WO2013052839A1 - Efficient processes for large scale preparation of phosphaplatins antitumor agents - Google Patents

Efficient processes for large scale preparation of phosphaplatins antitumor agents Download PDF

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Publication number
WO2013052839A1
WO2013052839A1 PCT/US2012/059016 US2012059016W WO2013052839A1 WO 2013052839 A1 WO2013052839 A1 WO 2013052839A1 US 2012059016 W US2012059016 W US 2012059016W WO 2013052839 A1 WO2013052839 A1 WO 2013052839A1
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Prior art keywords
phosphaplatins
reaction mixture
approximately
pyrophosphate
temperature
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PCT/US2012/059016
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English (en)
French (fr)
Inventor
Rathindra N. Bose
Shadi MOGHADDAS
Homa DEZVAREH
Original Assignee
Bose Rathindra N
Moghaddas Shadi
Dezvareh Homa
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Application filed by Bose Rathindra N, Moghaddas Shadi, Dezvareh Homa filed Critical Bose Rathindra N
Priority to MX2014004181A priority Critical patent/MX357865B/es
Priority to EP12838315.5A priority patent/EP2763537B1/en
Priority to CA2851254A priority patent/CA2851254A1/en
Priority to JP2014534791A priority patent/JP6027619B2/ja
Priority to CN201280059538.9A priority patent/CN104010508B/zh
Publication of WO2013052839A1 publication Critical patent/WO2013052839A1/en
Priority to HK15100298.2A priority patent/HK1199795A1/zh

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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07FACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F15/00Compounds containing elements of Groups 8, 9, 10 or 18 of the Periodic Table
    • C07F15/0006Compounds containing elements of Groups 8, 9, 10 or 18 of the Periodic Table compounds of the platinum group
    • C07F15/0086Platinum compounds
    • C07F15/0093Platinum compounds without a metal-carbon linkage
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61PSPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
    • A61P35/00Antineoplastic agents

