US4008285A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for making xylitol
Assignee: Individual
•
Filing: 1975-06-18
•
Granted: 1977-02-15
•
Expires: 1995-06-18
Abstract
Abstract A method for recovering xylitol from pentosan-, preferably xylan-containing raw materials including the steps of hydrolyzing the raw material, purifying the hydrolysate by ion exclusion and color removal, and then subjecting the purified solution to chromatographic fractionation to provide a solution containing a high level of xylose. The xylose solution is hydrogenated and a xylitol-rich solution is recovered by chromatographic fractionation using ion exchange resins.
Inventors
- 👤 Asko J. Melaja
- 👤 Lauri Hamalainen
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-28 22:06
CPC Classifications
C; C07; C07H; C07H3/00; C07H3/02
Claims Analysis
Total Claims: 30
Claim 1
Independent Claim
134 words
A method for the production of xylitol on a commercial scale from a pentose-rich solution obtained by acid hydrolysis of a pentosan-containing raw material which comprises the steps of a. removing suspended solids from the solution by mechanical filtration; b. removing inorganic salts and the major portion of organic impurities and color from the solution by ion exclusion; c. removing the balance of color and other organic impurities by treating the solution with a material selected from the group consisting of an ion exchange resin and activated carbon; d. fractionating the solution thus obtained by ion exchange chromatographic techniques to provide a xylose solution of high purity; e. catalytically hydrogenating the xylose solution; and f. subjecting the xylitol solution thus produced to ion exchange chromatographic fractionation to recover a xylitol fraction of high purity.
Claim 2
Independent Claim
134 words
A method for the production of xylitol on a commercial scale from a pentose-rich solution obtained by acid hydrolysis of a pentosan-containing raw material which comprises the steps of a. removing suspended solids from the solution by mechanical filtration; b. removing inorganic salts and the major portion of organic impurities and color from the solution by ion exclusion; c. removing the balance of color and other organic impurities by treating the solution with a material selected from the group consisting of an ion exchange resin and activated carbon; d. fractionating the solution thus obtained by ion exchange chromatographic techniques to provide a xylose solution of high purity; e. catalytically hydrogenating the xylose solution; and f. subjecting the xylitol solution thus produced to ion exchange chromatographic fractionation to recover a xylitol fraction of high purity.
Claim 3
Dependent Claim
145 words
The process of claim 1 wherein step (d) is accomplished by: a. providing a column of a salt of a polystyrene sulfonate cation exchange resin cross-coupled with di-vinyl benzene; b. submerging the column of resin in water; c. feeding the pentose-rich solution having a dry material content of 25 to 55% by weight in uniform supply to the resin surface in the column at a flow rate of 0.2 to 1.5 cubic meters per hour per square meter of the cross-section of the resin column; and d. recovering successively from the downstream side of the resin bed 1. an initial fraction containing mostly water but also containing other pentoses and a low concentration of xylose, 2. an intermediate fraction having a high concentration of xylose and small amounts of other pentoses, and 3. a final fraction containing other pentoses and a minor amount of xylose.
Claim 4
Dependent Claim
146 words
The process of claim 1, wherein step (f) is accomplished by: a. providing a column of a salt of a polystyrene sulfonate cation exchange resin cross-coupled with di-vinyl benzene; b. submerging the column of resin in water; c. feeding the xylitol-rich solution having a dry material content of 25 to 55% by weight in uniform supply to the resin surface in the column at a flow rate of 0.2 to 1.5 cubic meters per hour per square meter of the cross-section of the resin column; and d. recovering successively from the downstream side of the resin bed 1. an initial fraction containing mostly water but also containing other polyols and a low concentration of xylitol, 2. an intermediate fraction containing a high concentration of xylitol, together with small amounts of other polyols; and 3. a final fraction containing other polyols and a minor amount of xylitol.
Claim 5
Dependent Claim
33 words
The process of claim 3, wherein the salt of the resin is selected from the group consisting of alkaline earth metal salts, Fe + + + salts and Al + + + salts.
Claim 6
Dependent Claim
20 words
The process of claim 3, wherein the column of cation-exchanger, wherein used, is from 2.5 to 5 meters in depth.
Claim 7
Dependent Claim
18 words
The process of claim 3 wherein the resin used in step (a) is an alkaline earth metal salt.
