Methods and compositions for treating industrial wastewater

Patent metadata

Field	Value
Publication number	US-12459843-B2
Application number	US-201917417219-A
Country	US
Kind code	B2
Filing date	Dec 30, 2019
Priority date	Dec 28, 2018
Publication date	Nov 4, 2025
Grant date	Nov 4, 2025

Abstract

The present embodiments generally relate to methods and compositions for the removal of selenium from a fluid in need of treatment, such as, for example, industrial wastewaters. The methods and compositions for the removal of selenium generally comprise the use of one or more coagulants, such as at least one iron-containing coagulant, and one or more reducing agents, such as at least one sodium sulfite-based reducing agent.

First claim

The invention claimed is:

1 . A method for removing selenium from a fluid in need of treatment, wherein said method comprises adding one or more coagulants and one or more sulfite-based reducing agents to the fluid in an amount effective to reduce the amount of and/or remove at least a portion of the selenium from said fluid in need of treatment, thereby producing a fluid mixture comprising the one or more coagulant and the one or more sulfite-based reducing agents,
wherein the fluid mixture comprises a ratio of the sulfite-based reducing agent to the coagulant, in unit of ppm dry sulfite-based reducing agent:ppm dry coagulant, of between about 0.36 to about 0.48.

2 . The method of claim 1 , wherein:
i. said one or more coagulants comprise or consist of iron containing coagulants; ii. said one or more coagulants comprise or consist of ferrous chloride; iii. said one or more sulfite-based reducing agents comprise or consist of sodium metabisulfite; iv. said one or more coagulants comprise or consist of ferrous chloride and said one or more sulfite-based reducing agents comprise sodium metabisulfite; and/or v. a combination of any two or more of (i)-(iv).

3 . The method of claim 1 , wherein said method comprises:
a. adding one or more coagulants comprising ferrous chloride, and one or more sulfite-based reducing agents comprising sodium metabisulfite, to said fluid to produce the fluid mixture; b. conditioning the fluid mixture comprising the one or more coagulants and one or more reducing agents; c. adjusting a pH of the fluid mixture to between about 9 to about 10; d. conditioning the fluid mixture following pH adjustment; e. optionally adding one or more flocculants to said fluid mixture; f. allowing sludge to settle; and g. separating the selenium from the fluid mixture.

4 . The method of claim 3 , wherein:
i. step b. comprises conditioning said fluid mixture for 5-10 min, 5-15 min, 5-20 min, 5-25 min, 5-30 min, 5-35 min, 5-40 min, 5-45 min, 5-50 min, 5-55 min, or 5-60 min; ii. step d. is of a duration of time sufficient to achieve maximum selenium removal; iii. step d. comprises conditioning said fluid mixture for about 3-5 min, 5-10 min, 5-15 min, 5-20 min, 5-25 min, 5-30 min, 5-35 min, 5-40 min, 5-45 min, 5-50 min, 5-55 min, or 5-60 min; iv. a decrease in the duration of time of conditioning in step d., after adjusting the pH, results in a higher degree of selenium removal as compared to longer duration of time(s) that is a method comprising a 5 min. duration conditioning step removes more selenium than a method comprising a 10 min. duration conditioning step; v. an increase in the duration of time of conditioning in step b., prior to adjusting the pH, results in a higher degree of selenium removal as compared to longer duration of time(s) that is a method comprising a 30 min. duration conditioning step removes more selenium than a method comprising a 15 min. duration conditioning step; vi. step d. comprises conditioning said fluid mixture for about 3-5 min; vii. steps a.-e. comprise agitating said fluid mixture; viii. step e. comprises the addition of one or more polymer-based flocculants; ix. step c. comprises the addition of one or more caustic agents, optionally wherein the one or more caustic agents are selected from the group consisting of: lime, sodium sulfide, sodium hydroxide, potassium hydroxide, other caustic substances, and mixtures thereof; x. in step g. selenium is separated from the fluid mixture by (1) gravity settling, or (2) the use of centrifuges, hydrocyclones, decantation, filtration, thickeners, or other mechanical separation methods; xi. said one or more flocculants comprise one or more of the following: one or more polymer-based flocculants; one or more anionic polymer flocculants; one or more nonionic polymer flocculants; one or more high molecular weight anionic or nonionic polymer flocculants; one or more flocculant-grade homopolymers, copolymers, and terpolymers prepared from monomers such as (meth)acrylic acid, (meth)acrylamide, N-t-butyl acrylamide sulfonic acid (ATBS), and ethylene oxide; and mixtures thereof, xii. in step e. an amount of the one or more flocculants added is 5-100 ppm, 5-75 ppm, 5-50 ppm, 5-25 ppm, or 5-10 ppm; xiii. step b. increases the degree of selenium removal from said fluid as compared to a method that does not comprise step b.; xiv. step f. comprises allowing the sludge to settle for about 10 min. or more; and/or xv. a combination of any two or more of (i)-(xiv).

