US4874521A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Pulp mill effluent color removal process
Assignee: Officemax Inc
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Filing: 1988-10-18
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Granted: 1989-10-17
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Expires: 2008-10-18
Abstract
Abstract A method for removing color from the caustic effluent produced during kraft pulping and bleaching is characterized by heating the caustic effluent to a temperature and under a pressure sufficient to cause an alteration in the chemical structure of the lignin chromophores in the effluent. The cooked effluent is cooled and has its pressure reduced to near atmospheric pressure. An acid material, such as chlorine extract from the bleaching process, is added to the effluent to lower the pH of the effluent to between 2.6 and 3.8 to initiate flocculation of the altered chromophores of the effluent. During flocculation, the chromophores are continuously separated from the effluent in order to produce a relatively clean and color-free liquid which may be deposited in the sewer system of the pulp mill.
Inventors
- 👤 Harold L. Newman
- 👤 William S. Adams, Jr.
- 👤 Brace Boyden
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-02 01:25
CPC Classifications
C; C02; C02F; C02F9/00; C02F1/00; C02F1/02; C02F1/025; C02F1/66; C02F2103/00; C02F2103/26; C02F2103/28; Y; Y10; Y10S; Y10S210/00; Y10S210/902; Y10S210/917; Y10S210/918; Y10S210/919; Y10S210/928
Claims Analysis
Total Claims: 16
Claim 1
Independent Claim
133 words
A method for removing color from the caustic effluent produced during kraft pulping and bleaching, comprising the steps of (a) increasing the pressure of the effluent to between 200 and 600 psi to prevent the liquid within the effluent from changing phase; (b) heating the effluent to a temperature between 200° and 250° C. for a retention time up to 20 minutes in accordance with said temperature to alter the chemical structure of lignin chromophores in the effluent; (c) cooling the effluent to a temperature between 35° and 60° C.; (d) reducing the pressure of the effluent to between 0 to 10 psi; (e) lowering the pH of the effluent to between 2.6 and 3.8 to initiate flocculation of said altered chromophores in the effluent; and (f) separating said chromophores from the effluent.
Claim 2
Independent Claim
133 words
A method for removing color from the caustic effluent produced during kraft pulping and bleaching, comprising the steps of (a) increasing the pressure of the effluent to between 200 and 600 psi to prevent the liquid within the effluent from changing phase; (b) heating the effluent to a temperature between 200° and 250° C. for a retention time up to 20 minutes in accordance with said temperature to alter the chemical structure of lignin chromophores in the effluent; (c) cooling the effluent to a temperature between 35° and 60° C.; (d) reducing the pressure of the effluent to between 0 to 10 psi; (e) lowering the pH of the effluent to between 2.6 and 3.8 to initiate flocculation of said altered chromophores in the effluent; and (f) separating said chromophores from the effluent.
Claim 3
Dependent Claim
19 words
A method as defined in claim 1, wherein the pH of the effluent is lowered by adding acid thereto.
Claim 4
Dependent Claim
24 words
A method as defined in claim 2, wherein said acid comprises at least one of hydrochloric acid, phosphoric acid, sulfuric acid, and nitric acid.
Claim 5
Dependent Claim
50 words
A method as defined in claim 3, wherein following cooling of the effluent, the pressure thereof is reduced to between 75 and 125 psi, and further comprising the step of increasing the pressure of said acid to between 75 and 125 psi prior to adding said acid to the effluent.
Claim 6
Dependent Claim
21 words
A method as defined in claim 4, wherein said heating and cooling steps are performed by a dual flow heat exchanger.
Claim 7
Dependent Claim
51 words
A method as defined in claim 5, and further comprising the step of adding air to the effluent prior to the addition of acid, whereby upon addition of said acid, microbubbles are formed in the effluent which attach to said chromophores to carry said chromophores to the surface of the effluent.
Claim 8
Dependent Claim
31 words
A method as defined in claim 6, wherein said separation step is performed in a dissolved air floatation unit which skims the surface of the effluent to remove the chromophores therefrom.
Claim 9
Dependent Claim
13 words
A method as defined in claim 5, wherein said separation step comprises filtration.
Claim 10
Dependent Claim
14 words
A method as defined in claim 5, wherein said separation step comprises reverse osmosis.
Claim 11
Dependent Claim
18 words
A method as defined in claim 2, wherein said acid comprises chlorine extract resulting from bleaching the pulp.
Claim 12
Dependent Claim
23 words
A method as defined in claim 3, wherein said acid is added to the effluent prior to said pressure increasing and heating steps.
Claim 13
Independent Claim
122 words
A method for removing color from the effluent produced during kraft pulping and bleaching, comprising the steps of (a) increasing the pressure of an acid material to between 200 and 600 psi; (b) heating said acid material to a temperature between 200° and 250° C. for a period of time up to 20 minutes in accordance with said temperature; (c) cooling said acid material to a temperature between 35° and 60° C.; (d) reducing the pressure of said acid material to between 0 and 10 psi; (e) mixing said acid material with the effluent to lower the pH of the effluent to between 2.6 and 3.8 to initiate flocculation of chromophores in the effluent; and (f) separating said chromophores from the effluent.
Claim 14
Independent Claim
122 words
A method for removing color from the effluent produced during kraft pulping and bleaching, comprising the steps of (a) increasing the pressure of an acid material to between 200 and 600 psi; (b) heating said acid material to a temperature between 200° and 250° C. for a period of time up to 20 minutes in accordance with said temperature; (c) cooling said acid material to a temperature between 35° and 60° C.; (d) reducing the pressure of said acid material to between 0 and 10 psi; (e) mixing said acid material with the effluent to lower the pH of the effluent to between 2.6 and 3.8 to initiate flocculation of chromophores in the effluent; and (f) separating said chromophores from the effluent.
Claim 15
Dependent Claim
25 words
A method as defined in claim 12, wherein said acid material comprises at least one of hydrochloric acid, phosphoric acid, sulfuric acid, and nitric acid.
Claim 16
Dependent Claim
19 words
A method as defined in claim 13, wherein said acid material comprises chlorine extract resulting from bleaching the pulp.
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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) | 1992-10-16 | 1993-04-17 | 1993-10-17 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1996-10-16 | 1997-04-17 | 1997-10-17 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2000-10-16 | 2001-04-17 | 2001-10-17 | $7700.00 | Window Closed / Lapsed |