초록 ▼

Phosphinic acid (also called hypophosphorous acid), when used in very small quantities, is disclosed to act as a catalyst to accelerate the reaction rate of esterification of rosin with pentaerythritol. According to the process of the invention, a rosin is reacted with at least an equivalent amount

Phosphinic acid (also called hypophosphorous acid), when used in very small quantities, is disclosed to act as a catalyst to accelerate the reaction rate of esterification of rosin with pentaerythritol. According to the process of the invention, a rosin is reacted with at least an equivalent amount of pentaerythritol in the presence of phosphinic acid at a temperature of from about 180° C. to about 300° C. When tall oil rosin is esterified by the invention process, a rosin ester is produced without appreciable color degradation.

대표청구항 ▼

1. A process for esterifying rosin with at least an equivalent of pentaerythritol which comprises heating the rosin and pentaerythritol in the presence of phosphinic acid catalyst. 2. The process of claim 1 wherein the reaction is conducted in an inert environment for from 18 to 20 hours at from 180

1. A process for esterifying rosin with at least an equivalent of pentaerythritol which comprises heating the rosin and pentaerythritol in the presence of phosphinic acid catalyst. 2. The process of claim 1 wherein the reaction is conducted in an inert environment for from 18 to 20 hours at from 180° C. to 300° C. in the presence of 0.01% to less than 0.5% phosphinic acid, followed by a steam sparge and addition of sodium hydroxide in an amount sufficient to neutralize the phosphinic acid. 3. The process of claim 1 wherein the rosin is esterified with a 15-18% excess equivalent of pentaerythritol at from 250° C. to 280° C. 4. The process of claim 1, 2 or 3 wherein the rosin is selected from the group consisting of tall oil rosin, gum rosin and wood rosin. 5. The process of claim 1, 2 or 3 wherein the rosin is selected from the group consisting of disproportionated rosin, hydrogenated rosin and polymerized rosin. 6. In a process for esterifying rosin with pentaerythritol to obtain the corresponding ester, the improvement which comprises conducting the esterification reaction in an inert environment in the presence of from 0.01% to less than 0.5% phosphinic acid, based on the weight of the rosin, at a temperature of from about 180° C. to about 300° C. for up to 20 hours and neutralizing the phosphinic acid with sodium hydroxide. 7. The process of claim 6 wherein the rosin is esterified with a 15-18% excess equivalent of pentaerythritol in the presence of from 0.1% to 0.25% phosphinic acid and the reaction is conducted under an inert gas sparge. 8. The process of claim 6 wherein the esterification reaction is conducted at a temperature of from 250° C. to 280° C. 9. The process or claim 7 wherein the inert gas is nitrogen. 10. The process of claim 6, 7 or 8 wherein the rosin is selected from the group consisting of tall oil rosin, gum rosin and wood rosin. 11. The process of claim 6, 7 or 8 wherein the rosin is selected from the group consisting of disproportionated rosin, hydrogenated rosin and polymerized rosin. 12. A process for effecting tall oil rosin esterification which comprises reacting at a temperature ranging from 180° C. to 300° C. a tall oil rosin with pentaerythritol in an equivalent amount but not more than a 18% excess based on the equivalent weight of the rosin in the presence of from 0.01% to less than 0.5% phosphinic acid, based on the weight of the rosin, and, thereafter recovering a tall oil rosin-pentaerythritol ester having a color of 0-2 Gardner color units above the color of the rosin and a Ball and Ring softening point of from 95° C. to 105° C. 13. The process of claim wherein 12 wherein 0.1% to 0.25% phosphinic acid is employed and the reaction is conducted under an inert gas sparge. 14. The process of claim 12 wherein the reaction temperature range is from 250° C. to 280° C. 15. A tall oil rosin ester prepared by reacting a tall oil rosin with a 15-18% excess equivalent of pentaerythritol by heating the rosin and the pentaerythritol in an inert environment for from 18 to 20 hours at from 250° to 280° C. in the presence of from 0.01% to less than 0.5% phosphinic acid catalyst, followed by a steam sparge and the addition of sodium hydroxide in an amount sufficient to neutralize the phosphinic acid wherein the tall oil rosin ester exhibits both a color of 0-2 Gardner color units above the color of the tall oil rosin and a Ball and Ring softening point of from 95° C. to 105° C. 16. The product of claim 15 wherein the reaction is conducted in the presence of from 0.1% to 0.25% phosphinic acid and the inert environment is provided by an inert gas sparge. 17. The product of claim 16 wherein the inert gas is nitrogen.