Claim 8
Independent Claim
152 words
A method for the production of a mixture of polyols on a commercial scale from a pentose-rich solution obtained by acid hydrolysis of a pentosan-containing raw material which comprises the steps of a. removing suspended solids from the solution by mechanical filtration, b. removing inorganic salts and the major portion of color and other organic impurities by ion exclusion; c. removing the balance color and other organic impurities by treating the solution with a material selected from the group consisting of an ion exchanger resin and activated carbon; d. fractionating the solution thus obtained by ion exchange chromatographic techniques to provide a pentose solution of high purity, and having a high concentration of pentoses, e. catalytically hydrogenating the pentose solution to produce a mixture of polyols, and f. subjecting the polyol mixture to ion exchange chromatographic fractionation to recover a polyol fraction of high purity, free of unhydrogenated sugars and other impurities.
Claim 9
Independent Claim
152 words
A method for the production of a mixture of polyols on a commercial scale from a pentose-rich solution obtained by acid hydrolysis of a pentosan-containing raw material which comprises the steps of a. removing suspended solids from the solution by mechanical filtration, b. removing inorganic salts and the major portion of color and other organic impurities by ion exclusion; c. removing the balance color and other organic impurities by treating the solution with a material selected from the group consisting of an ion exchanger resin and activated carbon; d. fractionating the solution thus obtained by ion exchange chromatographic techniques to provide a pentose solution of high purity, and having a high concentration of pentoses, e. catalytically hydrogenating the pentose solution to produce a mixture of polyols, and f. subjecting the polyol mixture to ion exchange chromatographic fractionation to recover a polyol fraction of high purity, free of unhydrogenated sugars and other impurities.
Claim 10
Dependent Claim
81 words
The process of claim 7, wherein step (f) is accomplished by: a. providing a column of a salt of a polystyrene sulfonate cation exchange resin cross-coupled with di-vinyl benzene; b. submerging the column in water; c. feeding the polyol solution in uniform supply to the resin surface in the column, and d. recovering successively from the downstream side of the resin bed 1. a first fraction comprising unhydrogenated sugars and other impurities, and 2. a second fraction comprising substantially pure polyols.
Claim 11
Dependent Claim
34 words
The process of claim 8, wherein the second fraction comprising a mixture of polyols at (d) (2) is further separated by ion exchange chromatographic fractionation to recover the individual polyols in substantially pure form.
Claim 12
Dependent Claim
33 words
The process of claim 8, wherein the salt of the resin is selected from the group consisting of alkaline earth metal salts, Fe + + + salts and Al + + + salts.
Claim 13
Dependent Claim
17 words
The process of claim 8 wherein the salt of the resin is an alkaline earth metal salt.
Claim 14
Dependent Claim
53 words
The process of claim 8, wherein the salt of the resin is an Fe + + + or Al + + + salt, and wherein the second fraction comprising a mixture of polyols at (d) (2) is further separated by ion exchange chromatographic fractionation to recover the individual polyols in substantially pure form.
Claim 15
Dependent Claim
191 words
In a method for recovering xylitol on a commercial scale from an aqueous mixture of polyols which employs chromatographic techniques on a bed of polystyrene sulfonate cation exchange resin cross-coupled with di-vinyl benzene, the improvement comprising a two-stage fractionation procedure, one stage of the procedure comprising: 1. fractionation of the polyol mixture by passing it through a bed of said resin in an alkaline earth metal salt form to recover; a. a waste fraction having a low concentration of xylitol, and b. a xylitol-rich fraction; 2. crystallizing xylitol from the xylitol-rich fraction to obtain xylitol crystals and a polyol molasses; 3. subjecting the polyol molasses remaining after crystallization of the xylitol to a second stage fractionation procedure which comprises passing the molasses through a column of said resin in the A1 + + + or Fe + + + form to recover; a. a waste fraction containing a low level of xylitol, and b. a xylitol-rich fraction; 4. recovering xylitol crystals from said xylitol-rich fraction, leaving a residual polyol molasses; and 5. returning the residual polyol molasses to the first stage of the separation procedure in admixture with new polyol mixture.
Claim 16
Dependent Claim
191 words
In a method for recovering xylitol on a commercial scale from an aqueous mixture of polyols which employs chromatographic techniques on a bed of polystyrene sulfonate cation exchange resin cross-coupled with di-vinyl benzene, the improvement comprising a two-stage fractionation procedure, one stage of the procedure comprising: 1. fractionation of the polyol mixture by passing it through a bed of said resin in an alkaline earth metal salt form to recover; a. a waste fraction having a low concentration of xylitol, and b. a xylitol-rich fraction; 2. crystallizing xylitol from the xylitol-rich fraction to obtain xylitol crystals and a polyol molasses; 3. subjecting the polyol molasses remaining after crystallization of the xylitol to a second stage fractionation procedure which comprises passing the molasses through a column of said resin in the A1 + + + or Fe + + + form to recover; a. a waste fraction containing a low level of xylitol, and b. a xylitol-rich fraction; 4. recovering xylitol crystals from said xylitol-rich fraction, leaving a residual polyol molasses; and 5. returning the residual polyol molasses to the first stage of the separation procedure in admixture with new polyol mixture.
