METHODS FOR PRODUCING PHYCOTOXINS

Methods for producing phycotoxins from natural sources, wherein the phycotoxins have a definite compositional profile are described herein. In one embodiment, the phycotoxins are produced by cyanobacteria. In one embodiment, the phycotoxins are produced by continuously culturing cyanobacteria under strictly controlled conditions in order to produce a definite compositional profile. In another embodiment, organic nutrients are added to the culture that allows for higher concentrations of neosaxitoxin and saxitoxin or gonyaulatoxins 2 and 3 per weight of the algae. The phycotoxins are isolated primarily from the bacteria but can also be isolated from the culture medium. In one embodiment, the cyanobacteria produce only neosaxitoxin and saxitoxin in a ratio of about 6:1, 5:1, 4:1, or 3:1. In a preferred embodiment, the amount of saxitoxin is less than 20% by weight of the total amount of neosaxitoxin and saxitoxin produced. In another embodiment, the cyanobacteria produce only GTX2 and GTX 3.

Skip to: Description  ·  Claims  · Patent History  ·  Patent History
Description
FIELD OF THE INVENTION

This invention is in the field of methods of production of phycotoxins from natural sources, particularly methods for the continuous production of phycotoxins from cyanobacteria.

CROSS REFERENCE TO RELATED APPLICATIONS

This application claims priority under 35 U.S.C. 371 to PCT/IB2010/051188 filed Mar. 18, 2010, PCT/IB2010/051187 filed Mar. 18, 2010, Chilean Patent Application No. 722-2009 filed Mar. 24, 2009, and Chilean Patent Application No. 723-2009 filed Mar. 24, 2009, all of which are incorporated by reference.

BACKGROUND OF THE INVENTION

Phycotoxins ([phyco=seaweeds and algae] plus toxins) are a diverse group of substances produced by various aquatic plants in marine and fresh waters throughout the world. Not all aquatic plants produce toxins; and among those that do, not all, even from the same genera and species, produce toxins at all times and under all circumstances. Such toxins are associated with large fish kills and major kills of marine mammals. These toxins can also be found in shellfish.

Phycotoxins can also be produced by cyanobacteria. Five cyanobacteria are known to produce shellfish paralyzing phycotoxins, each of them having a characteristic composition with respect to the amount and type of phycotoxins produced (e.g., profile of phycotoxins):

(1) Cylindrospermopsis raciborskii, isolated from Brazil;

(2) Aphanizomenon flos-aquae, isolated from Portugal;

(3) Anabaena circinalis, isolated from Australia;

(4) Lyngbya wollei, isolated from North America; and

(5) Aphanizomenon(Aph) gracile (Lemm) Lemm (Pereira P LMECYA40).

Neosaxitoxin and saxitoxin are two specific phycotoxins produced by dinoflagellate species of the genera Alexandrium sp., Piridinium sp. and Gimnodinium sp. and cyanobacteria.

Neosaxitoxin and saxitoxin acts as specific blockers of the voltage-dependent sodium channels present in excitable cells. Due to the inhibition of sodium channels, the transmission of a nervous impulse is blocked preventing the release of neurotransmitters at the neuromotor junction, which prevents muscular contraction. Due to these physiological effects, these compounds are potentially useful in pharmacology when used as muscular activity inhibitors in pathologies associated with muscular hyperactivity, such as muscular spasms and focal dystonias, when administered locally. These compounds can also inhibit sensory pathways and generate an anesthetic effect when administered locally.

However, these compounds are not available commercially in the quantities necessary to manufacture pharmaceutical compositions. Therefore, there exists a need for improved methods to produce phycotoxins having a definite compositional profile, particularly phycotoxin mixtures containing only neosaxitoxin and saxitoxin or GTX 2 and GTX 3.

Therefore, it is an object of the invention to provide improved methods for producing phycotoxins having a definite compositional profile, particularly phycotoxin mixtures containing only neosaxitoxin and saxitoxin or GTX 2 and GTX 3.

It is another object of the invention to provide a continuous method for culturing cyanobacteria for the production of phycotoxins having a definite compositional profile, particularly phycotoxin mixtures containing only neosaxitoxin and saxitoxin or GTX 2 and GTX 3.

It is another object of the invention to produce substantially pure phycotoxins using the methods described herein.

