GREYWATER TREATMENT SYSTEM

Abstract

A system and method for removing contaminates from greywater that uses carbon dioxide (CO.sub.2) and a system that adjusts the pH between 6 and 9. The filtration system is cost effective, quick, and easy to use, resulting in purified water.

Claims

1. A system for the purification of greywater comprising: a) a large particle filter; b) a small fines filter; c) a CO.sub.2 source; d) a first bubbling chamber to receive CO.sub.2 from the CO.sub.2 source, which produces a carbonic acid; e) a pressure chamber to separate the solids from the carbonated greywater and retaining the carbonic acid state by keeping a pressure of about between 1 and 10 psi; and f) a second bubbling chamber to suspend the fines solids from the treated greywater.

2. The system for the purification of greywater according to claim 1, wherein the greywater is filtered by the large particle filter before adding the greywater to the bubbling chamber.

3. The system for the purification of greywater according to claim 1, wherein the greywater is filtered by the small fines filter after the treated greywater leaves the second bubbling chamber.

4. The system for the purification of greywater according to claim 1, wherein the carbonated greywater is at a pH of between about 6 and 7.

5. The system for the purification of greywater according to claim 1, wherein the CO.sub.2 source is carbon captured CO.sub.2.

6. A method for the treatment of greywater comprising: a) filtering the greywater with a large particle filter; b) adding the filtered greywater to a bubbling chamber; c) using a first single pass bubbling CO.sub.2 into the bubbling chamber until the filtered greywater is saturated with CO.sub.2 to a pH between 6 and 9 prior to entering a pressure chamber; d) transferring the saturated greywater to the pressure chamber at a pressure of about 1 to 10 psi until carbonic acid is created to suspend a majority of solids in the water; e) transferring the carbonic acid greywater and the suspended solids to a second bubbling chamber and bubbling CO.sub.2 to suspend any remaining solids in the water; and f) filtering the suspended solids through a small fines filter.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0020] FIG. 1 is a graphic of the system of the present invention.

[0021] FIG. 2 is a flow chart of the method of the present invention.

DETAILED DESCRIPTION OF THE INVENTION

[0022] While this invention is susceptible to embodiment in many different forms, there is shown in the drawings, and will herein be described in detail, specific embodiments with the understanding that the present disclosure of such embodiments is to be considered as an example of the principles and not intended to limit the invention to the specific embodiments shown and described. In the description below, like reference numerals are used to describe the same, similar, or corresponding parts in the several views of the drawings. This detailed description defines the meaning of the terms used herein and specifically describes embodiments in order for those skilled in the art to practice the invention.

Definitions

[0023] The terms “about” and “essentially” mean ±10 percent.

[0024] The terms “a” or “an”, as used herein, are defined as one or as more than one. The term “plurality”, as used herein, is defined as two or as more than two. The term “another”, as used herein, is defined as at least a second or more. The terms “including” and/or “having”, as used herein, are defined as comprising (i.e., open language). The term “coupled”, as used herein, is defined as connected, although not necessarily directly, and not necessarily mechanically.

[0025] The term “comprising” is not intended to limit inventions to only claiming the present invention with such comprising language. Any invention using the term comprising could be separated into one or more claims using “consisting” or “consisting of” claim language and is so intended.

[0026] Reference throughout this document to “one embodiment”, “certain embodiments”, “an embodiment”, or similar terms means that a particular feature, structure, or characteristic described in connection with the embodiment is included in at least one embodiment of the present invention. Thus, the appearances of such phrases in various places throughout this specification are not necessarily all referring to the same embodiment. Furthermore, the particular features, structures, or characteristics may be combined in any suitable manner in one or more embodiments without limitation.

[0027] The term “or”, as used herein, is to be interpreted as an inclusive or meaning any one or any combination. Therefore, “A, B, or C” means any of the following: “A; B; C; A and B; A and C; B and C; A, B, and C”. An exception to this definition will occur only when a combination of elements, functions, steps, or acts are in some way inherently mutually exclusive.

[0028] The drawings featured in the figures are for the purpose of illustrating certain convenient embodiments of the present invention and are not to be considered as limitation thereto. The term “means” preceding a present participle of an operation indicates a desired function for which there is one or more embodiments, i.e., one or more methods, devices, or apparatuses for achieving the desired function and that one skilled in the art could select from these or their equivalent in view of the disclosure herein, and use of the term “means” is not intended to be limiting.

[0029] As used herein, the term “purification” refers to the removal of contaminants in greywater that are part of the water that makes it greywater. Under ideal conditions, it means that the greywater is cleaned sufficiently to become potable water, but at least clean enough to use in other applications.

