Synthesis of alkylene carbonates using a catalyst system comprising metal halide and pyridine or pyridine derivative

Abstract

The present invention relates to a method to prepare alkylene carbonate of the formula (1) 1

Description

BACKGROUND OF THE INVENTION

[0001] 1. Field of the Invention

[0002] The present invention relates to a preparation method of an alkylene carbonate by reacting alkylene oxide and carbon dioxide in the presence of a catalyst system comprising metal halide and pyridine or pyridine derivative.

[0003] 2. Description of the Background Art

[0004] Alkylene carbonates are used in polycarbonate synthesis, as a solvent for polymer electrolyte, an intermediate in pharmaceutical process, an oxyaikylation agent in dyestuff synthesis, a protectant in processing plant and a solvent in textile production process

[0005] Alkylene carbonate has been prepared by reacting carbon dioxide and alkylene oxide in the presence of a catalyst, represented in Scheme 1. 2

[0006] wherein, R1 and R2 are each independently H, C1-C4 alkyl or phenyl group.

[0007] In the above reaction, however, there is a limitation that alkylene oxide either decomposes or polymerizes at higher reaction temperatures.

[0008] Many catalysts have been developed including inorganic salts, phosphonium halide and ammonium halides. For instance, Japanese Laid-Open Patent No S59-13776 introduced a method of using tetraalkyl halide such as tributyl methyl phosphonium iodide as a catalyst. Japanese Laid-Open Patent No. H9-67365 introduced a method of using KI as a catalyst and Japanese Laid-Open Patent No. H9-235252 describes a method of using polystyrene copolymer containing quaternary phosphonium groups.

[0009] These patents claim that the product yield is 50-95 % when the reaction is performed at 100-170 ° C. for 1-5 hours. However, in order to produce alkylene carbonate in high yield, long reaction time and high reaction temperature are required. Also the water content in the raw materials, carbon dioxide and alkylene oxide has to be reduced to than a few hundred ppms.

[0010] Japanese Laid-Open Patent No. H9-206846 introduced a method of using an ion change resin substituted with the catalysts such as CsOH, RbOH and ammonium halides. In U.S. Pat. No. 4,233,221, a method of using DOWEX and Amberlite ion exchange resin was reported with a low yield of 30-80% at 80-100° C.

[0011] Besides the above-mentioned materials, a phthalocyanine complex containing Co, Cr, Fe, Mn, Ni, Ti, V, or Zr has been used as catalysts. Also in Japanese Laid-Open Patent No. H7-206547, a catalyst system using a heteropolyacid whose hydrogen ion is substituted by Rubidium or Cesium ion was introduced. These two cases, however, require expensive catalysts with low yield of 30-90 % at relatively high reaction temperature of 120-180° C.

[0012] As mentioned above, the catalysts disclosed in the above arts have one or more problems in terms of activity, reaction condition, cost, water sensitivity, etc.

SUMMARY OF THE INVENTION

[0013] Therefore the object of the present invention is to provide a method of producing alkylene carbonate with a high yield in a short reaction time under mild reaction conditions.

[0014] As a result of the efforts made to achieve the above aim, the present inventors have found that a catalyst system comprising pyridines and metal halide compounds is more effective than the conventional catalyst system in producing alkylene carbonates by reacting alkylene oxide and carbon dioxide.

DETAlLED DESCRIPTION OF THE PREFERRED EMBODIMENTS

[0015] The present invention provide a method to prepare alkylene carbonate of the formula (1) 3

[0016] wherein, each of R1 and R2 is independently H, C1-C4 alkyl or phenyl group;

[0017] which method characterized by reacting alkylene oxide with carbon dioxide In the presence of a catalyst system comprising a) metal halide [MXm] and b) pyridine or pyridine derivative [Py], wherein Py is selected from a group of pyridines; M is a metal atom selected from the group consisting of Zn, Fe, Mn, Pb and In; X is a halogen selected from the group consisting of Cl, Br and I; and m is 2 or 3.

[0018] The pyridine derivatives include the compounds having the structures of the formulae (2), (3) or (4), and a copolymer between polyvinyl pyridine (PVP) and polyvinyl pyridine 4

[0019] wherein R3, R4 and R5 are each independently H, C1-C4 alkyl or phenyl; each of x, y and z is independently an integer from 0 to 3; and c is an integer from 2 to 4.

[0020] The molar ratio of pyridine [Py] to metal halide [MXm] is 10:1˜1:5, and more preferably 3:2˜1:1.

