US4074043A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Purification of tamarind gum
Assignee: General Mills Chemicals Inc
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Filing: 1976-03-15
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Granted: 1978-02-14
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Expires: 1996-03-15
Abstract
Abstract Air classification of finely ground crude tamarind gum provides a purified tamarind seed polysaccharide. The crude gum may also be admixed with finely divided siliceous matter or may be defatted prior to air classification to increase the degree of purification.
Inventors
- 👤 Duane A. Jones
- 👤 Wesley A. Jordan
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 14:27
CPC Classifications
C; C08; C08B; C08B37/00
Claims Analysis
Total Claims: 11
Claim 1
Independent Claim
78 words
A process for purification of crude tamarind seed polysaccharide comprising finely grinding crude tamarind seed kernel powder to a particle size of less than 100 microns, said particle size having a gradation of particle size and air classifying said finely ground crude tamarind seed kernel powder into at least a first fine fraction having an increased protein content and a decreased polysaccharide content and a second coarse fraction having a reduced protein content and an increased polysaccharide content.
Claim 2
Dependent Claim
78 words
A process for purification of crude tamarind seed polysaccharide comprising finely grinding crude tamarind seed kernel powder to a particle size of less than 100 microns, said particle size having a gradation of particle size and air classifying said finely ground crude tamarind seed kernel powder into at least a first fine fraction having an increased protein content and a decreased polysaccharide content and a second coarse fraction having a reduced protein content and an increased polysaccharide content.
Claim 3
Dependent Claim
21 words
The process of claim 1 wherein said ground powder has a particle size gradation of from about 5 to 100 microns.
Claim 4
Dependent Claim
63 words
The process of claim 2 wherein the finely ground crude tamarind seed kernel powder has a particle size distribution of from 15 to 30 percent is smaller than 10 microns, from 10 to 30 percent is between 10 and 20 microns, from 15 to 30 percent is between 20 and 40 microns and 15 to 20 percent is between 60 and 80 microns.
Claim 5
Dependent Claim
23 words
The process of claim 1 wherein said finely ground tamarind material is mixed with finely divided siliceous material prior to said air classification.
Claim 6
Dependent Claim
84 words
A process for purification of crude tamarind seed polysaccharide comprising defatting crude tamarind seed kernel powder, finely grinding said defatted tamarind seed kernal powder, finely grinding said defatted tamarind seed kernel powder to a particle size of less than 100 microns, air classifying said finely ground defatted tamarind seed kernel powder into at least a first fraction having an increased tamarind protein content and a decreased tamarind polysaccharide content and into a second fraction having a reduced protein content and an increased polysaccharide content.
Claim 7
Dependent Claim
84 words
A process for purification of crude tamarind seed polysaccharide comprising defatting crude tamarind seed kernel powder, finely grinding said defatted tamarind seed kernal powder, finely grinding said defatted tamarind seed kernel powder to a particle size of less than 100 microns, air classifying said finely ground defatted tamarind seed kernel powder into at least a first fraction having an increased tamarind protein content and a decreased tamarind polysaccharide content and into a second fraction having a reduced protein content and an increased polysaccharide content.
Claim 8
Dependent Claim
21 words
The process of claim 5 wherein said tamarind seed kernel powder is defatted by solvent extraction prior to said air classification.
Claim 9
Dependent Claim
28 words
The process of claim 6 wherein said solvent extraction is carried out utilizing a member of the group consisting of aliphatic hydrocarbons, aromatic hydrocarbons, halogenated hydrocarbons and alcohols.
Claim 10
Dependent Claim
19 words
The process of claim 6 wherein said solvent extraction is carried out utilizing ethylene dichloride, hexane, toluene or isopropanol.
Claim 11
Dependent Claim
26 words
The process of claim 1 wherein said second fraction is further separated into a fraction having increased polysaccharide content and a fraction having increased mechanical impurities.
References Cited (Backward Citations)
US3399189A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1981-02-13 | 1981-08-15 | 1982-02-14 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-02-13 | 1985-08-15 | 1986-02-14 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-02-13 | 1989-08-15 | 1990-02-14 | $7700.00 | Window Closed / Lapsed |