Patent Grant
7838641
The present invention concerns a modified procedure for the production of alginate having a high mannuronic acid-content, in which the initial pre-extraction step of the algae is modified by adjustment of pH in order to separately recover an alginate fraction of a very high mannuronic acid-content. Typically, with this modified procedure, the alginate fraction, when recovered from the initial pre-extraction step contains at least 80 mole % mannuronic acid in the alginate.
Alginates are isolated from marine brown algae. Alginate is also produced in soil bacteria such as Azotobacter vinelandii and Azotobacter crococcum and several different Pseudomonas sp. Brown algae are however generally the source of commercially available alginates.
Alginates are used in foodstuffs and in pharmaceutical, dental, cosmetic and other industrial products. The most common industrial applications are based on their hydro colloidal and poly electrolytical nature, which forms the basis for the gel-forming, thickening, stabilizing, swelling and viscosity-providing properties.
Alginates are salts of alginic acid, a linear, hetero polysaccharide consisting of (1-4) linked β-D-mannuronic acid, designated as M, and α-L-guluronic acid, designated as G. These two uronic acids have the following formulae:
The polymers exist as homopolymer sequences of mannuronic acid, called M-blocks, homopolymer sequences of guluronic acid called G-blocks, and mixed sequences of mannuronic and guluronic acid units, designated MG-blocks or alternating blocks.
The following scheme represents an illustration of the structure of alginates:
Alginates usually contain all three types of blocks and a block typically consists of three to thirty monomer units. The distribution of the blocks depends on the type of algae from which the alginate is isolated, as well as on the age and part of the plant. For example alginate from the stalk may have a different sequence and block composition compared with alginate isolated from the leaves. The time of year at which the algae are harvested also affects the block composition and sequence. According to common knowledge, the highest G-content can be found in the stem of old L. hyperborea. The leaf of the same species has a somewhat lower G-content and shorter G-blocks, but the content is still higher than most other species. Commercially available alginates usually have a G-content of 25%-70%.
Sources which have a high content of M-blocks are for example species of the brown algae genera Durvillea, Laminaria, Lessonia, Fucales and Ascophyllum, in particular the fruiting bodies of Ascophyllum during spring are rich in mannuronic acid.
Alginates which are rich in mannuronic acid have been shown to possess immunostimulating activity as described in U.S. Pat. No. 5,169,840.
Norwegian Patent No. 305,033, corresponding to U.S. Pat. No. 6,121,441 describes a procedure for producing uronic acid blocks from alginate. This patent is however concerned with a fractionated release of the different block-fractions; G, M and MG in an industrial suitable manner wherein the liquid volumes are kept down. Also the conditions described in the fractionated precipitation procedure are optimised in order to obtain pure fractions.
Other preparative processes for the production of Poly M-alginates, wherein the content of mannuronic acid is 80% (FM=0.80) are known from Rosell, K. G. and Srivastava, L. M., Can. J. Bot, 62 (1984), p. 2229-2236, Craigie, J. S. et al, Carbohydr. Polym., 4 (1984), p. 237-252 and Wedlock, D. J. et al., Food Hydrocolloids, 4 (1990), p. 41-47.
A simple modification of the pre-extraction step of an industrial process as in the present invention is however not described. The present invention which separately recovers, or retains a fraction of alginate of a high mannuronic acid-content therefore represents a simple and economic way of production compared with the processes of the prior art.
In PCT/US91/00475, a mannuronic acid-containing alginate wound healing composition and method of its use are described. The composition comprises biopolymers such as alginates of at least 70 mole % β-D-mannuronic acid (M). According to this publication on page 2, line 17, a few algae sources are capable of producing alginate having a G-content of less than 30%. However bacteria are stated as the preferred source of high M-containing alginate. The present invention differs essentially from this teaching in that it describes a modified industrial process for production of alginate, and further that this modified process keep an alginate fraction with a high mannuronic acid-content which is otherwise lost in the industrial standard extraction process.
The standard industrial process of production of water-extractable alginate has now been improved by the modification of the pre-extraction step or the so-called swelling step. This step is modified to be conducted at a certain pH. The pH is kept above about 2.3 in the pre-extraction step which surprisingly results in a 3D soluble alginate fraction with a very high mannuronic acid-content, preferably at least 80 mole % of M. This soluble alginate-fraction can be recovered in a separate fraction before the initiation of the extraction step in the standard procedure as set out below:
Possible intermediate washing steps with diluted acid solutions can be carried out between the different steps 1-9 above. In step 8 the base can be for example sodium or calcium carbonate, resulting in the corresponding sodium or calcium alginate in step 9.
In this invention the pH in the pre-extraction step (swelling step) is kept at a pH above “about 2.3” which means, as used herein, 2.3+/−0.1.
