Process for the manufacture of P4O6 with improved yield
View Patent ↗A process for the production of a reaction product consisting essentially of P 4 O 6 is carried out by reacting oxygen with phosphorus in an exothermic reaction in a reaction unit. Heat created by the exothermic reaction is removed by feeding P 4 O 6 and/or by-products of the process into the reaction unit. The generated reaction product is then quenched to a lower temperature where no essential decomposition of the reaction product occurs, and at least part of P 4 O 6 is separated from the reaction product obtained after quenching. The resulting yield of P 4 O 6 based on the phosphorus used is improved and the heat of the exothermic reaction can be controlled in an economic way.
1. A process for the production of a reaction product consisting essentially of P 4 O 6 by reacting oxygen, or a mixture of oxygen and an inert gas, with gaseous or liquid phosphorus in an exothermic reaction in a reaction unit maintaining an average temperature in said reaction unit suitable to generate the reaction product, by removing heat created by the exothermic reaction by feeding P 4 O 6 and/or by-products obtained from earlier reactions producing the reaction product or from the running process into the reaction unit, then quenching the generated reaction product in one or more quenching unit(s) to a lower temperature where no essential decomposition of the reaction product occurs, and separating at least part of P 4 O 6 from the reaction product obtained after quenching.
2. The process according to claim 1 , wherein a stream of by-products consisting of the remaining residue obtained by separating at least part of P 4 O 6 from the reaction product after quenching, or a fraction thereof, is fed into the reaction unit thereby removing heat created by the exothermic reaction.
3. The process according to claim 2 , wherein cooling of the reaction product in the reaction unit is effected by controlling the feeding of a stream of P 4 O 6 into the stream of by-products, and feeding the resulting stream into the reaction unit.
4. The process according to claim 1 , wherein cooling of the reaction product in the reaction unit is solely or additionally effected by controlling the feeding of a stream of P 4 O 6 into the reaction unit.
5. The process according to claim 1 , wherein the temperature of the reaction product in the reaction unit is maintained at an average temperature in the range of 1500 to 2200K.
6. The process according to claim 5 , wherein the temperature of the reaction product in the reaction unit is maintained at an average temperature in the range of 1600 to 2000K.
7. The process according to claim 1 , wherein the reaction product is maintained in the reaction unit for a residence time of at least 0.5 seconds.
8. The process according to claim 7 , wherein the residence time is between 1 and 60 seconds.
9. The process according to claim 1 , wherein the molar ratio of phosphorus (P 4 ) to oxygen (O 2 ) is in the range of from 1:2.7 to 1:3.3.
10. The process according to claim 1 , wherein the reaction product is quenched to a temperature below 700 K.
11. The process according to claim 1 , wherein the reaction product is quenched, or cooled after quenching, to a temperature below the boiling point of point of P 4 O 6 .
12. A process according to claim 1 , wherein liquid reaction product and/or liquid P 4 O 6 is added as a coolant to the reaction product to be quenched.