Patent US4778602A successfully refreshed from Google Patents.
US4778602A
Expired / Lapsed
US
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Method of producing multi-functional filtering medium
Assignee: Individual
•
Filing: 1986-04-28
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Granted: 1988-10-18
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Expires: 2006-04-28
Abstract
Abstract A filtering medium is economically produced by treating a highly humified peat source with an alkaline solution followed by mixing with a quaternary amine compound until the humic and fulvic acids have precipitated. A filter cake is formed from the residue by various means including acid oxidation, heating with or without acid reagent or by semi-coking to produce a final dried poduct having excellent filtering properties for hydrophobic compounds, as well as ion-exchange capacities for both anions and cations from aqueous solution.
Inventors
- 👤 Ralph S. Allen, III
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-04 18:18
CPC Classifications
C; C02; C02F; C02F1/00; C02F1/28; C02F1/283; B; B01; B01D; B01D39/00; B01D39/02; B01D39/04; B01D39/06; C01; C01B; C01B32/00; C01B32/30; C01B32/312; C01B32/318; C02F1/286
Claims Analysis
Total Claims: 15
Claim 1
Independent Claim
114 words
The method of producing a filtering medium comprising the steps of: (a) mixing a source of peat in an alkaline aqueous solution until the humic and fulvic acid fractions in the peat are solubilized; (b) precipitating said humic and fulvic acid fractions from said peat and alkaline aqueous solution by introducing into said solution 10-40 parts by weight of quaternary amine 100 parts by weight of the organic fraction of peat and mixing for a time period sufficient to precipitate said humic and fulvic acid fractions therefrom; (c) removing said humic and fulvic acid fractions from said solution; and (d) dehydrating said humic and fulvic acid fractions so removed to a substantially dry state.
Claim 2
Independent Claim
114 words
The method of producing a filtering medium comprising the steps of: (a) mixing a source of peat in an alkaline aqueous solution until the humic and fulvic acid fractions in the peat are solubilized; (b) precipitating said humic and fulvic acid fractions from said peat and alkaline aqueous solution by introducing into said solution 10-40 parts by weight of quaternary amine 100 parts by weight of the organic fraction of peat and mixing for a time period sufficient to precipitate said humic and fulvic acid fractions therefrom; (c) removing said humic and fulvic acid fractions from said solution; and (d) dehydrating said humic and fulvic acid fractions so removed to a substantially dry state.
Claim 3
Dependent Claim
41 words
The method according to claim 1, in which said humic and fulvic acid fractions are dehydrated by heating to an elevated temperature in a closed, pressurized container for a time period sufficient to dehydrate said fractions to a substantially dry state.
Claim 4
Dependent Claim
19 words
The method according to claim 2, said closed, pressurized container being pressurized to a pressure level of 40 psi.
Claim 5
Dependent Claim
20 words
The method according to claim 1, including the additional step of grinding the dehydrated fractions to a predetermined mesh size.
Claim 6
Dependent Claim
22 words
The method according to claim 1, in which said alkaline aqueous solution is selected from the group consisting of KOH or NaOH.
Claim 7
Dependent Claim
17 words
The method according to claim 5, in which said alkaline aqueous solution has a concentration of 0.5N.
Claim 8
Dependent Claim
18 words
The method according to claim 1, in which said quaternary amine is a dimethyl dyhydrogenated tallow ammonium chloride.
Claim 9
Independent Claim
96 words
The method of producing a filtering medium comprising the steps of: (a) mixing a highly humified source of peat in an alkaline aqueous solution until the humic and fulvic acid fractions in said peat are solubilized; (b) intermixing into said resultant solution a dimethyl (dihydrogenated tallow) ammonium chloride for a time period sufficient to precipitate the humic and fulvic acid fractions from said solution; (c) recoving said precipitated humic acid and fulvic acid fractions and activating same by dehydrating to a substantially dry state; and (d) grinding the dried resultant product to a desired mesh size.
Claim 10
Independent Claim
96 words
The method of producing a filtering medium comprising the steps of: (a) mixing a highly humified source of peat in an alkaline aqueous solution until the humic and fulvic acid fractions in said peat are solubilized; (b) intermixing into said resultant solution a dimethyl (dihydrogenated tallow) ammonium chloride for a time period sufficient to precipitate the humic and fulvic acid fractions from said solution; (c) recoving said precipitated humic acid and fulvic acid fractions and activating same by dehydrating to a substantially dry state; and (d) grinding the dried resultant product to a desired mesh size.
Claim 11
Dependent Claim
31 words
The method according to claim 8, in which said alkaline aqueous solution is selected from the group consisting of KOH and NaOH, said alkaline aqueous solution having a concentration of 0.5N.
Claim 12
Dependent Claim
33 words
The method according to claim 8, characterized by dehydrating said fractions by heating at a temperature of 200°-1000° C. in a closed, pressurized container which is pressurized to a level of 40 psi.
Claim 13
Dependent Claim
82 words
In the method of producing a filtering medium wherein a source of highly humified peat is treated to remove the humic and fulvic acid fractions therefrom, characterized by the step of activating said humic and fulvic acid fractions by heating to a temperature range of 200°-1000° C. in a closed, pressurized container for a time period sufficient to dehydrate said fractions to a substantially dry state, followed by grinding the resultant product to a predetermined mesh size in the range of 354-500.
Claim 14
Dependent Claim
82 words
In the method of producing a filtering medium wherein a source of highly humified peat is treated to remove the humic and fulvic acid fractions therefrom, characterized by the step of activating said humic and fulvic acid fractions by heating to a temperature range of 200°-1000° C. in a closed, pressurized container for a time period sufficient to dehydrate said fractions to a substantially dry state, followed by grinding the resultant product to a predetermined mesh size in the range of 354-500.
Claim 15
Dependent Claim
19 words
In the method according to claim 11, in which said container is pressurized to a level of 40 psi.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1991-10-18 | 1992-04-18 | 1992-10-18 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1995-10-18 | 1996-04-18 | 1996-10-18 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1999-10-18 | 2000-04-18 | 2000-10-18 | $7700.00 | Window Closed / Lapsed |