Definitions

  • the invention relates to efficient synthetic and reaction management processes for the production of phosphaplatin antitumor agents that can be applied to large scale industrial production.
  • Phosphaplatms are pyrophosphate coordinated platinum(II) and platinum(IV) complexes containing inert amine ligands (R. J. Mishur, et al., Synthesis and X-ray crystallographic Characterization of Monomeric Platinum(II)- and Platinum(IV)- Pyrophosphato Complexes, Inorg. Chem., 2008, 47, 7972-7982). These compounds show excellent antitumor activities against a variety of human cancers as demonstrated by both in vitro (R. N. Bose, et al., Non-DNA Binding Platinum Anticancer Agents: Remarkable Cytotoxic Activities of Platinum- phosphato Complexes Towards Human Ovarian Cancer Cells, Proc.
  • a process for synthesizing phosphaplatins on a large scale.
  • the process eliminates the need to use large volumes of starting materials by increasing the solubility of those starting materials in a low volume reaction mixture. Furthermore, the process eliminates the need to use concentration procedures during precipitation of the desired phosphaplatins. Finally, the process significantly reduces the reaction time.
  • platinum complex is slowly added to a reaction mixture containing concentrated pyrophosphate at a pH between about 6.0 to 8.5. After stirring, the temperature and pH are lowered to precipitate our desired phosphaplatins.
  • a process for recycling un-reacted platinum complex and pyrophosphate after a first synthesis of phosphaplatins. After the first synthesis, waste product is filtered from the reaction mixture and appropriate starting materials are added to yield further phosphaplatins.
  • Figure 1 Shows the general formula (I) of phosphaplatin antitumor agents
  • Rl and R2 are amine ligands, and R3 and R4 are either amine or other monodentate ligands.
  • Figure 2 Shows examples of cis-, trans- and optical isomers of general formula
  • Figure 3 Shows a schematic representation of large scale production of phosphaplatins.
  • Figure 4 Shows a Phosphorous-31 NMR spectrum of a reaction mixture produced from an embodiment of the present invention.
  • Figure 5 Shows HPLC data for products recovered after performing a process according to an embodiment of the present invention.
  • the present invention describes new processes for making large quantities of phosphaplatins that eliminates both large volumes of starting reaction mixtures and alleviates the concentration process for precipitation, and reduces the reaction time.
  • the phosphaplatins of the present invention can be described by general formula (I) depicted in Figure 1, where Rl and R2 are amine ligands, and R3 and R4 are either amine or other monodentate ligands.
  • Rl and R2 are amine ligands
  • R3 and R4 are either amine or other monodentate ligands.
  • Rl and R2 are amine ligands
  • R3 and R4 are either amine or other monodentate ligands.
  • Of particular interest are also the many chemical variations of these phosphaplatin structures, which include cis-, trans-, racemic and enantio-pure forms where the amine ligands contain chiral centers.
  • platinum reagents of general formula PtA 2 X 2 (where A is an inert monodentate ligand or A 2 is a bidentate ligand, and X is a replaceable ligand) are added to a saturated solution of H n Na 4 _ n P 2 0 7 at a pH of between about 6.0 and 8.5, preferably about 8, and at a temperature of between about 20°C and 60°C, preferably between about 20°C and 50°C, and more preferably about 40°C.
  • the reaction is stirred for approximately 6-15 hours (depending upon the process conditions previously mentioned since reaction time is reduced at higher temperatures).
  • the pH is adjusted with concentrated HN0 3 , and temperature is adjusted to about 0-5°C.
  • the reaction mixture is left on ice for 5 minutes (depending upon conditions) to precipitate out the phosphaplatins, and then the phosphaplatins are filtered out.
  • the temperature of the filtrate is adjusted to about 40°C and then let stand for about two hours, preferably a few minutes, to precipitate out dimers and oligomers, if any.
  • the pH of the filtrate is adjusted to between 6.0 and 8.5, preferably pH 8, appropriate amounts of pyrophosphate and starting platinum reagents are added to meet starting conditions, and the above steps are then repeated to yield further phosphaplatins.
  • a concentrated solution of tetrasodium pyrophosphate (-0.4 g) is prepared in a minimum volume of water at about 40°C by adjusting the pH with concentrated nitric acid. This limiting minimum volume is equal to the solubility of pyrophosphate at about pH 8 and at about 40°C.
  • the starting platinum compound (-0.1 g) is slowly added to the pyrophosphate solution under vigorous stirring until the platinum compound is completely dissolved in the solution.
  • the reaction mixture is then maintained at about 40°C for about 12 hr.
  • this total volume of the reaction mixture in this specific example can be on the order of about 10 mL instead of much larger prior art volumes, such as 250 mL.
  • nitric acid of desired concentration are added to lower the pH to about 2.
  • concentration and volume of nitric acid depend on the desired adjustment of final volume to precipitate the compound.
  • the final volume is calculated based on the solubility of pyrophosphate moiety at about pH 2 and at about 5°C so that the excess of un-reacted pyrophosphate does not precipitate out.
  • the desired phosphaplatin complex precipitates out.
  • the total volume after the pH adjustment can be brought to about 8-10 mL.
  • This improved method and process can be applied to all phosphaplatin compounds.
  • the process can be scaled up by increasing the concentration of reactants and adjusting the volumes accordingly.
  • one kilogram of a phosphaplatin complex can be synthesized in 10 to 20 L volumes, instead of the much larger five thousand liter volumes described in the prior art.
  • Another advantage of the disclosed process is its potential to recycle the mother liquor after collecting the first crop of phosphaplatins, which contains unused starting platinum complex and pyrophosphate along with the product that was not precipitated due to its inherent solubility.
  • the temperature of the mother liquor is increased again to 40 °C and the reaction mixture is let stand for 2 hrs, preferably a few minutes.
  • Undesired products including dimeric/polymeric pyrophosphate complexes (if any), are then filtered out.
  • additional pyrophosphate is added at a concentration necessary to exceed the amount of platinum reactant for the synthesis via a kinetic controlled process. Since up to 25% of the starting pyrophosphate ligand is consumed in the reaction, 75% of the un-reacted starting pyrophosphate can be reused.