SUMMARY OF THE INVENTION

Large scale methods for producing phycotoxins from natural sources, wherein the phycotoxins have a definite compositional profile, have been developed. The phycotoxins are produced by culturing cyanobacteria under strictly controlled conditions in order to produce a definite compositional profile. In a more particular embodiment, organic nutrients are added to the culture that allows for higher concentrations of neosaxitoxin and saxitoxin or gonyaulatoxins 2 and 3 per weight of the cyanobacteria. The phycotoxins are isolated primarily from the bacteria (e.g., cell pellet fraction) but can also be isolated from the culture medium.

In one embodiment, the cyanobacteria produce only neosaxitoxin and saxitoxin in a ratio of about 6:1, 5:1, 4:1, or 3:1. In a preferred embodiment, the amount of saxitoxin is less than 20% by weight of the total amount of neosaxitoxin and saxitoxin produced. In another embodiment, the cyanobacteria produce only GTX2 and GTX 3.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a bar graph showing the production of filaments in one culture day using MLA Medium modified with methionine, arginine and allantoic acid in continuous light conditions and the unmodified medium with light:darkness cycling.

 DETAILED DESCRIPTION OF THE INVENTION I. Definitions

“Definite compositional profile”, as used herein, refers to a mixture of particular phycotoxins. For example, a definite compositional profile can refer to a mixture containing only one, two, or three phycotoxins. In one embodiment, the mixture contains only two phycotoxins. In one embodiment, the mixture contains only neosaxitoxin (NEO) and saxitoxin (STX), wherein NEO is the major component (e.g., 60-80%). In another embodiment, the mixture contains only GTX2 and GTX3, wherein GTX 2 is the major component.

“Organic nutrients”, as used herein, refers to one or more organic compounds that, when added to the culture medium, promote formation of one or more particular phycotoxins. In one embodiment, the organic nutrients promote the formation of neosaxitoxin and saxitoxin or GTX2 and GTX3.

II. Methods for the Continuous Production of Phycotoxins

Methods for producing phycotoxins from a natural source, wherein the mixture of phycotoxins has a definite compositional profile are described herein.

A. Cyanobacteria

In one embodiment, the phycotoxins are produced from cyanobacteria, also referred to as blue-green algae. In theory any cyanobacteria can be used provides it produces, or can be induced t produce, a mixture of phycotoxins having a definite compositional profile. Suitable cyanobacteria include, but are not limited to, Cylindrospermopsis raciborskii, Aphanizomenon flos-aquae, Aphanizomenon(Aph) issatschenkoi (Usacev) Proskina-Lavrenco, Anabaena circinalis, Lyngbya wollei, Aphanizomenon gracile (Lemm) Lemm, and Aphanizomenon elenkinii var. Gracile Kashtanova.

In a preferred particular embodiment, the cyanobacterium is Aphanizomenon gracile (Lemm) Lemm and/or Aphanizomenon elenkinii var. Gracile Kashtanova. Aphanizomenon gracile (Lemm) Lemm can be collected from a variety of sources. However, in one embodiment, Aphanizomenon gracile (Lemm) Lemm was collected from Crato Lake, a reservoir in Portugal, isolated, and codified as LMECYA 41. A culture of a single cyanobacterium isolated from the sample was grown at 25° C. for 2-4 weeks until reaching a suitable development state for subsequent production.

B. Culture Medium

The cyanobacteria can be cultured in any medium that is suitable for the particular cyanobacteria to be cultured. In one embodiment, the cyanobacteria are cultured in a modified MLA medium. MLA medium is derived from ASM-1 medium. The composition of MLA medium and the method of making thereof is described in Kütz, J. Appl. Phycology, 8, 5-13 (1996). The medium contains the following ingredients: MgSO4.7H2O, NaNO3, K2HPO3, H3BO3, H2SeO3, biotin, vitamin B12, thiamine HCl, Na2EDTA, FeCl3.6H2O, NaHCO3, MnCl2.4H2O, CuSO4.5H2O, ZnSO4.7H2O, CoC12.6H2O, Na2MoO4.2H2O, and CaCl2.2H2O. Other ingredients that can be added to the medium include HCl (0.1 N), NaOH (0.1 N), KBr, Na2CO3, K2HPO4, (NH4)6Mo7O24.4H2O, Cd(NO3)2.4H2O, Ca(NO3)2.4H2O, Co(NO3)2.6H2O, Cr(NO3)3.9H2O, V2O5, MnSO4.H2O, NiSO4(NH4)2SO4.6H2O, Al2(SO4)3K2SO4.24H2O, Na Na2WO4.2H2O, KY, and combinations thereof.