Claim 17
Dependent Claim
194 words
In a method for recovering xylitol on a commercial scale from an aqueous mixture of polyols which employs chromatographic techniques on a bed of polystyrene sulfonate cation exchange resin cross-coupled with di-vinyl benzene, the improvement comprising a two-stage fractionation procedure, one stage of the procedure comprising: 1. fractionation of the polyol mixture by passing it through a bed of said resin in an alkaline earth metal salt form to recover; a. a waste fraction having a low concentration of xylitol, b. an intermediate polyol molasses fraction, and c. a xylitol-rich fraction; 2. crystallizing xylitol from the xylitol-rich fraction to obtain xylitol crystals and a polyol molasses; 3. combining the intermediate fraction in (1) (b) above with the polyol molasses obtained in (2) above to provide a polyol molasses feed for the next stage in the process; 4. subjecting the polyol molasses feed to a second stage fractionation procedure which comprises passing the molasses through a column of said resin in the Al + + + or Fe + + + form to recover; a. a waste fraction containing a low level of xylitol, b. an intermediate polyol molasses fraction, and c. a xylitol-rich fraction;
Claim 18
Dependent Claim
194 words
In a method for recovering xylitol on a commercial scale from an aqueous mixture of polyols which employs chromatographic techniques on a bed of polystyrene sulfonate cation exchange resin cross-coupled with di-vinyl benzene, the improvement comprising a two-stage fractionation procedure, one stage of the procedure comprising: 1. fractionation of the polyol mixture by passing it through a bed of said resin in an alkaline earth metal salt form to recover; a. a waste fraction having a low concentration of xylitol, b. an intermediate polyol molasses fraction, and c. a xylitol-rich fraction; 2. crystallizing xylitol from the xylitol-rich fraction to obtain xylitol crystals and a polyol molasses; 3. combining the intermediate fraction in (1) (b) above with the polyol molasses obtained in (2) above to provide a polyol molasses feed for the next stage in the process; 4. subjecting the polyol molasses feed to a second stage fractionation procedure which comprises passing the molasses through a column of said resin in the Al + + + or Fe + + + form to recover; a. a waste fraction containing a low level of xylitol, b. an intermediate polyol molasses fraction, and c. a xylitol-rich fraction;
Claim 19
Dependent Claim
52 words
recovering xylitol crystals from said xylitol-rich fraction, leaving a residual polyol molasses; 6. combining the residual polyol molasses from (5) above with the intermediate polyol molasses fraction from (4) (b); 7. returning the said combined polyol molasses fractions to the first stage of the separation procedure in admixture with new polyol mixture.
Claim 20
Dependent Claim
52 words
recovering xylitol crystals from said xylitol-rich fraction, leaving a residual polyol molasses; 6. combining the residual polyol molasses from (5) above with the intermediate polyol molasses fraction from (4) (b); 7. returning the said combined polyol molasses fractions to the first stage of the separation procedure in admixture with new polyol mixture.
