US4223129A
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US
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Continuous process for making alkyl aldosides from starch or other carbohydrates
Assignee: Staley Continental Inc
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Filing: 1978-09-01
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Granted: 1980-09-16
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Expires: 1998-09-01
Abstract
Abstract A continuous process for making alkyl aldosides from polysaccharides and more particularly mixed alkyl glycosides from starch by direct alcoholysis. A polysaccharide, such as starch, is slurried in an alcohol and passed through a heated, confined zone under pressure in the presence of an acid catalyst to form a mixed alkyl aldoside. The alcohols which may be used include methanol, ethanol, propanol and butanol, their isomers and mixtures thereof. Higher alkyl glycosides are surfactants and, in some instances, it is advantageous to use higher alcohols, such as decyl and dodecyl alcohols, to obtain particular surfactant properties in the resulting alkyl glycosides. Mixed alkyl glycosides are useful in detergent applications, and as backbone polymers in polyurethane foams.
Inventors
- 👤 Claris D. Roth
- 👤 Kenneth B. Moser
- 👤 William A. Bomball
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-27 14:29
CPC Classifications
C; C07; C07H; C07H15/00; C07H15/02; C07H15/04; B; B01; B01J; B01J19/00; B01J19/24; B01J19/2415; B01J19/243; C07H1/00; B01J2219/00; B01J2219/00049; B01J2219/00051; B01J2219/00054; B01J2219/00056; B01J2219/00069; B01J2219/00074; B01J2219/00087; B01J2219/00094; B01J2219/00099; B01J2219/00121; B01J2219/00123; B01J2219/0015; B01J2219/00153; B01J2219/00159; B01J2219/00162; B01J2219/00186
Claims Analysis
Total Claims: 17
Claim 1
Independent Claim
158 words
A method for directly and continuously converting a polysaccharide and monohydric alcohol slurry into a glycoside mixture, said method comprising the steps of: (a) continuously providing to a tubular reaction zone under a positive fluid pressure, a fluid feed slurry consisting essentially of polysaccharide, monohydric alcohol in an amount exceeding the polysaccharide weight and an effective amount of an acid catalyst sufficient to catalyze the conversion of said polysaccharide and monohydric alcohol to a glycoside mixture at an elevated temperature within said reaction zone; (b) heating said feed slurry within said continuous tubular reaction zone to an elevated temperature for a period of time sufficient to convert said fluid slurry into a fluid glycoside mixture while continuously providing additional feed slurry to said tubular reaction zone under a positive fluid pressure to force the converted fluid glycoside mixture through said tubular reaction zone; and (c) rapidly cooling and recovering the converted glycoside mixture from said tubular reaction zone.
Claim 2
Independent Claim
158 words
A method for directly and continuously converting a polysaccharide and monohydric alcohol slurry into a glycoside mixture, said method comprising the steps of: (a) continuously providing to a tubular reaction zone under a positive fluid pressure, a fluid feed slurry consisting essentially of polysaccharide, monohydric alcohol in an amount exceeding the polysaccharide weight and an effective amount of an acid catalyst sufficient to catalyze the conversion of said polysaccharide and monohydric alcohol to a glycoside mixture at an elevated temperature within said reaction zone; (b) heating said feed slurry within said continuous tubular reaction zone to an elevated temperature for a period of time sufficient to convert said fluid slurry into a fluid glycoside mixture while continuously providing additional feed slurry to said tubular reaction zone under a positive fluid pressure to force the converted fluid glycoside mixture through said tubular reaction zone; and (c) rapidly cooling and recovering the converted glycoside mixture from said tubular reaction zone.
Claim 3
Dependent Claim
69 words
The method of claim 1, wherein the polysaccharide and monohydric alcohol respectively consist essentially of starch and alkanol containing from 1 to 4 carbon atoms inclusive, and the slurry is heated and maintained under pressure and at an elevated temperature within said reaction zone for a period of time sufficient to convert the slurry to a glycoside mixture containing from about 65 to 90% alpha-alkyl glucoside and beta-alkyl glucoside.
Claim 4
Dependent Claim
111 words
The method of claim 1, in which the monohydric alcohol consists essentially of methanol, the continuous tubular reactor has a total length of at least about 50 feet, and has an internal diameter of about 0.18 to 6.0 inches, the temperature of the slurry within the reaction zone is maintained between 100°-400° C., and the average reaction time in the reaction zone ranges from about 2-30 minutes with said reaction conditions being sufficient to provide a glycoside mixture comprised of (in percent by weight): 45.67-51.54 alpha-methyl glucoside; 25.88-27.96 beta-methyl glucoside; 8.67-14.73 alpha- and beta- methyl diglycoside; 1.04-3.92 alpha- and beta- methyl triglycoside; 0.07-1.19 higher methyl glycoside; 5.26-7.54 glucofuran; and 1.02-3.34 dextrose.
