NOVEL DICARBANIONIC INITIATOR, A PROCESS FOR THE PREPARATION AND USE THEREOF

Abstract

The present invention provides a novel dicarbanionic initiator of formula (I).

Description

Claims

1. A novel dicarbanionic initiator of formula (I).

2. A process for the preparation of dicarbanionic initiator of formula (I) which comprises reacting 1-bromo-4-(4′-bromophenoxy)-2-pentadecyl benzene of formula (II)

3. A process as claimed in claim 2, wherein the freeze dried 1-bromo-4-(4′-bromophenoxy)-2-pentadecyl benzene is first mixed with a non polar solvent followed by the addition of alkyllithium compound.

4. A process as claimed in claim 2, wherein the alkyllithium compound used is represented by the general formula R1Li, wherein R1 is a primary, secondary or tertiary alkyl, containing 2 to 20 carbon atoms per molecule.

5. A process as claimed in claim 2, wherein the alkyllithium used is selected from the group consisting of ethyllithium, n-propyllithium isopropyllithium, n-butyllithium, sec-butyllithium, tert-butyllithium, pentyllithium, hexyllithium and tert-octyllithium.

6. A process as claimed in claim 2, wherein the non polar solvent used is selected from the group consisting of benzene, toluene and cyclohexane.

7. A process for the preparation of α,ω-difunctional polymer and triblock copolymer using dicarbanionic initiator of formula (I), the said process comprising the steps of: (a) polymerizing the monomer by using dicarbanionic initiator of formula (I) in a non polar solvent, at a temperature in the range of 5 to 250 C, for a period of about 24 hours to obtain the desired α,ω-difunctional polymer in solution,(b) capping the above said polymerization reaction by adding excess of ethylene oxide and deactivating the reaction by using degassed acidic methanol, followed by concentrating the reaction mixture and precipitating out the desired product of α,ω-difunctional polymer by using methanol; OR(c) further, copolymerizing α,ω-difunctional polymer obtained in step (a) with styrene by adding styrene to the reaction mixture obtained in step (a) and diluting it with a mixture of non polar solvent and allowing the reaction to continue for a period of 2-6 hours, at a temperature in the range of 20 to 300 C, followed by capping, degassing, concentrating and precipitation of the desired triblock copolymer by same process as given in step (b).

8. A process as claimed in claim 7, wherein the non polar solvent used in step (a) is selected from the group consisting of benzene, toluene and cyclohexane.

9. A process as claimed in claim 7, wherein the mixture of non polar solvent used in step (c) is a mixture of cyclohexane and tetrahydrofuran.

10. A process as claimed in claim 9, wherein the concentration of tetrahydrofuran in a mixture of cyclohexane and tetrahydrofuran is about 1 vol %.

11. A process as claimed in claim 7, wherein the α,ω-difunctional polymer obtained is selected from α,ω-difunctional polybutadienes, polyisoprenes and polystyrenes.

12. A process as claimed in claim 7, wherein the triblock copolymer obtained is selected from styrene-butadiene-styrene and styrene-isoprene-styrene.

13. A process as claimed in claim 7, wherein the yield of α,ω-difunctional obtained is in the range of 98 to 99%.

14. A process as claimed in claim 7, wherein the yield of styrene-butadiene-styrene obtained is in the range of 98 to 99%.

15. A process as claimed in claim 7, wherein the yield of styrene-isoprene-styrene is 97 to 98%.