Polyester production system employing an unagitated esterification reactor
View Patent ↗A polyester production system employing a vertically elongated esterification reactor. The esterification reactor of the present invention is an improvement over conventional CSTR esterification reactors because, for example, in one embodiment, the reactor requires little or no mechanical agitation. Further, in one embodiment, the positioning of the inlets and outlets of the reactor provides improved operational performance and flexibility over CSTRs of the prior art.
1. An apparatus comprising: a polyesterification reaction vessel containing a reaction mixture comprising at least one diol and at least one dicarboxylic acid and one or more reaction products of a diol and a dicarboxylic acid, and a plurality of vertically spaced heat exchange tubes located in said polyesterification reaction vessel, wherein said polyesterification reaction vessel is elongated along an upright central axis of elongation, wherein said polyesterification reaction vessel defines a fluid inlet, a plurality of vertically spaced liquid outlets, and a vapor outlet, wherein said fluid inlet is located at a lower elevation than said vapor outlet, wherein said liquid outlets are located at an elevation above said fluid inlet and below said vapor outlet, and
wherein the heat exchange tubes contain a heat exchange medium at a temperature higher than the temperature of the reaction mixture, and wherein the reaction mixture is not present in the heat exchange tubes.
2. The apparatus of claim 1 , wherein said polyesterification reaction vessel is not equipped with a mechanical agitator.
3. The apparatus of claim 1 , wherein said heat exchange tubes are located at an elevation above said fluid inlet and below said vapor outlet.
4. The apparatus of claim 1 , wherein said polyesterification reaction vessel has a height-to-diameter ratio in the range of from about 1.15:1 to about 8:1.
5. The apparatus of claim 4 , wherein said polyesterification reaction vessel has a maximum horizontal diameter (D), wherein said liquid outlets are radially spaced from said central axis by at least about 0.4D, wherein said fluid inlet is radially spaced from said central axis by at least about 1.5D.
6. The apparatus of claim 5 , wherein said liquid outlets and said fluid inlet are circumferentially spaced from one another by at least 90 degrees.
7. The apparatus of claim 1 , wherein said polyesterification reaction vessel comprises a generally upright, substantially cylindrical side wall defining said liquid outlets.
8. The apparatus of claim 1 , further comprising an upstream heat exchanger and an upstream disengagement vessel, wherein said upstream heat exchanger defines an exchanger inlet and an exchanger outlet, wherein said upstream disengagement vessel defines an disengagement fluid inlet, a disengaged vapor outlet, and a disengaged liquid outlet, wherein said exchanger outlet and said disengagement fluid inlet are coupled in fluid flow communication with one another, wherein said disengaged liquid outlet and said fluid inlet of said polyesterification reaction vessel are coupled in fluid flow communication with one another, wherein said disengaged liquid outlet and said exchanger inlet are coupled in fluid flow communication with one another.
9. The apparatus of claim 8 , wherein said heat exchanger is a shell-and-tube heat exchanger.
10. The apparatus of claim 8 , wherein said disengagement vessel is horizontally elongated.
11. A polyesterification reaction apparatus, comprising:
a polyesterification reaction vessel containing a reaction mixture comprising at least one diol and at least one dicarboxylic acid and one or more reaction products of a diol and a dicarboxylic acid, and a plurality of vertically spaced heat exchange tubes present in the polyesterification reaction vessel,
wherein the polyesterification reaction vessel defines a single vessel elongated along an upright central axis of elongation,
wherein the polyesterification reaction vessel has a fluid inlet, a plurality of vertically spaced liquid outlets, and a vapor outlet,
wherein the fluid inlet is located at a lower elevation than the vapor outlet,
wherein the liquid outlets are located at an elevation above the fluid inlet and below the vapor outlet, and
wherein the heat exchange tubes contain a heat exchange medium at a temperature higher than the temperature of the reaction mixture, and wherein the reaction mixture is not present in the heat exchange tubes.
12. The polyesterification reaction apparatus of claim 11 , wherein the polyesterification reaction vessel is not equipped with a mechanical agitator.
13. The polyesterification reaction apparatus of claim 11 , wherein the polyesterification reaction vessel has a height-to-diameter ratio of from 1.15:1 to 8:1.
14. The polyesterification reaction apparatus of claim 11 , further comprising:
an upstream heat exchanger and an upstream disengagement vessel,
wherein the upstream heat exchanger defines an exchanger inlet and an exchanger outlet,
wherein the upstream disengagement vessel defines a disengagement fluid inlet, a disengaged vapor outlet, and a disengaged liquid outlet,
wherein the exchanger outlet and the disengagement fluid inlet are coupled in fluid flow communication with one another,
wherein the disengaged liquid outlet and the fluid inlet of the polyesterification reaction vessel are coupled in fluid flow communication with one another, and
wherein the disengaged liquid outlet and the exchanger inlet are coupled in fluid flow communication with one another.