Concentrations ranges for these materials are shown in the table below:

Minimal Maximal concentration concentration Compound (g/l) (g/l) MgSO4 × 7H2O 3.71E−02 6.18E−02 NaNO3 1.28E−01 2.13E−01 K2HPO4 2.61E−02 4.35E−02 H3BO3 1.85E−03 3.09E−03 H2SeO4 9.68E−04 1.61E−03 Biotin 3.75E−08 6.25E−08 Vitamin B12 3.75E−08 6.25E−08 Thiamine HCl 7.50E−05 1.25E−04 CuSO4 × 5H2O 7.50E−06 1.25E−05 ZnSO4 × 7H2O 1.65E−05 2.75E−05 CoCl2 × 6H20 7.50E−06 1.25E−05 NaMoO4 × 2H20 4.50E−06 7.50E−06 Na2EDTA 3.27E−03 5.45E−03 FeCl3 × 6H2O 1.19E−03 1.98E−03 NaHCO3 4.50E−04 7.50E−04 MnCl2 × H2O 2.70E−04 4.50E−04

1. Organic Nutrients

In one embodiment, one or more organic nutrients which promote production of one or more particular phycotoxins are added to the culture medium. In one embodiment, one or more organic nutrients are added to the culture medium to promote production of only neosaxitoxin and saxitoxin or only GTX 2 and GTX3.

In one embodiment, the organic nutrients are selected from arginine, methionine, allantoic acid, and combinations thereof. In a particular embodiment, the organic nutrients arginine, methionine, and allantoic acid are added to the culture medium. The organic nutrients are present in an effective amount to promote production of a mixture of phycotoxins having a definite compositional profile. In one embodiment, the concentration of arginine is from about 2 to about 3.5 mM, the concentration of methionine is about 1 to about 2.2 mM, and the concentration of allantoic acid is from about 0.7 to about 1.3 mM in the final composition of the culture medium. In a particular embodiment, the concentration of arginine, methionine, and allantoic acid is about 2.8 mM, 1.7 mM, and 1 mM, respectively. The use of organic nutrients, particularly arginine, to drive the production of particular compounds contrasts with the prior art. For example, it has been reported that the use of organic nutrients has little or no effect on phycotoxin production in dinoflagellates. Further, it has been reported that incorporation of arginine into a culture medium containing Cylindrospermopsis raciborskii, which produced primarily saxitoxin and GTX 2/3 and small amount of dcSTX and dcGTX2/3, caused a 48% decrease in saxitoxin production for the D9 strain of the bacteria.

Cyanobacteria produced using the culture medium described above are resistant to contamination since the culture medium contains little, if any, materials needed to for the growth of other microorganisms. The MLA medium is a natural selection medium which is specific for the culturing of cyanobacteria.

C. Culture Conditions

Once the culture medium has been prepared, the cyanobacteria are typically inoculated at a concentration of 20-40 million filaments per 3 L of culture medium. The cyanobacteria can be cultured in any suitable container, such as a 250 ml Erlenmeyer flask. The container is placed in a culture chamber maintained at a temperature of about 15° C. to about 30° C., preferably from about 20° C. to about 25° C., more preferably at about 22° C.±2° C. The inoculum is generated using a light:darkness cycles of 16:8 hours.

The resulting inoculum is transferred into reactors, which are maintained under sterile conditions. The cyanobacteria are cultured at a temperature of about 15° C. to about 30° C., preferably from about 20° C. to about 25° C., more preferably at about 22° C.±2° C. The reactors can be sealed reactors or open reactors.

Cyanobacteria can be characterized by their division cycle. Depending on the division cycle, it is possible to remove 20-40% of the total reactor volume to isolate phycotoxins, provided an equivalent amount of fresh, sterile medium is used to replace the withdrawn portion. Aphanizomenon gracile (Lemm) Lemm has a reported division cycle of 0.33/day. This means that after 3 days, the cell mass of the culture has doubled. In one embodiment, one liter of medium from each 3-L reactor is withdrawn every 1-2 days for isolation of the phycotoxins. The volume removed is replaced with one liter of fresh, sterilized medium. Filament counting can be used to determine when a portion of the medium should be removed for isolation of the phycotoxins. The continuous withdrawal and replacement of medium every 1-2 provides a system for the continuous production of the cyanobacteria which produced phycotoxins. In a preferred embodiment, the time period between harvesting is less than 4 days.