5 . The method of claim 1 , wherein:
i. said method results in removal of 20-96%, 40-96%, 60-96%, or 80-96% of selenium from said fluid; ii. said method results in removal of an amount of selenium from said fluid such that said fluid meets a desired standard regarding the amount of selenium present in the fluid; iii. said method results in a selenium concentration in the fluid of about 100 ppb or less, about 90 ppb or less, about 80 ppb or less, about 70 ppb or less, about 60 ppb or less, about 50 ppb or less, about 40 ppb or less, about 30 ppb or less, about 20 ppb or less, about 13 ppb or less, about 10 ppb or less, about 5 ppb or less, or about 1 ppb or less; iv. an amount ranging from 10-10,0000 ppm, 10-5000 ppm, 10-4000 ppm, 10-3000 ppm, 10-2000 ppm, 10-1500 ppm, 10-1000 ppm, 10-800 ppm, 10-600 ppm, 10-400 ppm, 10-200 ppm, 10-100 ppm, 10-50 ppm, or 10-25 ppm of said one or more coagulants is added to said fluid; v. an amount ranging from 10-10,0000 ppm, 10-5000 ppm, 10-4000 ppm, 10-3000 ppm, 10-2000 ppm, 10-1500 ppm, 10-1000 ppm, 10-800 ppm, 10-600 ppm, 10-400 ppm, 10-200 ppm, 10-100 ppm, 10-50 ppm, or 10-25 ppm of said one or more sulfite-based reducing agents is added to said fluid; vi. said one or more coagulants and one or more sulfite-based reducing agents are added simultaneously to said fluid in need of treatment; vii. the addition of the one or more sulfite-based reducing agents and one or more coagulants is sequential; viii. said one or more sulfite-based reducing agents and/or one or more coagulants are added to the fluid in need of treatment in one or more doses as needed or in intervals, in a stepwise fashion, or in a continuous fashion; ix. said fluid in need of treatment comprises drinking water; ground water; well water; surface water comprising waters from lakes, ponds and wetlands; agricultural waters; wastewater comprising wastewater or leaching water from mining or industrial processes; industrial wastewater; geothermal fluids; and water from mining processes associated with smelting, mine dewatering, tailing impoundment treatment, chemical induced leaching, flotation, autoclave, or acid mine drainage; x. said fluid in need of treatment is produced from a mining process comprising a smelting process of gold, copper, iron, nickel, silver, phosphate, coal or molybdenum; or processes associated with mine dewatering, tailing impoundment treatment, chemical induced leaching, flotation, autoclave, or acid mine drainage; xi. said fluid in need of treatment comprises water and one or more oxyanions; xii. the fluid in need of treatment comprises selenate and/or selenite; xiii. the fluid in need of treatment comprises produced water; xiv. the fluid in need of treatment comprises water used in or derived from gas production and/or gas exploration processes; xv. the fluid in need of treatment comprises sea water or other brackish water; xvi. the fluid in need of treatment comprises boiler water, cooling water, seawater optionally in oil platform applications, brackish water, oilfield water, municipal treatment plant water, paper mill water comprising water used to process pulp, paper, and/or cardboard, mining water, water resulting from any part of a method associated with enhanced oil recovery, reverse osmosis process wat

Assignees

• Kemira Oyj

Inventors

• Yin Xihui
• Durand Jean Robert
• Strickland Forrest
• Casasus Anna

Classifications

• C02F2101/106

  Selenium compounds · CPC title

• C02F1/70

  by reduction {(C02F1/4676 takes precedence)} · CPC title

• C02F1/66

  by neutralisation; pH adjustment (for degassing C02F1/20; using ion-exchange C02F1/42; for flocculation or precipitation of suspended impurities C02F1/52; for removing dissolved compounds C02F1/58) · CPC title

• C02F1/56

  Macromolecular compounds · CPC title

• C02F1/5245 Primary

  using basic salts, e.g. of aluminium and iron · CPC title