IP Library Granted Patent US 7,825,059
Granted Patent B2
US 7,825,059 · App. 11/794,281 · Granted Nov 2, 2010

Process for preparing trioxepane composition and use thereof in crosslinking polymers

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Quick Facts
Patent No.
US 7,825,059
App. No.
11/794,281
Granted
Nov 2, 2010
Kind
B2
Abstract

Process to prepare a trioxepane compound of the following formula (I) comprising less than 3.5 wt % of dialkyl peroxide based on the total amount of peroxides, said process comprising the steps of reacting a glycol compound of the formula R 3 CHOH—CH 2 —C(CH 3 ) 2 OH with hydrogen peroxide in the presence of an acid to form a glycol hydroperoxide, purifying the glycol hydroperoxide, reacting the purified glycol hydroperoxide with a ketone or aldehyde of the formula R 1 R 2 CO in the presence of an acid to form the trioxepane compound, and purifying the trioxepane compound, wherein R 1 , R 2 , and R 3 are independently selected from hydrogen and a substituted or unsubstituted hydrocarbyl group, with the proviso that if R 1 and R 2 are both methyl groups, R 3 is not hydrogen. Initiator compositions comprising the so-prepared trioxepane compound are characterized by a high safe processing temperature in combination with a good crosslink efficiency.

Claims (27)

1. A process to prepare a trioxepane compound of the following formula (I)

comprising at least 1 ppm to less than 3.5 wt % of dialkyl peroxide based on the total amount of peroxides, said process comprising the steps of reacting a glycol compound of the formula R 3 CHOH—CH 2 —C(CH 3 ) 2 OH with hydrogen peroxide in the presence of an acid to form a glycol hydroperoxide, purifying the glycol hydroperoxide, reacting the purified glycol hydroperoxide with a ketone or aldehyde of the formula R 1 R 2 CO in the presence of an acid to form the trioxepane compound, and purifying the trioxepane compound, wherein R 1 , R 2 , and R 3 are independently selected from hydrogen and a substituted or unsubstituted hydrocarbyl group, with the proviso that if R 1 and R 2 are both methyl groups, R 3 is not hydrogen.

2. An initiator composition comprising a trioxepane compound of the formula (I)

and 1 ppm to 3.5 wt % of a dialkyl peroxide compound of the formula (II)

R 3 CHOH—CH 2 —C(CH 3 ) 2 —O—O—C(CH 3 ) 2 —CH 2 —CHOHR 3   (II)

based on the total amount of peroxides, wherein R 1 , R 2 , and R 3 are independently selected from hydrogen and a substituted or unsubstituted hydrocarbyl group, and optionally two of the group of R 1 , R 2 , and R 3 are linked to form a ring structure, and wherein if R 1 and R 2 in the trioxepane compound of formula (I) are both methyl groups, R 3 is not hydrogen.

3. The initiator composition according to claim 2 wherein R 1 and R 3 are selected from lower alkyl groups, such as methyl, ethyl, and isopropyl, R 2 is selected from hydrogen, methyl, ethyl, iso-propyl, iso-butyl, tert-butyl, amyl, iso-amyl, cyclohexyl, phenyl, CH 3 C(O)CH 2 —, C 2 H 5 OC(O)CH 2 —, HOC(CH 3 ) 2 CH 2 —, and

wherein R 4 is independently selected from any of the group of compounds given for R 1-3 .

4. A process to crosslink a crosslinkable polymer wherein a reaction mixture comprising the crosslinkable polymer is brought to a temperature suitable for starting the crosslink reaction of the crosslinkable polymer in the presence of an initiator composition of claim 2 .

5. The process according to claim 4 , wherein in the initiator composition, R 1 and R 3 are selected from lower alkyl groups, such as methyl, ethyl, and isopropyl, R 2 is selected from hydrogen, methyl, ethyl, iso-propyl, iso-butyl, tert-butyl, amyl, iso-amyl, cyclohexyl, phenyl, CH 3 C(O)CH 2 —, C 2 H 5 OC(O)CH 2 —, HOC(CH 3 ) 2 CH 2 —, and

wherein R 4 is independently selected from any of the group of compounds given for R 1-3 .