Once the portion of the medium is removed, the medium is centrifuged to produce a cell pellet containing the filament-forming cyanobacteria. The presence of filaments is indicative of a healthy culture medium and can be used to assay growth and/or presence of contaminants in the medium. Filaments can be quantified using an inverted microscope. In addition to isolating phycotoxins from the cell pellet, phycotoxins may be isolated form the supernatant (i.e., the medium remaining after centrifugation). However, under optimal conditions, the amount of toxins isolated from the supernatant is typically less than 5% of the total content obtained from the cell pellet.

Lighting conditions can also be used to increase phytotoxin production. For example, as described above, during the growth and development stage, the cyanobacteria were subject to light and darkness cycles, such as 16 hours of illumination and 8 hours of darkness. However, once the inoculum has been obtained and cultured to produce phycotoxins, the light and darkness cycles can be manipulated to maintain the cyanobacteria in the exponential growth phase. For example, the cyanobacteria can be subject to constant illumination with no darkness period. Illumination is preferably direct illumination. This is possible because cyanobacteria are photosynthetic organisms which require light and reach optimal development during the exponential growth phase. Alternative, the cyanobacteria can be exposed to different light and darkness cycles. Illumination can be done using natural light and/or artificial light, such as fluorescent tubes and/or white light emitting diodes (LEDs). Manipulation of the light and dark cycles in combination with the continuous withdrawal of medium allows one to maintain the cyanobacteria in the exponential growth phase, which maximizes phytotoxin production. Production of bacteria as described herein results in 60-125 times higher productivities.

Generally, incubation times of about 10 days were used to obtain optimal growth of the bacteria and a suitable number of filaments for processing. During the incubation time, temperature and/or lighting conditions were monitored. pH, salinity, ventilation, and agitation were not specifically monitored. However, these parameters can be varied as necessary to maintain optimal growth of the bacteria. The approximate amount of neosaxitoxin produced was 1.72×10−15 moles (femtomoles) of toxin per filament or 5.418×10−13 grams of toxin per filament.

III. Phycotoxins

The methods described herein can be used to produce mixtures of phycotoxins having a definite compositional profile. In one embodiment, the mixture contains no more than two phycotoxins. In one embodiment, the phycotoxins have the general formula shown below including the stereochemistry shown:

Specific phycotoxins are described in the table below:

Molecular Weight R1 R2 R3 R4 Toxin 242.3 H H H H doSTX 258.3 H H H H dcSTX 274.3 OH H H H dcNEO 301.3 H H H CONH2 STX 317.3 OH H H CONH2 NEO 337.3 H OSO3− H H doGTX2 337.3 H H OSO3− H doGTX3 353.3 H OSO3− H H dcGTX2 353.3 H H OSO3− H dcGTX3 369.3 OH OSO3− H H dcGTX1 369.3 OH H OSO3− H dcGTX4 380.4 H H H CONHSO3− B1 396.4 OH H H CONHSO3− B2 396.4 H OSO3− H CONH2 GTX2 396.4 H H OSO3− CONH2 GTX3 412.4 OH OSO3− H CONH2 GTX1 412.4 H OH OSO3− CONH2 GTX4 475.4 H OSO3− H CONHSO3− C1 475.4 H H OSO3− CONHSO3− C2 491.4 OH OSO3− H CONHSO3− C3 491.4 OH H OSO3− CONHSO3− C4

Other phycotoxins are described in Llewellyn, Nat. Prod. Rep., 23, 200-222 (2006).

In one embodiment, the methods described herein produce a mixture of phycotoxins containing only neosaxitoxin and saxitoxin, wherein the ratio of neosaxitoxin to saxitoxin is about 6:1, preferably about 5:1, more preferably about 4:1, most preferably about 3:1. In a particular embodiment, the mixture of phycotoxins contains only neosaxitoxin and saxitoxin, wherein the concentration of saxitoxin is less than 20% by weight of the total weight of the two compounds.

In another embodiment, the methods described herein produce a mixture of phycotoxins containing only gonyaulatoxins, such as a mixture GTX2 and GTX3. The ratio of GTX2 to GTX3 is about 9:1, preferably about 8:2, more preferably from about 7:3, most preferably from about 6:4.

