High-purity dibasic acid compositions and methods of making the same
High-purity dibasic acid compositions are generally disclosed. In some embodiments, the dibasic acid compositions are solutions or suspensions. In some other embodiments, the compositions are solid-state compositions. In some such embodiments, the solid-state compositions include a dibasic acid as a crystalline solid and further include a low quantity of certain impurities, such as monobasic acids, various esters, and the like. Methods and systems for making such high-purity dibasic acid compositions are also disclosed.
1. A method of hydrolyzing a dibasic ester, comprising:
introducing a first composition to a reactor, the first composition comprising at least 50 grams of a dibasic ester of formula (I) and an initial amount of water:
wherein
Y 1 is —(CH 2 ) 8 —, —(CH 2 ) 9 —, —(CH 2 ) 10 —, —(CH 2 ) 11 —,—(CH 2 ) 12 —, —(CH 2 ) 13 —, —(CH 2 ) 14 —, —(CH 2 ) 15 —, —(CH 2 ) 16 —,—(CH 2 ) 17 —, —(CH 2 )1 8 —, —(CH 2 19 8 —, —(CH 2 ) 20 —, —(CH 2 ) 21 —, or —(CH 2 ) 22 —; and
R 1 and R 2 are independently C 1-8 alkyl, C 2-8 alkenvl, or C 2-8 oxyalkenyl, each of which is optionally substituted one or more times by —OH; and
reacting the dibasic ester in the reactor with water to form a second composition comprising a dibasic acid and alcohols, wherein the dibasic acid is a compound of formula (II) and the alcohols are compounds of formula (111a) and formula (111b):
wherein Y 1 , R 1 and R 2 are as defined above for formula (I);
wherein during the reacting, at least a portion of the alcohols is removed from the reactor and additional amounts of water are added to the reactor, and wherein the mass-to-mass ratio of the additional amounts of water added during the reaction to the alcohols removed during the reaction ranges from 0.8:1 to 1.2:1.
2. The method of claim 1 , wherein the yield of dibasic acid is at least 75 percent.
3. The method of claim 1 , wherein R 1 and R 2 are independently methyl, ethyl, propyl, isopropyl, butyl, isobutyl, sec-butyl, tert-butyl, pentyl, tert-pentyl, neopentyl, hexyl, or 2-ethylhexyl.
4. The method of claim 3 , wherein R 1 and R 2 are methyl.
5. The method of claim 1 , wherein the reacting is carried out at a reactor temperature of 40° C. to 300° C.
6. The method of claim 1 , wherein at least 20 percent by weight of the alcohols are removed from the reactor during the reacting.
7. The method of claim 1 , wherein the alcohols are removed continuously or semi-continuously during the reacting.
8. The method of claim 1 , wherein the water is added continuously or semi-continuously during the reacting.
9. The method of claim 1 , wherein the mole-to-mole ratio of water to alcohols in the reactor is at least 1:1 during the reacting.
10. The method of claim 9 , wherein the mole-to-mole ratio of water to alcohols in the reactor is at least 2:1 during the reacting.
11. The method of claim 1 , wherein the concentration of O 2 in the reactor does not exceed 250 ppm during the reacting, based on the total number of gaseous species in the reactor.
12. A method of hydrolyzing a dibasic ester, comprising:
introducing a first composition to a reactor, the first composition comprising at least 50 grams of a dibasic ester of formula (I):
wherein
Y 1 is —(CH 2 ) 13 —, —(CH 2 ) 14 —, —(CH 2 ) 15 —, —(CH 2 ) 16 —,—(CH 2 ) 17 —, —(CH 2 )1 8 —, —(CH 2 19 8 —, —(CH 2 ) 20 —, —(CH 2 ) 21 —, or —(CH 2 ) 22 —; and
R 1 and R 2 are independently C 1-8 alkyl, C 2-8 alkenvl, or C 2-8 oxyalkenyl, each of which is optionally substituted one or more times by —OH; and
reacting the dibasic ester in the reactor with water to form a second composition comprising a dibasic acid and alcohols, wherein the dibasic acid is a compound of formula (II) and the alcohols are compounds of formula (111a) and formula (111b):
wherein Y 1 , R 1 and R 2 are as defined above for formula (I);
wherein during the reacting, at least a portion of the alcohols is removed from the reactor and water is added to the reactor, and wherein the mass-to-mass ratio of the water added during the reaction to the alcohols removed during the reaction ranges from 0.8:1 to 1.2:1.
13. The method of claim 12 , wherein the yield of dibasic acid is at least 75 percent.
14. The method of claim 12 , wherein R 1 and R 2 are independently methyl, ethyl, propyl, isopropyl, butyl, isobutyl, sec-butyl, tert-butyl, pentyl, tert-pentyl, neopentyl, hexyl, or 2-ethylhexyl.
15. The method of claim 14 , wherein R 1 and R 2 are methyl.
16. The method of claim 12 , wherein the reacting is carried out at a reactor temperature of 40° C. to 300° C.