The subject of the present invention is a novel process for preparing compounds of the diaminophenothiazinium type, in particular a process for purifying these compounds. It relates in particular to methylene blue, and the subject thereof is also the products resulting from this process, the degree of purity of which is higher than those known in the prior art. A subject of the present invention is also the use of these compounds for the preparation of medicaments.

Methylthioninium chloride, also known as methylene blue or 3,7-bis(dimethylamino)phenothiazin-5-ylium chloride, is an organic compound corresponding to the formula below:

This compound has for a long time been used as a redox indicator and dye, as an optical developer in biophysical systems, in nanoporous materials as a separating material, and in photoelectrochromic imaging. It is also known for its uses as an antiseptic, antiinfective, as an antidote and as a diagnostic agent. It finds uses in particular in gynecology, neonatology, cancerology, oncology, urology, ophthalmology and gastroenterology. New uses in the therapeutic field are in the process of being developed, such as the reduction of pathogenic contaminants in the blood (GB2373787), or the prevention or inhibition of an exaggerated hemodynamic reaction (WO03/082296).

Many methods of synthesis have been described for this compound, since the oldest in 1877 (German patent No. 1886). All these methods have in common the fact of using metal compounds in at least one synthetic step:

Patent DE-1886 describes a process in which oxidative coupling of N,N-dimethyl-1,4-diaminobenzene is carried out with H₂S and FeCl₃.

Fiez David et al., â€œFundamental Processes of Dye Chemistryâ€ , 1949, Interscience, 308-314 describes a process in which the thiazine ring is formed by treatment with manganese dioxide or with copper sulfate. This process also comprises a treatment with zinc chloride, with sodium dichromate and with aluminum thiosulfate.

Document WO 2005/054217 describes methylene blue derivatives and a process for the preparation thereof. The method for preparing these compounds uses phenothiazine as starting product. Now, all the known methods for preparing phenothiazine call for metal reactants of which the metal atoms chelate the phenothiazine at the end of the synthesis. The products obtained by means of this process are therefore naturally contaminated with metal residues, in addition to the usual organic contaminants such as azure B.

Document WO 2006/032879 describes a process for preparing methylene blue which comprises a reduction step with iron, an oxidation step with sodium dichromate and an oxidation step with copper sulfate.

These processes require tedious and expensive purifications to be carried out in order to reduce the impurities, in particular the metal impurities of methylene blue. Despite the subsequent purification steps, these various processes inevitably produce a methylene blue comprising many metal impurities and also organic impurities, in particular azure B, azure C and azure A.

Document WO 2006/032879 asserts that it is possible to achieve a level of metal impurities representing 10% of the maximum threshold fixed by the European Pharmacopeia, but, according to the examples, it is noted that this level is not obtained simultaneously for all metals, and the results of the purification steps are not always reproducible. A detailed analysis of the metal contents of various commercially available methylene blues is illustrated in this document.

The European Pharmacopeia was recently amended (April 2006) in terms of an increase in the tolerance thresholds for metal impurities since no producer of methylene blue was able to produce, and even less to produce in an industrial amount, a methylene blue of a quality meeting its previous requirements.

A first subject of the invention was therefore the development of a process for preparing methylene blue which provides access to a highly pure methylene blue, in particular which comprises a very low level of metal and organic impurities, which can be extrapolated to an industrial scale under satisfactory economic conditions and which is not subject to variations in quality. According to one variant, the process of the invention is a process for purifying methylene blue.

The process which has been developed applies not only to methylene blue, but also to other derivatives of diaminophenothiazinium type.

The process of the invention is a process for preparing compounds corresponding to formula (I) below:

in which each of R₁, R₂, R₃, R₄, R₅, R₆, R₇, R₈, R₉and R₁₀may be chosen, independently of the others, from the group constituted of:

- a hydrogen atom,
- saturated or unsaturated, linear, branched or cyclic C₁-C₆alkyl groups, optionally substituted with one or more functions chosen from a halogen atom, and a C₁-C₆alkoxy, C₁-C₆alkyloxycarbonyl or â€”CONH₂function,
- aryl groups optionally substituted with one or more functions chosen from: a C₁-C₄alkyl, a halogen atom, and a C₁-C₆alkoxy, C₁-C₆alkyloxycarbonyl or â€”CONH₂function,

it being understood that two Ri groups (i=1, 2 . . . 10) placed successively in figure (I) may be joined to form a ring. For example, R₁with R₅, or R₅with R₆, R₇with R₈, R₈with R₃, R₃with R₄, R₄with R₉, R₁₀with R₂, or R₂with R₁may consist of a single alkyl chain which is optionally substituted, so as to form a fourth ring,

in addition, each of R₅, R₆, R₇, R₈, R₉and R₁₀may be chosen, independently of the others, from the halogen atoms: F, Cl, Br and I,

X^âˆ’ represents an organic or inorganic anion.

