US4332589A
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Method for polymerization of lignosulfonates
Assignee: REED LIGNIN Inc 100 HWY 51 SOUTH ROTHSCHILD WI 54474-1198 A CORP OF
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Filing: 1980-11-24
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Granted: 1982-06-01
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Expires: 2000-11-24
Abstract
Abstract A method is provided for polymerizing lignosulfonate materials without undesirable viscosity build-up or gelling. The method comprises the steps of premethylolating the lignosulfonate under alkaline conditions followed by condensation of the premethylolated lignosulfonate at elevated temperatures and under neutral and acidic conditions. The resultant products are useful in any of a variety of applications wherein the surface active properties of lignosulfonates may be desirable. The products are useful as dispersants and especially as dye dispersants.
Inventors
- 👤 Stephen Y. Lin
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-29 18:33
CPC Classifications
C; C08; C08H; C08H6/00; C08G; C08G16/00; C08G16/02; C09; C09B; C09B67/00; C09B67/0071; C09B67/0084; C09B67/0085; C09B67/0086
Claims Analysis
Total Claims: 24
Claim 1
Independent Claim
69 words
A method for polymerizing lignosulfonate materials which comprises: (1) reacting a mixture of a lignosulfonate and formaldehyde while maintaining said reaction mixture under alkaline conditions for a period sufficient to form a methylolated lignosulfonate; and (2) effecting condensation of said methylolated lignosulfonate having a solids concentration from 10 to 55 percent under neutral or acidic conditions for a period sufficient to produce a fluid lignosulfonate of increased molecular weight.
Claim 2
Independent Claim
69 words
A method for polymerizing lignosulfonate materials which comprises: (1) reacting a mixture of a lignosulfonate and formaldehyde while maintaining said reaction mixture under alkaline conditions for a period sufficient to form a methylolated lignosulfonate; and (2) effecting condensation of said methylolated lignosulfonate having a solids concentration from 10 to 55 percent under neutral or acidic conditions for a period sufficient to produce a fluid lignosulfonate of increased molecular weight.
Claim 3
Dependent Claim
25 words
The method of claim 1 in which said lignosulfonate is reacted in step (1) at a pH within the range of about 10 to 12.
Claim 4
Dependent Claim
37 words
The method of claim 2 in which step (1) is conducted at a temperature within the range of about 60° C. to 90° C. for a period of time ranging from about 10 minutes to 2 hours.
Claim 5
Dependent Claim
31 words
The method of claim 3 in which said formaldehyde is present in an amount within the range of about 0.5 to about 4.5 moles of formaldehyde per 1,000 grams of lignosulfonate.
Claim 6
Dependent Claim
30 words
The method of claim 1 wherein step (2) is conducted at a pH below about 7 and a temperature within the range of about 90° C. to about 180° C.
Claim 7
Dependent Claim
12 words
The method of claim 1 wherein said lignosulfonate is spent sulfite liquor.
Claim 8
Dependent Claim
16 words
The method of claim 6 wherein said spent sulfite liquor has been at least partially desugared.
Claim 9
Independent Claim
127 words
A method for polymerizing lignosulfonate materials which comprises: (1) reacting a mixture of a lignosulfonate derived from spent sulfite liquor and from about 0.5 to 4.5 moles formaldehyde per 1,000 grams of lignosulfonate while maintaining the reaction mixture of lignosulfonate at a pH within the range of about 10 to 12 and a temperature of about 60° C. to about 90° C. for a period sufficient to form a methylolated lignosulfonate; and (2) effecting condensation of said methylolated lignosulfonate by subjecting the reaction mixture of step (1) having a solids concentration from 10 percent to 55 percent to a temperature of about 90° C. to about 180° C. while maintaining a pH below 7 for a period sufficient to produce a fluid lignosulfonate of increased molecular weight.
Claim 10
Independent Claim
127 words
A method for polymerizing lignosulfonate materials which comprises: (1) reacting a mixture of a lignosulfonate derived from spent sulfite liquor and from about 0.5 to 4.5 moles formaldehyde per 1,000 grams of lignosulfonate while maintaining the reaction mixture of lignosulfonate at a pH within the range of about 10 to 12 and a temperature of about 60° C. to about 90° C. for a period sufficient to form a methylolated lignosulfonate; and (2) effecting condensation of said methylolated lignosulfonate by subjecting the reaction mixture of step (1) having a solids concentration from 10 percent to 55 percent to a temperature of about 90° C. to about 180° C. while maintaining a pH below 7 for a period sufficient to produce a fluid lignosulfonate of increased molecular weight.
