Purification method using a low granulometry resin
The invention relates to a method for purifying a solution, the method comprising the following successive steps: —bringing a solution to be purified into contact with an ion exchange resin by suspending the ion exchange resin in the solution to be purified, the ion exchange resin having the form of particles having a size Dv50 smaller than or equal to 200 μm; —separating the solution into a purified solution and a loaded resin; —regenerating the loaded resin by passing at least one regenerating solution through a compact bed of loaded resin. The invention also relates to an assembly for implementing the method.
1. A method for purifying a solution, successively comprising:
contacting a solution to be purified with an ion exchange resin, by putting the ion exchange resin in suspension in the solution to be purified for a duration of time, thereby forming a purified solution and a loaded ion exchange resin, the ion exchange resin being in the form of particles having a Dv50 size equal to or less than 200 μm;
separating the purified solution from the loaded ion exchange resin, thereby forming a compact bed of loaded ion exchange resin; and
regenerating the ion exchange resin from the compact bed of loaded ion exchange resin, by passing at least one regenerating solution through the compact bed of loaded ion exchange resin.
2. The method according to claim 1 , wherein the solution to be purified being a sugar liquor, and wherein the method decolorizes the sugar liquor.
3. The method of claim 1 further comprising, before regenerating the ion exchange resin from the compact bed of loaded ion exchange resin:
washing the loaded ion exchange resin, and/or,
separating the loaded ion exchange resin and an additional dilute fraction of purified solution,
wherein when both washing and separating the loaded ion exchange resin, separating the loaded ion exchange resin occurs at the time of, or after, washing the loaded ion exchange resin.
4. The method of claim 1 , further comprising:
rinsing the ion exchange resin after regenerating the ion exchange resin.
5. The method of claim 1 , further comprising:
removing filter cake from the compact bed of loaded ion exchange resin after washing, or regeneration or rinsing.
6. The method of claim 1 , wherein suspension of the ion exchange resin in the solution to be purified is carried out in an agitated vessel.
7. The method of claim 1 , wherein separating the purified solution, regenerating the ion exchange resin from the loaded ion exchange resin, and optionally washing and/or rinsing of the resin, are performed by means of one or more filters, the loaded ion exchange resin being retained in the form of a compact bed on the one or more filters.
8. The method according to claim 7 , wherein the one or more filters are arranged at the outlet of a container used for the contacting step; or wherein the one or more filters are arranged in a filtering device separate from said container and connected thereto.
9. The method of claim 1 , wherein the ion exchange resin is in the form of particles having a Dv50 size equal to or less than 150 μm.
10. The method of claim 1 , wherein the compact bed of loaded ion exchange resin has a maximum size in a direction in which the regenerating solution is passed of equal to or less than 10 cm.
11. The method of claim 1 , wherein:
the regenerating solution used to regenerate the ion exchange resin from the compact bed of loaded ion exchange resin is partly derived from a preceding regeneration of ion exchange resin from the compact bed of loaded ion exchange resin; and/or
a washing solution used to wash the loaded ion exchange resin is partly derived from a preceding washing of loaded ion exchange resin, and/or from a preceding regeneration of loaded ion exchange resin; and/or
a rinsing solution used to rinse the ion exchange resin is partly derived from a preceding rinsing of the ion exchange resin.
12. The method of claim 1 , wherein the method operates continuously.
13. The method of claim 1 , wherein a plurality of batches of loaded ion exchange resin are derived from a plurality of separate steps of contacting a solution to be purified with an ion exchange resin and are grouped together in a single batch of loaded ion exchange resin for the regenerating step, and optionally a preceding wash step and/or a following rinse step.
14. The method of claim 1 , wherein the particles occupy a volume fraction during the contacting step with the solution to be purified which is equal to or less than 0.3.
15. The method of claim 1 , wherein the ion exchange resin has a volume and wherein the total volume of the at least one regenerating solution used is from 0.5 to 4 times the volume of the ion exchange resin.
16. The method of claim 1 , wherein the duration of contacting the ion exchange resin with the solution to be purified is from 1 minute to 6 hours.