The anions that can be used include, for example, the anions of inorganic acids such as, for example, hydrochloric acid, hydrobromic acid, sulfuric acid, phosphoric acid or nitric acid; the anions of organic acids such as, for example, acetic acid, trifluoroacetic acid, oxalic acid, tartaric acid, succinic acid, maleic acid, fumaric acid, gluconic acid, citric acid, malic acid, ascorbic acid or benzoic acid; they also include OH^âˆ’.

This process is characterized in that it comprises at least one step during which a compound of formula (II):

is subjected to a purification step under conditions which make it possible to separate metal compounds from the compounds of formula (II), the R₁, R₂, R₃, R₄, R₅, R₆, R₇, R₈, R₉and R₁₀groups having the same definition as in formula (I), and R representing a group chosen from:

- a phenyl or benzyl group, optionally substituted with one or more functions chosen from: a C₁-C₄alkyl, a halogen atom, a C₁-C₄haloalkyl and a nitro group,
- a linear, branched or cyclic C₁-C₈alkyl group,
- a C₁-C₈alkylamino group,
- a C₁-C₈alkoxy group,
- a phenyloxy or benzyloxy group optionally substituted on the aromatic nucleus with one or more functions chosen from: a C₁-C₄alkyl, a halogen atom, a C₁-C₄haloalkyl and a nitro group,

Z representing an atom chosen from O and S.

The purification of the compounds of formula (II) is carried out under conditions which make it possible to separate the metal compounds from the compounds of formula (II): filtration through a support capable of retaining the metal compounds, crystallization from an appropriate solvent, or any other method known to those skilled in the art.

When the purification is carried out by filtration through a support capable of retaining the metal compounds, such a support may be chosen from: a silica gel, an alumina gel (neutral, basic or acidic), an optionally modified diatomite, celite, a microporous membrane, resins grafted with metal-capturing groups and fibers grafted with metal-capturing groups, such as thiol, carboxylic acid or tertiary amine functions, or any other support having the property of retaining metals. Among the grafted fibers, mention may in particular be made of the products sold by the company Johnson Matthey under the trademark SmopexÂ®. Among the diatomites, mention may be made of the products sold by the company CECA under the trademark ClarcelÂ®.

The compound of formula (II) may be obtained starting from the compound of formula (I), by reduction of the compound of formula (I) and then by reaction of the amine function of the phenothiazinium ring with a suitable protective group R-CZ-Y in which R and Z have the same definition as above and Y represents a leaving group chosen from: a halogen atom such as F, Cl, I or Br, a C₁-C₆alkoxy group, a â€”OCOR (anhydride) group, and a hydroxyl group, optionally in the presence of an activator of the dicyclohexylcarbodiimide (DCC) type. Advantageously, R is chosen from a phenyl group and a toluoyl group.

When the compound of formula (II) is obtained starting from the compound of formula (I), the overall process is a purification of the compound of formula (I). However, the compound of formula (II) may be obtained by means of other processes which do not use the product (I) as starting product.

Some compounds of formula (II), such as benzoyl leuco methylene blue, are commercially available.

The compound represented by formula (I) may be represented by several equivalent resonant structures. By way of nonlimiting illustration, represented below are other structures which are equivalent to that of formula (I):

In formula (I) and in formula (II), R₁, R₂, R₃, R₄, R₅, R₆, R₇, R₈, R₉and R₁₀, which may be identical or different, are preferably chosen from a hydrogen atom and a C₁-C₄alkyl. Advantageously, R₅, R₈, R₉and R₁₀represent H.

More advantageously, one or more of the following requirements are met:

- X represents Cl or OH,
- R₁, R₂, R₃and R₄, which may be identical or different, are chosen from a hydrogen atom and methyl,
- R₆represents a hydrogen atom,
- R₇represents a hydrogen atom,
- Z represents O.