6. The process according to claim 4 , wherein the temperature is 160 to 500° C.

7. The process according to claim 6 , wherein the temperature is 170-400° C.

8. The process according to claim 4 , further comprising a step wherein a crosslinkable polymer is processed to a desired shape, to form a shaped article.

9. The process according to claim 8 , wherein the crosslinking step takes place simultaneously with or subsequent to the shaping step.

10. A process of modifying a polymer or copolymer comprising contacting the initiator composition of claim 2 with a polymeric material.

11. The process according to claim 10 , wherein contacting the initiator composition with the polymeric material is in the presence of free radicals thereby modifying the rheology of the polymer or copolymer.

12. The process according to claim 11 , wherein in the initiator composition is, R 1 and R 3 are selected from lower alkyl groups, such as methyl, ethyl, and isopropyl, R 2 is selected from hydrogen, methyl, ethyl, iso-propyl, iso-butyl, tert-butyl, amyl, iso-amyl, cyclohexyl, phenyl, CH 3 C(O)CH 2 —, C 2 H 5 OC(O)CH 2 —, HOC(CH 3 ) 2 CH 2 —, and

wherein R 4 is independently selected from any of the group of compounds given for R 1-3 .

13. The process according to claim 11 , wherein the polymer is polypropylene.

14. The process according to claim 10 , wherein contacting the initiator composition with the polymeric material is in the presence of a monomer thereby grafting monomers onto the polymer.

15. The process according to claim 14 , wherein in the initiator composition, R 1 and R 3 are selected from lower alkyl groups, such as methyl, ethyl, and isopropyl, R 2 is selected from hydrogen, methyl, ethyl, iso-propyl, iso-butyl, tert-butyl, amyl, iso-amyl, cyclohexyl, phenyl, CH 3 C(O)CH 2 —, C 2 H 5 OC(O)CH 2 —, HOC(CH 3 ) 2 CH 2 —, and

wherein R 4 is independently selected from any of the group of compounds given for R 1-3 .

16. The process according to claim 14 , wherein the polymer is polypropylene and the monomer is maleic anhydride.

17. A masterbatch comprising a crosslinkable polymer and an initiator composition of claim 2 .

18. The masterbatch according to claim 17 , wherein in the initiator composition, R 1 and R 3 are selected from lower alkyl groups, such as methyl, ethyl, and isopropyl, R 2 is selected from hydrogen, methyl, ethyl, iso-propyl, iso-butyl, tert-butyl, amyl, iso-amyl, cyclohexyl, phenyl, CH 3 C(O)CH 2 —, C 2 H 5 OC(O)CH 2 —, HOC(CH 3 ) 2 CH 2 —, and

wherein R 4 is independently selected from any of the group of compounds given for R 1-3 .

Assignments (3)
SECURITY INTEREST Recorded Oct 1, 2018
From: STARFRUIT US MERGER SUB 1 LLC; STARFRUIT US MERGER SUB 2 LLC; AKZO NOBEL SURFACE CHEMISTRY LLC; AKZO NOBEL CHEMICALS B.V.; AKZO NOBEL CHEMICALS INTERNATIONAL B.V.
To: WILMINGTON TRUST (LONDON) LIMITED, AS COLLATERAL AGENT
Reel/Frame 047231/0001 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 13, 2017
From: AKZO NOBEL N.V.
To: AKZO NOBEL CHEMICALS INTERNATIONAL B.V.
Reel/Frame 044427/0759 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 7, 2007
From: MEIJER, JOHN; NIJHOF, LEONARDUS BERNARDUS GERHARDUS MARIA; ROELOFS, HERMAN EVERT; TONNAER, HAIMO; VAN DE WORP, ROELOF
To: AKZO NOBEL N.V.
Reel/Frame 019798/0364 →