USPatent applicationPatented

Pharmaceutical parenteral formulation containing carglumic acid

Granted 31 Aug 2021 · 3 office actions

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Abstract

The present invention relates to a pharmaceutical formulation suitable for parenteral administration containing carglumic acid and a buffering agent having a pK a from 5.5 to 9.0 at 25° C.; according to an embodiment, the buffering agent may have a pK a from 7.5 to 8.5, preferably a pK a of about 8.07, such as trometamol. The formulation may also contain at least one bulking agent, such as mannitol. The invention also includes a method for manufacturing a lyophilised sterile formulation by freeze-drying a water solution containing carglumic acid, a buffering agent having a pK a from 5.5 to 9.0 at 25° C., preferably from 7.5 to 8.5, and optionally a bulking agent to obtain a freeze-dried powder.

Description

5 parts
›The present invention relates to a pharmaceutical formulation…

The present invention relates to a pharmaceutical formulation suitable for parenteral administration containing carglumic acid and a buffering agent having a pK a from 5.5 to 9.0 at 25° C.; according to an embodiment, the buffering agent may have a pK a from 7.5 to 8.5, preferably a pK a of about 8.07, such as trometamol. The formulation may also contain at least one bulking agent, such as mannitol. The invention also includes a method for manufacturing a lyophilised sterile formulation by freeze-drying a water solution containing carglumic acid, a buffering agent having a pK a from 5.5 to 9.0 at 25° C., preferably from 7.5 to 8.5, and optionally a bulking agent to obtain a freeze-dried powder.

›BACKGROUND

Carglumic acid, whose chemical formula is reported below, is an active principle that is used for the treatment of hyperammonaemia (high blood levels of ammonia).

It is marketed in the EU under the trademark Carbaglu® in the form of tablets that must be dispersed in water and ingested immediately or administered by fast push through a syringe via a nasogastric tube, generally in case of hospitalised patients or patients who are not able to swallow.

Carglumic acid is highly hygroscopic and suffers some instability problems. For instance, unopened Carbaglu® containers should be tightly closed and stored at 2 to 8° C. After its first opening, the container must be stored at a temperature above the refrigerated temperature but below 30° C.; furthermore, any unused tablet must be discarded after one month from the first opening.

Processes for manufacturing tablets containing carglumic acid by direct compression are disclosed in EP2777696 and CN105056246.

Due to long term instability of carglumic acid once solubilised, nowadays there are not ready-to-use intravenous or, anyway, injectable sterile formulations on the market containing carglumic acid that could be used for emergency purposes.

›DESCRIPTION OF THE INVENTION

The purpose of the present invention is providing a new solid pharmaceutical formulation having a higher content of carglumic acid than Carbaglu®, an improved dissolution profile and improved stability and which, once reconstituted with water, could be administered intravenously, for instance by infusion and/or injection, particularly when a rapid therapeutic effect is needed.

Another purpose of the invention is providing a method for manufacturing said pharmaceutical formulation that does not affect the stability of the active principle itself.

Another purpose of the invention is providing a method for manufacturing said pharmaceutical formulation which may stabilise the obtained sterile dosage form when stored at 2-8° C.

Another purpose of the invention is providing a method for manufacturing said pharmaceutical formulation which may stabilise the obtained sterile dosage form when stored at 25° C.

Which technical problems have been solved by means of a pharmaceutical formulation obtained through a freeze-drying process as discussed below.

Freeze-drying, also known as lyophilisation, is a dehydration process typically used to formulate into a dosage form a perishable or unstable active principle. Freeze-drying works by freezing a water mixture of the active principle together with one or more physiologically acceptable excipients and then reducing the surrounding pressure to allow the frozen water to sublimate directly from the solid phase to the gas phase.

In order to allow an effective and industrially applicable freeze-drying process, the water mixture to be frozen must also be chemically and physically stable and, possibly, should be a clear water solution (crystallization or precipitation should be avoided). An intravenously administrable formulation must also be a clear and sterile water-based solution.

The applicant has performed several tests in order to find the most appropriate conditions for obtaining a clear solution of carglumic acid at high concentrations, which included the use of HCl 0.5 M, NaOH 0.5 M or a phosphate and dextrose buffer; such attempts however failed, since no clear and stable solution of carglumic acid could be achieved.