The use of the modified MLA medium described herein resulted in a significant increase in the amount of specific phycotoxins produced compared to the used unmodified MLA medium. In one embodiment, the amount of neosaxitoxin produce using modified MLA medium is at least 10, 15, 20, 25, 30, 35, or more times greater than the amount produced using unmodified MLA medium.

EXAMPLES Example 1 Preparation of Culture Media

To prepare the culture medium, concentrated stock solutions of micronutrients, mineral salts and vitamins were prepared. All solutions were prepared with distilled water.

The Vitamin Stock Solution (Solution A) was prepared according to the amounts provided in Table 1:

TABLE 1 Composition of the Vitamin stock Solution (Solution A) Final Concentration Volume concentration (mg/ml) (ml) (mg/ml) Biotin 0.1 0.05 0.00005 Vitamin B12 0.1 0.05 0.00005 Thiamine HCl 0.1

1 mg of biotin was dissolved in 10 ml of distilled water. Similarly, 1 mg of vitamin B 12 was dissolved in 10 ml of distilled water. 0.05 ml of each of these two solutions was mixed with 10 mg of thiamine HCl and distilled water to a final volume of 100 ml.

The Micronutrient Stock Solution (Solution B) was prepared from primary solutions of CuSO4.5H2O (1 g/l), ZnSO4.7H2O (2.2 g/l), CoCl2.6H20 (1 g/l), NaMoO4.2H20 (0.6 g/l).

10 ml of each primary solution was added to 800 ml of the solution described in Table 2.

TABLE 2 Micronutrient Stock Solution Concentration Amount (g) (g/l) in 800 ml Na2EDTA 5.45 4.36 FeCl3•6H2O 1.975 1.58 NaHCO3 0.75 0.6 MnCl2•H2O 0.45 0.36

The solution was diluted to a final volume of 1 L with distilled water.

250 ml of a concentrated 40× stock of MLA medium was prepared by adding the volumes indicated for each component in Table 3 to 130 ml of distilled water.

TABLE 3 MLA medium composition Volume Component Solution (g/l) (ml) MgSO4•7H2O 49.4 10 NaNO3 85 20 K2HPO4 6.96 50 H3BO3 2.47 10 H2SeO4 1.29 10 Vitamin Stock (solution A) 10 Micronutrient Stock 10 (solution B)

For media to be sterilized by filtration through a 0.22 micron membrane, 1 L of MLA culture medium was prepared by combining the following volumes in Table 4.

TABLE 4 Culture medium to be sterilized by filtration Volume (g/l) (ml) Distilled water 964 40 × MLA Stock 25 NaHCO3 16.9 10 CaCl2•2H2O 29.4 1

For media to be sterilized using an autoclave (e.g., 121° C. for 15 minutes), the media are prepared by combining the volumes shown in Table 5 and adjusting the pH to 7.5-8 with a suitable acid, such as hydrochloric acid (e.g., HCl).

TABLE 5 Culture medium to be sterilized by autoclave Volume (g/l) (ml) Distilled water 973 40 × MLA Stock 25 NaHCO3 16.9 1 CaCl2•2H2O 29.4 1

The final concentrations of the various components are shown in Table 6.

TABLE 6 Culture medium Concentration in the ready- Compound to-use medium (g/l) MgSO4•7H2O 4.94E−02 NaNO3 1.70E−01 K2HPO4 3.48E−02 H3BO3 2.47E−03 H2SeO4 1.29E−03 Biotin 5.00E−08 Vitamin B12 5.00E−08 Thiamine HCl 1.00E−04 CuSO4•5H2O 1.00E−05 ZnSO4•7H2O 2.20E−05 CoCl2•6H20 1.00E−05 NaMoO4•2H20 6.00E−06 Na2EDTA 4.36E−03 FeCl3•6H2O 1.58E−03 NaHCO3 6.00E−04 MnCl2•H2O 3.60E−04

NaHCO3 and CaCl2.2H2O are added as needed, since their concentration depends on the type of sterilization (filtration or autoclaving) used for the medium.

All the solutions can be stored refrigerated for up to 1 month.

Prior to culturing the bacteria, arginine, methionine and allantoic acid were added at final concentrations of 2.8 mM arginine, 1.7 mM methionine and 1 mM allantoic acid.

