METHODS FOR PREPARING SQUALENE

Abstract

An improved method for preparing squalene from a squalene-containing composition, said method comprising the steps of (a) a purification distillation carried out at a temperature T.sub.1 (b) a denaturing distillation carried out at a temperature T.sub.2; wherein steps (a) and (b) may be performed in either order; T.sub.1 and T.sub.2 are sufficient to cause squalene to boil; T.sub.2>T.sub.1; and T.sub.2>200 C.

Claims

1. A method for the manufacture of an oil-in-water emulsion adjuvant comprising: (i) preparing squalene from a composition comprising squalene from a fish source by a process comprising steps of: (a) a purification distillation carried out at a temperature less than 140 C.; and (b) a denaturing distillation carried out at a temperature greater than or equal to 200 C.; wherein the purification step and the denaturing distillation step may be performed in either order; the temperature of the purification step and the denaturing distillation step is sufficient to cause the squalene to boil; and the denaturing distillation denatures and/or removes potential contaminant proteins and viruses, thereby rendering the squalene safe for human use as compared with non-denatured squalene; and (ii) preparing an oil-in-water emulsion adjuvant using the squalene prepared in step (i).

2. The method of claim 1, wherein the squalene prepared in step (i) is kept sterile following distillation treatment and prior to the preparation of the oil-in-water emulsion adjuvant in step (ii).

3. The method of claim 1, wherein the composition used in step (i) comprises one or more proteins.

4. The method of claim 3, wherein the composition comprises parvalbumin.

5. The method of claim 1, wherein the denaturing distillation is carried out at a pressure of from 0.5 mm Hg to 5.0 mm Hg.

6. The method of claim 1, wherein the purification distillation is carried out at a temperature of from 70 to 100 C.

7. The method of claim 1, wherein the denaturing distillation is carried out at a temperature greater than or equal to 210 C.

8. The method of claim 1, wherein the purification distillation is carried out at a pressure of from 0.5 m Hg to 5 m Hg.

9. The method of claim 1, wherein the purification distillation is carried out prior to the denaturing distillation.

10. The method of claim 1, wherein the composition used in step (i) is subjected to saponification.

11. The method of claim 10, wherein saponification comprises the addition of NaOH or KOH to the composition comprising squalene.

12. The method of claim 1, further comprising the step of combining the oil-in-water emulsion adjuvant with an antigen.

13. The method of claim 1, further comprising the step of packaging the oil-in-water emulsion adjuvant into a kit as a kit component together with an antigen component.

14. The method of claim 13, wherein the kit components are in separate vials.

15. The method of claim 14, wherein the vials are made from borosilicate glass.

16. The method of claim 13, wherein the antigen is an influenza virus antigen.

17. The method of claim 16, wherein the combination of the oil-in-water emulsion adjuvant and the antigen forms a vaccine composition and wherein the vaccine composition includes about 15 g, about 10 g, about 7.5 g, about 5 g, about 3.8 g, about 3.75 g, about 1.9 g, or about 1.5 g of hemagglutinin per influenza virus strain.

18. The method of claim 17, wherein the combination of the oil-in-water emulsion adjuvant and the antigen forms a vaccine composition and wherein the vaccine composition includes a thiomersal or 2-phenoxyethanol preservative.

19. The method of claim 1, wherein the composition comprises 99% squalene or more.

20. The method of claim 1, wherein the oil-in-water emulsion adjuvant comprises between 2-10% squalene.

21. The method of claim 1, wherein the oil-in-water emulsion adjuvant comprises about 5% squalene, about 0.5% polysorbate 80 and about 0.5% sorbitan trioleate by volume.