Claim 5
Dependent Claim
33 words
The method of claim 1 wherein the monohydric alcohol is at least one member selected from the group consisting of allyl alcohol and an alkanol containing from one to eighteen carbon atoms inclusive.
Claim 6
Dependent Claim
39 words
The method of claim 4, in which the catalyst is selected from the group consisting of hydrochloric acid, sulfuric acid, ortho-, meta-, and para-toluene-sulfonic acid, benzene-sulfonic acid, phosphoric acid, substituted benzene-sulfonic acids, ethane-sulfonic acid and combinations of the above.
Claim 7
Dependent Claim
37 words
The method of claim 5, in which the polysaccharide is starch, and the catalyst concentration in the slurry is continuously adjusted to the range of about 0.001 to 0.1 mole per mole of starch, dry solids basis.
Claim 8
Dependent Claim
48 words
The method of claim 6 wherein the feed slurry contains about 40-50% starch solids and acid catalyst and from about 50 to 60% methanol, with sufficient methanol being evaporated from the methyl glycoside mixture obtained from said reaction zone to provide at least 55% methyl glycoside mixture solids.
Claim 9
Dependent Claim
46 words
The method of claim 6, in which the average reaction time at elevated temperature is about 2-150 minutes and the temperature is quickly lowered after the conversion whereby a substantially pure alkyl glycoside mixture having a low color contamination and a minimum of by-products is obtained.
Claim 10
Independent Claim
105 words
A method for direct, continuous alcoholysis of starch to a mixture of alkyl glycosides, said method comprising the steps of: continuously making a fluid slurry of starch in monohydric alcohol in which the amount by weight of monohydric alcohol exceeds the amount by weight of polysaccharide, instantaneously heating said starch/monohydric alcohol slurry while moving said slurry through a confined zone comprising a continuous tubular reactor which is at least 50 feet in length, and in which the slurry is transferred therethrough by fluid pressure only under high temperature and pressure in the presence of an acid catalyst to continuously produce a mixture of alkyl glycosides.
Claim 11
Independent Claim
105 words
A method for direct, continuous alcoholysis of starch to a mixture of alkyl glycosides, said method comprising the steps of: continuously making a fluid slurry of starch in monohydric alcohol in which the amount by weight of monohydric alcohol exceeds the amount by weight of polysaccharide, instantaneously heating said starch/monohydric alcohol slurry while moving said slurry through a confined zone comprising a continuous tubular reactor which is at least 50 feet in length, and in which the slurry is transferred therethrough by fluid pressure only under high temperature and pressure in the presence of an acid catalyst to continuously produce a mixture of alkyl glycosides.
Claim 12
Dependent Claim
19 words
The method of claim 9, in which the temperature in the reactor is in the range of 100°-400° C.
Claim 13
Dependent Claim
72 words
The method of claim 9, in which the acid catalyst is selected from the group consisting of hydrochloric acid, sulfuric acid, phosphoric acid, ortho-, meta-, and para-toluenesulfonic acid, benzene-sulfonic acid, substituted benzene-sulfonic acid, ethane-sulfonic acid, and combinations of the above, and in which the alcohol is selected from the group consisting of methanol, ethanol, propanol, allyl alcohol, butanol, and alcohols having five to eighteen carbon atoms, their isomers, derivatives and mixtures thereof.
Claim 14
Dependent Claim
43 words
The method of claim 11, in which the starch monohydric alcohol slurry is about 40-45% solids, the catalyst comprises at least 0.005 moles of para-toluene-sulfonic acid per mole anhydroglucose unit, and the reaction temperature in the confined zone is at least 165° C.
Claim 15
Dependent Claim
67 words
The method of claim 11 in which the monohydric alcohol is methanol and the methanol/starch mole ratio in the slurry is in the range of 15:1 to 6.5:1, the reaction temperature in the confined zone is about 160°-180° C., the retention time in the confined zone is about 8-20 minutes, and the catalyst is present in an amount of at least about 0.004 moles per anhydroglucose units.
Claim 16
Dependent Claim
37 words
The method of claim 13 wherein the alcoholysis of the slurry within said confined zone is maintained under conditions sufficient to yield a mixture of alkyl glycosides containing from about 65% to 90% alpha- and beta-methyl glucoside.
Claim 17
Dependent Claim
38 words
The method of claim 11, in which the retention time of the starch in the confined zone is 5 to 20 minutes, the alcohol is methanol, and the molar ratio of methanol to starch is 6.5:1 to 9:1.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1983-09-16 | 1984-03-17 | 1984-09-16 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1987-09-16 | 1988-03-17 | 1988-09-16 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1991-09-16 | 1992-03-17 | 1992-09-16 | $7700.00 | Window Closed / Lapsed |