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US4426254A Expired / Lapsed US ⏱️ 0.0 years remaining

Solubilization of nonionic surfactants useful in wood pulp deresination

Assignee: HELLER FINANCIAL Inc AS AGENT
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Filing: 1982-05-05
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Granted: 1984-01-17
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Expires: 2002-05-05
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Abstract

Abstract A process for extracting resin from wood pulp by contacting the pulp at elevated temperature with an aqueous medium comprising between about 2 and 15 percent by weight sodium hydroxide and between about 0.2 and 1.0% weight of an ethylene oxide condensation product, and also comprising in specified proportion one or more substances selected from the group consisting of a C12 alpha-olefin sulfonate and a particular C21 dicarboxylic acid. The sulfonate and dicarboxylic acid substantially enhance solubilization of the condensation product deresination agent in the highly polar aqueous medium.

Inventors

  • 👤 Donald L. Wood
  • 👤 Judith E. Zweig

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-09 07:25
CPC Classifications
D; D21; D21C; D21C3/00; D21C3/22; D21C3/222; C; C09; C09K; C09K23/00; C09K23/42; D21C9/00; D21C9/08; D21C9/086; Y; Y10; Y10S; Y10S162/00; Y10S162/03

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 103 words
In a process for the manufacture of wood pulp which comprises treating a wood pulp by contact at elevated temperature with an aqueous medium containing between about 2 and 15 percent by weight sodium hydroxide and between about 0.2 and 1.0 percent by weight of an ethylene oxide condensation product deresination agent, the improvement which comprises incorporating into the aqueous medium a solubilizing agent which is a C 12 alpha-olefin sulfonate, with the provision that the weight ratio of said ethylene oxide condensation product in the aqueous medium to said solubilizing agent is between about 9 to 1 and about 1 to 1.
Claim 2
Dependent Claim 103 words
In a process for the manufacture of wood pulp which comprises treating a wood pulp by contact at elevated temperature with an aqueous medium containing between about 2 and 15 percent by weight sodium hydroxide and between about 0.2 and 1.0 percent by weight of an ethylene oxide condensation product deresination agent, the improvement which comprises incorporating into the aqueous medium a solubilizing agent which is a C 12 alpha-olefin sulfonate, with the provision that the weight ratio of said ethylene oxide condensation product in the aqueous medium to said solubilizing agent is between about 9 to 1 and about 1 to 1.
Claim 3
Dependent Claim 18 words
The process of claim 1, wherein the solubilizing agent is the sulfonate of substantially linear C 12 alpha-olefins.
Claim 4
Dependent Claim 22 words
The process of claim 1, or claim 2, wherein the aqueous medium contains at least about 5 percent by weight sodium hydroxide.
Claim 5
Dependent Claim 48 words
The process of claim 3, wherein the ethylene oxide condensation product is the product of the addition of an average of between about 8 and 14 moles of ethylene oxide to one mole of one or more alkanols in the C 9 to C 16 carbon number range.
Claim 6
Dependent Claim 30 words
The process of claim 4, wherein the weight ratio of the ethylene oxide condensation product to the solubilizing agent is between about 4 to 1 and about 1.5 to 1.

References Cited (Backward Citations)

US2668110A Cited
US2716058A Cited
US2999045A Cited
DE2164235A1 Cited
US4063886A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1987-01-16 1987-07-18 1988-01-17 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1991-01-16 1991-07-18 1992-01-17 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1995-01-16 1995-07-18 1996-01-17 $7700.00 Window Closed / Lapsed

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