# US 12,110,245 B2 · Method and apparatus for treating natural gas and oil well waste waters for removal of contaminants and dissolved solids > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 12,110,245 B2 - Document ID: US12110245B2 - Status: Granted - Kind: B2 - Application number: 16/191,688 - Filed: 2018-11-15 - Published: 2019-08-15 - Granted: 2024-10-08 - Earliest claimed: 2013-02-01 - Assignees: Eau Midstream, Inc. - Applicants: Eau Midstream, Inc. - Inventors: Francis C. Miller; Steven B. Addleman - Web page: https://patentgrep.com/patent/US12110245B2 ## CPC - C02F 9/00: Multistage treatment of water, waste water or sewage - C02F 1/441: {by reverse osmosis} - C02F 1/463: by electrocoagulation - C02F 1/66: 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) - C02F 1/78: with ozone {(C02F1/4672 takes precedence)} - C02F 1/004: {using large scale industrial sized filters} - C02F 1/283: {using coal, charred products, or inorganic mixtures containing them} - C02F 1/52: by flocculation or precipitation of suspended impurities {(C02F1/463 takes precedence)} - C02F 1/5236: {using inorganic agents} - C02F 1/56: Macromolecular compounds - C02F 1/72: by oxidation {(C02F1/4672 takes precedence)} - C02F 1/722: {Oxidation by peroxides} - C02F 5/02: Softening water by precipitation of the hardness - C02F 5/06: using calcium compounds - C02F 11/121: by mechanical de-watering - C02F 2101/108: {Boron compounds} - C02F 2103/10: from quarries or from mining activities - C02F 2103/365: {from petrochemical industry (e.g. refineries)} - C02F 2209/00: Controlling or monitoring parameters in water treatment - C02F 2209/03: Pressure - C02F 2209/05: Conductivity or salinity - C02F 2209/055: Hardness - C02F 2209/11: Turbidity - 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) ## Abstract A method for treating wastewater is disclosed. The method is useful in particular for treating wastewater that is generated from the process of drilling, hydraulic fracturing and/or cleaning a bore of an oil or natural gas well bore. The method may include performing cold lime softening of the wastewater to form waste salt flocs, filtration of waste salt flocs, ozonation of the filtrate from the filtration, and reverse osmosis of the filtrate to produce a purified permeate. ## Claims ### Claim 1 A method for treating wastewater from an oil or gas well, the wastewater containing (a) suspended solids comprising at least one of a rock dust and a drilling mud, (b) residual water, and (c) organic contaminants including at least one of volatile organic compounds, oil or gas well drilling fluids, diesel oil, or natural crude oil, the method comprising: a) infusing a gas containing ozone into a stream of the wastewater, and causing oxidation and decomposition of the at least one of volatile organic compounds, oil or gas well drilling fluids, diesel oil, or natural crude oil in the stream of the wastewater to result in carbon dioxide, and water; b) adding aluminum chlorohydrate to the stream of the wastewater, and causing coagulation of the suspended solids to form suspended solids flocs in the stream of the wastewater, and causing coagulation of at least a portion of the residual water to form residual water flocs in the stream of the wastewater, wherein a concentration of the aluminum chlorohydrate in the stream of the wastewater is between about 0.001 to about 0.01 parts of the aluminum chlorohydrate per part of the wastewater; c) adding a flocculant to cause growth of the suspended solids flocs and growth of the residual water flocs to separable flocs entrained in the stream of the wastewater; d) delivering the stream of the wastewater through a filter medium of a filter, retaining the separable flocs on the filter medium of the filter, and discharging a clarified wastewater stream from the filter; e) causing precipitation of dissolved waste salts in the clarified wastewater stream, and separating precipitated waste salts from the clarified wastewater stream to produce a softened wastewater stream; f) delivering the softened wastewater stream to a first vessel, and injecting hydrogen peroxide solution and nano-sized bubbles of ozone into the softened wastewater in the first vessel to produce oxidized wastewater including residual ozone and trace residual organic matter in the first vessel; g) delivering a first oxidized wastewater stream from the first vessel to a carbon filter, causing decomposition of the residual ozone in the first oxidized wastewater stream, and separating the trace residual organic matter from the first oxidized wastewater stream to produce a second oxidized wastewater stream including remaining dissolved waste salts; and h) delivering the second oxidized wastewater stream to a first reverse osmosis membrane and causing reverse osmosis through the first reverse osmosis membrane, and separation of a first portion of the remaining dissolved waste salts from the second oxidized wastewater stream to produce a first permeate wastewater stream. ### Claim 2 (depends on 1) The method of claim 1, further comprising delivering the first permeate wastewater stream to a second reverse osmosis membrane thus causing separation and removal of dissolved boron salts to a produce a second permeate wastewater stream having a first concentration of dissolved boron salts of less than 5 parts per million, and a concentrate having a second concentration of dissolved boron salts greater than the concentration of dissolved boron salts in the first permeate wastewater stream. ### Claim 3 (depends on 2) The method of claim 2, further comprising causing precipitation of the dissolved boron salts from the concentrate by addition of magnesium hydroxide to the concentrate, and separating the precipitated boron salts from the concentrate to produce a first purified wastewater stream. ### Claim 4 (depends on 1) The method of claim 1, wherein the clarified wastewater stream is at an elevated temperature greater than the temperature of the first permeate wastewater stream, and wherein the method further comprises delivering the clarified