US4001114A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Waste water treatment process
Assignee: SCM Corp
•
Filing: 1975-05-19
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Granted: 1977-01-04
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Expires: 1995-05-19
Abstract
Abstract Waste water feed contaminated with fatty residue and a recycle of froth from a later stage of the process are acidulated; the resulting less dense oil phase is separated from the remaining denser aqueous phase; the pH of the latter then is raised to at least about 6 and it subjected to a dissolved air flotation operation for producing (a) a froth for recycle into admixture with said waste water feed, and (b) a treated water underflow substantially free of initial fatty residue content.
Inventors
- 👤 Joel J. Joseph
- 👤 John R. Keigher
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-28 22:47
CPC Classifications
B; B01; B01D; B01D17/00; B01D17/02; B01D17/0205; B01D17/0208; B01D17/04; B01D17/047
Claims Analysis
Total Claims: 5
Claim 1
Independent Claim
123 words
In a process for treating waste water contaminated with fatty residue wherein said waste water is subjected to density separation for removing accumulated lighter oil phase from denser aqueous phase; and said denser aqueous phase is treated with flocculating agent and sufficient base for rendering pH of same at least about 6; and the resulting treated denser aqueous phase subjected to dissolved air flotation for recovery of stripped water product phase from formed oily froth; the improvement which comprises: mildly acidulating with acid said waste water to pH of about 3-5.5 prior to said density separation step; and permitting said oil froth collected from said dissolved air flotation step to flow by gravity into admixture with said waste water admitted to said process.
Claim 2
Dependent Claim
123 words
In a process for treating waste water contaminated with fatty residue wherein said waste water is subjected to density separation for removing accumulated lighter oil phase from denser aqueous phase; and said denser aqueous phase is treated with flocculating agent and sufficient base for rendering pH of same at least about 6; and the resulting treated denser aqueous phase subjected to dissolved air flotation for recovery of stripped water product phase from formed oily froth; the improvement which comprises: mildly acidulating with acid said waste water to pH of about 3-5.5 prior to said density separation step; and permitting said oil froth collected from said dissolved air flotation step to flow by gravity into admixture with said waste water admitted to said process.
Claim 3
Dependent Claim
18 words
The process of claim 1 wherein the stripped water product phase is passed to a subsequent purification operation.
Claim 4
Dependent Claim
15 words
The process of claim 2 wherein said subsequent purification operation is treatment with activated sludge.
Claim 5
Dependent Claim
21 words
The process of claim 1 wherein the flow of said denser aqueous phase from step (b) thereof is maintained substantially constant.
References Cited (Backward Citations)
US1807833A
Cited
US1947709A
Cited
US2217143A
Cited
US3192155A
Cited
US3259567A
Cited
US3419493A
Cited
US3707464A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1980-01-04 | 1980-07-05 | 1981-01-04 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-01-04 | 1984-07-05 | 1985-01-04 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-01-04 | 1988-07-05 | 1989-01-04 | $7700.00 | Window Closed / Lapsed |