US4001202A
Expired / Lapsed
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Process for making sulfonated lignin surfactants
Assignee: Westvaco Corp
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Filing: 1975-10-17
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Granted: 1977-01-04
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Expires: 1995-10-17
Abstract
Abstract Disclosed herein is an improved process for producing sulfonated lignin surfactants for use as dispersants for disperse dyes and vat dyes. The improved process is to react a sulfonated lignin and epihalohydrin under certain conditions to block a portion of the free-phenolic hydroxyl group and at the same time cross-link the lignin molecules to increase the molecular weight. Another aspect of the process of this invention is to oxidize the thus treated lignin to stabilize its properties. Dispersants made according to this process have improved fiber staining and heat stability properties over other lignin-based dispersants.
Inventors
- 👤 Peter Dilling
- 👤 Gerald Prazak
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-26 04:43
CPC Classifications
C; C08; C08H; C08H6/00; C09; C09B; C09B67/00; C09B67/0071; C09B67/0084; C09B67/0085; C09B67/0086
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
85 words
In a process for modifying a sulfonated lignin to provide dye dispersant properties by reacting a sulfonated lignin with an epihalohydrin the improvement comprising, reacting an aqueous solution of a sulfonated lignin at a solids concentration between 5% and 35% with from 0.1 to 2.0 moles of an epihalohydrin per 1,000 grams of lignin at a temperature between 20° C. and 100° C. and a starting pH between 9 and 13 until the sulfonated lignin-epihalohydrin adduct has a viscosity below 500 cps. at 25° C.
Claim 2
Dependent Claim
85 words
In a process for modifying a sulfonated lignin to provide dye dispersant properties by reacting a sulfonated lignin with an epihalohydrin the improvement comprising, reacting an aqueous solution of a sulfonated lignin at a solids concentration between 5% and 35% with from 0.1 to 2.0 moles of an epihalohydrin per 1,000 grams of lignin at a temperature between 20° C. and 100° C. and a starting pH between 9 and 13 until the sulfonated lignin-epihalohydrin adduct has a viscosity below 500 cps. at 25° C.
Claim 3
Dependent Claim
30 words
The process according to claim 1 wherein said epihalohydrin is epichlorohydrin and the amount of epichlorohydrin is between 0.75 mole and 1.5 moles of epichlorohydrin per 1,000 grams of lignin.
Claim 4
Dependent Claim
25 words
The process according to claim 2 wherein the reaction pH is maintained between 10.5 and 12.5 and the temperature between 50° C. and 90° C.
Claim 5
Dependent Claim
27 words
The process according to claim 1 further comprising, stabilizing the sulfonated lignin-epihalohydrin adduct with an oxidant selected from the group consisting of air, oxygen and hydrogen peroxide.
Claim 6
Dependent Claim
110 words
In a process for modifying a sulfonated lignin to provide dye dispersant properties by reacting a sulfonated lignin with an epihalohydrin the improvement consisting essentially of; a. reacting an aqueous solution of a sulfonated lignin at a solids concentration of between 5% and 35% with from 0.1 to 2.0 moles of an epihalohydrin per 1,000 grams of lignin at a temperature between 20° C. and 100° C. and a starting pH between 9 and 13 until the sulfonated lignin-epihalohydrin adduct has a viscosity below 500 cps. at 25° C., and b. stabilizing said sulfonated lignin-epihalohydrin adduct with an oxidant selected from the group consisting of air, oxygen and hydrogen peroxide.
Claim 7
Dependent Claim
110 words
In a process for modifying a sulfonated lignin to provide dye dispersant properties by reacting a sulfonated lignin with an epihalohydrin the improvement consisting essentially of; a. reacting an aqueous solution of a sulfonated lignin at a solids concentration of between 5% and 35% with from 0.1 to 2.0 moles of an epihalohydrin per 1,000 grams of lignin at a temperature between 20° C. and 100° C. and a starting pH between 9 and 13 until the sulfonated lignin-epihalohydrin adduct has a viscosity below 500 cps. at 25° C., and b. stabilizing said sulfonated lignin-epihalohydrin adduct with an oxidant selected from the group consisting of air, oxygen and hydrogen peroxide.
Claim 8
Dependent Claim
30 words
The process according to claim 5 wherein said epihalohydrin is epichlorohydrin and the amount of epichlorohydrin is between 0.75 mole and 1.5 moles of epichlorohydrin per 1,000 grams of lignin.
Claim 9
Dependent Claim
25 words
The process according to claim 5 wherein the reaction pH is maintained between 10.5 and 12.5 and the temperature between 50° C. and 90° C.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1980-01-04 | 1980-07-05 | 1981-01-04 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-01-04 | 1984-07-05 | 1985-01-04 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-01-04 | 1988-07-05 | 1989-01-04 | $7700.00 | Window Closed / Lapsed |