Patent US4309291A successfully refreshed from Google Patents.
US4309291A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method of and apparatus for continuous flow flocculation and clarification
Assignee: Massachusetts Institute of Technology
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Filing: 1977-06-29
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Granted: 1982-01-05
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Expires: 1997-06-29
Abstract
Abstract A method of and apparatus for continuously removing dispersed particles which can be flocculated from a liquid containing said particles, such as wastewaters, wherein flocculation of said particles is caused to take place in a turbulent pipe flow by the injection and rapid mixing of a coagulant and/or coagulant aid in said turbulent pipe flow which simultaneously flocculates said particles and transports the mixture of flocculated particles and liquid into a settling tank for clarification. A controlled quantity of dispersed floc from said settling tank is continuously recirculated into said pipe flow at a station where mixing of the coagulant and/or coagulant aid is achieved, so as to reduce the length of said pipe to a desired size and the flow rate of said injected coagulant and/or coagulant aid.
Inventors
- 👤 Ronald F. Probstein
- 👤 Michael A. Delichatsios
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 20:02
CPC Classifications
C; C02; C02F; C02F1/00; C02F1/52; C02F1/5281; B; B01; B01D; B01D21/00; B01D21/01
Claims Analysis
Total Claims: 6
Claim 1
Independent Claim
178 words
A method of continuously removing solid particles which can be flocculated from a liquid mixture containing said solid particles, comprising providing a flocculation pipe that discharges into a settling tank, the pipe having peripheral walls that delimit a substantially uniform, open, flow cross-section throughout the length of the pipe and being devoid of internal structure within the confines of said peripheral walls, continuously introducing said mixture and a required quantity of coagulant and/or coagulant aid into said pipe remote from the discharge into the settling tank and causing the contents of the pipe to flow through the pipe at a flow velocity sufficient to produce turbulent flow conditions throughout the pipe, with a rate of turbulent energy dissipation per unit mass in the pipe and a length of flow in the pipe great enough to ensure that flocculation occurs substantially entirely in the pipe, rather than in the settling tank, and with negligible deposition of particles and floc in the pipe, said rate of energy dissipation being less than about 70 erg/sec.gm to avoid particle and floc breakup.
Claim 2
Independent Claim
178 words
A method of continuously removing solid particles which can be flocculated from a liquid mixture containing said solid particles, comprising providing a flocculation pipe that discharges into a settling tank, the pipe having peripheral walls that delimit a substantially uniform, open, flow cross-section throughout the length of the pipe and being devoid of internal structure within the confines of said peripheral walls, continuously introducing said mixture and a required quantity of coagulant and/or coagulant aid into said pipe remote from the discharge into the settling tank and causing the contents of the pipe to flow through the pipe at a flow velocity sufficient to produce turbulent flow conditions throughout the pipe, with a rate of turbulent energy dissipation per unit mass in the pipe and a length of flow in the pipe great enough to ensure that flocculation occurs substantially entirely in the pipe, rather than in the settling tank, and with negligible deposition of particles and floc in the pipe, said rate of energy dissipation being less than about 70 erg/sec.gm to avoid particle and floc breakup.
Claim 3
Dependent Claim
57 words
A method as claimed in claim 1, further comprising providing a recirculation pipe leading from the settling tank to the flocculation pipe remote from the settling tank, and continuously recirculating dispersed floc from the settling tank to the flocculation pipe through the recirculation pipe and mixing the recirculated dispersed floc with the flow in the flocculation pipe.
Claim 4
Dependent Claim
76 words
A method in accordance with claim 2, further comprising controlling the flow conditions in the recirculation pipe so that the rate of energy dissipation per unit mass in the recirculation pipe is greater than that in the flocculation pipe, so that the stable floc size in the recirculation pipe is less than the stable floc size in the flocculation pipe, and so that there is negligible deposition of floc on the walls of the recirculation pipe.
Claim 5
Dependent Claim
43 words
A method in accordance with claim 1, wherein the length of flow in the flocculation pipe is sufficient to reduce the total number of solid particles per unit volume of the mixture in the pipe by a factor of at least approximately 4.
Claim 6
Dependent Claim
25 words
A method in accordance with claim 1, wherein the rate of turbulent energy dissipation per unit mass in the flocculation pipe is about 60 erg/sec.gm.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1985-01-04 | 1985-07-06 | 1986-01-05 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1989-01-04 | 1989-07-06 | 1990-01-05 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1993-01-04 | 1993-07-06 | 1994-01-05 | $7700.00 | Window Closed / Lapsed |