Methods for removing metals from plating operation
The present invention relates to compounds and methods for removing metals, e.g., ionic cobalt from an electroless plating operation, preferably to levels less than 5 ppm. The metals can then be either landfilled or regenerated for electrowinning and reuse. The invention utilizes an ion exchange media comprised of a silica backbone and functionalized with phosphonate groups.
1. A method of removing metals from an electroless plating operation, comprising adding to said operation a composition including a compound of Formula 1:
wherein R and R 1 are each independently hydrogen, a linear or branched C 1-40 alkyl, C 2-40 alkenyl or C 2-40 alkynyl group, an aryl or C 1-40 alkylaryl group or optionally a complex metal ion M n+ /n wherein n is an integer from 1 to 8; the free valences of the silicate oxygen atoms are saturated by one or more of: silicon atoms of other groups of Formula 1, hydrogen, a linear or branched C 1-12 alkyl group or by cross-linking bridge members R 3 q M 1 (OR 2 ) m O k/2 or A1(OR 2 ) 3-p O p/2 or R 3 A1(OR 2 ) 2-r O r/2 ; where M 1 is Si or Ti; R 2 is a linear or branched C 1-12 alkyl group; and R 3 is a linear or branched C 1-6 alkyl group; k is an integer from 1 to 4 and q and m are integers from 0 to 2; such that m+k+q=4; and p is an integer from 1 to 3; and r is an integer from 1 to 2; or other oxo metal bridging systems; x, y and z are integers such that the ratio of x:y+z, varies from 0.00001 to 100,000 with the fragments [O 3/2 SiCH(CH 2 PO(OR)(OR 1 ))CH 2 CH 2 SiO 3/2 ] x and [O 3/2 SiCH 2 CH 2 PO(OR)(OR 1 )] y always present while the integer z varies from 0 to 200y.
2. The method as recited in claim 1 , wherein the amount of compound is from about 0.5-5 mmole/g.
3. The method as recited in claim 1 , wherein the metals are removed from the electroless plating operation to levels less than 5 ppm.
4. The method as recited in claim 1 , wherein said metals include cobalt.
5. The method as recited in claim 4 , wherein the cobalt can be regenerated for reclamation.
6. The method as recited in claim 1 , wherein the particle size of the compound utilized is from 5-500 um.
7. The method as recited in claim 6 , wherein the particle size of the compound utilized is from 20-100 um.
8. The method as recited in claim 1 , wherein the compound is used in conjunction with a nanofilter.
9. The method as recited in claim 1 , wherein the pH of treatment is from 6-10.
10. The method as recited in claim 9 , wherein the pH of treatment is ftom 7.5-9.