US4733009A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method for separating glycine and L-serine from a solution containing same
Assignee: Mitsui Chemicals Inc
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Filing: 1986-07-16
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Granted: 1988-03-22
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Expires: 2006-07-16
Abstract
Abstract Disclosed is a method for separating lycine and L-serine from a solution containing both of them in the dissolved state and, in particular, a reaction solution obtained from a fermentation or enzymic conversion process for the preparation of L-serine by using glycine as the raw material. This method is based on a chromatographic technique utilizing the differential affinity of L-serine and glycine for a strongly acidic ion exchange resin.
Inventors
- 👤 Shoichiro Miyahara
- 👤 Toshio Matsumoto
- 👤 Tooru Miyahara
- 👤 Akio Sakaguchi
- 👤 Kazunari Nitta
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-30 23:39
CPC Classifications
C; C12; C12P; C12P13/00; C12P13/04; C12P13/06
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
110 words
A method for separating glycine and L-serine from a solution thereof which comprises: (a) passing a solution containing both glycine and L-serine in the dissolved state through a column of a strongly acidic ion exchange resin having an effective size of 0.15 to 0.40 mm and a uniformity coefficient of not greater than 1.7 at a linear velocity of not greater than 2 meters per hour, followed by passing water through the column at a linear velocity of not greater than 2 meters per hour to obtain an effluent fraction containing a substantial portion of said L-serine charged as an effluent, while retaining the glycine within the column, and then
Claim 2
Independent Claim
110 words
A method for separating glycine and L-serine from a solution thereof which comprises: (a) passing a solution containing both glycine and L-serine in the dissolved state through a column of a strongly acidic ion exchange resin having an effective size of 0.15 to 0.40 mm and a uniformity coefficient of not greater than 1.7 at a linear velocity of not greater than 2 meters per hour, followed by passing water through the column at a linear velocity of not greater than 2 meters per hour to obtain an effluent fraction containing a substantial portion of said L-serine charged as an effluent, while retaining the glycine within the column, and then
Claim 3
Dependent Claim
20 words
(b) bringing an alkaline solution into contact with the column to obtain an eluate containing substantially all of said glycine.
Claim 4
Dependent Claim
20 words
(b) bringing an alkaline solution into contact with the column to obtain an eluate containing substantially all of said glycine.
Claim 5
Dependent Claim
42 words
The method as claimed in claim 1 wherein the solution containing both glycine and L-serine is a solution obtained from a fermentation or enzymatic conversion process using glycine as the raw material and containing a mixture of unreacted glycine and formed L-serine.
Claim 6
Dependent Claim
27 words
The method as claimed in claim 1 wherein the solution is passed through the column at a linear velocity of not greater than 1 meter per hour.
Claim 7
Dependent Claim
40 words
The method as claimed in claim 1, wherein the amount of resin used is such that the total amount of cations present in the solution to be treated is within the limit of the total exchange capacity of the resin.
Claim 8
Dependent Claim
29 words
The method as claimed in claim 1, which further comprises, prior to passing the solution containing glycine and L-serine through the column, washing the column with dilute hydrocloric acid.
Claim 9
Dependent Claim
27 words
The method as claimed in claim 1, wherein said column of strongly acidic ion exchange resin has a resin bed of at least 1000 mm in height.
Claim 10
Dependent Claim
27 words
The method as claimed in claim 1, wherein said solution containing glycine and L-serine is passed through the column at a temperature of 60° C. or below.
Claim 11
Dependent Claim
22 words
The method as claimed in claim 1, wherein said alkaline solution is aqueous ammonia having a concentration of about 0.1 to 5%.
Claim 12
Dependent Claim
17 words
The method as claimed in claim 8, wherein said aqueous ammonia has a concentration of about 1%.
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) | 1991-03-22 | 1991-09-21 | 1992-03-22 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1995-03-22 | 1995-09-21 | 1996-03-22 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1999-03-22 | 1999-09-21 | 2000-03-22 | $7700.00 | Window Closed / Lapsed |