22. The method of claim 1, wherein the fish oil is shark liver oil.

23. A method for the manufacture of an oil-in-water emulsion comprising: (i) preparing squalene from a composition comprising squalene from a fish source by a process comprising steps of: (a) a purification distillation carried out at a temperature less than 140 C.; and (b) a denaturing distillation carried out at a temperature greater than or equal to 200 C.; wherein the purification step and the denaturing distillation step may be performed in either order; the temperature of the purification step and the denaturing distillation step is sufficient to cause the squalene to boil; and the denaturing distillation denatures and/or removes potential contaminant proteins and viruses, thereby rendering the squalene safe for human use as compared with non-denatured squalene; and (ii) preparing an oil-in-water emulsion using the squalene prepared in step (i).

24. The method of claim 24, wherein the squalene prepared in step (i) is kept sterile following distillation treatment and prior to the preparation of the oil-in-water emulsion adjuvant in step (ii).

25. The method of claim 24, wherein the composition used in step (i) comprises one or more proteins.

26. The method of claim 26, wherein the composition comprises parvalbumin.

27. The method of claim 24, wherein the denaturing distillation is carried out at a pressure of from 0.5 mm Hg to 5.0 mm Hg.

28. The method of claim 24, wherein the purification distillation is carried out at a temperature of from 70 to 100 C.

29. The method of claim 24, wherein the denaturing distillation is carried out at a temperature greater than or equal to 210 C.

30. The method of claim 24, wherein the purification distillation is carried out at a pressure of from 0.5 m Hg to 5 m Hg.

31. The method of claim 1, wherein the purification distillation is carried out prior to the denaturing distillation.

32. The method of claim 1, wherein the composition used in step (i) is subjected to saponification.

33. The method of claim 32 wherein saponification comprises the addition of NaOH or KOH to the composition comprising squalene.

Description

MODES FOR CARRYING OUT THE INVENTION

Example 1

[0121] FIG. 1 shows a schematic of a distillation apparatus which may be used for the purification and/or denaturing distillation steps of the method of the present invention. The process described with reference to FIG. 1 may be carried out without the addition of any solvent to the composition comprising squalene. In the embodiment shown in FIG. 1, the composition comprising squalene is placed in a feed vessel (1) overlaid with nitrogen. One end of an inlet line (3) has a polypropylene prefilter and is placed in the feed vessel, while the other end of the inlet line has a stainless steel needle (19-ga.) which is inserted into the top of a distillation apparatus (5). The distillation apparatus comprises a chamber (7) shaped like a tube with a cylindrical hot finger (9) protruding through the centre. Ethyl benzoate, which has a boiling point of 212 C., is heated below the finger to provide heat to the wall of the hot finger. Although ethyl benzoate is used in this embodiment, it is clear that a solvent having a higher boiling point could be used to increase the temperature of the hot finger. During distillation, the distillation apparatus may be evacuated. The composition comprising squalene may be drawn into the distillation apparatus, e.g. through the use of a lower pressure within the distillation apparatus, through the stainless steel needle and dripped (11) onto the heated wall of the hot finger. As the composition comprising squalene is heated, those components whose boiling point is below 212 C. at the pressure within the distillation apparatus will volatilize. In order to volatilize squalene using the system of FIG. 1, the pressure within the distillation apparatus should be selected to lower the boiling point of squalene to 212 C. or less (e.g. approximately 1.5 mm Hg or less). The volatilized components will condense on the outer wall of the chamber (7), which will be cooled by the ambient air, and will run down the walls into a collection flask (13), which may also be under vacuum. Non-volatile components, e.g. proteins, remain on the wall of the hot finger and flow down into the residue flask (15). Extremely volatile components may be drawn off through the vacuum line, reducing their levels in the squalene condensate.

[0122] Squalene which has already been subjected to purification distillation was distilled using this apparatus. Regardless of source, the final squalene regularly had a purity of 99.9%, an acid value of <0.03 mg KOH/g, and a saponification value <2 mg/g. The denaturing distillation reduced the moisture content of the squalene e.g. from 0.022% to 0.010%, from 0.006 to 0.005%, or from 0.010% to 0.006%.