Example 2 Culture of Aphanizomenon (Aph) gracile (Lemm) Lemm

Each reactor containing 3 liters of the culture medium described in Example 1 was inoculated with 35 million filaments of Aphanizomenon (Aph) gracile (Lemm) Lemm. The reactors were maintained at a temperature of 22° C.±2° C., with permanent illumination from fluorescent tubes. Once the culture reached the exponential phase, one-third of the total reactor volume was collected (1 liter) and replaced with 1 liter of fresh medium. The culture had a doubling time of 0.33 times per day.

The removed culture medium containing cyanobacteria was centrifuged at 10,000 g for 20 minutes.

The yields obtained are expressed as a function of the number of filaments, since the presence of filaments (association of individual cells) is an indicator of the quality of the culture and of the permanent reproduction and development of the cells. A filament-rich culture is a “healthy” culture and is in permanent development. The cell pellet is a pellet formed of the filaments. The number of filaments for various batches is shown in Table 7.

TABLE 7 Number of Aphanizomenon (Aph) gracile (Lemm) filaments per milliliter of culture as a function of time Filaments of cyanobacteria in the Batch Culture day pellet per ml Collected volume (ml) 1 Day 1 590,000 1000 2 Day 2 598,000 1000 3 Day 3 630,000 1000 4 Day 4 596,000 1000 5 Day 5 626,000 1000 6 Day 6 788,000 1000 7 Day 7 534,000 1000 8 Day 8 756,000 1000 9 Day 9 754,000 1000 10 Day 10 614,000 1000 11 Day 11 622,000 1000 12 Day 12 608,000 1000 13 Day 13 770,800 1000

The cell pellet of each batch is the volume obtained from one liter of culture harvested each day from the reactor. This can also be carried out every other day, to achieve a larger number of filaments. Under the culture conditions used, it is preferable to carry out the harvest no more than 4 days apart, to avoid culture deterioration and phytotoxin production decrease.

Example 3 Comparison of the Culture with Simple (Unmodified) MLA Medium and the Modified MLA Medium of the Present Invention

FIG. 1 shows the difference between a culture of Aphanizomenon gracile in the simple (unmodified) MLA medium and a culture of Aphanizomenon gracile with the modified MLA culture medium containing the additives to promote production of neosaxitoxin and saxitoxin. The addition of arginine, methionine, and allantoic acid resulted in a significant increase in filament production which results in an increase in phycotoxin production.

Table 8 shows the concentration of the different phycotoxins in the supernatant and the yield of cyanobacterial filaments. Table 8 also indicates the concentration of filaments per ml of culture medium.

TABLE 8 Concentration of the different phycotoxins in the supernatant and the yield of cyanobacterial filaments Concentration of Concentration phycotoxin per in the supernatant filament neoSTX STX neoSTX STX neoSTX STX Cyano. mM mM μg/ml μg/ml pg/fil. pg/fil fil./ml* 8.98 3.5 2.83 1.05 2.42 0.9 1,170,000,00 13.66 4.91 4.3 1.47 3.44 1.18 1,250,000,00 3.42 1.03 1.08 0.31 1.71 0.49 630,000,00 17.82 4.78 5.61 1.43 9.42 2.41 596,000,00 17.81 4.02 5.61 1.21 13.17 2.83 426,000,00 7.66 1.47 2.41 0.44 4.94 0.91 488,000,00 10.87 2.19 3.42 0.66 10.25 1.97 334,000,00 10.52 2.07 3.31 0.62 4.38 0.82 756,000,00 10.77 1.96 3.39 0.59 7.47 1.3 454,000,00 17.24 2.99 5.43 0.9 13.12 2.16 414,000,00 5.31 0.41 1.67 0.12 5.19 0.38 322,000,00 12.26 2.17 3.86 0.65 9.47 1.59 408,000,00 9.84 1.94 3.1 0.58 17.42 3.27 178,000,00 STX: saxitoxin neoSTX: neosaxitoxin Cyano. fil.: cyanobacterial filaments *Cyanobacterial filaments are associations of 20 to 100 cyanobacterial cells. These cyanobacteria form filaments in solution and those filaments are counted using the magnification of an inverted microscope.

Table 9 shows different phycotoxin production batches. It is shown that the mean yield of phycotoxin per filament is much higher when using the modified MLA medium with the growth conditions described herein in comparison with the culture in simple (unmodified) MLA medium as described in the prior art. For example, the amount of neosaxitoxin produced using the modified MLA medium is more than 25 times the amount produced using non-modified MLA medium.

