US4861492A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method of dewatering sewage sludge particularly on recessed plate pressing equipment
Assignee: ChampionX LLC
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Filing: 1987-09-03
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Granted: 1989-08-29
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Expires: 2007-09-03
Abstract
Abstract Method for dewatering sewage sludge with the aid of organic polymeric flocculating agents (polyelectrolytes) made preferably by emulsion polymerization. To obtain optimum dewatering results, a substantial amount of the aqueous phase of the sludge is removed by decantation after flocculant addition prior to the dewatering treatment proper. The flocculated and thickened sludge may then be dewatered much more quickly with the dewatering behavior improved additionally by causing a reactivating flocculation to take place on the delivery side of the sludge feed pump. The Figures show a preferred embodiment of the inventive sludge dewatering system using a recessed plate press.
Inventors
- 👤 Josef Lehmkuhl
- 👤 Ulrich Nikesch
- 👤 Kurt Presslein
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-07 09:06
CPC Classifications
C; C02; C02F; C02F11/00; C02F11/12; C02F11/121; C02F11/122; B; B01; B01D; B01D21/00; B01D21/01; B01D21/02; B01D21/30; B01D21/32; B01D21/34; B01D36/00; B01D36/04; C02F1/00; C02F1/52; C02F1/54
Claims Analysis
Total Claims: 7
Claim 1
Independent Claim
240 words
A method of dewatering sewage sludge in a filter press including a filter cloth wherein organic polymeric flocculants are added to the sludge to improve the dewatering behavior of the sludge and water is removed from the flocculated sludge in a preparatory stage, comprising the steps of: adding a flocculating amount of an aqueous cationic acrylamide copolymer solution to form a flocculated sludge; maturing the flocculated sludge in a conditioning container for at least two minutes in the absence of mechanical strain prior to feeding it to the filter press, thickening the flocculated sludge in said conditioning container by separating part of the sludge water by decantation using a pump to transport the thickened sludge to the filter press; adding an additional amount of the organic polymeric flocculant to the thickened sludge on the delivery side of the sludge pump to reactivate the flocculated solids agglomerates, wherein the weight ratio of pre-decantation flocculant addition to reactivating flocculant addition is within the range of 3:1 to 9:1; delivering the reactivated solids agglomerates directly to the filter press; and filtering the sludge to provide a filter cake containing at least about 40% dry solids which do not stick to the filter cloth, said aqueous cationic acrylamide polymer solution having been prepared by inverting a water-in-oil emulsion of the polymer, and said aqueous cationic acrylamide polymer solution containing hydrophobic components which hydrophobise the filter cloth during filtering to facilitate filter cake removal therefrom.
Claim 2
Independent Claim
240 words
A method of dewatering sewage sludge in a filter press including a filter cloth wherein organic polymeric flocculants are added to the sludge to improve the dewatering behavior of the sludge and water is removed from the flocculated sludge in a preparatory stage, comprising the steps of: adding a flocculating amount of an aqueous cationic acrylamide copolymer solution to form a flocculated sludge; maturing the flocculated sludge in a conditioning container for at least two minutes in the absence of mechanical strain prior to feeding it to the filter press, thickening the flocculated sludge in said conditioning container by separating part of the sludge water by decantation using a pump to transport the thickened sludge to the filter press; adding an additional amount of the organic polymeric flocculant to the thickened sludge on the delivery side of the sludge pump to reactivate the flocculated solids agglomerates, wherein the weight ratio of pre-decantation flocculant addition to reactivating flocculant addition is within the range of 3:1 to 9:1; delivering the reactivated solids agglomerates directly to the filter press; and filtering the sludge to provide a filter cake containing at least about 40% dry solids which do not stick to the filter cloth, said aqueous cationic acrylamide polymer solution having been prepared by inverting a water-in-oil emulsion of the polymer, and said aqueous cationic acrylamide polymer solution containing hydrophobic components which hydrophobise the filter cloth during filtering to facilitate filter cake removal therefrom.
Claim 3
Dependent Claim
23 words
The method of claim 1 further including varying the ratio of the flocculant additions to correspond to pressure changes in the filter press.
Claim 4
Dependent Claim
28 words
The method of claim 2 further including controlling conditioning container refill and decantate separation by measuring turbidity in the conditioning container or in the decantate discharge tube thereof.
Claim 5
Dependent Claim
57 words
The method of claim 1 which includes a non-pressurized starting phase which tends towards a final or high pressure phase as sludge builds up on the filter press in which the reactivating flocculant addition in the final or high pressure phase is adjusted to about 1.5 to 3.5 times the amount added in the non-pressurized starting phase.
Claim 6
Dependent Claim
28 words
The method of claim 1 further including controlling conditioning container refill and decantate separation by measuring turbidity in the conditioning container or in the decantate discharge tube thereof.
Claim 7
Dependent Claim
15 words
The method of claim 1 in which the filter press is a recessed plate press.
References Cited (Backward Citations)
US3493501A
Cited
US3531404A
Cited
DE2249607A1
Cited
DE2302142A1
Cited
US4105558A
Cited
US4198298A
Cited
US4151080A
Cited
FR2432482A1
Cited
SU791627A1
Cited
US4411797A
Cited
US4431548A
Cited
US4341628A
Cited
US4404099A
Cited
US4397746A
Cited
US4415446A
Cited
US4479879A
Cited
US4439325A
Cited
US4576723A
Cited
US4659483A
Cited
US4675116A
Cited
JPH05328853A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1992-08-28 | 1993-02-27 | 1993-08-29 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1996-08-28 | 1997-02-27 | 1997-08-29 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2000-08-28 | 2001-02-27 | 2001-08-29 | $7700.00 | Window Closed / Lapsed |