PLASTICIZER COMPOSITION AND RESIN COMPOSITION INCLUDING THE SAME (As Amended)
US-2018171103-A1 · Jun 21, 2018 · US
US11407706B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11407706-B2 |
| Application number | US-201917273279-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 18, 2019 |
| Priority date | Nov 28, 2018 |
| Publication date | Aug 9, 2022 |
| Grant date | Aug 9, 2022 |
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Provided is a method for manufacturing a terephthalate-based composition, the method comprising:a step (S1) of flowing in a dialkyl terephthalate in which alkyl has 7 to 10 carbon atoms and a primary alcohol with a low boiling point having 4 or 5 carbon atoms into a reactor and performing transesterification of the dialkyl terephthalate and the primary alcohol with a low boiling point; anda step (S2) of extracting in a reduced pressure an unreacted material and a by-product from the reactor after finishing the transesterification,wherein the step S1 comprises a pressure-applying step in which the pressure of the reactor is 1.5 to 2.5 bar.
Opening claim text (preview).
The invention claimed is: 1. A method for manufacturing a terephthalate-based composition, the method comprising: step (S1) of flowing in a dialkyl terephthalate in which alkyl has 7 to 10 carbon atoms and a primary alcohol with a low boiling point having 4 or 5 carbon atoms into a reactor and performing transesterification of the dialkyl terephthalate and the primary alcohol with a low boiling point; and a step (S2) of extracting in a reduced pressure an unreacted material and a by-product from the reactor after finishing the transesterification, wherein the step S1 comprises a pressure-applying step in which the pressure of the reactor is 1.5 to 2.5 bar, and a standard pressure step in which the pressure of the reactor is standard pressure, and wherein the pressure-applying step occurs during 65% or more of a whole time period of the step S1. 2. The method according to claim 1 , wherein the pressure-applying step occurs during 65% to 80% of a whole time period of the step S1. 3. The method according to claim 1 , wherein the standard pressure step is applied after the pressure-applying step in step S1. 4. The method according to claim 1 , wherein in the pressure-applying step the pressure of the reactor is 1.5 to 2.0 bar. 5. The method according to claim 1 , wherein the dialkyl terephthalate is di(2-ethylhexyl) terephthalate. 6. The method according to claim 1 , wherein the primary alcohol with a low boiling point is butanol. 7. The method according to claim 1 , wherein the unreacted material is a primary alcohol with a low boiling point having 4 or 5 carbon atoms, and the by-product is a primary alcohol with a high boiling point having 7 to 10 carbon atoms, which is produced by the transesterification. 8. The method according to claim 1 , wherein the reactor is a batch type reactor.
by reacting an ester group with a hydroxy group · CPC title
Batch processes · CPC title
Controlling or regulating processes (controlling or regulating in general G05) · CPC title
Separation; Purification; Stabilisation; Use of additives · CPC title
Terephthalic acid esters · CPC title
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