US 4,539,119 AGranted

Process for the treatment of waste and contaminated waters with improved recovery of aluminum and iron flocculating agents

OwnerEverett D. Canninventor

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Abstract

Waste-containing (contaminated) waters are treated for reuse and disposal with acceptable environmental improvements by adding a sulfate salt of aluminum and/or iron alkalized to form a waste-cohering hydroxide floc in one or more treatment plants, recovering the flocs and wastes by contacting with sulfur oxides to redissolve the aluminum and/or iron for reuse, in which case low cost sulfur containing fuels are utilized to provide heat and sulfur for recovering over one-half of the sulfur dioxide for reuse and reducing the lime required to neutralize the acidity.

Claims7

Dependent claims

In a process for the treatment of domestic sewage and industrial waste waters containing suspended solids and phosphates wherein said solids are separated from said waste waters by introducing into said waste water a flocculating agent selected from the group consisting of the sulfates of iron and aluminum under neutral to weak acid conditions to effectively convert the flocculating agent to its hydroxide and thereby form a flocculating concentrate containing the hydroxide of said flocculating agent and said suspended solids, the improved method of recovering and recycling said flocculating agents and of disposing of said suspended solids which comprises:

contacting said concentrate with at least one sulfur oxide gas in an amount sufficient to convert the hydroxide of said flocculating agent to a member of the group consisting of sulfates, sulfites, and bisulfites and with oxygen in an amount sufficient to convert said sulphites and bisulfites to water soluble sulfates to thereby redissolve said flocculating agent, said contacting including contacting said concentrate countercurrently in a first sulfur dioxide absorption chamber with a flue gas comprising sulfur dioxide and air produced in a second sulfur dioxide absorption chamber at ambient temperatures to absorb substantially all the sulfur dioxide present in said flue gas into said concentrate, contacting the concentrate containing absorbed surlfur dioxide countercurrently in said second sulfur dioxide absorption chamber with a flue gas comprising sulfur dioxide, sulfur trioxide and air produced in a third sulfur dioxide absorption chamber to reduce the pH of said concentrate to about 1.0, passing said concentrate to a first retention chamber for at least about 2 hours at ambient temperatures, contacting said concentrate countercurrently in said third sulfur dioxide adsorption chamber with a furnace flue gas stream containing sulfur dioxide, sulfur trioxide, and air, to raise the temperature of said concentrate to about 77.degree. F., passing said concentrate to a second retention chamber for at least about 2 hours to complete the reaction of the sulfur dioxide with said concentrate, mixing said concentrate with an effective amount of lime and sulfur containing fuels to adjust the pH of said concentrate to about 4.5 and precipitate the phosphates of said flocculating agent, separating the resulting soluble flocculating agent from separated solids comprising said suspended solids, said phosphates, and said sulfur containing fuels, recycling said flocculating agent to said treatment process, and drying and burning said separated solids to form said furnace flue gas and disposable solids.

Dependencies are inferred from the claim text.

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Abstract

contacting said concentrate with at least one sulfur oxide gas in an amount sufficient to convert the hydroxide of said flocculating agent to a member of the group consisting of sulfates, sulfites, and bisulfites and with oxygen in an amount sufficient to convert said sulphites and bisulfites to water soluble sulfates to thereby redissolve said flocculating agent, said contacting including contacting said concentrate countercurrently in a first sulfur dioxide absorption chamber with a flue gas comprising sulfur dioxide and air produced in a second sulfur dioxide absorption chamber at ambient temperatures to absorb substantially all the sulfur dioxide present in said flue gas into said concentrate, contacting the concentrate containing absorbed surlfur dioxide countercurrently in said second sulfur dioxide absorption chamber with a flue gas comprising sulfur dioxide, sulfur trioxide and air produced in a third sulfur dioxide absorption chamber to reduce the pH of said concentrate to about 1.0, passing said concentrate to a first retention chamber for at least about 2 hours at ambient temperatures, contacting said concentrate countercurrently in said third sulfur dioxide adsorption chamber with a furnace flue gas stream containing sulfur dioxide, sulfur trioxide, and air, to raise the temperature of said concentrate to about 77.degree. F., passing said concentrate to a second retention chamber for at least about 2 hours to complete the reaction of the sulfur dioxide with said concentrate, mixing said concentrate with an effective amount of lime and sulfur containing fuels to adjust the pH of said concentrate to about 4.5 and precipitate the phosphates of said flocculating agent, separating the resulting soluble flocculating agent from separated solids comprising said suspended solids, said phosphates, and said sulfur containing fuels, recycling said flocculating agent to said treatment process, and drying and burning said separated solids to form said furnace flue gas and disposable solids.