Method for the manufacture of phosphonoalkyl iminodiacetic acid
View Patent ↗An improved method for the manufacture of phosphonoalkyl iminodiacetic acid M 2 PO 3 —X—N—(CH 2 COOM) 2 wherein X is a C 1-6 linear or branched alkyl group; and M is selected from hydrogen, alkali, earth-alkali, ammonium and protonated amine is disclosed. The iminodiacetic acid starting material is reacted with a substantially stoichiometric amount of phosphorous acid, in the presence of a large excess of phosphoric acid to thereby yield a reaction medium insoluble reaction product (PAI-DA) which can be separated from the reaction medium. In a particularly preferred approach, the phosphorous acid is prepared in situ starting from liquid P 4 O 6 .
1. A method for the manufacture of a phosphonomethyl iminodiacetic acid or a salt thereof having the formula:
M2PO3—CH2—N—(CH2COOM)2
Wherein M is selected from hydrogen, alkali, earth-alkali, ammonium and protonated amine; comprising the steps of:
a) reacting iminodiacetic acid with phosphorous acid whereby the phosphorous acid is used in a molar ratio of phosphorous acid: iminodiacetic acid of from 0.7:1 to 1.5:1 in the presence of phosphoric acid whereby the molar ratio of phosphoric acid: phosphorous acid is of from 9:0.8 to 1:1 and formaldehyde in a molar ratio formaldehyde: iminodiacetic acid of from 2:1 to 0.5:1, at a temperature in the range of from 45° C. to 200° C. for a period of from 1 minute to 10 hours, to thereby yield a substantially reaction medium insoluble product;
b) separating the insoluble reaction product from the reaction medium, and optionally water washing the insoluble reaction product, wherein the mother liquid is, after the separation of the reaction product, recycled into the reaction medium, wherein the term “phosphoric acid” means phosphoric acid prepared in situ starting from P2O5, with the proviso that hydrochloric acid is not present in the reaction medium.
2. The method in accordance with claim 1 wherein the molar ratio of phosphoric acid: phosphorous acid is from 6:1 to 1.2:1 and wherein the molar ratio of phosphorous acid: iminodiacetic acid is from 0.8:1 to 1.3:1.
3. The method in accordance with claim 2 wherein the molar ratio of phosphoric: phosphorous is from 4:1.5 to 1.2:1 and wherein the molar ratio of phosphorous:
iminodiacetic acid is from 0.9: to 1.1:1.
4. The method in accordance with claim 1 wherein the molar ratio of formaldehyde: iminodiacetic acid is from 1.5:1 to 0.7:1.
5. The method in accordance with claim 1 wherein the reaction is carried out at a temperature in the range of from 70 ° C. to 150 ° C. combined with an approach selected from:
(A) conducting the reaction under ambient pressure with or without distillation of water and non-reacted formaldehyde;
(B) conducting the reaction in a closed vessel under autogenous pressure built up;
(C) conducting the reaction in a combined distillation and pressure arrangement whereby the reaction vessel containing the reaction mixture is kept under ambient pressure at the reaction temperature followed by circulating the reaction mixture through a reactor operated under autogenous pressure built up thereby gradually adding the formaldehyde and other reactants; and
(D) a continuous process arrangement, optionally under autogenous pressure built up, whereby the reactants are continuously injected into the reaction mixture and the phosphonic acid reaction product is withdrawn on a continuous basis.
6. The method in accordance with claim 1 wherein:
the molar ratio of phosphoric: phosphorous is from 6:1 to 2:1;
the molar ratio of formaldehyde: iminodiacetic acid is from 1.3:1 to 0.8:1;
the temperature is from 100° C. to 150° C.; and
the duration (period) is from 10 minutes to 4 hours.
7. The method in accordance with claim 6 wherein:
the molar ratio of phosphoric: phosphorous is from 5:1 to 3:1;
the molar ratio of phosphorous: iminodiacetic acid is from 1.1:1 to 0.9:1;
the molar ratio of formaldehyde: iminodiacetic acid is from 0.9: 1 to 1.1:1;
the temperature is from 110 ° C. to 140 ° C.; and
the duration (period) is from 30 minutes to 2 hours.
8. The method in accordance with claim 1 wherein the level of chlorine in the reaction medium is 2000 ppm or less, expressed in relation to the phosphorous acid (100%).
9. The method in accordance with claim 8 wherein the level of chlorine in the reaction medium is less than 400 ppm of chlorine expressed in relation to the phosphorous acid (100%).
10. The method in accordance with claim 9 wherein the level of chlorine in the reaction medium is less than 200 ppm of chlorine expressed in relation to the phosphorous acid (100%).
11. The method in accordance with claim 1 wherein the phosphorous acid is prepared in situ by adding P4O6 to an aqueous reaction medium:
(a) containing phosphoric acid in a level to maintain the pH in the reaction medium below 5, whereby the reaction medium contains in addition to the water and the phosphoric acid the iminodiacetic acid; or
(b) containing the iminodiacetic acid and the phosphoric acid to maintain the pH, at all times, below 5; or
(c) simultaneously with the iminodiacetic acid provided the pH of the reaction medium is maintained, at all times, below 5.
12. The method in accordance with claim 11 wherein the P4O6 is manufactured by reacting oxygen and phosphorus in essentially stoichiometric amounts in a reaction unit at a temperature in the range of from 1600 to 2000 K with a reaction residence time from 0.5 to 30 seconds, followed by quenching the reaction product at a temperature below 700 K and refining the reaction product by distillation.
13. The method in accordance with claim 12 wherein the level of elementary phosphorus in the P4O6 is below 1000 ppm, expressed in relation to P4O6 (100%).