Supported quaternary phosphonium catalyst, preparation and use thereof

1. A process for producing a supported quaternary phosphonium catalyst, comprising a step of reacting a tertiary phosphine of the following formula (2) with a macromolecular agent of the following formula (3), wherein the ratio by weight of the tertiary phosphine to the macromolecular agent is 1 to 20 : 80 to 99,

wherein R 1 , R 2 and R 3 are different from or identical to each other, and are each independently selected from the group consisting of a C 6-20 aryl, or a C 6-20 aryl substituted by one or more C 1-6 straight-chain or branched alkyl or C 2-6 straight-chain or branched alkenyl,

represents a covalent bond,

wherein X is a halogen atom, L is a bivalent bonding group,

 is one or more carrier selected from the group consisting of silica, zeolite, and kieselguhr,

represents a covalent bond, and

wherein the reaction temperature is 100 to 190 ° C., and the reaction duration is 10 to 40 h.

2. The process according to claim 1 , wherein the reaction temperature is 120 to 190 ° C., and the reaction duration is 10 to 30 h.

3. The process according to claim 1 , wherein the macromolecular agent is produced by a reaction between the carrier and a halogenation agent of the following formula (4), wherein the ratio by weight of the halogenation agent to the carrier is 0.005 to 0.15: 1,

wherein X is a halogen atom, L is a bivalent bonding group, M is Ti, Si or Zr. R 4 , R 5 and R 5 are different from or identical to each other, and each independently represents a C 1-4 straight-chain or branched alkoxy.

4. The process according to claim 3 , wherein in the reaction between the carrier and the halogenation agent, the reaction temperature is 70 to 140° C., and the reaction duration is 1 to 60h.

5. The process according to claim 3 , wherein said X is Cl, and the process further comprises a step of contacting the macromolecular agent with one or more modifying agent selected from the group consisting of a bromination agent and an iodization agent before reacting the macromolecular agent with the tertiary phosphine, wherein the ratio by weight of the modifying agent to the macromolecular agent is 0.01 to 1:1.

6. The process according to claim 1 , wherein the ratio by weight of the tertiary phosphine to the macromolecular agent is 1 to 15:85 to 99, and in formula (3), L is a bivalent bonding group selected from the group consisting of an optionally substituted C 1-20 straight-chain or branched alkylene, an optionally substituted C 2-20 straight-chain or branched alkenylene, or an optionally substituted C 2-20 straight-chain or branched alkynylene, wherein the alkylene, the alkenylene or the alkynylene is optionally interfered by one or more interfering group selected from the group consisting of —O—, —S—, —NR a —(R a is a C 1-4 alkyl), and phenylene.

7. The process according to claim 6 , wherein in formula (3), L is a C 2-8 straight-chain alkylene.

8. The process according to claim 3 , wherein the ratio by weight of the halogenation agent to the carrier is 0.01 to 0.1:1, and in formula (4), L is a bivalent bonding group selected from the group consisting of an optionally substituted C 1-20 straight-chain or branched alkylene, an optionally substituted C 2-20 straight-chain or branched alkenylene, or an optionally substituted C 2-20 straight-chain or branched alkynylene, wherein the alkylene, the alkenylene or the alkynylene is optionally interfered by one or more interfering group selected from the group consisting of —O—, —S—, —NR a —(R a is a C 1-4 alkyl), and phenylene.

9. The process of claim 1 , wherein the supported quaternary phosphonium catalyst comprises the following average molecular structure (I):

wherein X is a halogen atom, R 1 , R 2 and R 3 are different from or identical to each other, and are each independently selected from the group consisting of a C 6-20 aryl, or a C 6-20 aryl substituted by one or more C 1-6 straight-chain or branched alkyl or C 2-6 straight-chain or branched alkenyl, L is a bivalent bonding group,

 is one or more carrier selected from the group consisting of silica, zeolite, and kieselguhr,

represents a covalent bond,

• represents an ionic bond,

n is an averaged number such that the ratio by weight of the moiety

 to the moiety

 is 1 to 25:75 to 99.

10. The process of claim 9 , wherein the supported quaternary phosphonium catalyst has an elution loss D of less than 1%, wherein the elution loss D is determined according to a method comprising weighting 2g of the supported quaternary phosphonium catalyst with a P content of P1 (unit: wt %), (1) suspending the supported quaternary phosphonium catalyst in 40ml methanol, stirring (at a stirring speed of 100 rpm) the resultant at 100° C. for 4h, then immediately filtering the resultant so as to separate the supported quaternary phosphonium catalyst, (2) then, suspending the separated supported quaternary phosphonium catalyst in 40ml methanol, stirring (at a stirring speed of 100 rpm) the resultant at 100° C. for 4h, then immediately filtering the resultant so as to separate the supported quaternary phosphonium catalyst, repeating the process (2) for further 10 times, and then determining the P content of the finally separated supported quaternary phosphonium catalyst as P2 (unit: wt %), and then calculating the elution loss D as follows:

D =( P 1- P 2)/ P 1×100%.

