Apparatus, systems, and methods for purification of isocyanate mixtures
The present disclosure relates, according to some embodiments, to apparatus, systems, and/or methods for fractionating a feed mixture comprising, for example, one or more isocyanates, light components, solvents and/or heavier components. In some embodiments, fractionating an isocyanate feed mixture may comprise distilling the feed mixture in a non-adiabatic fractionating apparatus comprising a prefractionating section and/or column and a main section and/or column, which comprises a rectification section, a side section, and a stripping section. For example, isocyanates may be separated from light component(s), solvent(s) and/or heavier component(s). A fractionating apparatus may be configured and arranged, in some embodiments, as a dividing wall column. According to some embodiments of the disclosure, apparatus, systems, and/or methods may be energy efficient and/or may have a broad operating range.
1. A method for fractionating an isocyanate feed mixture comprising a light component comprising lights and solvent, a middle-boiling component comprising an isocyanate, and a heavy boiling component comprising other components of the feed mixture heavier than light, solvent, and isocyanate, using a fractionating apparatus comprising a prefractionating section, a rectification section, a stripping section, and a side section, the method comprising:
(a) moving the isocyanate feed mixture after stripping in a stripping section into the prefractionating section,
(b) warming the contents of the prefractionating section and forming a prefractionating section vapor stream PS VS and a prefractionating section liquid stream PS LS by heating at least a portion of the prefractionating section liquid stream PS LS in at least one external reboiler,
(c) moving at least a portion of the prefractionating section vapor stream PS VS to the rectification section,
(d) cooling the contents of the rectification section to form a rectification section vapor product stream RS VPS and a condensate liquid,
(e) removing from the fractionating apparatus at least a portion of the rectification section vapor product stream RS VPS ,
(f) removing from the fractionating apparatus at least a portion of the condensate liquid as a rectification section liquid product stream RS LPS ,
(g) removing from the rectification section at least a portion of the condensate liquid as a rectification section liquid stream RS LS ,
(h) moving at least a portion of the rectification section liquid stream RS LS to the side section,
(i) moving at least a portion of the rectification section liquid stream RS LS to the prefractionating section,
(j) heating at least a portion of the prefractionating section liquid stream PS LS to form a second prefractionating section vapor stream sPS VS and a second prefractionating section liquid stream sPS LS and combining each with their respective first streams,
(k) moving at least a portion of the prefractionating section liquid stream PS LS from the prefractionating section to the stripping section,
(l) heating the contents of the stripping section to form a stripping section vapor stream SS VS and a stripping section lower product stream SS LPS ,
(m) removing from the fractionating apparatus at least a portion of the stripping section liquid product stream SS LPS ,
(n) moving at least a portion of the stripping section vapor stream SS VS to the side section,
(o) commingling at least a portion of the rectification section liquid stream RS LS and at least a portion of the stripping section vapor stream SS VS in the side section under conditions that permit formation of a side section vapor stream SdS VS , a side section liquid product stream SdS LPS , and a side section liquid stream SdS LS ,
(p) removing from the fractionating apparatus at least a portion of the side section liquid product stream SdS LPS ,
(q) moving at least a portion of the side section vapor stream SdS VS to the rectification section, and
(r) moving at least a portion of the side section liquid stream SdS LS to the stripping section,
wherein the concentration of the light component in the isocyanate feed mixture is from about 5 weight percent or molar percent to about 90 weight percent or molar percent,
the concentration of the middle-boiling component in the isocyanate-containing feed mixture is from about 2 weight percent or molar percent to about 95 weight percent or molar percent, and
the concentration of the heavy boiling component in the isocyanate-containing feed mixture is from about 0.1 weight percent or molar percent to about 50 weight percent or molar percent, with the proviso that the concentration of the light component is (i) higher than the middle-boiling component and (ii) higher than the heavy boiling component.
2. A method for fractionating an isocyanate feed mixture according to claim 1 , wherein the middle-boiling component comprises less than about 20 weight percent of the isocyanate feed mixture.
3. A method for fractionating an isocyanate feed mixture according to claim 1 , wherein the weight or molar ratio of the side section liquid product stream SdS LPS to the isocyanate feed mixture is more than about 20%.
4. A method for fractionating an isocyanate feed mixture according to claim 1 , wherein the side section liquid product stream SdS LPS comprises an isocyanate.
5. A method for fractionating an isocyanate feed mixture according to claim 1 , wherein the side section liquid product stream SdS LPS comprises toluene diisocyanate.
6. A method for fractionating an isocyanate feed mixture according to claim 1 , wherein the side section liquid product stream SdS LPS consists of one or more isocyanates.
7. A method for fractionating an isocyanate feed mixture according to claim 1 , wherein (j) heating at least a portion of the prefractionating section liquid stream PS LS to form a second prefractionating section vapor stream sPS VS and a second prefractionating section liquid stream sPS LS comprises heating at least a portion of the prefractionating section liquid stream PS LS in at least one internal reboiler or in at least one external reboiler.
8. A method for fractionating an isocyanate feed mixture according to claim 1 , wherein the prefractionating section, the rectification section, the stripping section, and the side section form a non-adiabatic dividing wall column.
9. A method for fractionating an isocyanate feed mixture according to claim 1 , wherein (i) moving at least a portion of the rectification section liquid stream RS LS to the prefractionating section further comprises:
moving the at least a portion of the rectification section liquid stream RS LS to the prefractionating section, wherein the weight or molar ratio of the at least a portion of the rectification section liquid stream RS LS to the prefractionating section vapor stream PS VS is from about 0 to about 0.75.
10. A method for fractionating an isocyanate feed mixture according to claim 1 further comprising (s) moving at least a portion of the stripping section vapor stream to the prefractionating section.
11. A method for fractionating an isocyanate feed mixture according to claim 10 , wherein (s) moving at least a portion of the stripping section vapor stream SS VS to the prefractionating column further comprises:
moving the at least a portion of the stripping section vapor stream SS VS to the prefractionating section, wherein the weight or molar ratio of the at least a portion of the stripping section vapor stream SS VS to the prefractionating section liquid stream PS LS is from about 0.01 to about 0.5.
12. A method for fractionating an isocyanate feed mixture according to claim 1 further comprising maintaining a pressure in the prefractionating section that is higher than the pressure in the rectification section.
13. A method for fractionating an isocyanate feed mixture according to claim 1 further comprising maintaining a pressure in the fractionating apparatus that is less than atmospheric pressure.
14. A method for fractionating an isocyanate feed mixture according to claim 1 further comprising maintaining at least a portion of the fractionating apparatus at a temperature of from about 50° C. to about 250° C.
15. A method for fractionating an isocyanate feed mixture according to claim 8 , wherein the non-adiabatic fractionating apparatus consumes from about 0.4 to about 1.0 kilowatts per kilogram of isocyanate produced in the side section liquid product stream SdS LPS .
16. A method for fractionating an isocyanate feed mixture according to claim 8 , wherein the non-adiabatic fractionating apparatus consumes less than about 0.4 kilowatts per kilogram of isocyanate produced in the side section liquid product stream SdS LPS .