Nevertheless, as it shall be appreciated from the attached experimental section, trometamine (also known as TRIS), which is a buffering agent having a pK a from 7.5 and 9.0 at 25° C., surprisingly provided excellent results even at high carglumic acid concentrations. In addition, excellent results in terms of manufacturability and product stability were also surprisingly obtained using mannitol as the bulking agent.

The subject-matter of the present invention is thus represented by a pharmaceutical formulation containing carglumic acid or a pharmaceutically acceptable salt or derivative thereof and a buffering agent having a pK a from 5.5 to 9.0 at 25° C., preferably a pK a from 7.5 and 8.5 at 25° C., more preferably a pK a of about 8.07, such as trometamol.

According to an embodiment of the invention, the formulation may also contain at least one bulking agent, such as, but not limited to mannitol. Other bulking agents that may be used in the formulation of the present invention are lactose, threalose, glycine, dextrane, sucrose, glucose, fructose, sorbitol, inositol.

The pharmaceutical formulation according to the present invention may also contain one or more physiologically acceptable excipients in addition to said buffering agent and said bulking agent.

According to a further embodiment, the carglumic acid:trometamol molar ratio is from 1:1 and 1:2.5, preferably about 1:2.

According to a further embodiment, the weight ratio between carglumic acid and the bulking agent, such as mannitol, is from 25:32 and 25:50, preferably about 25:40.

According to a further embodiment, the pharmaceutical formulation of the present invention may be a powder that should be reconstituted in water before use.

According to another embodiment, each dosage form may contain from 400 to 600 mg of carglumic acid, preferably about 500 mg of carglumic acid; in case of dosage forms intended to be used by patients belonging to the paediatric population, each dosage form may contain from 25 to 200 mg of carglumic acid, preferably about 50 mg of carglumic acid.

According to a further embodiment, the pharmaceutical formulation of the present invention may be a water solution, namely either the mixture that will be subjected to freeze-drying in order to provide the above-mentioned lyophilised product or the solution to be administered intravenously once reconstituted with water; such a water solution preferably has a carglumic acid concentration higher than 2% weight/volume, preferably higher than or equal to 2.5% weight/volume.

According to the best embodiment of the invention, the formulation contains carglumic acid, trometanol and mannitol, the carglumic acid:trometamol molar ratio is from 1:1 and 1:2.5, preferably about 1:2 and the carglumic acid:mannitol weight ratio is from 25:32 and 25:50, preferably about 25:40

The subject-matter of the present invention is also represented by a method for manufacturing a powder, which comprises subjecting to freeze-drying a water solution containing carglumic acid, a buffering agent having a pK a from 7.5 and 9.0 at 25° C. (such as trometamol) and a bulking agent (such as mannitol) to obtain a freeze-dried powder.

A further subject-matter of the invention is then represented by a method for treating hyperammonaemia which comprises administering the present pharmaceutical formulation to a human in need of such a treatment.

›Definitions · 1 of 2

Unless otherwise defined, all terms of art, notations and other scientific terminology used herein are intended to have the meanings commonly understood by those of skill in the art to which this disclosure pertains. In some cases, terms with commonly understood meanings are defined herein for clarity and/or for ready reference; thus, the inclusion of such definitions herein should not be construed to represent a substantial difference over what is generally understood in the art.

In particular, the term “physiologically acceptable excipient” herein refers to a substance devoid of any pharmacological effect of its own and which does not produce adverse reactions when administered to a mammal, preferably a human. Physiologically acceptable excipients are well known in the art and are disclosed, for instance in the Handbook of Pharmaceutical Excipients, sixth edition 2009, herein incorporated by reference.

The term “Pharmaceutically acceptable salts or derivatives” herein refers to those salts or derivatives which possess the biological effectiveness and properties of the salified or derivatized compound and which and which do not produce adverse reactions when administered to a mammal, preferably a human. The pharmaceutically acceptable salts may be inorganic or organic salts; examples of pharmaceutically acceptable salts include but are not limited to: carbonate, hydrochloride, hydrobromide, sulphate, hydrogen sulphate, citrate, maleate, fumarate, trifluoroacetate, 2-naphthalenesulphonate, and para-toluenesulphonate. Further information on pharmaceutically acceptable salts can be found in Handbook of pharmaceutical salts , P. Stahl, C. Wermuth, WILEY-VCH, 127-133, 2008, herein incorporated by reference. The pharmaceutically acceptable derivatives include the esters and the ethers.

