Color removal with zipgem filtration media for water and wastewater treatment
View Patent ↗Described herein relates to an optimum, low maintenance and low-cost filtration media which may be implemented near a source water location as a pretreatment to remove tannic acid and/or humic acid (color) from dissolved natural organic matter (NOM) (i.e., tannic acid, humic acid) to impede the prompt production of disinfection by-products collectively termed trihalomethanes in drinking water treatment processes. In an embodiment, the filtration media may comprise a composition having a ratio of at least 83% sand, at most 5% clay, at most 6% ZVI and at most 6% perlite by percent volume.
1 . A filtration media comprising:
at least one silicon atom;
at least one aluminum atom;
at least one zero-valence-iron (hereinafter “ZVI”) atom;
wherein the filtration media comprises a composition of at least 85% sand, at most 5% clay, at most 6% ZVI atom, and at most 4% perlite by percent volume;
wherein the ratio of the at least one ZVI atom to the at least one grain of sand is at most 0.071 by percent volume;
wherein the filtration media comprises a surface area of at most 3.00 m 2 ·g −1 ;
wherein the filtration media comprises a porosity of at least 29.0% of percent surface area;
wherein the filtration media construct comprises a density of at least 2.50 g·cm −3 ; and
wherein the filtration media comprises a saturated hydraulic conductivity of at least 10 −5 m·s −1 .
2 . The filtration media of claim 1 , wherein the filtration media further comprises at least one potassium atom, at least one calcium atom, or both.
3 . The filtration media of claim 1 , wherein the filtration media comprises a heterogenous morphological structure.
4 . The filtration media of claim 1 , wherein the filtration media is configured to maintain an effluent concentration below 40 color units of the Platinum-Cobalt Scale (hereinafter “Pt—CO”).
5 . The filtration media of claim 1 , wherein the filtration media is configured to inhibit ponding, clogging, or both within at least one pour of the filtration media for at least 40,000 minutes.
6 . The filtration media of claim 1 , wherein the filtration media is configured to maintain an adsorption capacity of at least 25.0 mg Pt—Co·g −1 .
7 . A method of optimizing a color removal reaction within a water sample, the method comprising:
incorporating a filtration media into the water sample, the filtration media comprising:
at least one silicon atom;
at least one aluminum atom;
at least one zero-valence-iron (hereinafter “ZVI”) atom;
wherein the filtration media comprises a composition of at least 85% sand, at most 5% clay, at most 6% ZVI atom, and at most 4% perlite by percent volume;
wherein the ratio of the at least one ZVI atom to the at least one grain of sand is at most 0.071 by percent volume;
wherein the filtration media comprises a surface area of at most 3.00 m 2 ·g −1 ;
wherein the filtration media comprises a porosity of at least 29.0% of percent surface area;
wherein the filtration media construct comprises a density of at least 2.50 g·cm −3 ; and
wherein the filtration media comprises a saturated hydraulic conductivity of at least 10 −5 m·s −1 ; and
wherein the incorporation of the filtration media to the water sample thereof optimizes the color removal reaction within the water sample.
8 . The method of claim 7 , wherein the filtration media is configured to operate continuously in the water sample for at least 14,000 minutes.
9 . The method of claim 7 , wherein the filtration media is configured to inhibit ponding, clogging, or both within at least one pour of the aluminum-doped ZVI-quartz construct for at least 40,000 minutes.
10 . The method of claim 7 , wherein the filtration media configured to maintain an adsorption capacity of at least 25.0 mg of Pt—Co·g −1 .
11 . A method of synthesizing a filtration media, the method comprising:
providing at least one zero-valent iron (“ZVI”) material;
mixing the ZVI material with sand, clay, and perlite in proportions of at least 85% sand, at most 5% clay, at most 6% ZVI, and at most 4% perlite by percent volume; and
subjecting the mixture to heat treatment to produce a filtration media having a porosity of at least 29%, a BET specific surface area of at most 3.0 m 2 ·g −1 , a density of at least 2.50 g·cm −3 , and a saturated hydraulic conductivity of at least 10 −5 m·s −1 .
12 . The method of claim 11 , wherein the heat treatment is conducted at a temperature of at least 850° C.
13 . The method of claim 11 , wherein the heat treatment is configured to promote formation of a heterogeneous morphological structure within the filtration media.
14 . The method of claim 11 , wherein the filtration media synthesized is configured to inhibit ponding, clogging, or both within at least one pour of the filtration media for at least 40,000 minutes.