Ion exchange process
A method is described that relates to reducing amounts of regenerant waste or increasing the concentration of regenerant waste from ion exchange processes. A method is described that may allow a batch ion exchange process to compete on these factors with continuous or simulated continuous ion exchange processes, and/or to improve the efficiency in operation continuous or simulated continuous ion exchange processes. A specific application addressed is the treatment of water in the Coal Bed Methane Process.
1. A batch ion exchange process wherein the regenerant waste profile exiting the process is collected as three fractions comprising:
a first leading fraction which is recycled for dilution of a concentrated regenerant or for dissolving a solid regenerant;
a second center fraction which is the product regenerant waste sent forward for subsequent processing following ion exchange; and
a third trailing fraction which is recycled for dilution of a concentrated regenerant or for dissolving a solid regenerant.
2. The process of claim 1 , wherein the ion exchange process is for treatment of water derived from the Coal Bed Methane Process.
3. The process of claim 1 , wherein the ion exchange process uses a strong cation exchange resin.
4. The process of claim 1 , wherein the ion exchange process uses a weak cation exchange resin.
5. The process of claim 1 , wherein the concentrated regenerant is an acid selected from the group: hydrochloric acid, sulfuric acid, phosphoric acid, and acetic acid.
6. The process of claim 1 , wherein the leading fraction is about 5% to 25% of the total profile volume.
7. The process of claim 1 , wherein the trailing fraction is about 5% to 25% of the total profile volume.
8. A continuous or simulated continuous ion exchange process wherein 5% to 25% of the exiting regenerant waste is collected and used for dilution of a concentrated regenerant or for dissolving a solid regenerant.
9. The process of claim 8 , wherein the ion exchange process is for treatment of water derived from the Coal Bed Methane Process.
10. The process of claim 8 , wherein the ion exchange process uses a strong cation exchange resin.
11. The process of claim 8 , wherein the ion exchange process uses a weak cation exchange resin.
12. The process of claim 8 , wherein the concentrated regenerant is an acid selected from the group: hydrochloric acid, sulfuric acid, phosphoric acid, and acetic acid.
13. A continuous or simulated continuous exchange process comprising:
providing a column filled with a strong or weak cation resin bed in the hydrogen form;
passing a quantity of liquid through said column exchanging the hydrogen in the resin for cations in the liquid; and
regenerating the resin in the column with an acid by passing a quantity of acid through the column, said acid being diluted prior to its passage through said column by liquid which has previously passed through said column and now forms part of a previous regenerant waste profile.
14. The process of claim 13 wherein said liquid which forms part of a regenerant waste profile is taken from a leading fraction of the regenerant waste profile.
15. The process of claim 14 wherein the leading fraction of the regenerant waste constitutes about 5% to about 25% of the total regenerant waste profile.
16. The process of claim 13 wherein said liquid which forms part of said regenerant waste profile is taken from a trailing fraction of the regenerant waste profile.
17. The process of claim 16 wherein said trailing fraction of the regenerant waste profile constitutes about 5% to about 25% of the total regenerant waste profile.
18. The process of claim 13 wherein said liquid which forms part of a regenerant waste profile is taken from a leading fraction of the regenerant waste profile and a trailing fraction of the regenerant waste profile.
19. The process of claim 18 wherein said liquid which forms part of a regenerant waste profile constitutes up to about 50% of the regenerant waste profile.