IP Library › Granted Patent US 12,246,978
Granted Patent B2
US 12,246,978 · App. 16/952,840 · Granted Mar 11, 2025

Water treatment system and method

Inventors: Julian Fisher (Dallas, TX); Randy A Galgon (Nuremberg, PA); Patrick Ryan (Minneapolis, MN); Jaren Leet (Walnut Creek, CA); Ray Stickney (Port Rowan, CA)
Assignee: Hyperion Water Technologies LLC
C02F9/00B01D53/343B01D53/76C02F1/004C02F2001/007C02F1/048C02F1/20C02F1/24C02F1/325C02F1/34C02F1/40C02F1/78C02F2101/32C02F2103/10C02F2103/365C02F2301/046C02F2303/04
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Quick Facts
Patent No.
US 12,246,978
App. No.
16/952,840
Granted
Mar 11, 2025
Kind
B2
Abstract

A water treatment system and method. Influent water produced from an oil and gas production or the like is circulated in a multistage unit where the water is treated by degassing the water by saturating the water with air, stripping volatile compounds from the water, evaporating non-aqueous phase liquid petroleum from the water, repeatedly stripping and equilibrating inorganic carbons in the water, subliming semi-solids from the water, and breaking colloids in the water using continuous cavitation. Water from the multistage unit is clarified through floatation and sedimentation and biological material in the water is inactivated using irradiation. Water is then filtered before being provided as treated water for an application specific process such as electro desalination reversal, fracking reuse, or other wastewater recovery.

Claims (75)

1. A method for treating water, the method comprising:

supplying influent water to a multiple stage processing unit;

processing the water in each stage of the multiple stage processing unit by performing each of the steps of:

degassing the water by saturating the water with air;

stripping volatile compounds from the water;

evaporating non-aqueous phase liquid petroleum from the water;

decarbonating the water;

subliming semi-solids from the water;

resolving emulsions in the water; and

breaking colloids in the water using continuous cavitation; and

depositing and ripening petroleum solids;

wherein each stage of the processing unit is connected in series to an adjacent stage; and

wherein a portion of the water from a given stage is circulated to a fluid inlet of a subsequent stage; and

wherein gas emissions from a given stage are circulated to a gas inlet of a preceding of stage;

clarifying the water discharged from the multiple stage processing unit through floatation and sedimentation;

inactivating volatile microbes in the water discharged from the processing unit;

filtering the water discharged from the processing unit; and

combusting gaseous emissions.

2. The method of claim 1 wherein the multiple stage processing unit comprises a series of six stages; and

wherein the influent water is supplied to an inlet of a first stage of the series of stages; and

wherein a portion of the water from the first stage is circulated to an inlet of a second stage; and

wherein a portion of the water from a final sixth stage of the series of stages is circulated to a clarifier for the clarifying step;

wherein control gas is supplied to the final sixth stage; and

wherein air emissions from the sixth stage are circulated to a fifth stage of the series of stages; and

wherein gas emissions from the first stage are circulated to a unit for step of combusting gaseous emissions.

3. The method of claim 1 further comprising the steps of:

injecting ozone into the multiple stage processing system; and

skimming a residue from the water in the first stage of the processing system.

4. The method of claim 1 wherein the filtering step comprises filtering water using a plurality of ceramic filters.

5. The method of claim 1 wherein the degassing step comprises passing the water across a deflector in a venturi system and circulating the water in a degassing sump.

6. The method of claim 1 wherein the stripping step comprises passing the water through a stripper having a venturi system.

7. The method of claim 1 wherein the stripping step comprises passing the water through a venturi system and into a sump; and

wherein the degassing step comprises circulating the water in the sump; and

wherein the evaporating step comprises forcing the water from the venturi system through a residual layer in the sump at high pressure.

8. A method for treating an influent water in each stage of a multiple stage processing unit, the method comprising:

degassing the water by saturating the water with air;

stripping volatile compounds from the water;

evaporating non-aqueous phase liquid petroleum from the water;

decarbonating the water, and killing or inactivating volatile microbes in the water.

9. The method of claim 8 where the step of decarbonating the water comprises repetitively stripping and equilibrating the total inorganic carbon specie in the water.

10. The method of claim 8 further comprising:

clarifying the water through floatation and sedimentation; and

filtering the water.

11. The method of claim 8 further comprising:

subliming semi-solids from the water; and

breaking the colloids in the water using continuous cavitation.

12. The method of claim 8 further comprising the step of combusting gaseous emissions.

13. A system for treating produced water, the system comprising:

a multiple stage processing unit, wherein each stage comprises:

a fluid mobilization unit comprising:

a fluid chamber having at least one partition;

a fluid inlet attached to the chamber;

a pump; and

a fluid outlet; and

a fluid processing component comprising:

a degassing sump, the sump having a water outlet;

a stripper positioned above the sump, the stripper having at least one water inlet operatively connected to the fluid outlet;

an air inlet adjacent the stripper;

a gas exhaust adapted to circulate gases from the sump to the stripper;

wherein the pump operates to move fluid from the fluid chamber to the water inlet of the processing component; and

a regenerative thermal oxidizer;

a clarifier unit;

an ultraviolet irradiation unit; and

a filtration unit;

wherein exhaust gases from a first stage of the processing unit are circulated to the thermal oxidizer; and

wherein influent water is adapted to be supplied to the fluid inlet of the first stage; and

wherein fresh air is adapted to be supplied to the air inlet of a final sixth stage of the processing unit.

14. The system of claim 13 wherein the water outlet of the first stage is operatively connected to the fluid inlet of a second stage of the processing unit; and

fluid inlet of a second stage of the processing unit; and

wherein the gas exhaust of the final sixth stage is operatively connected to the air inlet of a fifth stage of the processing unit.

15. The system of claim 13 wherein the first stage of the processing unit further comprises a skimmer operatively connected to the sump.

16. The system of claim 13 wherein the sump comprises a fluid conduit disposed proximate a base of the sump; and

wherein the fluid conduit has a first end operatively connected to the water outlet of the sump and a second end disposed in fluid communication with fluid in the sump.

17. The system of claim 13 wherein the irradiation unit comprises a vent; and

wherein gases vented from the vent are circulated to the multiple-stage processing unit.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 4, 2025
From: HYPERION H2O LLC
To: HYPERION WATER TECHNOLOGIES LLC
Reel/Frame 070106/0890 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 19, 2020
From: FISHER, JULIAN; GALGON, RANDY A.; RYAN, PATRICK; LEET, JAREN; STICKNEY, RAY
To: HYPERION H20 LLC
Reel/Frame 054425/0132 →
Continuity (2)
Provisional Application 62938267 · Nov 20, 2019
Related Publication 20210147272A1 · May 20, 2021
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