IP Library Granted Patent US 9,079,170
Granted Patent B2
US 9,079,170 · App. 13/579,649 · Granted Jul 14, 2015

Method for producing diaryl carbonate

Inventors: Budianto Nishiyama (Tokyo, JP); Nobuhisa Miyake (Tokyo, JP)
Assignee: Asahi Kasei Chemicals Corporation
B01J31/0214B01J31/0252C07C68/06B01J2531/42B01J2531/46
View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 9,079,170
App. No.
13/579,649
Granted
Jul 14, 2015
Kind
B2
Abstract

The present invention provides a method for continuously producing a diaryl carbonate stably for a long time with high productivity. The method for producing a diaryl carbonate according to the present invention comprises a step (1) of obtaining an alkylaryl carbonate; a step (2) of obtaining a reaction product from the alkylaryl carbonate; a step (3) of separating the diaryl carbonate and a high boiling component from the reaction product; and a step (4) of recycling the high boiling component into the steps (1) and/or (2), wherein the high boiling component recycled in the step (4) includes a particular compound, and the particular compound satisfies a particular condition.

Claims (65)

1. A method for producing a diaryl carbonate, using a metal-containing catalyst composition as a reaction catalyst, comprising:

a step (1) of subjecting a dialkyl carbonate and an aromatic monohydroxy compound to a transesterification reaction so as to obtain an alkylaryl carbonate, and removing an alcohol as by-product from a reaction system;

a step (2) of subjecting the alkylaryl carbonate obtained in the step (1) to a transesterification or disproportionation reaction so as to obtain a reaction product including the diaryl carbonate;

a step (3) of distilling the reaction product obtained in the step (2) to separate the reaction product into a low boiling component including the diaryl carbonate and a high boiling component including the reaction catalyst; and

a step (4) of recycling the high boiling component separated in the step (3) into the steps (1) and/or (2),

wherein:

the high boiling component separated in the step (3) includes 70% by mass or less of a component having a higher boiling point than that of the diaryl carbonate;

the high boiling component separated in the step (3) includes a compound represented by the formula (1):

wherein Ar 1 represents an unsubstituted or substituted arylene group having 6 to 20 carbon atoms, X and Y—O are located at an ortho position to each other, X represents a hydroxy group or a substituent given by the formula (2) or (3), and Y represents hydrogen or a substituent given by the formula (3), the formulas (2) and (3) being as follows:

wherein R 1 represents a linear or branched aliphatic group having 1 to 12 carbon atoms, an alicyclic aliphatic group having 5 to 12 carbon atoms, or an unsubstituted or substituted aryl group having 6 to 20 carbon atoms; and

the high boiling component recycled in the step (4) includes compounds given by (i) to (iii):

(i) a compound of the formula (1) where X represents the formula (2) or (3), and Y represents the formula (3);

(ii) a compound of the formula (1) where X represents a hydroxy group, and Y represents the formula (3), and/or a compound of the formula (1) where X represents the formula (3), and Y represents hydrogen;

(iii) a compound of the formula (1) where X represents a hydroxy group, and Y represents hydrogen;

the compounds of (i) to (iii) satisfying conditions given by (iv) to (vi), respectively:

(iv) total moles of the compounds of (i)/moles of metal atoms is 0.005 to 20;

(v) total moles of the compounds of (ii)/moles of metal atoms is 0.005 to 4; and

(vi) moles of the compound of (iii)/moles of metal atoms is less than 2.

2. The method for producing the diaryl carbonate according to claim 1 , wherein the metal-containing catalyst composition is a titanium-containing catalyst composition.

3. The method for producing the diaryl carbonate according to claim 2 , wherein the titanium-containing catalyst composition is a titanium-containing composition formed of a diaryl carbonate and an aryloxytitanium composition, and titanium constituting the aryloxytitanium composition has a content of 0.1 to 20% by mass based on 100% by mass of the titanium-containing composition.

4. The method for producing the diaryl carbonate according to claim 3 , wherein the titanium constituting the aryloxytitanium composition is tetravalent.

