PRODUCTION OF NITROGEN-CONTAINING CHELATORS
Reaction pathways and conditions for the production of nitrogen-containing chelators, such as a glycine derivative, as described herein. In particular, the present disclosure describes a process for the production of a nitrile intermediate by reacting a tetra-amino compound with an aldehyde and a hydrogen cyanide to form the nitrile intermediate. The nitrile intermediate may then be further processed to produce the chelators at a high yield and/or a high purity.
1 . A process for preparing a nitrile intermediate, the process comprising:
reacting a tetra-amino compound with a hydrogen cyanide and an aldehyde in an aqueous solution to form the nitrile intermediate.
2 . The process of claim 1 , wherein the nitrile intermediate is formed at a yield greater than 5%.
3 . The process of claim 1 , wherein the nitrile intermediate is crystalline.
4 . The process of claim 1 , wherein the tetra-amino compound has a formula:
wherein R 1 , R 2 , R 3 , R 4 , R 5 , and R 6 are independently (C 1 -C 5 )alkyl or (C 1 -C 5 )alkenyl.
5 . The process of claim 1 , wherein the aldehyde is acetaldehyde.
6 . The process of claim 1 , wherein the tetra-amino compound is 1,3,5,7-tetraazaadamantane.
7 . The process of claim 1 , wherein the nitrile intermediate is alanine-N,N-dinitrile.
8 . The process of claim 1 , wherein the reacting comprises:
providing a tetra-amino compound solution comprising the tetra-amino compound;
adding the aldehyde to the tetra-amino compound solution to form a first intermediate solution;
adjusting the pH of the first intermediate solution to a pH ranging from 2.0 to 7.0;
adding the hydrogen cyanide to the first intermediate solution to form a second intermediate solution;
heating and/or chilling the second intermediate solution to a first temperature; and
heating and/or chilling the heated second intermediate solution to the second temperature.
9 . The process of claim 8 , wherein the first temperature is from about 30° C. to about 80° C.
10 . The process of claim 8 , wherein the second temperature is less than 25° C.
11 . The process of claim 8 , wherein a temperature ramp rate from the first temperature to the second temperature is from 0.5° C./min to 5° C./min.
12 . The process of claim 8 , wherein the hydrogen cyanide is added to the first intermediate solution at a rate from 0.01 g/minute to 1 g/minute.
13 . The process of claim 8 , wherein the reacting comprises adding a nitrile intermediate seed to the reaction mixture.
14 . The process of claim 13 , wherein the amount of nitrile intermediate seed added is less than 1% the theoretical yield of the nitrile intermediate.
15 . The process of claim 1 , further comprising forming a glycine derivative from the nitrile intermediate.
16 . The process of claim 15 , wherein the glycine derivative has a formula
wherein:
R is (C 1 -C 10 )alkyl, (C 1 -C 10 )haloalkyl, (C 1 -C 10 )alkenyl, or (C 1 -C 10 )alkyl carboxylate
X is hydrogen, an alkali metal, an alkaline earth metal, or ammonium,
a is from 0 to 5, and
b is from 0 to 5.
17 . The process of claim 15 , wherein the forming the glycine derivative comprises hydrolyzing the nitrile intermediate.
18 . The process of claim 17 , wherein the hydrolyzing comprises reacting the nitrile intermediate with an inorganic hydroxide selected from the group consisting of ammonium hydroxide, calcium hydroxide, lithium hydroxide, magnesium hydroxide, potassium hydroxide, sodium hydroxide, and combinations thereof.
19 . The process of claim 15 , wherein the glycine derivative is alanine-N,N-diacetic acid derivative.
20 . The process of claim 15 , wherein the glycine derivative is formed at a yield of at least 60%.