Advantageously, the compound of formula (I) is tetramethylthionine chloride or methylene blue.

According to another variant, the compound of formula (I) is dimethylthionine chloride or Azure A, or trimethylthionine chloride or Azure B, or monomethylthionine chloride or Azure C.

According to the invention, the process for preparing the compound of formula (I) comprises at least one step for purification of a compound of formula (II); in particular, this purification comprises at least one step for filtration of a compound of formula (II) through a support capable of retaining metal compounds, such as a silica gel, an alumina gel (neutral, basic or acidic), an optionally modified diatomite, a resin functionalized with metal-capturing agents, fibers functionalized with metal-capturing agents, celite, a microporous membrane or any other support capable of retaining metal compounds.

In greater detail, according to this variant, the compound of formula (II) is solubilized in an appropriate solvent, and a filter is prepared with the filtration support which is introduced into an appropriate receptacle, such as a glass column, a sintered glass filter or an industrial spin-dryer. The receptacle packed with the chosen filtration support is moistened, preferably with the same solvent as that in which the compound of formula (II) is dissolved.

The solution containing the compound of formula (II) is deposited on the filter, the solution which passes through the filter is recovered, and the filter is rinsed several times with a solvent which may be identical to or different than that having served to solubilize the compound of formula (II). The eluted fractions are recovered and optionally concentrated.

Among the solvents that can be used to solubilize the compounds of formula (II), mention may preferably be made of: chlorinated solvents, for instance dichloromethane or chloroform, alcohols such as isopropanol, ethanol or methanol, or acetonitrile, ethyl acetate or tetrahydrofuran, or a mixture of these solvents.

The solution of the compound of formula (I) is advantageously of a concentration ranging from 1 g/l to 10³g/l. Lower concentrations result in the use of solvent volumes that are too large, with consequences regarding the safety and the size of the material. Higher concentrations are difficult to envision owing to the solubility of the products.

It is envisioned to use approximately 0.1 to 10 kg of filtration support per kg of product to be filtered. It is advantageously envisioned to rinse the filter with 0.1 to 50 l of solvent per kg of product of formula (II) until complete elution of the product of formula (II). The process of the invention has the advantage of freeing the product of formula (II) of its metal impurities.

When it is chosen to purify the compound of formula (II) by crystallization, a solvent is advantageously chosen from: an alcohol such as ethanol and a chlorinated solvent such as methylene chloride.

Advantageously, the compound of formula (II) is produced starting from the compound of formula (I) which is reacted with a protective group R-CZ-Y in which Y is advantageously chosen from: F, Cl, Br, I, a C₁-C₆alkoxy group, an â€”OCOR (anhydride) group, and a hydroxyl group, optionally in the presence of an activator of the dicyclohexylcarbodiimide (DCC) type.

The reaction is carried out conventionally in a basic or neutral medium in water or in a mixture of water and another solvent such as, for example, acetonitrile, tetrahydrofuran, dichloromethane or any other appropriate organic solvent.

The reaction is exothermic, and cooling means which make it possible to maintain the temperature of the mixture at about ambient temperature are preferably used.

The starting product (I) is either commercially available or is prepared by known methods, such as those described in WO 2006/032879.

In general, the products of formula (I) are prepared by means of synthetic processes which call for the use of metal derivatives which are found as impurities in the products (I). This is the case of methylene blue, but also of azure A, of azure B and of azure C.

The compounds of formula (I) cannot be freed of their metal and organic impurities directly, simply and efficiently. The prior art methods call for successive recrystallizations which do not have satisfactory yields and which produce products for which the level of residual impurities is difficult to control.

In addition, the products of formula (I) have the property of chelating metals, whereas the products (II) are nonchelating. The purification thereof is therefore much more efficient that the direct purification of the compounds of formula (I).

In the various steps of the process of the invention, care is taken to use non-metal materials and reactants and solvents devoid of metal residues so as not to introduce any external contamination.

