. at a heating rate of 15° C./min, and the temperature was held for 30 minutes. Thereafter, the reactant mixture was heated from 260° C. to 275° C. at a heating rate of 1.5° C./min, and the temperature was held for 30 minutes. Next, the reactant mixture was further heated from 275° C. to 285° C. at a heating rate of 1.5° C./min, and the temperature was held for 70 minutes, to yield a white or yellowish crude glycolide.
The crude glycolide was washed using a 0.1 wt. % alkali solution and deionized water to be neutral, and then vacuum dried at 20° C. for 24 hours. The obtained glycolide has a yield of 98.1% and a purity of 99.9%.
150 kg of a 70 wt. % glycolic acid aqueous solution was added to a reactor for dehydrative oligomerization. First, the glycolic acid aqueous solution was heated from room temperature to 110° C. at a heating rate of 1.5° C./min, and then dehydrated under atmosphere for 1.5 hour. Second, the glycolic acid aqueous solution was heated from 110° C. to 150° C. at a heating rate of 1.5° C./min, and then dehydrated under atmosphere for 1.5 hour. Third, the glycolic acid aqueous solution was further heated from 150° C. to 165° C. at a heating rate of 1.5° C./min, and then dehydrated under atmosphere for 1.5 hour. Fourth, the glycolic acid aqueous solution was further heated from 165° C. to 210° C. at a heating rate of 1.5° C./min, and the absolute pressure of the glycolic acid aqueous solution was reduced from atmosphere to 95.0 torr at a decompression rate of 1.5 torr/min. Hold the temperature and the pressure for 1.5 hour. Thereafter, the absolute pressure of the glycolic acid aqueous solution was reduced from 95.0 torr to 20.0 torr at a decompression rate of 1.5 torr/min for 2.0 hour. A product of oligoglycolic acid having a weight-average molecular weight (Mw) of 6.0×103 was obtained, and a yield thereof was 100%.
105.0 g of benzimidazole and 105.0 g of creatine were added to the product of oligoglycolic acid. The absolute pressure of the reactant mixture was reduced from atmosphere to 5.0 torr at a decompression rate of 1.5 torr/min. Under the pressure, the reactant mixture was heated to 260° C. at a heating rate of 15° C./min, and the temperature was held for 30 minutes. Thereafter, the reactant mixture was heated from 260° C. to 275° C. at a heating rate of 1.5° C./min, and the temperature was held for 30 minutes. Next, the reactant mixture was further heated from 275° C. to 285° C. at a heating rate of 1.5° C./min, and the temperature was held for 70 minutes, to yield a white or yellowish crude glycolide.
The crude glycolide was washed using a 0.1 wt. % alkali solution and deionized water to be neutral, and then vacuum dried at 20° C. for 24 hours. The obtained glycolide has a yield of 99.0% and a purity of 99.9%.
150 kg of a 70 wt. % glycolic acid aqueous solution was added to a reactor for dehydrative oligomerization. First, the glycolic acid aqueous solution was heated from room temperature to 110° C. at a heating rate of 1.5° C./min, and then dehydrated under atmosphere for 1.5 hour. Second, the glycolic acid aqueous solution was heated from 110° C. to 150° C. at a heating rate of 1.5° C./min, and then dehydrated under atmosphere for 1.5 hour. Third, the glycolic acid aqueous solution was further heated from 150° C. to 165° C. at a heating rate of 1.5° C./min, and then dehydrated under atmosphere for 1.5 hour. Fourth, the glycolic acid aqueous solution was further heated from 165° C. to 210° C. at a heating rate of 1.5° C./min, and the absolute pressure of the glycolic acid aqueous solution was reduced from atmosphere to 95.0 torr at a decompression rate of 1.5 torr/min. Hold the temperature and the pressure for 1.5 hour. Thereafter, the absolute pressure of the glycolic acid aqueous solution was reduced from 95.0 torr to 20.0 torr at a decompression rate of 1.5 torr/min for 2.0 hour. A product of oligoglycolic acid having a weight-average molecular weight (Mw) of 6.0×103 was obtained, and a yield thereof was 100%.
75.0 g of benzimidazole and 150.0 g of phosphocreatine were added to the product of oligoglycolic acid. The absolute pressure of the reactant mixture was reduced from atmosphere to 5.0 torr at a decompression rate of 1.5 torr/min. Under the pressure, the reactant mixture was heated to 260° C. at a heating rate of 15° C./min, and the temperature was held for 30 minutes. Thereafter, the reactant mixture was heated from 260° C. to 275° C. at a heating rate of 1.5° C./min, and the temperature was held for 30 minutes. Next, the reactant mixture was further heated from 275° C. to 285° C. at a heating rate of 1.5° C./min, and the temperature was held for 70 minutes, to yield a white or yellowish crude glycolide.
The crude glycolide was washed using a 0.1 wt. % alkali solution and deionized water to be neutral, and then vacuum dried at 20° C. for 24 hours. The obtained glycolide has a yield of 99.2% and a purity of 99.9%.
It will be obvious to those skilled in the art that changes and modifications may be made, and therefore, the aim in the appended claims is to cover all such changes and modifications.
| Number | Date | Country | Kind |
|---|---|---|---|
| 201610809645.9 | Sep 2016 | CN | national |
This application is a continuation-in-part of International Patent Application No. PCT/CN2017/100510 with an international filing date of Sep. 5, 2017, designating the United States, now pending, and further claims foreign priority benefits to Chinese Patent Application No. 201610809645.9 filed Sep. 7, 2016. The contents of all of the aforementioned applications, including any intervening amendments thereto, are incorporated herein by reference. Inquiries from the public to applicants or assignees concerning this document or the related applications should be directed to: Matthias Scholl P.C., Attn.: Dr. Matthias Scholl Esq., 245 First Street, 18th Floor, Cambridge, Mass. 02142.
| Number | Date | Country | |
|---|---|---|---|
| Parent | PCT/CN2017/100510 | Sep 2017 | US |
| Child | 16293595 | US |
