# US 5,798,043 A · Control of anaerobic wastewater treatment > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 5,798,043 A - Document ID: US5798043A - Status: Granted - Kind: A - Application number: 08/982,030 - Filed: 1997-12-01 - Granted: 1998-08-25 - Earliest claimed: 1997-12-01 - Assignees: Khudenko Engineering, Inc. - Inventors: Boris Mikhailovich Khudenko - Web page: https://patentgrep.com/patent/US5798043A ## CPC - C02F 3/286: {including two or more steps} - C02F 3/00: Biological treatment of water, waste water, or sewage {(C02F1/006 takes precedence)} - C02F 3/1231: {Treatments of toxic sewage} - C02F 3/1257: {Oxidation ditches} - C02F 3/28: Anaerobic digestion processes - C02F 3/301: {Aerobic and anaerobic treatment in the same reactor} - C02F 3/308: {Biological phosphorus removal} - Y02E 50/30: Fuel from waste, e.g. synthetic alcohol or diesel - Y02W 10/10: Biological treatment of water, waste water, or sewage - C02F: TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE (separation in general B01D; special arrangements on waterborne vessels of installations for treating water, waste water or sewage, e.g. for producing fresh water, B63J; adding materials to water to prevent corrosion C23F; treating radioactively-contaminated liquids G21F9/04; regeneration of reactants for recirculation into processes, see the relevant places for the processes) - Y02E: REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION - Y02W: CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT ## Abstract A method of controlling wastewater treatment in multi step system comprising at least one anaerobic step and at least one carbon dioxide stripping step by a combination of (1) recuperable abiotic species and carbon dioxide stripping, wherein the recuperable species can be metal ions such as calcium and iron, the said species are charged in the treatment system and form soluble carbonates maintaining the carbonic acid equilibrium and pH in anaerobic process steps and recuperated and retained in the system as insoluble carbonates or hydroxides formed in the carbon dioxide stripping step, and (2) conditioning the sludge by cultivating methanogens in the sludge in a dedicated process zone called sludge conditioner, and recycling the conditioned sludge in the reactor, wherein the volatile fatty acids are rapidly consumed by thus provided methanogens. Dramatic reduction in reagent requirements for pH and other purposes is achieved. The system can be controlled using excess reagent content and excess conditioned sludge supply. In extreme situations, simple automatic control can be used. The process can be automated using a differential pH metering, wherein one pH meter is reading pH in the carbon dioxide stripping reactor, and another pH meter measures pH in a portion of water with carbon dioxide stripped. The level of pH in a water portion with depleted carbon dioxide indicates whether carbon dioxide needs to be additionally stripped or the recycle rate from the stripping step should be increased, and/or the conditioned sludge recycle needs to be increased. ## Claims ### Claim 1 In a method for controlling treatment of wastewater conducted with biomass in a multi step system comprising at least one anaerobic treatment step and at least one carbon dioxide stripping step, wherein the said wastewater and the said biomass are sequentially treated in the said at least one anaerobic treatment step and the said at least one carbon dioxide stripping step the improvement is provided comprising the step of charging at least one recuperable abiotic control specie to at least one step in the said multi step system, whereby the said abiotic control species form insoluble carbonates or hydroxides in the said at least one carbon dioxide stripping step and at least partially convert into soluble bicarbonates in the said at least one anaerobic step. ### Claim 2 (depends on 1) The method as claimed in claim 1, and further providing steps of separating at least a portion of the said biomass from the said multi step system, digesting the said separated biomass to produce digested biomass, and feeding at least a portion of the said digested biomass in at least one step of the said multi step system. ### Claim 3 (depends on 2) The method as claimed in claim 2, and further providing steps of pH measurement in the said anaerobic step, varying the rate of feeding the said digested biomass in at least one step in the said multi step system, and varying the recycle rate of the said insoluble carbonates from the said at least one carbon dioxide stripping step to the said at least one anaerobic step. ### Claim 4 (depends on 3) The method as claimed in claim 3, and further providing steps of differential pH measurement and controlling efficiency of the said at least one step of carbon dioxide stripping. ### Claim 5 (depends on 1) The method as claimed in claim 1, wherein the said wastewater is selected from the group comprising water, wastewater, aqueous industrial, agricultural and production materials, industrial, agricultural and production gases, polluted air, gaseous vent emissions, solid waste, materials of plant, animal, or fossil origin, and solid industrial, agricultural or production streams, and combinations thereof. ### Claim 6 (depends on 1) The method as claimed in claim 1, wherein the operation mode of at least one step in the said multi step system is selected from the group comprising batch operation, continuous operation, and combinations thereof. ### Claim 7 (depends on 6) The method as claimed in claim 6, wherein the said batch operation mode comprises steps of filling-stripping, reacting-stripping, settling, and decanting the said wastewater. ### Claim 8 (depends on 7) The method as claimed in claim 7, and further providing a step of sludge conditioning. ### Claim 9 (depends on 1) The method as claimed in claim 1, wherein the said carbon dioxide stripping step is combined with at least one step of the said multi step system selected from the group comprising an obligate anaerobic se facultative anaerobic step, anoxic treatment step, aerobic treatment step and obligate aerobic step, and combinations thereof. ### Claim 10 (depends on 1) The method as claimed in claim 1, wherein the arrangement of the said steps in the said multi step system is selected from a group comprising sequential treatment steps parallel treatment steps, parallel-sequential treatment steps, treatment steps in a race track arrangement, and treatment steps with recirculating the said wastewater and the said biomass among and between the said steps, and combinations thereof. ### Claim 11 (depends on 1) The method as claimed in claim 1, wherein the said biomass in the said steps of the said multi step system is composed of organisms selected from the group comprising obligate aerobic, facultative aerobic, anoxic, facultative anaerobic, and obligate anaerobic microorganisms, and mixtures thereof. ### Claim 12 (depends on 1) The method as claimed in claim 1, wherein the said recuperable abiotic control specie is selected from the group comprising calcium, magnesium, zinc, aluminum, iron, nickel, cobalt, manganese, cesium, and combinations thereof. ### Claim 13 (depends on 12) The method as claimed in claim 12, wherein the said recuperable abiotic control specie is selected from the group comprising zero-valent metals, salts, metal oxides, metal hydroxides, organometallic compounds, and combinations thereof. ### Claim 14 (depends on 1) The method as claimed in claim 1, wherein digestion gas is generated in the said anaerobic step, and further providing steps selected from a group comprising discharging the said digestion gas to the atmosphere, utilizing the said digestion gas, combusting the said digestion gas for elimination, and combinations thereof.