Example 2

Measurement of the Saponification Value

[0123] The saponification value is the number of mg of potassium hydroxide required to neutralize the free acids and saponify the esters contained in 1.0 g of the substance.

[0124] Procedure (USP <401>): place 1.5 g to 2 g of the substance in a tared, 250 mL flask, weigh accurately, and add it to 25.0 mL of a 0.5 N alcoholic potassium hydroxide. Heat the flask on a steam bath, under a suitable condenser to maintain reflux for 30 minutes, frequently rotating the contents. Then add 1 mL of phenolphthalein TS, and titrate the excess potassium hydroxide with 0.5N hydrochloric acid VS. Perform a blank determination under the same conditions. The difference between the volumes, in mL, of 0.5 N hydrochloric acid consumed in the actual test and in the blank test, multiplied by 56.1 and the exact normality of the 0.5N hydrochloric acid VS, and divided by the weight in g of the specimen taken, is the saponification value.

[0125] Depending on the source of the squalene, a saponification value of <1.4 mg/g could be obtained.

Example 3

Measurement of the Acid Value

[0126] The acidity of fats and fixed oils may be expressed as the number of mL of 0.1 N alkali required to neutralize the free acids in 10.0 g of substance. The Acid Value is the number of mg of alkali required to neutralize the free acids in 1.0 g of the substance.

[0127] Procedure (USP <401>): dissolve about 10.0 g of the substance, accurately weighed, in 50 mL of a mixture of equal volumes of alcohol and ether (which has been neutralized to phenolphthalein with 0.1 N sodium hydroxide) contained in a flask. If the test specimen does not dissolve in the cold solvent, connect the flask with a suitable condenser and warm slowly, with frequent shaking, until the specimen dissolves. Add 1 mL of phenolphthalein TS, and titrate with 0.1 N sodium hydroxide VS until the solution remains faintly pink after shaking for 30 seconds. Calculate either the Acid Value. If the volume of 0.1 N alkali VS required for the titration is less than 2 mL, a more dilute titrant may be used, or the sample size may be adjusted accordingly. The results may be expressed in terms of the volume of titrant or in terms of the equivalent volume of 0.1 N sodium hydroxide.

[0128] Depending on the source of the squalene, an acid value of 0.03 mg KOH/g could be obtained.

Example 4

Spiking Studies

[0129] A number of spiking studies were carried out to demonstrate the efficacy of the denaturing distillation.

[0130] To determine the levels of impurity removed by the denaturing distillation, a squalene composition was spiked with specified quantities of contaminants (e.g. water) as well as possible decomposition products of the squalene (e.g. formaldehyde, acetaldehyde and acetone). The spiked solutions underwent a denaturing distillation according to the present invention and were analyzed for the spiked species.

[0131] 4 kg of a squalene composition was spiked e.g. with 0.3 mL (0.2 g) of acetaldehyde (>99.5% purity), 0.3 mL (0.2 g) of acetone (>99.9% purity), 0.55 mL of 37 wt. % aqueous solution of formaldehyde (0.2 g) and 3.65 g water prior to a denaturing distillation as described in example 1. The distillate was collected in three fractions and analyzed for the spiked species alongside the spiked starting material. The results are presented in Table 1 below:

TABLE-US-00001 TABLE 1 Waste Spiked Denaturing distillation fractions Non- Starting First Second Third volatile Test/Method Material Fraction Fraction Fraction Residue Moisture 0.02 0.03 0.02 0.02 N/A Content (%) Acetone 50.9 5.0 5.7 1.1 N/A (mg/Kg or ppm) Acetaldehyde 12.4 0.9 1.9 0.9 N/A (mg/Kg or ppm) Formaldehyde 2.2 0.7 0.9 not N/A (mg/Kg or ppm) detected

[0132] The results in Table 1 show that the acetone, acetaldehyde and formaldehyde concentrations all decreased following the denaturing distillation.

[0133] It will be understood that the invention has been described by way of example only and modifications may be made whilst remaining within the scope and spirit of the invention.