US4015067A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method of preparing polysaccharide ethers and apparatus
Assignee: Dow Chemical Co
•
Filing: 1975-08-18
•
Granted: 1977-03-29
•
Expires: 1995-08-18
Abstract
Abstract Polysaccharide ethers are prepared in a novel continuous process in which a slurry of a polysaccharide, an alkali metal hydroxide, and an etherifying agent, with or without an inert diluent, are mixed in the substantial absence of molecular or free oxygen and fed through a sinuous tubular reactor under pressure, so that the etherification reaction is continuous. The apparatus for preparing the reaction mixture is also novel.
Inventors
- 👤 Gordon Y. T. Liu
- 👤 Carl P. Strange
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-24 10:46
CPC Classifications
C; C08; C08B; C08B1/00; C08B1/06; C08B11/00; C08B11/02; C08B11/04; C08B11/08; C08B11/193
Claims Analysis
Total Claims: 18
Claim 1
Independent Claim
133 words
A method of preparing an ether of a polysaccharide comprising 1. continuously preparing a slurry of a finely divided polysaccharide, an alkali metal hydroxide in an amount sufficient to provide from about 0.25 to about 1.7 parts by weight based on the polysaccharide, and an etherifying ingredient with or without an inert carrier fluid in the substantial absence of free oxygen, 2. feeding said slurry into a tubular reactor, free of obstructions to passage of the slurry, under a pressure of from about 100 to about 400 psig at a rate to provide a reaction period of from about 10 to about 60 minutes at a temperature of from about 30 to about 135° C. 3. removing the reacted slurry from the reactor and 4. purifying and recovering the ether of the polysaccharide.
Claim 2
Independent Claim
133 words
A method of preparing an ether of a polysaccharide comprising 1. continuously preparing a slurry of a finely divided polysaccharide, an alkali metal hydroxide in an amount sufficient to provide from about 0.25 to about 1.7 parts by weight based on the polysaccharide, and an etherifying ingredient with or without an inert carrier fluid in the substantial absence of free oxygen, 2. feeding said slurry into a tubular reactor, free of obstructions to passage of the slurry, under a pressure of from about 100 to about 400 psig at a rate to provide a reaction period of from about 10 to about 60 minutes at a temperature of from about 30 to about 135° C. 3. removing the reacted slurry from the reactor and 4. purifying and recovering the ether of the polysaccharide.
Claim 3
Dependent Claim
23 words
The method of claim 1 in which the pressure is 200-350 psig and the temperature ranges from about 90° to about 110° C.
Claim 4
Dependent Claim
70 words
The method of claim 2 in the slurry based on a part of cellulose consists essentially of from about 0.25 to about 1.7 parts by weight of NaOH, from about 0.6 to about 20 parts by weight of CH 3 Cl, from about 0.6 to about 20 parts by weight of propylene oxide, the pressure is from 300 psig and the temperature ranges from about 65° to about 90° C.
Claim 5
Dependent Claim
24 words
The method of claim 3 in which the NaOH content is from about 0.5 to about 1.2 parts by weight per part of cellulose.
Claim 6
Dependent Claim
73 words
The method of claim 1 in which the slurry based on one weight part of cellulose consists essentially of from about 0.25 to about 1.7 parts by weight of NaOH, from about 0.6 to about 20 parts by weight of ethylene oxide, and from about 0.6 to about 20 parts by weight of CH 3 Cl, the pressure is about 300 psig and the temperature ranges from about 65° to about 100° C.
Claim 7
Dependent Claim
17 words
The method of claim 1 in which the NaOH is added as a 40-73 percent aqueous solution.
Claim 8
Dependent Claim
11 words
The method of claim 1 in which alkali is 73-100 percent.
Claim 9
Dependent Claim
47 words
The method of claim 1 in which the slurry, based on a part of cellulose, consists essentially of about 1 part of NaOH, about 4.5 parts propylene oxide, and about 10 parts of MeCl, the pressure is about 300 psig and the temperature is about 65° C.
Claim 10
Dependent Claim
61 words
The method of claim 1 in which the slurry, based on a pound of cellulose, consists essentially of about one part by weight of NaOH, about 8.25 parts by weight of CH 3 Cl and about 5.5 parts by weight of propylene oxide, the pressure is about 300 psig and the reaction temperature is from about 70° to about 90° C.
Claim 11
Dependent Claim
54 words
The method of claim 1 in which the slurry, based on a pound of cellulose, consists essentially of about 0.9 part of NaOH, about 6.5 parts of CH 3 Cl and about 6.5 parts of propylene oxide, the pressure is about 300 psig and the temperature is from about 65° to about 90° C.
Claim 12
Dependent Claim
25 words
The method of claim 2 in which the unreacted CH 3 Cl, propylene oxide and by-product dimethyl ether are recovered and recycled to the slurry.
Claim 13
Dependent Claim
13 words
The method of claim 1 in which the etherifying ingredient is methyl chloride.
Claim 14
Dependent Claim
13 words
The method of claim 1 in which the etherifying ingredient is propylene oxide.
Claim 15
Dependent Claim
19 words
The method of claim 1 in which the etherifying ingredients contain a mixture of ethylene oxide and propylene oxide.
Claim 16
Dependent Claim
21 words
The method of claim 1 in which a mixture of methyl chloride, ethylene oxide and propylene oxide is the etherifying ingredient.
Claim 17
Dependent Claim
19 words
The method of claim 1 in which the etherifying ingredient is a mixture of ethylene oxide and butylene oxide.
Claim 18
Dependent Claim
19 words
The method of claim 1 in which the etherifying ingredient is a mixture of methyl chloride and butylene oxide.
References Cited (Backward Citations)
CA632046A
Cited
US2476331A
Cited
US3278520A
Cited
US3314809A
Cited
US3351583A
Cited
US3453261A
Cited
US3615254A
Cited
US3544556A
Cited
US3915959A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1980-03-28 | 1980-09-27 | 1981-03-29 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-03-28 | 1984-09-27 | 1985-03-29 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-03-28 | 1988-09-27 | 1989-03-29 | $7700.00 | Window Closed / Lapsed |