After the product of formula (II) has been purified, in particular subjected to a filtration, according to the process of the invention, a step for deprotection of the amine of the phenothiazine ring of the compound of formula (II) is advantageously carried out. This deprotection is carried out by any means known to those skilled in the art, while avoiding the introduction of metal contaminants and under conditions which prevent degradation of the compound of formula (I). Among the means that can be used for the deprotection of the R-CZ-group, mention may be made of: quinones, for instance 2,3-dichloro-5,6-dicyano-1,4-benzoquinone (DDQ), HNO₃, HClO₄, I₂, HCl, H₂SO₄, H₂O₂, and a treatment with ultraviolet radiation. A quinone is preferably used for this step, and very preferably 2,3-dichloro-5,6-dicyano-1,4-benzoquinone. Advantageously, this deprotection reaction is carried out in a solvent chosen from: ethyl acetate, acetonitrile, tetrahydrofuran and acetone. The solvent preferred for this step is acetonitrile.

Advantageous deprotection conditions make provision for the use of from 0.80 to 1.1 molar equivalents of DDQ relative to the compound (II), even more advantageously from 0.85 to 1.05 molar equivalents of DDQ relative to the compound (II), advantageously from 0.90 to 1 molar equivalent. Preferably, this deprotection is carried out at a temperature of between âˆ’40Â° C. and âˆ’5Â° C. Although not completely excluded, a lower temperature would have the drawback of lengthening the reaction times, and a higher temperature could lead to the formation of by-products.

Depending on the means of deprotection used, it may be necessary to carry out an ion exchange in order to obtain the compound of formula (I) comprising the desired X^âˆ’ anion. Preferably, this ion exchange is carried out by treatment with HCl, advantageously in ethyl acetate. Other solvents could be used, but some are capable of leading to the formation of by-products.

The conditions for deprotection of the compounds of formula (II) disclosed above are particularly advantageous in that they make it possible to achieve a compound of formula (I) without introducing metal impurities during this step or forming organic impurities. According to one variant of the invention, it may be envisioned to purify the compound of formula (II) by means other than filtration on a support capable of retaining metals, for instance by crystallization from an appropriate solvent. According to this variant, the compound of formula (II) is subsequently deprotected using any deprotection means not involving the use of metal compounds, in particular using a quinone, in particular DDQ, preferably under the conditions disclosed above.

Another subject of the invention is therefore a process for preparing compounds corresponding to formula (I) described above, characterized in that it comprises at least one step for deprotection of the R-CZ-group of the amine of the phenothiazine ring of the compound of formula (II) using deprotection means not involving the use of metal compounds.

The expression â€œdeprotection means not involving the use of metal compoundsâ€ is intended to mean the use of non-metal reactants, and of solvents not comprising metal residues (preferably <0.01 ppm), in reactors not comprising any metal parts, for instance enameled reactors.

Among the means that can be used for the deprotection of the R-CZ-group, mention may be made of: quinones, for instance 2,3-dichloro-5,6-dicyano-1,4-benzoquinone (DDQ), HNO₃, HClO₄, I₂, HCl, H₂SO₄, H₂O₂, and a treatment with ultraviolet radiation. A quinone is preferably used for this step, and very preferably 2,3-dichloro-5,6-dicyano-1,4-benzoquinone. Advantageously, the conditions for using DDQ which were described above are employed.

The method for deprotection of the compound (II) so as to give the compound (I) makes it possible to achieve a compound (I) which does not comprise any additional metal impurities compared with the product (II). In addition, these deprotection conditions prevent the formation of organic degradation products. In fact, the compounds of formula (I) have a limited stability and the use of certain treatment conditions results in degradations, for example of methylene blue to Azure A, B and C which are then difficult to separate.

The process of the invention makes it possible to have access to a compound of formula (I) which is devoid of metal contaminants and which has a high chemical purity, in a manner which is reliable, reproducible and applicable on an industrial scale. These qualities are essential for being able to provide a product of formula (I) of pharmaceutical quality.

In particular, the preparation or purification process of the invention is the only one which makes it possible to obtain, in industrial amounts and reproducibly, a methylene blue or tetramethylthionine chloride which comprises 0.02 Î¼g/g or less of cadmium per g of methylene blue. Such a product constitutes another subject of the invention.

Another subject of the invention is a methylene blue or tetramethylthionine chloride which has a degree of purity of greater than 97%, preferably greater than 98%, even better greater than 99%, measured by HPLC (high performance liquid chromatography) under the conditions of the European Pharmacopeia 5.4 (edition of April 2006) and which comprises less than 4.5 Î¼g/g of aluminum, advantageously less than 3 Î¼g/g of aluminum, even more advantageously less than 2.5 Î¼g/g of aluminum per g of methylene blue.