The term “bulking agent” herein refers to a physiologically acceptable excipient that increases the volume or the weight of a pharmaceutical formulation keeping its utility or functionality intact.

The term “buffering agent” herein refers to a weak acid or base used to maintain the acidity (pH) of a water solution near a chosen value after the addition of another acid or base.

The term “IV” herein means intravenous injection or intravenously injectable.

The term “ICH conditions” herein refers to the thermohygrometric conditions of storage of Drug Products that are intended for already marketed products or submissions of new Marketing Authorizations (MA), outlined by the International Council on Harmonisation (ICH) guidelines.

The terms “approximately” and “about” herein refers to the range of the experimental error, which may occur in a measurement.

The terms “comprising”, “having”, “including” and “containing” are to be construed as open-ended terms (i.e. meaning “including, but not limited to”) and are to be considered as providing support also for terms as “consist essentially of”, “consisting essentially of”, “consist of” or “consisting of”.

The terms “consist essentially of”, “consisting essentially of” are to be construed as a semi-closed terms, meaning that no other ingredients which materially affects the basic and novel characteristics of the invention are included (optional excipients may thus included).

The terms “consists of”, “consisting of” are to be construed as closed terms.

The term “paediatric population” herein refers to that part of the population from birth to eighteen years.

Experimental Section

Preliminary Solubility Trials

Preliminary solubility trials have been performed using carglumic acid solutions buffered at pH from 5.0 to 5.7 with NaOH (0.5 M) or phosphate; the test were not successful since the solutions were not stable and gave an unknown degradation product (with molecular ion at 159 [m+H]+ detected in HPLC-mass-spectrometry) not present in the solution of carglumic acid in water.

Carglumic acid solution in HCl 0.5 M also did not result stable up to 24 hours, since two known impurities were detected in concentrations above the accepted limits.

After the failure of the preliminary tests with HCl, NaOH or phosphate, two different approaches were considered to develop a freeze-dried product of carglumic acid for injection (500 mg/vial), namely:

freeze-dried formulation containing carglumic acid and bulking agent to be reconstituted with a diluent containing trometamol as buffering agent; freeze-dried formulation containing carglumic acid, trometamol and bulking agent.

Initial solubility trials were set up to understand which manufacturing and formulation approach could be more suitable.

a. Carglumic Acid in Water Solution

100 ml of solution were prepared dissolving 2.5 g of carglumic acid in water. A white suspension was obtained. The suspension was stirred for 30 minutes without obtaining a clear solution. The solution was heated at about 45° C. A complete solution was obtained at pH=1.9

Carglumic Acid in Water Solution with Trometamol

100 ml of solution were prepared dissolving 5 g of trometamol in water; 2.5 g of carglumic acid were then added. A clear solution was obtained immediately at room temperature, with pH=8.2

Both formulations were observed after 24 hours storage at RT, 5° C. and −20° C. The results are summarized in table 1.

These results demonstrated that the presence of a buffering agent having a pK a from 7.5 and 9.0 at 25° C., such as trometamol, is essential to obtain a clear and stable lyophilisable solution.

Bulking Agent Selection

The first lyophilisation trial was performed in order to select the bulking agent. Laboratory-scale batches (2000 ml) of placebo solutions containing mannitol and lactose as bulking agents were prepared. 20 ml vials were prepared and lyophilised for each formulation. The quali-quantitative compositions of the formulations are reported in table 2.

The appearance of the mannitol formulation at the end of lyophilisation cycle resulted in a white quite compact cake; the lactose formulation appearance was a dark yellow melted cake. Mannitol was thus selected as the preferred bulking agent for carglumic acid formulation development.

›Definitions · 2 of 2

Bulk Solution Formulation Screening for pH and Osmolality

Different formulations of carglumic acid (API) and trometamol (TRIS) molar ratio and bulking agent concentrations were prepared in order to measure pH and osmolality at the end of solutions' preparation. The quali-quantitative compositions of the formulations are reported in table 3.

Since the formulation must be intravenously injectable, the pH target should be in the range of 6.5-7.5 while osmolality should be in the range of 0.290-0.600 Osm/Kg when the cake is reconstituted with water for injection. In view of their osmolality and pH, formulations A, F, L, and N were selected for a lyophilisation trial. The results of the lyophilisation trial are summarized in table 4.