5. The method for producing the diaryl carbonate according to claim 3 , wherein the aryloxytitanium composition has 1 or more and 4 or less aryloxy groups per titanium atom.

6. The method for producing the diaryl carbonate according to claim 3 , wherein the aryloxytitanium composition is phenoxytitanium.

7. The method for producing the diaryl carbonate according to claim 1 , wherein a reaction solvent is used in the steps (1) and/or (2), and the metal-containing catalyst composition is soluble in the reaction solvent or forms a homogeneous phase with the reaction solvent.

8. The method for producing the diaryl carbonate according to claim 1 , wherein at least one of the compounds of formula (1) is selected from a group of compounds represented by the following formulas (4) to (8):

wherein Ar 2 represents an unsubstituted or substituted arylene group having 6 to 20 carbon atoms, Ar 3 represents an unsubstituted or substituted aryl group having 6 to 20 carbon atoms, and two substituents on Ar 2 are located at an ortho position to each other;

wherein Ar 4 represents an unsubstituted or substituted arylene group having 6 to 20 carbon atoms, R 2 represents a linear or branched aliphatic group having 1 to 12 carbon atoms, or an alicyclic aliphatic group having 5 to 12 carbon atoms, and two substituents on Ar 4 are located at an ortho position to each other;

wherein Ar 5 represents an unsubstituted or substituted arylene group having 6 to 20 carbon atoms, and two hydroxy groups on Ar 5 are located at an ortho position to each other;

wherein Ar 6 represents an unsubstituted or substituted arylene group having 6 to 20 carbon atoms, Ar 7 and Ar 8 each independently represent an unsubstituted or substituted aryl group having 6 to 20 carbon atoms, and two substituents on Ar 6 are located at an ortho position to each other; and

wherein Ar 9 represents an unsubstituted or substituted arylene group having 6 to 20 carbon atoms, Ar 10 represents an unsubstituted or substituted aryl group having 6 to 20 carbon atoms, R 3 represents a linear or branched aliphatic group having 1 to 12 carbon atoms, or an alicyclic aliphatic group having 5 to 12 carbon atoms, and two substituents on Ar 9 are located at an ortho position to each other.

9. The method for producing the diaryl carbonate according to claim 1 , wherein the steps (1) and/or (2) is performed in the presence of a composition A comprising a diaryl carbonate, an aryloxytitanium composition, and a compound represented by the following formulas (X) and/or (Y), and

the composition A has a ratio of total moles of the compounds represented by the following formulas (X) and (Y) to moles of titanium atoms (a total of the compounds represented by the formulas (X) and (Y)/titanium atoms) from 0.005 to 4, the formulas (X) and (Y) being:

wherein Ar 21 represents an unsubstituted or substituted arylene group having 6 to 20 carbon atoms, Ar 22 represents an unsubstituted or substituted aryl group having 6 to 20 carbon atoms, and two substituents on Ar 21 are located at an ortho position to each other; and

wherein Ar 23 represents an unsubstituted or substituted arylene group having 6 to 20 carbon atoms, Ar 24 and Ar 25 each independently represent an unsubstituted or substituted aryl group having 6 to 20 carbon atoms, and two substituents on Ar 23 are located at an ortho position to each other.

10. The method for producing the diaryl carbonate according to claim 9 , wherein in the steps (1) and/or (2), obtaining the alkylaryl carbonate and/or production of the diaryl carbonate is started by feeding the composition A.

11. The method for producing the diaryl carbonate according to claim 1 , further comprising

sampling the high boiling component recycled in the step (4),

adding a monodentate or polydentate ligand capable of coordination to the metal atoms, to the sampled high boiling component at 1 equivalent or more with respect to titanium atoms therein so as to prepare an analysis sample, and

analyzing the analysis sample to quantify the compounds given by (i) to (iii) included in the high boiling component.

12. The method for producing the diaryl carbonate according to claim 11 , further comprising

performing control so that the compounds given by (i) to (iii) included in the high boiling component recycled in the step (4) not extend beyond the conditions of (iv) to (vi), respectively,

after the step of quantifying the compounds given by (i) to (iii) according to claim 10 .