Claim 21
Independent Claim
207 words
A method for the production of xylitol on a commercial scale from a pentose-rich solution obtained by acid hydrolysis of a pentosan-containing raw material which comprises the steps of a. removing suspended solids from the solution by mechanical filtration; b. removing inorganic salts and the major portion of organic impurities and color from the solution by ion exclusion; c. removing the balance of color and other organic impurities by treating the solution with a material selected from the group consisting of an ion exchange resin and activated carbon; d. fractionating the solution thus obtained by ion exchange chromatographic techniques to provide a xylose solution of high purity; e. catalytically hydrogenating the xylose solution; f. providing a column of Fe + + + or A1 + + + salt of a polystyrene sulfonate cation exchange resin cross-coupled with di-vinyl benzene; g. submerging the column of resin in water; h. feeding the pentose-rich solution having a dry material content of 25 to 55% by weight in uniform supply to the resin surface in the column at a flow rate of 0.2 to 1.5 cubic meters per hour per square meter of the cross-section of the resin column; and i. recovering successively from the downstream side of the resin bed
Claim 22
Independent Claim
207 words
A method for the production of xylitol on a commercial scale from a pentose-rich solution obtained by acid hydrolysis of a pentosan-containing raw material which comprises the steps of a. removing suspended solids from the solution by mechanical filtration; b. removing inorganic salts and the major portion of organic impurities and color from the solution by ion exclusion; c. removing the balance of color and other organic impurities by treating the solution with a material selected from the group consisting of an ion exchange resin and activated carbon; d. fractionating the solution thus obtained by ion exchange chromatographic techniques to provide a xylose solution of high purity; e. catalytically hydrogenating the xylose solution; f. providing a column of Fe + + + or A1 + + + salt of a polystyrene sulfonate cation exchange resin cross-coupled with di-vinyl benzene; g. submerging the column of resin in water; h. feeding the pentose-rich solution having a dry material content of 25 to 55% by weight in uniform supply to the resin surface in the column at a flow rate of 0.2 to 1.5 cubic meters per hour per square meter of the cross-section of the resin column; and i. recovering successively from the downstream side of the resin bed
Claim 23
Dependent Claim
35 words
an initial fraction containing mostly water but also containing other polyols and a low concentration of xylitol, 2. an intermediate fraction containing a high concentration of xylitol, together with small amounts of other polyols; and
Claim 24
Dependent Claim
35 words
an initial fraction containing mostly water but also containing other polyols and a low concentration of xylitol, 2. an intermediate fraction containing a high concentration of xylitol, together with small amounts of other polyols; and
Claim 25
Dependent Claim
12 words
a final fraction containing other polyols and a minor amount of xylitol.
Claim 26
Dependent Claim
12 words
a final fraction containing other polyols and a minor amount of xylitol.
Claim 27
Independent Claim
182 words
A method for the production of a mixture of polyols from a pentose-rich solution obtained by acid hydrolysis of a pentosan-containing raw material which comprises the steps of a. removing suspended solids from the solution by mechanical filtration, b. removing inorganic salts and the major portion of color and other organic impurities by ion exclusion; c. removing the balance of color and other organic impurities by treating the solution with a material selected from the group consisting of an ion exchanger resin and activated carbon; d. fractionating the solution thus obtained by ion exchange chromatographic techniques to provide a pentose solution of high purity, and having a high concentration of xylose, e. hydrogenating the pentose solution to produce a mixture of polyols, f. providing a column of an Fe + + + or A1 + + + salt of a polystyrene sulfonate cation exchange resin cross-coupled with di-vinyl benzene; g. submerging the column in water; h. feeding the polyol solution in uniform supply to the resin surface in the column, and i. recovering successively from the downstream side of the resin bed
Claim 28
Independent Claim
182 words
A method for the production of a mixture of polyols from a pentose-rich solution obtained by acid hydrolysis of a pentosan-containing raw material which comprises the steps of a. removing suspended solids from the solution by mechanical filtration, b. removing inorganic salts and the major portion of color and other organic impurities by ion exclusion; c. removing the balance of color and other organic impurities by treating the solution with a material selected from the group consisting of an ion exchanger resin and activated carbon; d. fractionating the solution thus obtained by ion exchange chromatographic techniques to provide a pentose solution of high purity, and having a high concentration of xylose, e. hydrogenating the pentose solution to produce a mixture of polyols, f. providing a column of an Fe + + + or A1 + + + salt of a polystyrene sulfonate cation exchange resin cross-coupled with di-vinyl benzene; g. submerging the column in water; h. feeding the polyol solution in uniform supply to the resin surface in the column, and i. recovering successively from the downstream side of the resin bed
Claim 29
Dependent Claim
17 words
a fraction comprising unhydrogenated sugars and other impurities, and 2. a second fraction comprising substantially pure polyols.
Claim 30
Dependent Claim
17 words
a fraction comprising unhydrogenated sugars and other impurities, and 2. a second fraction comprising substantially pure polyols.
References Cited (Backward Citations)
US2917390A
Cited
US2890972A
Cited
US2818851A
Cited
US3305395A
Cited
US3420709A
Cited
US3558725A
Cited
US3579380A
Cited
US3784408A
Cited
US3830770A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1980-02-15 | 1980-08-16 | 1981-02-15 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-02-15 | 1984-08-16 | 1985-02-15 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-02-15 | 1988-08-16 | 1989-02-15 | $7700.00 | Window Closed / Lapsed |