TABLE 9 Production of neosaxitoxin and saxitoxin as a function of the number of filaments in the modified MLA medium and unmodified MLA medium Production of phycotoxins in Production of phycotoxins in modified MLA medium and simple MLA medium with permanent illumination light: darkness cycling neoSTX STX neoSTX STX pg/fil. pg/fil pg/fil. pg/fil 2.42 0.9 0.09 0.03 3.44 1.18 0.13 0.04 1.71 0.49 0.06 0.02 9.42 2.41 0.35 0.09 13.17 2.83 0.49 0.1 4.94 0.91 0.18 0.03 10.25 1.97 0.38 0.07 4.38 0.82 0.16 0.03 7.47 1.3 0.28 0.05 13.12 2.16 0.48 0.08 5.19 0.38 0.19 0.01 9.47 1.59 0.35 0.06 17.42 3.27 0.65 0.12 Average 7.88 1.55 0.29 0.06

The yields obtained in these experiments show a surprising and unexpected increase in the production of phycotoxins (e.g., neosaxitoxin and saxitoxin) per cyanobacterial filament cultured in the modified MLA medium (Table 8), when compared to the production of the cyanobacterial filaments cultured with unmodified MLA in small culture flasks, with no continuous aeration, and with light (day):darkness (night) cycles (Table 9).

In the examples described herein, cyanobacteria are always in the logarithmic growth phase, with permanent illumination 24 hours a day and with permanent collection of cyanobacteria, inducing permanent growth by adding new nutrients in a volume that is equivalent to the volume collected in each harvest.

Unless defined otherwise, all technical and scientific terms used herein have the same meanings as commonly understood by one of skill in the art to which the disclosed invention belongs. Publications cited herein and the materials for which they are cited are specifically incorporated by reference.

Those skilled in the art will recognize, or be able to ascertain using no more than routine experimentation, many equivalents to the specific embodiments of the invention described herein. Such equivalents are intended to be encompassed by the following claims.

Claims

1. A method for the continuous production of phycotoxins from cyanobacteria, the method comprising

inoculating a culture medium with the cyanobacteria, wherein the culture medium comprises one or more organic nutrients that stimulate production of saxitoxin, neosaxitoxin, gonyaulatoxin 2, gonyaulatoxin 3, and combinations thereof in the cyanobacteria; and
harvesting the cyanobacteria to isolate the phycotoxins.

2. The method of claim 1, wherein the cyanobacteria is selected from the group consisting of Cylindrospermopsis raciborskii; Anphanizomenon flos-aquae; Aphanizomenon (APh) issatschenkoi (usaceb) Proskina-Lavrenco; Aphanizomenon gracile (Lemm) Lemm; Anabaena circinalis; Lyngbya wollei; and combinations thereof.

3. The method of claim 2, wherein the cyanobacteria is Aphanizomenon gracile (Lemm) Lemm.

4. The method of claim 1, wherein the organic nutrients are selected from the group consisting of arginine, methionine, allantoic acid, and combinations thereof.

5. The method of claim 4, wherein the micronutrients comprise arginine, methionine, and allantoic acid.

6. The method of claim 1, wherein the cyanobacteria produce only neosaxitoxin and saxitoxin.

7. The method of claim 6, wherein the ratio of neosaxitoxin to saxitoxin is approximately 6:1.

8. The method of claim 6, wherein the ratio of neosaxitoxin to saxitoxin is approximately 5:1.

9. The method of claim 6, wherein the ratio of neosaxitoxin to saxitoxin is approximately 4:1.

10. The method of claim 6, wherein the ratio of neosaxitoxin to saxitoxin is approximately 3:1.

11. The method of claim 1, wherein the cyanobacteria produce only gonyaulatoxin 2 and gonyaulatoxin 3.

12. Neosaxitoxin produced by the method of claim 1.

13. The neosaxitoxin of claim 12, wherein the structure is

14. Saxitoxin produced by the method of claim 1.

15. The saxitoxin of claim 14, wherein the structure is

Patent History
Publication number: 20150099879
Type: Application
Filed: Dec 15, 2014
Publication Date: Apr 9, 2015
Inventor: Marcelo Santiago Logas Gonzalez (Santiago)
Application Number: 14/570,373