Claim 11
Dependent Claim
41 words
The method of claim 8 wherein step (1) is effected for a period ranging from about 10 minutes to 2 hours, the pH is within the range of 10.5 to 11.5 and the temperature is between 70° C. to 80° C.
Claim 12
Dependent Claim
41 words
The method of claim 9 wherein step (2) is effected for a period ranging from about 1 to 5 hours, the pH is within the range of 3 to 6, and the temperature is between about 120° C. to 160° C.
Claim 13
Dependent Claim
51 words
As a composition of matter, a fluid polymerized lignosulfonate derived by acidic condenation of a premethylolated lignosulfonate material having a solids concentration from 10 to 55 percent at elevated temperatures under acidic or neutral conditions, said premethylolated lignosulfonate having been obtained by reaction of a lignosulfonate and formaldehyde under alkaline conditions.
Claim 14
Dependent Claim
51 words
As a composition of matter, a fluid polymerized lignosulfonate derived by acidic condenation of a premethylolated lignosulfonate material having a solids concentration from 10 to 55 percent at elevated temperatures under acidic or neutral conditions, said premethylolated lignosulfonate having been obtained by reaction of a lignosulfonate and formaldehyde under alkaline conditions.
Claim 15
Dependent Claim
15 words
The composition of claim 11 wherein said lignosulfonate material is derived from spent sulfite liquor.
Claim 16
Dependent Claim
15 words
The composition of claim 12 wherein said spent sulfite liquor is at least partially desugared.
Claim 17
Dependent Claim
35 words
The composition of claim 11 wherein said premethylolated lignosulfonate material has been condensed by subjection to a temperature within the range of about 90° C. to about 180° C. at a pH below about 7.
Claim 18
Dependent Claim
49 words
The composition of claim 11 wherein said premethylolated lignosulfonate is the product of the reaction of lignosulfonate with from about 0.5 to about 4.5 moles formaldehyde per 1,000 grams of lignosulfonate at a pH of about 10 to 12 and a temperature of about 60° C. to 90° C.
Claim 19
Dependent Claim
91 words
As a composition of matter, a fluid polymerized lignosulfonate derived by condensation of a premethylolated lignosulfonate material having a solids concentration from 10 percent to 55 percent at a pH below about 7 and a temperature within the range of about 90° C. to about 180° C.; said premethylolated lignosulfonate being the product of the reaction of lignosulfonate with from about 0.5 to 4.5 moles of formaldehyde per 1,000 grams of lignosulfonate at a pH of about 10 to 12 and a temperature of about 60° C. to about 90° C.
Claim 20
Dependent Claim
91 words
As a composition of matter, a fluid polymerized lignosulfonate derived by condensation of a premethylolated lignosulfonate material having a solids concentration from 10 percent to 55 percent at a pH below about 7 and a temperature within the range of about 90° C. to about 180° C.; said premethylolated lignosulfonate being the product of the reaction of lignosulfonate with from about 0.5 to 4.5 moles of formaldehyde per 1,000 grams of lignosulfonate at a pH of about 10 to 12 and a temperature of about 60° C. to about 90° C.
Claim 21
Dependent Claim
36 words
The composition of claim 16 wherein said premethylolated lignosulfonate is condensed at a pH within the range of 3 to 6 and a temperature of about 70° C. to 80° C. for a least 1 hour.
Claim 22
Dependent Claim
34 words
The composition of claim 17 wherein said premethylolated lignosulfonate is obtained by reaction at a pH within the range of about 10.5 to 11.5 and a temperature of about 70° C. to 80° C.
Claim 23
Dependent Claim
32 words
A dyestuff composition comprising a water-insoluble dye and a fluid, polymerized lignosulfonate of claim 11, said lignosulfonate being present in a weight ratio to said dye of from about 0.5:1 to 2:1.
Claim 24
Dependent Claim
19 words
The composition of claim 19 wherein said dye is selected from the group consisting of disperse and vat dyes.
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) | 1985-05-31 | 1985-11-30 | 1986-06-01 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1989-05-31 | 1989-11-30 | 1990-06-01 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1993-05-31 | 1993-11-30 | 1994-06-01 | $7700.00 | Window Closed / Lapsed |