Formulation A gave a cake with the desired characteristics. This formulation was reconstituted with 20 ml and 25 ml of water for injection to check osmolality, obtaining a value of 0.569 osml/kg for the formulation reconstituted with 20 ml and a value of 0.444 osml/kg if reconstituted with 25 ml.

Considering the results so far obtained for each formulation, formulation A (with API:trometamol molar ratio 1:2 and mannitol as bulking agent at 4% in solution) was chosen for development.

Additional trials were performed in order to check if it were possible to decrease the osmolality value by a slight reduction of the bulking agent, but the cake appearance was not satisfactory as appeared partially melted.

An additional trial named formulation C (API/trometamol 1:1, mannitol 4%) was performed maintaining the same ratio of API/excipients by a adding the remaining amount of trometamol in the solution of reconstitution in order to optimize and reduce the length of the freeze drying process.

The process parameters and conditions applied for manufacturing formulation A and formulation C are listed in the “Methods” section.

Formulation A and formulation C were further subjected to a HPLC stability test under stressed conditions at 60° C. after 24 and 72 hours; the HPLC method is described in the “Methods” section. The results of the HPLC tests, which are summarized in table 5, showed that formulation A is more stable and presents a lower percentage of impurities than formulation C.

Based on the results of the development activities performed, formulation A was considered the most appropriate and then selected for further development.

As reported above, during the freeze drying cycle optimization, different trometamol:API molar ratios were tried so to speed up the process and to optimise the solid state properties as well. Both the carglumic acid:trometamol 1:1 ratio and the 1:2 one showed good manufacturability in terms of process. Despite of this, the further accelerated stability study described above indicates that the formulation with the ratio 1:2 has an improved stability profile if compared to the 1:1 molar ratio. Surprisingly, due to the hygroscopic character of carglumic acid, although the water content of the 1:2 formulation is higher than the one detected in the 1:1 formulation, the chemical stability is better using the 1:2 ratio. Thus, the increased trometamol amount seems to protect the API from degradation triggered by the free water still remaining after process completion.

Stability Study (Technical Batch Under ICH Conditions):

After completion of the development work, a stability study under ICH conditions was also performed to gather data about the long-term (commercial) stability of the selected formulation A. The results obtained up to 12 months with a vial of lyophilized formulation A containing 500 mg of carglumic acid stored at 2-8° C. are summarised in table 6.

The results obtained up to 12 months with a vial of lyophilized formulation A containing 500 mg of carglumic acid stored at 25° C./60% RH are summarised in table 7.

All the chemical and physical results obtained so far are fully matching the specifications required for commercial purposes at both 2-8° C. and 25° C. storage conditions.

Methods

Manufacturing Method:

The freeze drying cycle applied for the manufacturing of both formulation A and formulation C is described below.

Batch size: 2 liters batch

Bulk solution was filled into one tray of 31/39 vials with 20 ml filling volume. One tray was filled with mannitol solution to fully load the freeze-drier and the product lyophilized according to the lyophilization cycle described in table 8.

At the end of the cycle, the vials were stopped under partial nitrogen (700 mbar) within the freeze-drier chamber and sealed with flip-off caps.

HPLC Method:

Materials and Reagents

Carglumic acid Reference Standard

Deionized water, Milli Q grade or equivalent

Methanol, HPLC grade

KH 2 PO 4 , ACS Reagent

H 3 PO 4 85%, ACS Reagent

Equipment

HPLC system Agilent 1100 series or equivalent equipped with UV-VIS detector, cooled auto sampler, degassing system and column oven

Acquisition Data System

HPLC column Develosil 5 μm, RPAQUEOUS-AR C30, 250×4.6 mm or equivalent

Pre-column Gemini C18 or equivalent

Balance accurate to 0.001 mg

High precision laboratory glassware

Chromatographic Conditions

Column temperature: 25° C.

Mobile phase A: KH 2 PO 4 50 mM pH 2.0 per H 3 PO 4 85%

Mobile hase B: CH 3 OH

Flow rate: 1.0 ml/min

Injection volume: 50 μl

Autosampler temperature: 5° C.