In the aspect of this invention, the mannuronic acid-rich fraction is recovered separately, the pH of the pre-extraction step is kept to a pH above about 2.3, and the liquid fraction is isolated from the suspension of the pre-extraction or swelling step by filtration, or any other standard separation method like centrifugation, or sieving. Subsequently the alginate can optionally be precipitated from the liquid fraction in any conventional manner with alcohol, acid or salt, such as ethanol, hydrochloric acid, sulphuric acid or calcium chloride.
The process according to the invention, wherein the pH is kept at a: pH above about 2.3 in the pre-extraction step, led to a yield in the range 0.05-10% by weight, preferably within 2%-6% by weight of the mannuronic acid-rich fraction as stated in table 2, on page 8. The alginate recovered has a M-content of at least 80 mole %. The present invention thus offers an economic and simple method of production of a high-content mannuronic acid alginate, which is an alginate product particularly suitable for medically, veterinary and dietary applications.
An aspect of this invention concerns a process for production of alginate having a mannuronic acid-content of at least 80 mole %, wherein the said alginate is produced by:
a) adding algae or seaweed to water under stirring, in a ratio of 1:3 to 1:20 respectively, at a pH above about 2.3, while maintaining a temperature above 20° C. for at least 30 minutes, and
b) separating said alginate from the solid material of the suspension in a) by a standard separation method such as filtration, and optionally
c) recovering said alginate.
The alginate fraction is isolated from the solid material by filtration, or any other suitable standard separation method such as centrifugation or sieving, and the alginate with a mannuronic acid-content is optionally recovered from the solution by precipitation with acid, salt or alcohol.
The starting material of the present invention is algae or seaweed, in particular brown algae, which is treated with formaldehyde, in order to fixate the phenols and preserve the algae. Further the algae can be washed with acid to remove the highly viscous fucoglycans. It is understood that the algae can be pre-treated in any known manner. Commercially available alginates, most preferably dried and milled algae of the species Durvillea can be used, but also fresh, whole or unmilled algae from Durvillea, Laminaria, Lessonia, Ascophyllum or Fucales are suitable as starting materials in the present process.
The invention is illustrated by the following non-limiting examples.
Description of the Process:
Starting raw material from different Durvillea species, D. potatorum (milled) as sample 1 and D. antarctica (not milled) as sample 2 were added to water in the amounts set forth in the table below, and stirred by hand from time to time, at a temperature of 55° C. for 3.5 hours. After storage at ambient temperature over the night, the algae were extracted a second time at 55° C. for 1 hour, then 2.5 ml formaldehyde was added and the extraction continued for 1 hour.
“Pre-extraction” Step
Filtration
The suspension was then sieved on a 60-mesh filter and washed two times with an excess of water. The solution was then filtrated with filter aid on a vacuum funnel and thereafter on a membrane filter.
Acid Precipitation
The solution was then allowed to cool to 10° C. and was then added NaCl to a 0.5%-concentration. Thereafter drops of dilute 5. 5M hydrochloric acid was carefully added by stirring with magnet to a pH 1.8. A white precipitate was formed. The suspension was, after being kept at 10° C. for 30 minutes, sieved on a 120 mesh-filter cloth and pressed carefully by hand resulting in pasty, yellow mass that turned to fine fiber after pressing.
Neutralization
All the acid material was transferred to a 250 ml vessel and added water to bring the volume to 200 ml, before neutralized to pH 7, with solid soda ash under magnetic stirring.
Filtration
The solution was once again filtrated on a 0.8 micron filter membrane of cellulose nitrate.
Alcohol Precipitating
The filtrate was cooled to 10° C. and precipitated with isopropyl alcohol in the ratio 1:1. The fibers formed were washed once with 70 volume % isopropyl alcohol and then a second time with 100 volume % isopropyl alcohol
Drying
The fibers were drawn out with a pincer and then freeze-dried.
Results are given in table 1.
D. potatorum
D. antarctica
Analysis of Product
D. potatorum
D. antarctica
Block-Distribution of Product Measured on NMR 400 Hz
D. potatorum
D. antarctica
Table 2 shows yields of mannuronic acid from other seaweed-samples produced as in example 1.
Ascophyllum nodosum,
Durvillea antarctica,
Durvillea antarctica,
Durvillea antarctica,
Durvillea antarctica,
Durvillea potatorum,
Lessonia trabeculata,
Lessonia nigrescens,
Laminaria hyperborea,
Saragassum, Tanzania,
Macrocystes pyrifera,
Laminaria japonica,
Fucus spiralis,
It is possible to further increase the content of mannuronic acid by addition of salt in the “pre-extraction” step.
Description of the process:
“Pre-Extraction” Step
20 gram Durvillea antarctica (milled coarse particles >70 mesh) algae from Chile August 1996 was added 500 ml water and a certain amount of NaCl, and was extracted under stirring on a Jar test machine, at stirring speed 140 rpm for 2 hours, at a temperature of 20° C. The salt was added to a concentration in the solution (% by weight), as set forth in table 3.
Durvillea
Antarctica
Sieving
The material was then sieved on a 400 mesh filtration cloth and pressed by hand. The sieved solution was weighed and pH measured as given in table 4.
