LOW METAL CONTENT POLYOLEFIN FILTER MEMBRANE
Provided are certain polyolefinic membranes which are useful as components of filters for liquid purification. Advantageously, the filter membranes of the disclosure possess greatly reduced concentrations of certain trace metals, thus making them particularly useful in the filtration of liquids used in the fabrication of microelectronic devices. In one aspect, the disclosure provides a filter membrane comprising a polyolefin, wherein said polyolefin has less than about 4 ppm total of metals chosen from titanium, aluminum, iron, zinc, and magnesium.
1 . A filter membrane comprising a polyolefin, wherein the sum of the amount of titanium, aluminum, iron, zinc and magnesium in the polyolefin is less than about 4 ppm, as determined by MARS 6 Microwave Acid Digestion Method Note Compendium.
2 . The membrane of claim 1 , wherein the sum of the amount of titanium, aluminum, iron, zinc, and magnesium in the polyolefin is less than about 3 ppm.
3 . The membrane of claim 1 , wherein the sum of the amount of titanium, aluminum, iron, zinc, and magnesium in the polyolefin is less than about 1 ppm.
4 . The membrane of claim 1 , wherein the polyolefin has less than about 1 ppm of ruthenium, as determined by MARS 6 Microwave Acid Digestion Method Note Compendium.
5 . The membrane of claim 1 , wherein the polyolefin is chosen from polyethylene and polyethylene-co-polybutylene.
6 . The membrane of claim 1 , wherein the polyolefin is an ultra-high molecular weight polyethylene.
7 . The membrane of claim 1 , wherein the polyolefin has a number average molecular weight of about 330,000 to 2,200,000 Daltons.
8 . The membrane of claim 1 , wherein the polyolefin has a number average molecular weight of about 700,000 Daltons to about 1,500,000 Daltons.
9 . The membrane of claim 1 , wherein the polyolefin is prepared by:
A. contacting cis- or trans-cyclooctene with a Ru II catalyst, followed by
B. removal or extraction of the Ru II catalyst, followed by
C. hydrogenation with a hydrazine-type or hydrazido-type reducing agent.
10 . The membrane of claim 9 , wherein the Ru II catalyst is chosen from
i. (1,3-Bis(2,6-diisopropylphenyl)-4-((4-ethyl-4-methylpiperzain-1-ium-1-yl)methyl)imidazolidin-2-ylidene)(2-isopropoxybenzylidene)ruthenium(II) chloride dihydrate;
ii. (1,3-dimesityl-4-((trimethylammonio)methyl)imidazolidin-2-ylidene)dichloro(2-isopropoxybenzylidene)ruthenium(II) chloride;
iii. (4-((4-ethyl-4-methylpiperazin-1-ium-1-yl)methyl)-1,3-dimesitylimidazolidin-2-ylidene)dichloro(2-isopropoxybenzylidene)ruthenium(H) chloride;
iv. (1,3-dimesityl-4-((trimethylammonio)methyl)imidazolidin-2-ylidene)dichloro(2-isopropoxybenzylidene)ruthenium(II) hexafluorophosphate; and
v. (1,3-dimesityl-4-((trimethylammonio)methyl)imidazolidin-2-ylidene)dichloro(2-isopropoxybenzylidene)ruthenium(II) tetrafluoroborate.
11 . The membrane of claim 1 , wherein the polyolefin is a polyethylene-co-polybutylene by contacting polybutadiene with hydrogen in the presence of a hydrazido-type or hydrazine-type reducing agent.
12 . A filter comprising a filter membrane comprising a polyolefin, wherein the sum of the amount of titanium, aluminum, iron, zinc and magnesium in the polyolefin is less than about 4 ppm, as determined by MARS 6 Microwave Acid Digestion Method Note Compendium.
13 . The filter of claim 12 , wherein the sum of the amount of titanium, aluminum, iron, zinc, and magnesium in the polyolefin is less than about 3 ppm.
14 . The filter of claim 12 , wherein the sum of the amount of titanium, aluminum, iron, zinc, and magnesium in the polyolefin is less than about 1 ppm.
15 . The filter of claim 12 , wherein the polyolefin has less than about 1 ppm of ruthenium, as determined by MARS 6 Microwave Acid Digestion Method Note Compendium.
16 . The filter of claim 12 , wherein the polyolefin is chosen from polyethylene and polyethylene-co-polybutylene.
17 . The filter of claim 12 , wherein the polyolefin is an ultra-high molecular weight polyethylene.
18 . The filter of claim 12 , wherein the polyolefin has a number average molecular weight of about 330,000 to 2,200,000 Daltons.
19 . The filter of claim 12 , wherein the polyolefin has a number average molecular weight of about 700,000 Daltons to about 1,500,000 Daltons.
20 . A method for removing an impurity from a liquid, which comprises contacting the liquid with the filter of claim 12 .