Process to prepare alkyl phenyl phosphates
A process is provided for reacting dichloromonophenyl phosphate and monochlorodiphenyl phosphate with aliphatic alcohol in the presence of a Lewis acid catalyst and absence of solvent, at a temperature above 60 to 200° C. and pressure of 0.001 to 1.1 bara, and sparging the reaction mixture with an inert carrier gas if the pressure is above 0.67 bars. Mixtures of monoalkyl biphenyl phosphates and dialkyl monophenyl phosphates and use of such mixtures as a plasticizer and/or flame retardant, are also provided.
1. A process for producing alkylphenyl phosphates comprising the steps of reacting a dichloromonophenyl phosphate and monochlorodiphenyl phosphate with an aliphatic alcohol, in the presence of a Lewis acid catalyst, in the absence of solvent, at a temperature of above 60 to 200° C., and at a pressure of 0.001 to 1.1 bar absolute pressure (bara), and
sparging the reaction mixture with an inert carrier gas in the event the pressure is above 0.67 bara.
2. The process according to claim 1 wherein the Lewis acid catalyst is magnesium chloride.
3. The process according to claim 1 wherein the removal of the by-product HCl is enhanced by sparging with a dry inert carrier gas.
4. The process according to claim 1 wherein the Lewis acid catalyst is used in an amount of 100 to 1.750 ppm, based on the total amount of phenyl chlorophosphate starting materials.
5. A process to prepare a mixture of monoalkyl diphenyl phosphates and dialkyl monophenyl phosphates wherein phosphorus oxychloride is reacted with phenol in a first step resulting in a mixture of diphenyl monochlorphosphates and monophenyl dichlorophosphates; and the mixture of diphenyl monochlorophosphates and monophenyl dichlorophosphates resulting from the first step is reacted with an aliphatic alcohol in a second step, in accordance with the process according to claim 1 .
6. The process according to claim 5 wherein the Lewis acid catalyst is completely added to the first step of the process and in the second step of the process no additional Lewis acid catalyst is added.
7. The process according to claim 5 wherein at least part of the monophenyl dichlorophosphate from the first step is recycled, so that the alkyl diphenyl phosphate to dialkyl phenyl phosphate ratio of the product mixture of the second step is greater than the diphenyl chlorophosphate to monophenyl dichlorophosphate ratio resulting from the first reaction step without a recycle stream.
8. The process according to claim 5 wherein at least part of the monophenyl dichlorophosphate is removed from the reaction mixture from the first reaction step by a distillation or rectification step.
9. The process according to claim 1 comprising an additional purification step.
10. The process according to claim 1 that is a continuous, semi-continuous or batch process.
11. The process according to claim 2 wherein the removal of the by-product HCl is enhanced by sparging with a dry inert carrier gas and the Lewis acid catalyst is magnesium chloride.
12. The process according to claim 2 wherein the Lewis acid catalyst is used in an amount of 100 to 1.750 ppm, based on the total amount of phenyl chlorophosphate starting materials.
13. The process according to claim 3 wherein the Lewis acid catalyst is used in an amount of 100 to 1.750 ppm, based on the total amount of phenyl chiorophosphate starting materials.
14. The process according to claim 6 wherein at least part of the monophenyl dichlorophosphate from the first step is recycled, so that the alkyl diphenyl phosphate to dialkyl phenyl phosphate ratio of the product mixture of the second step is greater than the diphenyl chlorophosphate to monophenyl dichlorophosphate ratio resulting from the first reaction step without a recycle stream.
15. The process according to claim 6 wherein at least part of the monophenyl dichlorophosphate is removed from the reaction mixture from the first reaction step by a distillation or rectification step.
16. The process according to claim 7 wherein at least part of the monophenyl dichlorophosphate is removed from the reaction mixture from the first reaction step by a distillation or rectification step.
17. A process to prepare a mixture of monoalkyl diphenyl phosphates and dialkyl monophenyl phosphates wherein in a first step phosphorus oxychloride is reacted with phenol and in a second step in accordance with the process according to claim 2 the mixture of diphenyl monochlorophosphates and monophenyl dichlorophosphates resulting from the first step is reacted with an aliphatic alcohol.