  • the first reaction is conducted using ten-fold excess of pyrophosphate ligand.
  • the starting platinum complex needs to be replenished until the mole ratio of platinum:pyrophosphate reaches 1 :4.
  • additional pyrophosphate is added to meet the kinetic criteria and to avoid the formation of dimeric product.
  • a low-volume synthesis of phosphaplatins is obtained by removing the chloride or iodide ligand from the starting platinum complex, thus creating a highly soluble di-aqua-platinum(II) compound, and reacting that compound with the pyrophosphate moiety. Under such conditions, the reaction yields several minor products in addition to the major monomeric phosphaplatin complexes.
  • Platinum (IV) complexes were also synthesized following the low-volume strategy by oxidizing the platinum (II) complexes with hydrogen peroxide at the end of the incubation time at pH 6-8 (see Example 6). Hence, the invention is equally applicable to low- volume synthesis of platinum (II) and platinum (IV) complexes.
  • the disclosed processes lead to the elimination or minimization of the formation of undesired complexes, including dimeric and oligomeric species, by slowly adding the starting platinum substrates.
  • This slow addition of starting platinum reactants ensures a condition of excess pyrophosphate environment that prevents the formation of undesired dimeric and oligomeric platinum complexes.
  • rapid precipitation in the processes disclosed herein can be accomplished by merely lowering the temperature, and does not require the need for concentrating the reaction mixture.
  • the leftover, un-reacted pyrophosphate can be reused for the next batch, which can represent up to 75% of the initial quantity. As a result, the overall cost of the process is significantly decreased.
  • the present invention is useful for the treatment of cancer patients, and other clinical applications. It can also be used in other applications where significant quantities of compounds are desired.
  • Example 1 Low-Volume Synthesis of (trans-1, 2-Cyclohexanediamine) (dihydrogen pyrophosphate) platinum (II) (trans-dach-2) or (1R, 2R-cylohexanediamine) dihydrogen-pyrophosphato-platinum(II) (RR-dach-2).
  • Sodium pyrophosphate decahydrate (0.4 g) was dissolved in 25 mL of distilled water at 60°C and the pH of the solution was adjusted to 8 with 1M HNO 3 .
  • the downfield peak at 1.93 ppm is for the monomeric pyrophosphate complex, and the peak at -5.62 is for the excess un-reacted pyrophosphate ligand.
  • the reaction time can be shortened considerably. In fact, prolonged reaction times beyond 9 hr at 60 C seemed to reduce the product peak.
  • it is possible to reduce the reaction time by increasing the temperature below the decomposition of the pyrophosphate ligand. Following the incubation period, the solution was filtered to remove any un-reacted starting material and was concentrated to 5-7 mL by rotary evaporation under vacuum at 48°C.
  • Example 2 HPLC Characterization.
  • Figure 5(a) shows a high performance liquid chromatogram of the products recovered after the above first reaction cycle recorded immediately after dissolving the product (1 mg) in 600 of 25 mM sodium bicarbonate at pH 7.5. A 50 aliquot of the sample was injected for the separation. Each separation was repeated three times.
  • the high performance liquid chromatography experiments were performed on a Waters HPLC system equipped with a dual gradient programmer and a photodiode array detector (Waters).
  • the HPLC peaks at 3.04 and 4.2 min correspond to the deligated pyrophosphate ligand and the desired monomeric complex (phosphaplatin), respectively. It is understood that the released ligand and the dimeric compound are formed due to dynamic behavior of the compound in acidic solution, which is absent at neutral pH where only the monomeric compound exists in solution.
  • Example 3 Mass Spectrometry Characterization.
  • the mass spectrometric analysis of final product and collected HPLC fractions of the final product were performed on LCQ DECA-XP (Thermo-Finnigans) mass spectrometer by direct infusion using 500 syringe (2.30 mm diameter) at a ⁇ / ⁇ flow rate (infused volume 32 ⁇ ⁇ ).
  • the mass spectrometer was set to positive ion polarity (+MS), dry temperature of 350 °C, capillary voltage 30.22 V, sheath gas flow rate at 49.36 1/min, dry gas 5.00 1/min, and tube lens voltage 15.0 V.
  • the mass to charge ratios were collected from 150 to 2000.
  • the collected fractions were also identified via mass spectrometry.
  • the peak at m/z 486.4 corresponds to the desired monomeric complex (phosphaplatin).
  • the peak at m/z 508.1 corresponds to its sodium adduct.
  • Example 4 NMR Characterization. NMR experiments were performed on a JEOL ECA-500 MHz instrument equipped auto-tune broadband n-15-P31 probe using the JEOL delta operation's software. Proton decoupled P-31 resonances were recorded at 202 MHz and their chemical shifts are reported with respect to 85% phosphoric acid at 0.0 ppm. A pulse of 4.6-microsecond with a repetition time of 0.8 s was used to generate Fourier induction decay. Typically, 52 K data points were collected within 31.72 KHz frequency domain. A line- broadening factor of 1.0 Hz was introduced before Fourier Transformation.
  • the P-31 NMR spectrum displayed a single peak at 2.02 ppm (trans-dach-2).
  • the product exhibited a single P-31 NMR resonance at 2.02 ppm.
  • the P-31 NMR spectrum displayed a single peak at 1.92 ppm (RR-dach-2).
  • Example 5 Recycling the un-reacted materials from leftover mother liquor.
  • Example 2 The mother liquor left over from the isolation of the product in Example 1 above was used for a second cycle of synthesis by replenishing 0.1 g pyrophosphate ligand along with the 0.1 g of the starting platinum complex. The exact same process explained in Example 1 was followed to isolate the product. The yield of the product again was consistent with the first crop as noted above.
  • the HPLC chromatogram, mass spectra, and P-31 NMR of the product isolated in Example 2 resemble that of the product isolated in Example 1.
  • Example 6 Low- Volume Synthesis of (irans-l,2-Cyclohexanediamine)-irans- dihydroxo(dihydrogen pyrophosphate) platinum(IV).
  • Sodium pyrophosphate decahydrate (0.4 g) was dissolved in 25 mL of distilled water at 60°C and the pH of solution was adjusted to 8 with 1M HNO 3 .
  • the solution was left at 60°C for 15 minutes and 0.1 g of the precursor compounds (i.e. cz ' s-dichloro(trans-l,2-cyclohexanediamine) platinum(II) was added in small quantities in a 30 min period.
  • the mixture was incubated at 60°C for 12 hours.