[0030] As used herein, the term “greywater” refers to wastewater that is generated in households or office buildings from streams without fecal contamination, i.e., all streams, except for the wastewater from toilets. Sources of greywater include sinks, showers, baths, washing machines, or dishwashers. During the process, the greywater can be filtered at ambient temperatures or between -10° F. and 125° F.

[0031] As used herein, the term “large particle filter” refers to a water filter that is capable of filtering out particles greater than about 10 microns.

[0032] As used herein, the term “small fines filter” refers to a water filter that is capable of filtering out particles less than 1-10 microns.

[0033] As used herein, the term “first bubbling chamber” refers to a chamber that can hold a quantity of greywater and then have CO.sub.2 gas bubbled throughout the greywater until 90% saturation is achieved.

[0034] As used herein, the term “pressure chamber” refers to a chamber for placing the carbonated greywater. The pressure chamber is kept under pressure at between about 1 and 10 psi. This supersaturates the greywater with CO.sub.2 creating carbonic acid, which breaks the bond with solids from the water.

[0035] As used herein, the term “second bubbling chamber” refers to a chamber for placing the supersaturated greywater in the bubbling CO.sub.2 to separate clean water from solids. In one embodiment, two or more of the chambers could be the same chamber with just a different process occurring.

[0036] As used herein, the term “CO.sub.2 source” refers to a source of CO.sub.2 in the gaseous form that can be injected into the bubbling chamber in order to carbonate the water. Any source is contemplated. In one embodiment, the CO.sub.2 is obtained by carbon capture technology.

[0037] The process of creating clean water starts with filtering large particles and fines from the greywater. This can be done at any point in the process, but in one embodiment, the large particle filtration is the first step and the small fines (particle) filtration is last after passing through the system. Greywater is placed into a bubbling chamber, and gaseous CO.sub.2 is bubbled through the greywater until it reaches the specific saturation of 6.4 pH or true carbonic acid (H.sub.2CO.sub.3). The carbonated greywater is then transferred to a pressure chamber and flows through the pressure chamber at a rate of 30 to 150 gallons per minute at about 1 to 10 psi, depending on the size of the pressure chamber and pump. The process of forcing the carbonic acid under pressure creates a steady stream of micro-implosions that generates just enough energy to separate the solids from the water. The water then passes through the third chamber where CO.sub.2 is injected at 6 psi to bubble and break the chemical bond between the water and any fines solids that did not separate in the reaction chamber, which is then run through the final fines filtration of 1 micron and other carbon based filters, sometimes including activated charcoal. The water can be manually filtered (any filter pore size) one more time resulting in clean water.

Drawings

[0038] Now referring to the drawings, FIG. 1 is a graphic representation of the system 1 of the present invention. In this view, greywater 2 is passed through a large particle filter 3 before being placed in the first bubbling chamber 4. A gaseous CO.sub.2 source 5 bubbles CO.sub.2 6 though greywater in the bubbling chamber 4 to form a saturated carbonated solution at ambient pressures. The saturated carbonated solution is transferred 8 to pressure chamber 9, where it is subjected to a pressure between about 1 and 10 psi. This transfer results in a supersaturated carbonation and creates carbonic acid, which separates the solids from the water. Lastly, the cleaned water is placed in a second bubbling chamber 11 and CO.sub.2 is bubbled through the water, which suspends fines in the water. Finally, the water, which is separated 12, passes through a small fines filter 13 to produce clean water 14.

[0039] FIG. 2 is a flow chart of an embodiment of the method of purification of greywater of the present invention. In this view, greywater 20 is filtered for large particles 21. The filtered greywater is placed in the first bubbling chamber 22 and CO.sub.2 22a is bubbled therein. The water is transferred to the pressure chamber 23 for supersaturation and energy to separate a majority of the solids from the carbonic acid. The water is then placed in the second bubbling chamber 24 for removal of solids. Lastly, the water is passed through a small fines filter 25 to create clean recyclable water 26.

[0040] Those skilled in the art to which the present invention pertains may make modifications resulting in other embodiments employing principles of the present invention without departing from its spirit or characteristics, particularly upon considering the foregoing teachings. Accordingly, the described embodiments are to be considered in all respects only as illustrative, and not restrictive, and the scope of the present invention is, therefore, indicated by the appended claims rather than by the foregoing description or drawings. Consequently, while the present invention has been described with reference to particular embodiments, modifications of structure, sequence, materials, and the like apparent to those skilled in the art still fall within the scope of the invention as claimed by the applicant.