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US3678031A Expired / Lapsed US ⏱️ 0.0 years remaining

Slurry process for the production of absorptive carboxy methyl cellulose fibers

Assignee: Georgia Pacific Nonwovens LLC
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Filing: 1970-10-21
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Granted: 1972-07-18
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Expires: 1990-10-21
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Abstract

Abstract Alkali metal salts of carboxymethyl cellulose are prepared by producing and then etherifying alkali cellulose under conditions selected to result in a molar excess of neutralized acidic etherifying reagent to moles of unreacted neutralizing reagent together with extended etherifying time and temperature conditions, i.e., about 3 to about 24 hours at about 60*C. to about 80*C. to yield substantially insoluble acidic products, which products are white in color, have a reflectance brightness of about 70 to about 80, have a normally soluble degree of substitution range of about 0.4 to 1.2 and are absorptive and retentive of up to about 70 times their weight of aqueous solutions.

Inventors

  • 👤 Howard L Schoggen

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-24 20:53
CPC Classifications
C; C08; C08B; C08B11/00; C08B11/20; A; A61; A61L; A61L15/00; A61L15/16; A61L15/22; A61L15/28; C08B11/02; C08B11/04; C08B11/10; C08B11/12

Claims Analysis

Total Claims: 5
Claim 1
Independent Claim 279 words
In a slurry process for the production of sodium carboxymethyl cellulose, exhibiting increased absorptive and retentive capacity wherein cellulose is slurried in an aqueous solution of isopropanol and contacted in a first step with sodium hydroxide and the resulting alkali cellulose is contacted with monochloroacetic acid in a second step and thereby etherified to a conventionally soluble d.s. while still slurried in said aqueous solution of isopropanol; the improvement which consists of maintaining a total liquid to cellulose ratio in said steps of about 25 to 40 to 1, by weight, while contacting the cellulose and the alkali cellulose in said steps with about 1.5 moles of sodium hydroxide per mole of monochloroacetic acid and using about 2.2 moles of monochloroacetic acid per mole of anhydroglucose unit of cellulose after neutralization of at least 0.5, to produce an essentially acid product while further maintaining as liquid ratios in said steps, a water to cellulose ratio of about 3.3 to 1, by weight, and an isopropanol to water ratio of about 8 to 1, by weight, while contacting the slurried cellulose with the sodium hydroxide at a slurry temperature of about 5*C. to about 25*C. for a period of about 0.2 to about 0.6 hour and thereafter contacting the thus produced alkali cellulose with the monochloroacetic acid at a slurry temperature of about 60*C. to about 80*C. for a period of about 3 hours to about 12 hours to produce sodium carboxymethyl cellulose exhibiting a d.s. of about 0.4 to about 1.2, a water solubility of less than about 35 percent, a WRV of about 1000 to about 7000 and a SRV of about 400 to about 2,500 is produced.
Claim 2
Dependent Claim 272 words
In a slurry process for the production of sodium carboxymethyl cellulose, exhibiting increased absorptive and retentive capacity wherein cellulose is slurried in an aqueous solution of isopropanol and contacted in a first step with sodium hydroxide and the resulting alkali cellulose is contacted with monochloroacetic acid and thereby etherified to a conventionally soluble d.s. while still slurried in said aqueous solution of isopropanol; the improvement which consists of maintaining a total liquid to cellulose ratio in said steps of about 30 to 1, by weight, while contacting the cellulose and the alkali cellulose in said steps with about 1.5 moles of sodium hydroxide per mole of monochloroacetic acid and using aboUt 2.2 moles of monochloroacetic acid per mole of anhydroglucose unit of cellulose, while maintaining a mole ratio of sodium hydroxide to anhydroglucose unit of cellulose after neutralization of at least 0.5, to produce an essentially acid product while further maintaining as liquid ratios in said steps, a water to cellulose ratio of about 3.3 to 1, by weight, and an isopropanol to water ratio of about 8 to 1, by weight, while contacting the slurried cellulose with the sodium hydroxide at a slurry temperature of about 20*C. for a period of about 0.5 hour and thereafter contacting the thus produced alkali cellulose with the monochloroacetic acid at a slurry temperature of about 80*C. for a period of about 3 hours, to produce sodium carboxymethyl cellulose exhibiting a d.s. of about 0.4 to about 1.2, a water solubility of less than about 35%, a WRV of about 1000 to about 7000 and a SRV of about 400 to about 2500 is produced.
Claim 3
Dependent Claim 67 words
An essentially acidic sodium carboxymethyl cellulose having a d.s. of about 0.4 to about 1.2 and exhibiting a WRV of about 1, 000 to about 7000 together with a SRV of about 400 to about 2, 500, which sodium carboxymethyl cellulose is further characterized by having a reflectance brightness of about 70 to about 80 like the reflectance brightness exhibited by conventional slurry sodium carboxymethyl cellulose products.
Claim 4
Dependent Claim 65 words
An essentially acidic sodium carboxymethyl cellulose having a d.s. of about 0.7 to about 0.9 and exhibiting a WRV of about 2000 to about 4000 together with a SRV of about 1,000 to about 1,500, which sodium carboxymethyl cellulose is further characterized by having a reflectance brightness of about 70 to about 80 like the reflectance brightness exhibited by conventional slurry sodium carboxymethyl cellulose products.
Claim 5
Dependent Claim 56 words
An essentially acidic sodium carboxymethyl cellulose having a d.s. of about 0.8 and exhibiting a WRV of about 3,000 together with a SRV of about 1,300, which sodium carboxymethyl cellulose is further characterized by having a reflectance brightness of about 70 to about 80 like the reflectance brightness exhibited by conventional slurry sodium carboxymethyl cellulose products.

References Cited (Backward Citations)

US2517577A Cited
US2639281A Cited
US2772999A Cited
US2816889A Cited
US3347855A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1975-07-18 1976-01-17 1976-07-18 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1979-07-18 1980-01-17 1980-07-18 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1983-07-18 1984-01-17 1984-07-18 $7700.00 Window Closed / Lapsed

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