System and method for manufacturing ester-based composition
US-2020317599-A1 · Oct 8, 2020 · US
US11512166B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11512166-B2 |
| Application number | US-202016838778-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 2, 2020 |
| Priority date | Apr 4, 2019 |
| Publication date | Nov 29, 2022 |
| Grant date | Nov 29, 2022 |
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The present disclosure relates to a method for continuously manufacturing an ester-based composition and a manufacturing system therefor, the method improving a manufacturing yield by optimizing process variables of each reactor of a reaction unit in which a plurality of reactors are connected in series.
Opening claim text (preview).
The invention claimed is: 1. A method for manufacturing an ester-based composition, the method comprising: a step S1 of injecting a polycarboxylic acid and an alcohol having 3 to 10 alkyl carbon atoms into a mixer to form a reaction mixture; a step S2 of continuously injecting the reaction mixture into a reaction unit in which a total of N reactors are connected in series from a first reactor to an N-th reactor, thereby continuously manufacturing reaction products; a step S3 of continuously moving the reaction products into a separation unit to remove the unreacted alcohol; and a step S4 of injecting the unreacted alcohol removed from the separation unit back into any one reactor of the reaction unit, wherein N is an integer of 3 or greater, and Formulas 1) and 2) are satisfied: T n1-1 ≤T n1 1) E n2-1 ≥E n2 ≥E 1 2) wherein, in Formulas 1) and 2), n1 is an integer of 2 to N, and n2 is an integer of 3 to N, T x =Temperature of an x-th reactor E x ={(Number of moles of the alcohol injected into an x-th reactor−c*Number of moles of polycarboxylic acid injected into an x-th reactor)/(c*Number of moles of polycarboxylic acid injected into the first reactor)*100%} wherein c is the number of carboxylic acid groups contained in one molecule of the polycarboxylic acid, and in T x and E x , x is an integer of 1 to N. 2. The method of claim 1 , wherein the separation unit comprises one or more separation columns or a purification tank of a drum type. 3. The method of claim 1 , further comprising a step S1-1 of adding a catalyst to the reaction mixture between the step S1 and the step S2; or a step S1-2 of adding a catalyst to the polycarboxylic acid and the alcohol before the step S1. 4. The method of claim 3 , wherein the catalyst is tetraalkyl titanate. 5. The method of claim 1 , wherein the step S1 further comprises a step in which the reaction mixture is heated to 50-200° C. 6. The method of claim 1 , wherein T 1 is 100-220° C. and T N is 200-250° C. 7. The method of claim 1 , wherein E 1 is −30 to 80% and E N is 0 to 80%. 8. The method of claim 1 , further comprising a step S5 of injecting the alcohol having 3 to 10 alkyl carbon atoms into the reaction products from which the unreacted alcohol is removed to perform a trans-esterification reaction, wherein the alcohol injected in the step S5 is different from the alcohol injected in the step S1. 9. The method of claim 1 , wherein the polycarboxylic acid is one or more selected from the group consisting of a dicarboxylic acid, a tricarboxylic acid, and a tetracarboxylic acid. 10. The method of claim 9 , wherein the dicarboxylic acid is one or more selected from the group consisting of a linear dicarboxylic acid having 2 to 10 carbon atoms, a terephthalic acid, a phthalic acid, an isophthalic acid, a cyclohexane dicarboxylic acid, an anhydride thereof, and a derivative thereof, the tricarboxylic acid is one or more selected from the group consisting of a citric acid, a trimellitate acid, a cyclohexane tricarboxylic acid, an anhydride thereof, and a derivative thereof, and the tetracarboxylic acid is one or more selected from the group consisting of a benzenetetracarboxylic acid, a furantetracarboxylic acid, a cyclohexane tetracarboxylic acid, a tetrahydrofuran tetracarboxylic acid, an anhydride thereof, and a derivative thereof. 11. A system for manufacturing an ester-based composition, the system comprising: a mixer in which a reaction mixture of a polycarboxylic acid and an alcohol having 3 to 10 alkyl carbon atoms is formed; a reaction unit having N number of reactors connected in series in which an esterification reaction of the reaction mixture is performed, wherein N is an integer of 3 or greater; a separation unit including one or more separation columns for receiving reaction products and removing the unreacted alcohol therefrom; a recovery unit for injecting the unreacted alcohol removed from the separation unit back into a reactor of the reaction unit; and a variable control unit that controls the temperature of each reactor and the amount of the alcohol injected into the reactor to satisfy Formulas 1) and 2) below: T n1-1 ≤T n1 1) E n2-1 ≥E n2 ≥E 1 2) wherein, in Formulas 1) and 2), n1 is an integer of 2 to N, and n2 is an integer of 3 to N, T x =Temperature of an x-th reactor E x ={(Number of moles of the alcohol injected into an x-th reactor−c*Number of moles of polycarboxylic acid injected into an x-th reactor)/(c*Number of moles of polycarboxylic acid injected into the first reactor)*100%} wherein c is the number of carboxylic acid groups contained in one molecule of the polycarboxylic acid, and in T x and E x , x is an integer of 1 to N. 12. The system of claim 11 , further comprising a trans-reaction unit for performing a trans-esterification reaction by adding the alcohol having 3 to 10 alkyl carbon atoms to the reaction products from which the unreacted alcohol has been removed, wherein the alcohol injected from the trans-reaction unit is different from the alcohol injected from the mixer.
Terephthalic acids · CPC title
Details of the reactor · CPC title
Controlling the temperature of the process · CPC title
Germanium, tin, lead, arsenic, antimony, bismuth, titanium, zirconium, hafnium, vanadium, niobium, tantalum, or compounds thereof {(C08G63/823 takes precedence)} · CPC title
Controlling the temperature · CPC title
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