Process including a carbonation step
AssigneeT&L Sugars Limited
InventorsJohn Kerr, Anthony Baiada, Robert Jansen, Matthew Shue, Gordon Walker
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AssigneeT&L Sugars Limited
InventorsJohn Kerr, Anthony Baiada, Robert Jansen, Matthew Shue, Gordon Walker
Estimating the term…
The invention relates to a process for the removal of contaminants from a liquor, the process comprising: introducing a metal or ammonium hydroxide into the liquor; introducing the liquor into a reaction vessel; bubbling a carbon dioxide gas comprising at least 25% carbon dioxide through the liquor within the reaction vessel; and separating the precipitate formed by the carbonatation of the metal hydroxide from the liquor, the precipitate comprising at least some of the contaminants from the liquor; wherein, on average, the liquor is resident within the reaction vessel for a period of no more than about 60 minutes. The invention also relates to a process for the removal of contaminants from a liquor, the process comprising: introducing a metal or ammonium hydroxide into the liquor and bubbling a carbon dioxide gas comprising at least 25% carbon dioxide through the liquor to form a precipitate by carbonatation in a period of no more than about 60 minutes. The carbonatation processes may be included in sugar refining or water softening and/or decontamination processes. A use of a carbon dioxide gas comprising at least 25% carbon dioxide in a carbonatation process for removing contaminants from a hydroxide-treated liquor is also provided, wherein the process forms a precipitate in a period of no more than about 60 minutes.
A process for the removal of contaminants from a liquor, the process comprising:
A process for the removal of contaminants from a liquor, the process comprising:
A process of carbonatation, comprising using a carbon dioxide gas comprising from 50% to 100% carbon dioxide in a carbonatation process for removing contaminants from a hydroxide-treated liquor, wherein the process forms a precipitate in a period of no more than 60 minutes and wherein the size of the precipitate is controlled by altering the pH profile of the liquor in the reaction vessel, and wherein the pH profile of the liquor is altered by recycling a portion of the liquor into the reaction vessel.
Dependencies are inferred from the claim text.