11. The process of claim 1 , wherein the reaction temperature is 190 ° C.

12. The process according to claim 9 , wherein in the average molecular structure (I), L is a bivalent bonding group selected from the group consisting of an optionally substituted C 1-20 straight-chain or branched alkylene, an optionally substituted C 2-20 straight-chain or branched alkenylene, or an optionally substituted C 2-20 straight-chain or branched alkynylene, wherein the alkylene, the alkenylene, or the alkynylene is optionally interfered by one or more interfering group selected from the group consisting of —O—, —S—, —NR a —(R a is a C 1-4 alkyl) and phenylene, and the ratio by weight of the moiety

 to the moiety

 is 1 to 20:80 to 99.

13. The process according to claim 12 , wherein in the average molecular structure (I), L is a C 2-8 straight-chain alkylene.

14. The process according to claim 10 , wherein the supported quaternary phosphonium catalyst has an elution loss D of less than 0.5%.

15. A process for producing a dialkyl carbonate, comprising:

producing a supported quaternary phosphoniim catalyst by reacting a tertiary phosphine of the following formula (2) with a macromolecular agent of the following formula (3), wherein the ratio by weight of the tertiary phosphine to the macromolecular agent is 1 to 20:80 to 99.

wherein R 1 , R 2 and R 3 are different from or identical to each other, and each independently slelcted from the group consisting of a C 6-20 aryl, or a C 6-20 aryl substituted by one or more C 1-6 straight-chain or branched alky or C 2-6 straight-chain or branched atkenyl,

represents a covalent bond.

wherein X is a halogen atom, L is a bivalent bonding group,

 is one or more carrier selected from the group consisting of silica, zeolite, and kieselguhr,

represents a covalent bond, and

wherein the reaction temperature is 100 to 190 ° C., and the reaction duration is, 10 to 40 h; and

contacting a C 2-10 alkylene carbonate with a monohydric C 1-10 alkanol in the presence of the supported quaternary phosphonium catalyst.

16. The process according to claim 15 , wherein in the step of contacting the C 2-10 alkylene carbonate with the monohydric C 1-10 alkanol in the presence of the supported quaternary phosphonium catalyst, the reaction temperature is 60 to 140 ° C, the reaction duration is 0.1 to 20 h, the ratio by mol of the monohydric C 1-10 alkanol to the C 2-10 alkylene carbonate is 2 to 10:1, and the ratio by weight of the supported quaternary phosphonium catalyst to the C 2-10 alkylene carbonate is 0.005 to 0.5:1.

17. The process of claim 15 , wherein the supported quaternary phosphonium catalyst comprises the following average molecular structure (I):

wherein X is a halogen atom, R 1 , R 2 and R 3 are different from or identical to each other, and are each independently selected from the group consisting of a C 6-20 aryl, or a C 6-20 aryl substituted by one or more C 1-6 straight-chain or branched alkyl or C 2-6 straight-chain or branched alkenyl, L is a bivalent bonding group,

 is one or more carrier selected from the group consisting of silica, zeolite, and kieselguhr,

represents a covalent bond,

• represents an ionic bond,

n is an averaged number such that the ratio by weight of the moiety

 to the moiety

 is 1 to 25:75 to 99.

18. The process according to claim 17 , wherein in the average molecular structure (I), L is a bivalent bonding group selected from the group consisting of an optionally substituted C 1-20 straight-chain or branched alkylene, an optionally substituted C 2-20 straight-chain or branched alkenylene, or an optionally substituted C 2-20 straight-chain or branched alkynylene, wherein the alkylene, the alkenylene or the alkynylene is optionally interfered by one or more interfering group selected from the group consisting of —O—, —S—, —NR a —(R a is a C 1-4 alkyl) and phenylene, and the ratio by weight of the moiety

 to the moiety

 is 1 to 20:80 to 99.

19. The process according to claim 18 , wherein in the average molecular structure (I), L is a C 2-8 straight-chain alkylene.

20. The process according to claim 17 , wherein the supported quaternary phosphonium catalyst has an elution loss D of less than 1%, wherein the elution loss D is determined according to a method comprising weighting 2 g of the supported quaternary phosphonium catalyst with a P content of P1 (unit: wt %), (1) suspending the supported quaternary phosphonium catalyst in 40 ml methanol, stirring (at a stirring speed of 100 rpm) the resultant at 100° C. for 4 h, then immediately filtering the resultant so as to separate the supported quaternary phosphonium catalyst, (2) then, suspending the separated supported quaternary phosphonium catalyst in 40 ml methanol, stirring (at a stirring speed of 100 rpm) the resultant at 100° C. for 4 h then immediately filtering the resultant so as to separate the supported quaternary phosphonium catalyst, repeating the process (2) for further 10 times, and then determining the P content of the finally separated supported quaternary phosphonium catalyst as P2 (unit: wt %), and then calculating the elution loss D as follows:

D =( P 1- P 2)/ P 1 ×100%

21. The process according to claim 20 , wherein the supported quaternary phosphonium catalyst has an elution loss 0 of less than 0.5%.

22. The process of claim 15 , wherein in the reaction between the tertiary phosphine of formula (2) and the macromolecular agent of formula (3) the reaction temperature is 190 ° C.