The process of the invention is also the only one to give access to a methylene blue or tetramethylthionine chloride which has a degree of purity of greater than 97%, preferably greater than 98%, even better greater than 99%, measured by HPLC under the conditions of the European Pharmacopeia 5.4 (edition of April 2006) and which comprises less than 0.5 Î¼g/g of tin per g of methylene blue. Such a product constitutes another subject of the invention.

The process of the invention is also the only one to give access to a methylene blue or tetramethyl-thionine chloride which has a degree of purity of greater than 97%, preferably greater than 98%, even better greater than 99%, measured by HPLC under the conditions of the European Pharmacopeia 5.4 (edition of April 2006) and which comprises less than 0.95 Î¼g/g of chromium, advantageously less than 0.90 Î¼g/g, even better less than 0.80 Î¼g/g per g of methylene blue.

The process of the invention is the only one to give access, in an industrial amount, to a methylene blue or a tetramethylthionine chloride comprising less than 3% of impurities, preferably less than 2%, even better less than 1%, measured by HPLC under the conditions of the European Pharmacopeia 5.4 (edition of April 2006) and a level of metal impurities of less than 20 Î¼g/g, advantageously less than 15 Î¼g/g, even more advantageously less than 10 Î¼g/g.

Another subject of the invention is a compound of formula (I), with the exclusion of methylene blue or tetramethylthionine chloride and comprising an overall level of metal impurities of less than 100 Î¼g/g, advantageously less than 50 Î¼g/g, in particular less than 30 Î¼g/g. Preferably, this compound meets one or more of the following requirements:

- purity greater than 97%, preferably greater than 98%, even better greater than 99%, measured by HPLC under the conditions of the European Pharmacopeia 5.4 (edition of April 2006),
- aluminum level of less than 5 Î¼g/g, advantageously less than 4 Î¼g/g, even more advantageously less than 3 Î¼g/g,
- cadmium level of less than 0.1 Î¼g/g, advantageously less than 0.05 Î¼g/g, even better less than 0.02 Î¼g/g,
- tin level of less than 0.5 Î¼g/g, advantageously less than 0.4 Î¼g/g and even more advantageously less than 0.3 Î¼g/g.

Methylene blue has been used for decades in the treatment of various infections. It is used as an antiseptic, anti-infective, as an antidote and as a diagnostic agent. Recently, its antiviral activity has been demonstrated, and it could be used in the preparation of a medicament for combating a pathological condition such as an infection, in particular a septic shock, the presence of pathogenic contaminants in the blood or the plasma, an exaggerated hemodynamic reaction, an infection with HIV, West Nile virus or the hepatitis C virus, Alzheimer's disease, malaria, breast cancer or manic depressive disorders.

Finally, it could also be used in cosmetics or for products for ophthalmic application.

For all these therapeutic uses, and in particular in the context of the prevention and treatment of Alzheimer's disease, it is necessary to have a methylene blue which has a high degree of purity and in particular which comprises very few metal impurities.

A medicament comprising a methylene blue of the invention, in a pharmaceutically acceptable carrier, constitutes another subject of the invention.

The carrier and the amounts of methylene blue to be administered are well known to those skilled in the art.

Another subject of the invention is a process for preparing a medicament comprising a compound of formula (I), characterized in that this process comprises at least one process step as described above, in particular a step for purification of the compound of formula (I) and/or a step for deprotection of the compound (II) so as to give (I).

EXPERIMENTAL SECTION

A commercially available methylene blue is purified in accordance with the process of FIG. 1.

1â€”Synthesis of Benzoyl Leuco Methylene Blue (Step A)

The following are introduced into a 120 l jacketed reactor equipped with a stirrer, and under nitrogen:

- 80 l of distilled water,
- 4.2 kg (10.7 mol) of methylene blue sold by the company Leancare Ltd under the reference CI-52015, comprising large amounts of metal impurities (Al, Fe, Cu, Cr).

The mixture is left to stir for 15 min and then 6.9 kg of sodium hydrosulfite Na₂S₂O₄in an aqueous solution at 85% are added. The color changes from blue to beige. The mixture is left to stir for a further 45 min, and then 2.69 kg of sodium hydroxide in the form of pellets are added. The reaction temperature is maintained between 18 and 20Â° C. The duration of the addition is 30 min and the resulting mixture is left to stir for a further 30 min. 7.90 l of benzoyl chloride are subsequently added dropwise. The reaction mixture turns a green-beige color. The duration of the addition is 2 h and the resulting mixture is then left to stir for 20 h.