Filtration
The sieved solution was then filtrated by vacuum (water suction pump) on a funnel with filter paper. The viscosity of the filtrated solution was measured on a glass tube and the results are given in table 5.
Acid Precipitating
The filtrate was cooled to below 15° C. and each of the samples were added drops of 5.5 M hydrochloric acid until the pH reached 1.8-2.0, under stirring with a magnetic stirrer. A fiber shaped precipitate was formed. The precipitate was then sieved on a 400-mesh filtration cloth and pressed by hand.
Neutralization
The alginic acid was then diluted with water and neutralized with solid soda; ash to pH 6-7 under stirring until completely dissolved.
Alcohol Precipitating
The solution was then cooled and precipitated with equal parts of isopropyl alcohol. Thereafter washed with 70 volume % isopropyl alcohol, and repeatedly washed with pure 100 volume % isopropyl alcohol.
Drying
The precipitated fiber was pulled out by a pincer and transferred to a vessel and freeze dried overnight in vacuum.
Results
The results are shown in table 6, wherein the amount of yield was calculated assuming that no alginate was lost and that all the alginate is dissolved in the water added.
Description of the Process:
The content of mannuronic acid in the separate fraction was further increased by addition of CaCl2. The starting material was D. antarctica from Chile that was milled to coarse particles of a size >70 mesh.
“Pre-Extraction”
The amounts and conditions of the “pre-extraction” step are set out in table 7. The “pre-extraction” (extraction) was carried out under stirring on Jar tester with about 140 rpm.
Filtration
The material was then sieved on a 400-mesh filter and pressed by hand. The solution was then heated to about 30° C. and filtrated with paper on a vacuum Suction flask.
Acid Precipitation
The solution was then cooled to 10° C. and added sodium chloride to 0.5%. Then drops of 5.5 M HCl were added, with carefully magnetic stirring until pH 1.8. A white precipitate was formed. The material suspension was then stored for 30 minutes and sieved on 400-mesh filtration cloth and pressed carefully by hand. The material was a pasty yellow mass, which turned to fine bright fibers after pressing.
Neutralization
The acid material was then transferred to a 250 ml vessel and added water to bring the volume to 200 ml and then neutralized to pH 7 with solid soda ash under magnetic stirring.
Alcohol Precipitating
The filtrate was then cooled to 10° C. and precipitated on stirring with 100 volume % isopropyl alcohol in a ratio 1:1. Large fibers were precipitated. The fibers were washed twice with 70 volume % isopropyl alcohol and finally with 100 volume % isopropyl alcohol.
Drying
The fibers were then pulled out by a pincer, and thereafter freeze dried overnight under vacuum.
Results
The results are given in tables 9 and 10 which show the yields and the increase in content of mannuronic acid in the alginate with more than 80% M, from maximum 91% M when salt not was added (confer table 2), to a maximum of 95% M when salt was added to the “pre-extraction” step.
Description of a standard process for the production of alginate with a very high mannuronic acid content.
Fresh Ascophyllum nodosum algae from Karmøy, Norway were used as starting material.
Pressing
50 kg of algae were pressed on a roller press type “Haller” with a capacity of 280 kg of algae per hour. A total of 300 ml of extract was collected.
Filtration
The extract was filtrated on coarse filter paper with use of water suction.
Acid Precipitating
Volume of 255 g was added 1,5% NaCl and then drops of 5.5 M diluted hydrochloric acid until pH reached 1.5. Yellow flocs precipitated and was sieved from the solution on a 400 mesh filtration cloth and pressed by hand.
Neutralisation
The flocks dissolved by adding 50 ml of water and solid soda ash to pH 9. The solution was then filtrated with black band filter paper.
Alcohol Precipitation
The solution was precipitated with equal amounts of isopropyl alcohol. The precipitated material was sieved on a 400-mesh filtration cloth and washed once with acetone. The material was then dried 4 hours by 105° C.
Results
The results are given in table 11 below
A. nodosum
The mannuronic acid content of the alginate prepared in reference example 5, was 94.4% M-block and 91.8% MM-block.
| Number | Date | Country | Kind |
|---|---|---|---|
| 20015874 | Nov 2001 | NO | national |
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/NO02/00431 | 11/21/2002 | WO | 00 | 6/1/2004 |
| Publishing Document | Publishing Date | Country | Kind |
|---|---|---|---|
| WO03/046199 | 6/5/2003 | WO | A |
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| 2128551 | Le Gloahee | Aug 1938 | A |
| 3396158 | Haug | Aug 1968 | A |
| 5596084 | Sanderson et al. | Jan 1997 | A |
| 6121441 | Simensen et al. | Sep 2000 | A |
| Number | Date | Country |
|---|---|---|
| 19836960 | Feb 2000 | DE |
| 862702 | Mar 1961 | GB |
| 9851710 | Nov 1998 | WO |
| 0156404 | Aug 2001 | WO |
| Number | Date | Country | |
|---|---|---|---|
| 20050038237 A1 | Feb 2005 | US |
