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US4248769A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for washing of crude tall oil soap from the sulfate pulping process

Assignee: Linotek Oy
•
Filing: 1979-03-13
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Granted: 1981-02-03
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Expires: 1999-03-13
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Abstract

Abstract A method for washing of crude tall oil soap obtained from the sulfate pulping process using alkalized spent acid from tall oil acidulation as washing liquid by mixing the crude soap and the washing liquid coming from the process and by cooling the mixture in a separation tank by either stirring with a slowly moving agitator or by circulating the soap or soap mixture through a pump and a cooler.

Inventors

  • 👤 Ake A. Johansson

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-07 07:33
CPC Classifications
C; C11; C11D; C11D15/00

Claims Analysis

Total Claims: 4
Claim 1
Independent Claim 111 words
A method for washing crude soap from the sulphate cellulose process using alkaline mother liquor from tall oil cooking as washing liquid, comprising mixing the crude soap and the washing liquid vigorously at the temperature of 60°-80° C. that they have when they are coming from said sulphate cellulose process, transferring the mixture thus obtained into a separation tank, effecting separation between soap and washing liquid in the tank by a combined agitation and cooling operation at a temperature of 40°-50° C., whereby the mixture of the soap and the washing liquid is cooled to said temperature, and thereafter separately removing the washed soap and the washing liquid from the tank.
Claim 2
Independent Claim 111 words
A method for washing crude soap from the sulphate cellulose process using alkaline mother liquor from tall oil cooking as washing liquid, comprising mixing the crude soap and the washing liquid vigorously at the temperature of 60°-80° C. that they have when they are coming from said sulphate cellulose process, transferring the mixture thus obtained into a separation tank, effecting separation between soap and washing liquid in the tank by a combined agitation and cooling operation at a temperature of 40°-50° C., whereby the mixture of the soap and the washing liquid is cooled to said temperature, and thereafter separately removing the washed soap and the washing liquid from the tank.
Claim 3
Dependent Claim 34 words
A method as claimed in claim 1, in which said separation between soap and washing liquid in the tank is effected by stirring with a slowly moving cooled agitator disposed in the separation tank.
Claim 4
Dependent Claim 84 words
A method as claimed in claim 1, in which said separation between soap and washing liquid in the tank is effected by circulating the mixture of the soap and the washing liquid through a pump and a cooler, by withdrawing material from the surface of the separation tank to the pump and returning the withdrawn material after passage through the cooler into the material within the tank near the interface between the soap and the washing liquid at an intermediate point in the tank.

References Cited (Backward Citations)

US3575952A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-02-03 1984-08-04 1985-02-03 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-02-03 1988-08-04 1989-02-03 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-02-03 1992-08-04 1993-02-03 $7700.00 Window Closed / Lapsed

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