IP Library Granted Patent US 7,119,220
Granted Patent B2
US 7,119,220 · App. 10/371,290 · Granted Oct 10, 2006

Process for preparing dimethyl propanephosphonate

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Quick Facts
Patent No.
US 7,119,220
App. No.
10/371,290
Granted
Oct 10, 2006
Kind
B2
Abstract

Process for preparing dimethyl propanephosphonate, characterized in that dimethyl phosphite is reacted with propene in the presence of a free-radical former at a reaction temperature of 60 to 95° C., the half life of the free-radical former being 0.1 to 20 min at the reaction temperature.

Claims (13)

1. Process for preparing dimethyl propanephosphonate, comprising reacting dimethyl phosphite with propene in the presence of a free-radical former at a reaction temperature of 60 to 95° C., the half life of the free-radical former being 0.1 to 20 min at the reaction temperature,

wherein the dimethyl propanephosphonate is prepared at a yield that is more than 95% and formation of trimethyl phosphate in the amount of more than 0.1% by weight is avoided.

2. Process according to claim 1 , wherein the reaction temperature is 80 to 95° C.

3. Process according to claim 1 , wherein the half life of the free-radical former is 0.5 to 10 min at the reaction temperature.

4. Process according to claim 1 , wherein the free-radical former is used in an amount of 0.1 to 5 mol % based on propene.

5. Process according to claim 1 , wherein the free-radical former is used in an amount of 0.3 to 2 mol %, based on propene.

6. Process according to claim 1 , wherein tert-butyl peroxyneodecanoate or dilauroyl peroxide is used as free-radical former.

7. Process according to claim 1 , wherein the molar ratio of dimethyl phosphite propene is 1.0:1.0 to 3.0:1.0.

8. Process according to claim 1 , wherein the molar ratio of dimethyl phosphite to propene is 1.1:1.0 to 2.3:1.0.

9. Process according to claim 1 , wherein dimethyl phosphite with a trimethyl phosphate content of 0 to 0.1% by weight is used.

10. Process according to claim 1 , wherein dimethyl phosphite with a trimethyl phosphate content of 0 to 0.01% by weight is used.

11. Process according to claim 1 , wherein the reaction is carried out at a pressure of 150 to 6 000 mbar (absolute).

12. Process according to claim 1 , wherein the reaction is carried out at a pressure of 500 to 950 mbar (absolute).

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 1, 2006
From: BAYER AG
To: LANXESS DEUTSCHLAND GMBH
Reel/Frame 018584/0319 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 21, 2003
From: HANSEL, JAN-GERD; JABS, GERT; KAULEN, JOHANNES; ADAMS, HANS-GEORG; FROEHLEN, HANS-GUENTER
To: BAYER AKTIENGESELLSCHAFT
Reel/Frame 013815/0058 →