REMOVING MERCURY AND OTHER HEAVY METALS FROM INDUSTRIAL WASTEWATER
A method of removing one or more heavy metals including mercury from industrial wastewater by use of a filtration and/or a solid-liquid separation system by use of a water soluble ethylene dichloride ammonia polymer.
1 . A method of removing one or more heavy metals including mercury from industrial wastewater by use of a filtration process comprising the following steps:
a. maintaining the pH of said industrial wastewater to achieve at least the hydroxide precipitation of mercury;
b. adding an effective amount of a water soluble ethylene dichloride ammonia polymer having a molecular weight of from about 500 to about 10,000 daltons that contain from about 5 to about 50 mole percent of dithiocarbamate salt groups to react with at least mercury in said industrial wastewater;
c. passing said treated industrial wastewater through a filter device excluding a UF or MF membrane; and
d. optionally back-flushing said filter device to remove solids from the filter device.
2 . The method of claim 1 , wherein said effective amount of said water soluble ethylene dichloride ammonia polymer is from 10 ppm to about 1000 ppm based upon actives.
3 . The method of claim 1 further comprising the step of: adjusting the pH of said industrial wastewater before step (a) to de-complex metals from one or more chelants, if present, in said industrial wastewater and subsequently or simultaneously adding one or more chelant scavengers, optionally wherein said pH adjustment before step (a) is to less than 4.
4 . The method of claim 1 further comprising treating the industrial wastewater with one or more water-soluble polymers after step (b) and before passing through said filter device.
5 . The method of claim 1 , wherein said filter device has a separation rating in the range of 0.001 to 10 μm or 0.1 μm to 10 μm.
6 . The method of claim 1 , wherein the water soluble ethylene dichloride ammonia polymer has a molecular weight of about 2,000 to about 2,000,000 daltons.
7 . The method of claim 4 , wherein said water-soluble polymers are selected from a group consisting of: amphoteric polymers, cationic polymers, zwitterionic polymers, anionic polymers and a combination thereof.
8 . The method of claim 7 , wherein the amphoteric polymers are selected from the group consisting of: dimethylaminoethyl acrylate methyl chloride quaternary salt/acrylic acid copolymer, diallyldimethylammonium chloride/acrylic acid copolymer, dimethylaminoethyl acrylate methyl chloride salt/N,N-dimethyl-N-methacrylamidopropyl-N-(3-sulfopropyl)-ammonium betaine copolymer, acrylic acid/N,N-dimethyl-N-methacrylamidopropyl-N-(3-sulfopropyl)-ammonium betaine copolymer and DMAFA.MCQ/Acrylic acid/N,N-dimethyl-N-methacrylamidopropyl-N-(3-sulfopropyl)-ammonium betaine terpolymer.
9 . The method of claim 7 , wherein the dosage of the amphoteric polymers are from about 1 ppm to about 2000 ppm of active solids, or wherein the amphoteric polymers have a molecular weight of about 5,000 to about 2,000,000 daltons.
10 . The method of claim 7 , wherein the amphoteric polymers have a cationic mole charge equivalent to an anionic mole charge equivalent ratio of about 3.0:7.0 to about 9.8:0.2.
11 . The method of claim 7 , wherein the cationic polymers are selected from the group consisting of: polydiallyldimethylammonium chloride; polyethyleneimine; polyepiamine; polyepiamine crosslinked with ammonia or ethylenediamine; condensation polymer of ethylenedichloride and ammonia; condensation polymer of triethanolamine and tall oil fatty acid; poly(dimethylaminoethylmethacrylate sulfuric acid salt); and poly(dimethylaminoethylacrylate methyl chloride quaternary salt).
12 . The method of claim 7 , wherein the cationic polymers are copolymers of acrylamide and one or more cationic monomers selected from the group consisting of: diallyldimethylammonium chloride, dimethylaminoethylacrylate methyl chloride quaternary salt, dimethylaminoethylmethacrylate methyl chloride quaternary salt and dimethylaminoethylacrylate benzyl chloride quaternary salt.
13 . The method of claim 7 , wherein the dosage of cationic polymers is from about 0.1 ppm to about 1000 ppm active solids.
14 . The method of claim 7 , wherein the cationic polymers have a cationic charge of at least about 2 mole percent.
15 . The method of claim 7 , wherein the cationic polymers have a cationic charge of 100 mole percent.
16 . The method of claim 7 , wherein the cationic polymers have a molecular weight of about 2,000 to about 10,000,000 daltons or from about 20,000 to 2,000,000 daltons.
17 . The method of claim 7 , wherein the zwitterionic polymers are composed of about 1 to about 99 mole percent of N,N-dimethyl-N-methacrylamidopropyl-N-(3-sulfopropyl)-ammonium betaine and about 99 to about 1 mole percent of one or more nonionic monomers.
18 . The method of claim 1 , wherein the filter device is selected from the group consisting of: a single media filter, a bag filter, a sand filter, a multimedia filter, a cartridge filter, a diatomaceous filter, a drum filter with a coated media, a drum filter with a coated media containing diatomaceous earth, and a combination thereof.
19 . The method of claim 1 further comprising: passing a filtrate from said filter device through an ultrafiltration or a microfiltration membrane, and optionally wherein filtrate from said ultrafiltration or microfiltration membrane is passed through an additional membrane, wherein said additional membrane is a nanofiltration membrane or a reverse osmosis membrane.
20 . The method of claim 1 , wherein the said industrial wastewater is from an industrial process selected from the group consisting of: power generation, semiconductor manufacturing, circuit board manufacturing, metal finishing, metal plating, refining, and automotive.
21 . A method of removing one or more heavy metals including mercury from industrial wastewater by use of a solid-liquid separation process comprising the following steps:
a. maintaining the pH of said industrial wastewater to achieve at least the hydroxide precipitation of mercury;
b. adding an effective amount of a water soluble ethylene dichloride ammonia polymer having a molecular weight of from about 500 to about 10,000 daltons that contain from about 5 to about 50 mole percent of dithiocarbamate salt groups to react with at least mercury in said industrial wastewater; and
c. passing said treated industrial wastewater through a solid liquid-separation device, excluding a UF or MF membrane, and
d. optionally passing said industrial wastewater from step c) through one or more additional solid liquid-separation devices, optionally wherein said solid liquid-separation devices are selected from the group consisting of: a UF or a MF membrane.
22 . The method of claim 21 , wherein said solid-liquid separation device is selected from the group consisting of: a centrifuge, a lamellae plate clarifier, or a combination thereof.
23 . The method of claim 21 further comprising: passing a filtrate from said solid liquid separation device through an ultrafiltration or a microfiltration membrane, and optionally wherein filtrate from said ultrafiltration or microfiltration membrane is passed through an additional membrane, wherein said additional membrane is a nanofiltration membrane or a reverse osmosis membrane.