wastewater stream through a first passageway of a heat exchanger while delivering the first permeate wastewater stream through a second passageway of a heat exchanger in counterflow with respect to the direction of flow of the clarified wastewater stream flowing through the first passageway of the heat exchanger. ### Claim 5 (depends on 1) The method of claim 1, further comprising measuring concentration of waste salts in the wastewater, and executing an algorithm by a programmable logic controller to produce the first permeate wastewater stream based upon the concentration of waste salts in the wastewater. ### Claim 6 (depends on 1) The method of claim 1, wherein the separating the precipitated waste salts from the clarified wastewater stream to produce a softened wastewater stream is performed within a single unbaffled horizontal flow vessel. ### Claim 7 (depends on 6) The method of claim 6, wherein the filter is comprised of a housing comprised of a bottom wall, a side wall, and an outlet; the filter medium is comprised of a bottom panel disposed along the bottom wall, and a side panel disposed along the side wall; and a first inflatable bladder disposed between the bottom wall of the housing and the bottom panel of the filter medium; and wherein the method further comprises: a) adding sodium carbonate to the softened wastewater stream to result in a pH of not less than 10.1 in the softened wastewater stream; b) delivering the softened wastewater stream into the housing of the filter through a floating boom conduit at a fluid velocity exiting the floating boom conduit of less than 0.15 feet per second; c) retaining the softened wastewater stream in the filter for at least 60 minutes; d) maintaining the fluid velocity of the softened wastewater stream in the filter at less than 0.0015 feet per second, thereby causing separation of precipitated carbonate salts from the softened wastewater stream to produce clarified fluid in the housing of the filter; and e) withdrawing the clarified fluid from the housing of the filter through a floating skimming funnel located distally from the floating boom conduit. ### Claim 8 A method for treating wastewater from an oil or gas well, the wastewater containing (a) suspended solids comprising at least one of a rock dust and a drilling mud, (b) residual water, and (c) organic contaminants including at least one of volatile organic compounds, oil or gas well drilling fluids, diesel oil, or natural crude oil, the method comprising: a) infusing a gas containing ozone into a stream of the wastewater, and causing oxidation and decomposition of the at least one of volatile organic compounds, oil or gas well drilling fluids, diesel oil, or natural crude oil in the stream of the wastewater to result in carbon dioxide, water, and a residual water in the stream of the wastewater; b) adding aluminum chlorohydrate to the stream of the wastewater, and causing coagulation of the suspended solids to form suspended solids flocs in the stream of the wastewater, and causing coagulation of at least a portion of the residual water to form residual water flocs in the stream of the wastewater, wherein a concentration of the aluminum chlorohydrate in the stream of the wastewater is between about 0.001 to about 0.01 parts of the aluminum chlorohydrate per part of the wastewater; c) adding a flocculant to cause growth of the suspended solids flocs and growth of the residual water flocs to separable flocs entrained in the stream of the wastewater; d) delivering the stream of the wastewater through a filter medium of a filter, retaining the separable flocs on the filter medium of the filter, and discharging a clarified wastewater stream from the filter; e) delivering the clarified wastewater stream to a first vessel, and injecting hydrogen peroxide solution and nano-sized bubbles of ozone into the clarified wastewater stream in the first vessel to produce oxidized wastewater in the first vessel; f) delivering a first oxidized wastewater stream from the first vessel to a carbon filter, causing decomposition of residual ozone in the first oxidized wastewater stream, and separating trace residual organic matter from the first oxidized wastewater stream to produce a second oxidized wastewater stream; and g) delivering the second oxidized wastewater stream to a first reverse osmosis membrane and causing reverse osmosis through the first reverse osmosis membrane, and separation of a first portion of remaining dissolved waste salts from the second oxidized wastewater stream to produce a first permeate wastewater stream. ### Claim 9 (depends on 8) The method of claim 8, further comprising delivering the first permeate wastewater stream to a second reverse osmosis membrane and causing separation and removal of dissolved boron salts to a produce a second permeate wastewater stream having a first concentration of dissolved boron salts of less than 5 parts per million, and a concentrate having a second concentration of dissolved boron salts greater than the concentration of dissolved boron salts in the first permeate wastewater stream. ### Claim 10 (depends on 9) The method of claim 9, further comprising causing precipitation of the dissolved boron salts from the concentrate by addition of magnesium hydroxide to the concentrate, and separating the precipitated boron salts from the concentrate to produce a first purified wastewater stream. ### Claim 11 (depends on 8) The method of claim 8, wherein the clarified wastewater stream is at an elevated temperature greater than the temperature of the first permeate wastewater stream, and wherein the method further comprises delivering the clarified wastewater stream through a first passageway of a heat exchanger while delivering the first permeate wastewater stream through a second passageway of a heat exchanger in counterflow with respect to the direction of flow of the clarified wastewater stream flowing through the first passageway of the heat exchanger. ### Claim 12 (depends on 1) The method of claim 1, wherein the flocculant is an anionic flocculant.