[0021] The amount of metal halide is preferably 0.005˜0.1 moles per mole of alkylene oxide. In case the amount of the metal halide used is less than 0.005 mol reaction becomes too slow. And in case the amount of the catalyst is more than 0.1 mol, the reaction rate and selectivity do not improve any further.

[0022] Considering the equipment and operating cost, it is preferable to operate a reaction at a pressure of 10-100 atm.

[0023] The reaction temperature is preferably 60 ˜140° C. The reaction proceeds too slow at lower reaction temperature lower than 60° C. When the reaction temperature is too high, alkylene oxide either decomposes or undergoes a self-polymerization reaction and the reaction becomes non-specific.

[0024] Although the above reaction could be performed in the absence of the solvent, it is possible to use solvent to prevent excess heat production during the reaction. It is preferable to use aIlkylene carbonate that is produced from the raw material alkylene oxide as a solvent, For instance, ethylene carbonate is a preferable solvent when ethylene carbonate is synthesized from ethylene oxide and propylene carbonate is preferable when propylene carbonate is synthesized from propylene oxide.

[0025] The reaction could be performed by a batch process using the reactor provided with a stirrer or by a continuous process using a bubble column. The invention will be further illustrated by the following examples, but not limited to the examples given.

[0026] Example1.

[0027] A 200 ml high pressure reactor, ethylene oxide (16.80 g9 380 mmol), pyridine (158 mg, 2.0 mmol) and ZnBr2 (223 mg, 1.0 mmol) were charged and pressurized with 10 atm of carbon dioxide. After increasing the temperature to 100° C., carbon dioxide was introduced again up to the pressure of 30 atm

[0028] During the reaction, carbon dioxide was continuously supplied from a reservoir tank to maintain the pressure to 30 atm.

[0029] After the reaction for 1 hour, the volatile components were removed by nitrogen flush and the solid product was separated and weighed to be 315 g. The yield was analyzed 93.8 % by gas-liquid chromatography.

[0030] Examples 2-8

[0031] Alkylene carbonate was synthesized by using different metal halides under identical conditions as in Example 1 The molar ratio of pyridine and metal halides was fixed at 2 1 and the number of moles of the metal halide was set to 1 mmol The results are shown in Table 1. 1 TABLE 1 Example Metal halide compound Product weight (g) Yield (%) 2 FeBr2 27.6 82.1 3 FeBr3 27.0 80.3 4 ZnCl2 17.3 51.5 5 Znl2 32.4 96.4 6 MnBr2 26.2 78.1 7 Pbl2 23.5 70.0 8 InCl3 20.1 59.8

[0032] Examples 9-16

[0033] The process of Example 1 was repeated except that pyridine derivative was used in place of pyridine. The results are shown in Table 2. 2 TABLE 2 Example Pyridine compound Product weight (g) Yield (%)  9 2-methyl pyridine 31.3 93.2 10 2-ethyl pyridine 30.9 92.0 11 2-propyl pyridine 29.1 86.6 12 2-n-butyl pyridine 28.8 85.8 13 2-phenyl pyridine 28.6 85.3 14 1,2-bis(4-pyridyl) ethane 31.1 92.5 15 1,2-bis(2-pyridyl) ethane 30.5 90.7 16 Polyvinylpyridine 30.9 92.0

[0034] Example 17-23

[0035] The reaction was performed under the identical conditions as in Example 1 except that the molar ratio of pyndine to ZnBr2 was varied in the range 10:1˜1:5. The results are shown in Table 3. 3 TABLE 3 Example a:b Product weight (g) Yield (%) 17 10 1   28.6 85.3 18 5:1 31.0 92.2 19 2:1 31.0 92.4 20 1:1 31.0 92.4 21 1:2 30.4 90.6 22 1:3 30.6 91.1 23 1:5 29.4 87.4

[0036] Example 24-27

[0037] The reaction was performed under the identical condition as in Example 1 except that the reaction temperature was varied in the range 60 - 120° C. The results are in Table 4, 4 TABLE 4 Yield Example Reaction Temperature (° C.) Product weight (g) (%) 24 60 11.8 31.5 25 80 29.6 88.1 26 100 31.0 92.4 27 120 32.3 96.3

[0038] Example 28-30

[0039] The reaction was performed underthe identical conditions as in Example except that the reaction pressure was varied in the range 20-100 atm The results are shown in Table 5. 5 TABLE 5 Example Reaction Pressure (atm) Product weight (g) Yield (%) 28 20 30.0 90.2 29 50 31.2 92.9 30 100 32.0 95.3