Treatment:

After the stirring has been stopped, the mixture is allowed to separate by settling out for 15 min and the supernatant is drawn up. 80 l of water (25 volumes) are added and, after stirring and separation by settling out, the supernatant is again drawn up. 24 l of EtOH are added and, after stirring for approximately 5 min, 16 l of water are added. After having stirred for 15 min, the mixture is filtered through a receiver. This operation is repeated 3 times. After drying, 2.9 kg (yield: 66%) of benzoyl leuco methylene blue are obtained.

2â€”Purification

4.25 kg of benzoyl leuco methylene blue derived from the first step, solubilized in 30 l of CH₂Cl₂, are used. The solution is filtered through 3 parts of silica (Merck Gerudan Si60) (11.5 kg) and 0.5 kg of Fontainebleau sand, with rinsing being carried out with 30 liters of CH₂Cl₂. The CH₂Cl₂is removed by evaporation under vacuum. 6 l of ethanol are added. The mixture is left to stir in the cold and then filtered through a receiver. The resulting product is dried under vacuum. 3.4 kg of purified benzoyl leuco methylene blue are obtained (yield: 80%).

Purity: +99% HPLC

Metals: the content of metals (in Î¼g/g) is given for 3 tests in table 1.

TABLE 1TestTest 1Test 2Test 3Al0.50.50.1Cu000.4Fe000.1Zn0.90.70.5Ni0.10.10.1Cr0.30.30.03Mo0.10.10.1Mn0.0200Sn0.50.40.5Pb53.22.4Cd0.20.20.07

3â€”Debenzoylation

The following are introduced into a 100 l jacketed enameled reactor at ambient temperature:

- 45 l of acetonitrile (ACN),
- 1.6 kg of benzoyl leuco methylene blue derived from the second step, and stirred. The mixture is allowed to stir for 30 min at ambient temperature and then the temperature is decreased to âˆ’18Â° C. 950 g of DDQ solubilized in 4 l of ACN are added in one portion. The mixture is left to stir for 2 h at âˆ’18Â° C. Filtration is performed. A complex of the 3,7-bis(dimethylamino)phenothiazine with the DDQ is obtained and is used directly in the subsequent step.

4â€”Salification

The cake derived from the third step is reintroduced, in several pieces, into the jacketed enameled reactor. 4 l of EtOAc are added. The mixture is left to stir for 30 min at ambient temperature. The temperature is decreased to âˆ’18Â° C. 2.5 kg of HCl in 16 l of EtOAc (4N solution) are added. The mixture is stirred for 2 h at âˆ’18Â° C. The mixture is filtered and then the cake is reintroduced into the reactor. 30 l of EtOAc are added at âˆ’18Â° C. and the mixture is again filtered.

5â€”Neutralization

30 l of acetone are added, followed by a solution of 200 g of NaOH solubilized in 500 ml of water. The mixture is filtered. The product derived from the fourth step is introduced into the reactor with 30 l of acetone. The medium is stirred for 1 h at ambient temperature. The pH is 4.0. The medium is filtered. It is left under vacuum on the receiver.

6â€”Purification and Hydration

1.9 kg of the product from the fifth step and 30 l of a 50/50 mixture of CH₂Cl₂/EtOH are introduced into a 40 l enameled reactor under N₂, at ambient temperature. The resulting mixture is refluxed (43Â° C.). It is filtered under hot conditions with a microfiber filter (Whatman GF/D). This operation is carried out twice. The reactor is cleaned with demineralized water. The filtrate is reintroduced into the reactor. 24 liters of solvent are distilled under vacuum at 28Â° C. (3 h). The medium is put back into the reactor. 1 l of microfiltered water is added. The mixture is cooled to âˆ’18Â° C. 40 l of EtOAc are added and the resulting mixture is left stirring overnight in the cold. It is filtered. It is made into a paste with 10 l of EtOAc. 1.4 kg of purified methylene blue in the trihydrate form are obtained.

The metal impurities are analyzed and reported in table 2.

TABLE 2ElementAmount (Î¼g/g)Al1.3Cu0.5Fe1.9Zn1.7Ni0.5Cr0.8Mo0.2Mn0.08Sn0.4Pb0.1Cd0.04