Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
273 words
A combined biological-chemical method for detoxifying a slurry of sludge of the municipal sewage or industrial organic type, which sludge contains excess-waste thermophilic bacteria, biodegradable organic material, sulfur, and toxic heavy metals in insoluble form, which comprises the sequential steps of: (a) introducing a sufficient quantity of the sludge slurry into an enclosed insulated reactor vessel to fill the same to about one-half of its volume; (b) aerating the slurry with ambient air by means of a self-aspirating aerator, and simultaneously cutting foam produced thereby, thereby to effect autoheating of the slurry by the thermophilic bacteria to a temperature maintained in the thermophilic range of from about 43° C. to about 70° C., said autoheating being achieved by conservation of the metabolic heat of oxidation of the biodegradable organic material in said insulated reactor vessel; (c) retaining said autoheated slurry in said reactor for a hydraulic retention time of 3 to 8 days sufficient to destroy the pathogenic bacteria and increase the oxidation reduction potential to a level greater than +500 mv, whereby the sulfur and heavy metals are converted to a desired higher oxidation state; (d) adding to said autoheated slurry a quantity of concentrated acid in an amount sufficient to acidify said slurry to a pH value ranging from 1.0 to 3.0 for an acidification period of 6 to 12 hours sufficient to solubilize the heavy metals while maintaining said oxidation reduction potential at a level greater than zero mv, and the temperature in the thermophilic range; and (e) dewatering the acidified slurry to remove the solubilized heavy metals therefrom, thereby to produce dewatered, detoxified acidic sludge and acidic, heavy-metal-containing water.
Claim 2
Dependent Claim
273 words
A combined biological-chemical method for detoxifying a slurry of sludge of the municipal sewage or industrial organic type, which sludge contains excess-waste thermophilic bacteria, biodegradable organic material, sulfur, and toxic heavy metals in insoluble form, which comprises the sequential steps of: (a) introducing a sufficient quantity of the sludge slurry into an enclosed insulated reactor vessel to fill the same to about one-half of its volume; (b) aerating the slurry with ambient air by means of a self-aspirating aerator, and simultaneously cutting foam produced thereby, thereby to effect autoheating of the slurry by the thermophilic bacteria to a temperature maintained in the thermophilic range of from about 43° C. to about 70° C., said autoheating being achieved by conservation of the metabolic heat of oxidation of the biodegradable organic material in said insulated reactor vessel; (c) retaining said autoheated slurry in said reactor for a hydraulic retention time of 3 to 8 days sufficient to destroy the pathogenic bacteria and increase the oxidation reduction potential to a level greater than +500 mv, whereby the sulfur and heavy metals are converted to a desired higher oxidation state; (d) adding to said autoheated slurry a quantity of concentrated acid in an amount sufficient to acidify said slurry to a pH value ranging from 1.0 to 3.0 for an acidification period of 6 to 12 hours sufficient to solubilize the heavy metals while maintaining said oxidation reduction potential at a level greater than zero mv, and the temperature in the thermophilic range; and (e) dewatering the acidified slurry to remove the solubilized heavy metals therefrom, thereby to produce dewatered, detoxified acidic sludge and acidic, heavy-metal-containing water.
Claim 3
Dependent Claim
24 words
The method as recited in claim 1, wherein said autoheated slurry is retained in said reactor for a period of 3 to 5 days.
Claim 4
Dependent Claim
23 words
The method as recited in claim 2, wherein the preferred retention time of said autoheated slurry in said reactor vessel is five days.
Claim 5
Dependent Claim
33 words
The method as recited in claim 1, and further including the step of transferring said autoheated slurry from said reactor into an insulated effluent tank, and acidifying said slurry in said effluent tank.
Claim 6
Dependent Claim
24 words
The method a recited in claim 1, and further including the step of transferring said slurry in succession through a series of reactor vessels.
Claim 7
Dependent Claim
60 words
The method as recited in claim 5, wherein said series of reactor vessels consists of three said reactors, and further wherein said slurry is retained in each said reactor for at least one day, and further including the step of recovering heat from said autoheated slurry, whereby each said reactor will be maintained at a temperature of approximately 65° C.
Claim 8
Dependent Claim
41 words
The method as recited in claim 1, wherein said concentrated acid is selected from the group consisting of sulfuric acid and hydrochloric acid, and further wherein the preferred pH value range of said acidified autoheated slurry is from 1.5 to 2.5.
Claim 9
Dependent Claim
41 words
The method as recited in claim 1, and further including the step of aerating said autoheated slurry under controlled conditions during said acidification period to maintain said oxidation reduction potential at a level conducive for the acid solubilization of heavy metals.
Claim 10
Dependent Claim
23 words
The method as recited in claim 1, and further including the additional step of recovering said heavy metals from said acidic, heavy-metal-containing water.
Claim 11
Dependent Claim
47 words
The method as recited in claim 1, and further including the step of incorporating said method in parallel with existing sludge treatment systems wherein a portion of the sludge stream flowing through said existing system is directed into said reactor vessel and thereon through said detoxification system.
Claim 12
Dependent Claim
41 words
The method as recited in claim 10, and further including the step of combining said dewatered, detoxified acidic sludge with non-acidic sludge from said existing treatment system, the pH and alkalinity of the resulting mixture being acceptable for direct land application.