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PCT/US2012/059016 2011-10-05 2012-10-05 Efficient processes for large scale preparation of phosphaplatins antitumor agents WO2013052839A1 (en)

Priority Applications (6)

Application Number Priority Date Filing Date Title
MX2014004181A MX357865B (es) 2011-10-05 2012-10-05 Procedimientos eficientes para preparación a gran escala de agentes antitumorales de fosfaplatinos.
EP12838315.5A EP2763537B1 (en) 2011-10-05 2012-10-05 Efficient processes for large scale preparation of phosphaplatins antitumor agents
CA2851254A CA2851254A1 (en) 2011-10-05 2012-10-05 Efficient processes for large scale preparation of phophaplatins antitumor agents
JP2014534791A JP6027619B2 (ja) 2011-10-05 2012-10-05 ホスファプラチン系抗腫瘍剤の大規模調製のための効率的プロセス
CN201280059538.9A CN104010508B (zh) 2011-10-05 2012-10-05 用于大规模制备磷铂类抗肿瘤剂的高效方法
HK15100298.2A HK1199795A1 (zh) 2011-10-05 2015-01-12 大規模製備磷鉑類抗腫瘤劑的高效方法

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US201161543540P 2011-10-05 2011-10-05
US61/543,540 2011-10-05
US201213922917A 2012-10-05 2012-10-05
US13922917 2012-10-05

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US11154529B2 (en) 2016-04-06 2021-10-26 Phosplatin Therapeutics Inc. Phosphaplatin liquid formulations

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Publication number Priority date Publication date Assignee Title
US11154529B2 (en) 2016-04-06 2021-10-26 Phosplatin Therapeutics Inc. Phosphaplatin liquid formulations

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