METHOD FOR EXTRACTING ASTAXANTHIN

Abstract: Astaxanthin is extracted from crustacean shells by means of a solvent chosen from carboxylic acid esters containing from 1 to 5 carbon atoms; the operation is carried out practically at ambient temperature.

Description: "METHOD FOR EXTRACTING ASTAXANTHIN" The flesh of trout and salmon, when in their natural environment, has a colour which varies from pink to red, This coloration is not due to a component necessarily present in the flesh itself, but is the result of the depositing of carotenoids (mainly astaxanthin) which are present in the crustacea which form the food of the aforementioned fish, namely shrimps and zooplankton. In recent years, production farms for trout and salmon have increased considerably, but the flesh of these latter is of a different or softer colour than the flesh of the natural fish, which could be a symptom of insufficient or at least different feeding. For this reason, special methods have been developed for returning the flesh coloration of fish to tones very close to natural tones, these methods being based on the use of synthetic canthaxanthin and dried and/or frozen shrimps which are administered with the diet. The aforesaid substances however have certain drawbacks, including the following: - canthaxanthin is synthesised chemically, and enters the human alimentary cycle by way of the fish flesh, accompanied by all the problems which arise from this in terms of toxicity; in addition, the colour of the fish flesh is unstable with time; - shrimp or prawn shells1 a waste product deriving from the shelling, decompose too rapidly, are voluminous, and more over the addition of large quantities thereof to the diet can cause alterations in the fish mineral content in the medium and long term. The aforesaid problems have suggested the use of astaxanthin, and all research activity is now centred on the production and extraction thereof. This product is extracted at the present time from crustacean shells using triglyceride oils of animal or vegetable origin (US. 3,906,112) as an alternative to methods which use more or less polar solvents such as acetone, hexane, ethanol, ether and the like, which give rise to a series of disadvantages and drawbacks such as process difficulties and product instability. Extraction with oil is motivated by the fact that astaxanthin is sufficiently stable in a solution thereof, and also for commercial reasons in that astaxanthin/oil solutions of different proportions have been marketed. However oil as an extraction medium is not free from drawbacks. Firstly, the pigment must be extracted at high temperature 0 (90-150 0), which can lead to its partial decomposition if a suitable antioxidant is not added. In addition, the residual oil must be removed from the shells if these are to be subsequently used for producing chitin and/or chitosan. Finally, when extraction is carried out at a temperature of less than 10000, it is difficult to remove the water contained in the organic extract due to the fact that it is emulsified. If the extraction were to be carried out above 1000C, a long period would be necessary for evaporating all the water contained in the shells, leading to considerable complications from the industrial aspect and a high energy consumption. The applicant has now discovered a method, constituting the subject matter of the present invention, for extracting astaxanthin from crustacean shells which besides resulting in a high yield does not suffer from any of the aforesaid drawbacks. In carrying out the extraction, the method in question uses 8 solvent chosen from carboxylic acid esters of the general formula EMI3.1 in which R is hydrogen or sn alkyl radical with preferably up 2 to. 3 carbon atoms, and R is again an alkyl radical which can be the same as or different from 321; particular advantages have been found by using acetic esters. Tie extraction can be carried out over the entire temperature range in which the solvent is in its liquid state, but it is prefersble to operate between 15 and 250C in that this temperature range gives high extraction yields without requiring critical operating conditions. The operation can also be carried out in air, as the astaxan- thin does not oxidise due to the relatively mild extractive conditions. In addition, the use of special antioxidants is superfluous. The weight ratio of dry shells to solvent can vary widely according to the process used (continuous or batch), the apparatus used (type of agitation, type of filtration etc.) and the required final astaxanthin concentrstion. Particular -advantages have been found by operating at a ratio of between 1:3 and 1:3. The extraction time is of the order of 4.5 minutes, but goes to completion in a time of 10-20 minutes. The average yield is 10-40% higher than the yield obtained by the usual extraction methods. It has however been noted that the yield is also related to the time for which the shells have been stored, and the storage temperature. In general, an increase in storage time leads to a yield reduction because of astaxanthin decomposition. EXAFriPLE 1 2.13 kg of prawn shells containing 47% of dry matter, preserved for ten days at -250C and having a size of 3-4 mm (ground with a rotating knife mill) were mixed with ethyl acetate in a weight ratio of 1:5 with respect to the dry matter and kept stirring for about 20 minutes. liter this, they were filtered under pressure and the filtrate was collected and evaporated to constant weight. Spectrophotometric analysis was carried out on the semisolid residue consisting essentially of fatty substances and free astaxanthin and/or its esters for the quantitative determination thereof 0 392 mg of astaxanthin were extracted by this procedure. EXAMPLE 2 Using an analogous method to that described in example 1, but under a stream of nitrogen, 368.86 mg of astaxanthin per kilo of dry shells were extracted, EXAMPLE 3 Under the same conditions as described in example 1 but carrying out the extraction at 600C, 371.4 mg of astaxanthin per kilo of dry shells were extracted. EXA)iPLE 4 Under the same extraction conditions as described in example 1 but using methyl acetate as the extraction solvent, 350 m & of astaxanthin per kilo of dry shells were extracted.

Claims: CLAIMS: 1. A method for extracting astaxanthin from crustacean shells consisting of treating the shells with a solvent chosen from carboxylic acid alkyl esters of general formula S ¯oR2 in which R1 is hydrogen or an alkyl radical of up to 2 5 carbon atoms, and R is sn alkyl radical the same as or different from R1. 2.. A method for extracting astaxanthin as claimed in the preceding claim, wherein the ratio of dry shells te solvent varies between 1:3 and 1:3. 3. A method for extracting astaxanthin as claimed in claim 1, wherein the operation is carried out within the temperature range in which the solvent is in the liquid state. 4. A method for extracting astaxanthin as claimed in the preceding claim, wherein the operation is preferably carried out at a temperature of between 15 and 250".

Inventors: CELIA, GIOVANNI
Applicants: ANIC S.P.A.
Application year: 1982
Main classification: C09B61
IPC codes: C09B61, C07C67, A23L1, C07C401, C07C403