13. The method for producing the diaryl carbonate according to claim 1 , further comprising

sampling the high boiling component recycled in the step (4),

adding at least one additive to the sampled high boiling component at 1 equivalent or more with respect to the metal atoms therein so as to prepare an analysis sample, the additive being selected from the group consisting of water, polyhydroxy compounds, nitrogen-containing heterocyclic compounds, sulfur-containing heterocyclic compounds, fluorine-substituted alcohols, and fluorine-substituted organic acids, and

analyzing the analysis sample by gas or liquid chromatography so as to quantify the compounds given by (i) to (iii) included in the high boiling component.

14. The method for producing the diaryl carbonate according to claim 1 , wherein the dialkyl carbonate used in the step (1) is a compound represented by the formula (9):

wherein R 4 represents a linear or branched aliphatic group having 1 to 12 carbon atoms, or an alicyclic aliphatic group having 5 to 12 carbon atoms,

the aromatic monohydroxy compound used in the step (1) is a compound represented by the formula (10):

Ar 11 —OH  (10)

wherein Ar 11 represents an unsubstituted or substituted aryl group having 6 to 20 carbon atoms,

the alkylaryl carbonate obtained in the step (1) is a compound represented by the formula (11):

wherein R 5 represents a linear or branched aliphatic group having 1 to 12 carbon atoms, or an alicyclic aliphatic group having 5 to 12 carbon atoms, and Ar 12 represents an unsubstituted or substituted aryl group having 6 to 20 carbon atoms, and

the diaryl carbonate obtained in the step (2) is a compound represented by the formula (12):

wherein Ar 13 represents an unsubstituted or substituted aryl group having 6 to 20 carbon atoms.

15. The method for producing the diaryl carbonate according to claim 14 , wherein R 4 in the formula (9) is an aliphatic alkyl group having 1 to 8 carbon atoms.

16. The method for producing the diaryl carbonate according to claim 1 , wherein the reactions in the steps (1) and (2) are performed using a reaction apparatus comprising at least one selected from the group consisting of an agitation tank, an agitation tank with multistage impellers, a packed column, a distillation column, a multistage distillation column, a continuous multistage distillation column, a reactor comprising an internal support, and a forced circulation reactor.

17. The method for producing the diaryl carbonate according to claim 16 , wherein in the step (1), the dialkyl carbonate and the aromatic monohydroxy compound are continuously fed to the reaction apparatus, and

in the step (2), the reaction product obtained is continuously removed from the reaction apparatus.

18. The method for producing the diaryl carbonate according to claim 1 , wherein the metal atoms in the metal-containing catalyst composition in the step (1) or (2) have a content of 0.0001 to 20% by mass.

19. The method for producing the diaryl carbonate according to claim 1 , wherein the steps (1) and (2) have a reaction temperature of 150 to 300° C., and a reaction time of 0.05 to 50 hr.

20. The method for producing the diaryl carbonate according to claim 1 , wherein the distillation in the step (3) is performed by a distillation column,

the distillation column has a temperature of 150 to 300° C. at a column bottom, and

the distillation column provides a residence time of 0.02 to 100 hr at a column bottom.

21. The method for producing the diaryl carbonate according to claim 1 , wherein the diaryl carbonate is diphenyl carbonate.

Assignments (2)
MERGER Recorded Jul 13, 2016
From: ASAHI KASEI CHEMICALS
To: ASAHI KASEI KABUSHIKI KAISHA
Reel/Frame 039321/0670 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 17, 2012
From: NISHIYAMA, BUDIANTO; MIYAKE, NOBUHISA
To: ASAHI KASEI CHEMICALS CORPORATION
Reel/Frame 028805/0580 →
Priority Claims (2)
JP 2010-037928 · Feb 23, 2010 · national
JP 2010-037930 · Feb 23, 2010 · national
Continuity (1)
Related Publication 20120316357A1 · Dec 13, 2012