[0040] Example 31-34

[0041] The reaction was performed under the identicail condition as in Example 1 except that the molar ratio of ZnBr2 to ethylene oxide was varied in the range 0.0005-0.1. The molar ratio of pyridine /ZnBr2 and the amount of ethylene oxide were fixed as 2:1and 16, 80 g (380mmol), respectively The results are shown in Table 6. 6 TABLE 6 ZnBr2/ethylene oxide Example (mole ratio) Product weight (g) Yield (%) 31 0.0005 23.5 70.1 32 0.001 31.0 92.2 33 0.01 32.9 98 1 34 0.1 33.3 99.2

[0042] Example 35-38

[0043] The reaction was performed under the identical condition as in Example 1 except that different kind of alkylene oxide was used, The result are shown in Table 7. 7 TABLE 7 Yield Example Alkylene oxide Product weight (g) (%) 35 Propylene oxide 36.3 93.5 36 2-methyl-1,2-epoxy propane 39.4 88.7 37 2,3-epoxy butane 38.9 87.6 38 Styrene oxide 56.6 90.8

[0044] Example 39-40

[0045] The reaction were performed under the identical condition as in Example 1 that ethylene carbonate or propylene carbonate was used as a solvent. The amount of the solvent used was 200 % of ethylene oxide by weight. The are shown in Table 8. 8 TABLE 8 Example Solvent Product weight (g) Yield (%) 39 Ethylene carbonate 30.9 92.1 40 Propylene carbonate 30.9 91.9

[0046] According to the present invention, alkylene carbonates can be synthesized in high yield under a mild reaction condition The catalyst of the present invention has several advantages in terms of economical point of view because it is inexpensive, highly active and reusable.

[0047] As the present invention may be embodied in several forms without departing from the spirit or essential characteristics thereof, it should also be understood that the abovedescribed embodiments are not limited by any of the details of the foregoing description, unless otherwise specified, but rather should be construed broadly within its spirit and scope as defined in the appended claims, and therefore all changes and modifications that fall within the meets and bounds of the claims, or equivalence of such meets and bounds are therefore intended to be embraced by the appended claims.

Claims

1. A method to prepare alkylene carbonate of the formula (1)

5

wherein, R1 and R2 are each independently H, C1-C4 alkyl or phenyl group;

which method characterized by reacting alkylene oxide with carbon dioxide in the presence of a catalyst system comprising a) metal halide [MXm] and b) pyridine or pyridine derivative [Py], wherein Py is selected from a group of pyridines; M is a metal atom selected from the group consisting of Zn, Fe, Mn, Pb and In; X is a halogen selected from the group consisting of Cl, Br and I; and m is 2 or 3.

2. The method according to claim 1, wherein the pyridine ligand Py has a structure selected from the group consisting of the formulae (2), (3) and (4)

6

wherein R3, R4 and R5 are each independently H, C1-C4 alkyl or phenyl; each of x, y and z is independently an integer from 0 to 3; and c is an integer from 2 to 4.

3. The method according to claim 1, wherein the molar ratio of [Py] to [MXm] is 10:1˜1:5.

4. The method according to claim 2, wherein the molar ratio of [Py] to [MXm] is 10:1˜1:5.

5 The method according to claim 3, wherein the molar ratio of [Py] [MXm] is 3:2˜1:1.

6. The method according to claim 4, wherein the mole ratio of [Py] to [MXm] is 3:2˜1:1.

7. The method according to claim 1, wherein the molar ratio of the catalyst to alkylene oxide is 0.0005˜0.1:1.

8. The method according to claim 2, wherein the molar ratio of the catalyst to alkylene oxide is 0.0005˜0.1:1.

9. The method according to claim 1, wherein the reaction temperature is 60- b 140° C.

10. The method according to claim 2, wherein the reaction temperature is 60-140° C.

11. The method according to claim 1, wherein the reaction pressure is 10˜100 atm.

12. The method according to claim 2, wherein the reaction pressure is 10˜100 atm.

13. The method according to claim 1, wherein solvent is not used in the reaction.

14. The method according to claim 2; wherein solvent is not used in the reaction.

15. The method according to claim 1, wherein the identical material to the produced alkylene carbonate is used as a solvent.

16. The method according to claim 2, wherein the identical material to the produced alkylene carbonate is used as a solvent.

17. The method according to claim 15, wherein the solvent is selected from ethylene carbonate and propylene carbonate.

18. The method according to claim 16, wherein the solvent is selected from ethylene carbonate and propylene carbonate.