Detection wavelength: UV at 215 nm

Elution mode: Gradient as reported in table 9

Under these conditions the retention time (Rt) of carglumic acid is about 6.6 min. Slight variations of the mobile phase composition and the flow rate may be carried out to provide a suitable elution time and to meet the requirements of the SST

›Tables in the description — 8
TABLE 1 — Room
Formulationtemperature5° C.−20° C.*
Carglumic acid in waterClearCrystallinePowder
solutionsolutionprecipitateprecipitate
Carglumic acid in waterClearClearClear
solution with trometamolsolutionsolutionsolution
*= after thawing
TABLE 2
Component1 ml1 vial (20 ml)
Formula for mannitol placebo
Mannitol40 mg800 mg
Trometamol32 mg640 mg
HCl 37%For adjustment to pH = 8
Water for injectionQs to 1 mlQs to 20 ml
Formula for lactose placebo
Lactose40 mg800 mg
Trometamol32 mg640 mg
HCl 37%For adjustment to pH = 8
Water for injectionQs to 1 mlQs to 20 ml
TABLE 3
API:Bulking
Formu-TRISBulkingAPI:TRISagentOsmolality
lationmgagent mgmolar ratio(g/100 ml)pH(Osmol/kg)
A25:32401:24%6.550.582
B25:50401:34%8.310.763
C25:16401:14%4.020.477
D25:40401:2.54%7.880.671
E25:35401:2.24%7.560.615
F25:32201:22%6.580.465
G25:32101:21%4.350.386
H25:3251:20.5%4.770.316
I25:32—1:2—4.880.289
L25:33101:2.11%6.830.399
M25:3351:2.10.5%6.840.358
N25:33—1:2.1—7.040.341
TABLE 4
API:TRISBulking agentBulk solutionCake
Formulationmolar ratio(g/100 ml)pHdensity (g/mL)Appearance
A1:24%6.701.031White compact
F1:22%6.471.024Partially
collapsed
L1:2.11%6.991.021Collapsed
N1:2.1—7.081.017Collapsed
Placebo—4%10.88—White compact
TABLE 6 — Lyophilized Drug Product Results
TestT01 Month2 Months3 Months6 Months9 Months12 Months
AppearanceFreeze-UnchangedUnchangedUnchangedUnchangedUnchangedUnchanged
dried,
white,
compact
cake
Assay mg/vial504.7500.4504.1496.6498.2510.1503.1
Assay %100.9100.1100.899.399.6102.0100.6
Related Substances % (1)(2)
Specified
Related
Substances
Glutamic acidNDNDNDNDNDNDND
RRT0.47
IMP 6 RRTNDNDNDNDNDNDND
1.20
IMP 1 RRT<0.10<0.10<0.10<0.10<0.10<0.10<0.10
1.93(0.011)(0.013)(0.008)(0.005)(0.005)(0.006)(0.007)
IMP 2 RRT<0.10<0.10<0.10<0.10<0.10<0.10<0.10
2.21(0.003)(0.004)(0.004)(0.002)(0.001)(0.001)(0.001)
IMP 5a RRT<0.10<0.10<0.10<0.10<0.10<0.10<0.10
2.34(0.015)(0.015)(0.023)(0.019)(0.019)(0.022)(0.020)
IMP 5b RRTNDNDNDNDNDNDND
2.77
Each OtherNDNDNDNDNDND
Individual
Related
Substance
Total Related<0.10<0.10<0.10<0.10<0.10<0.10<0.10
Substances
Water Content1.4%1.5%1.3%1.4%1.4%1.3%1.5%
Reconstituted solution in Sterile Water for Injections
Results
T01 Month2 Months3 Months6 Months9 Months12 Months
Test(3)(3)(3)(4)(4)(4)(4)
Reconstitution≈1 min≈1 min≈1 min≈1 min≈1 min≈1 min≈1 min
Time
Appearance ofClear,UnchangedUnchangedUnchangedUnchangedUnchangedUnchanged
Reconstitutedsolution,
Solutionfree
from
visible
particles
pH of6.36.36.36.46.36.36.3
Reconstituted
Solution
Note (1):
The results <0.10% (LOQ) are reported in brackets only for information.
Note (2):
The Total Related Substances % is the sum of the reportable (≥0.10%) specified and unspecified impurities.
Note (3):
The reconstitution volume is 20 ml
Note (4):
The reconstitution volume is 25 ml
TABLE 7 — Lyophilized Drug Product Results
TestT01 Month2 Months3 Months6 Months9 Months12 Months
AppearanceFreezeUnchangedUnchangedUnchangedUnchangedUnchangedUnchanged
dried,
white
compact
cake
Assay504.7495.8508.3498.5499.1509.1503.0
mg/vial
Assay %100.999.2101.799.799.8101.8100.6
Related Substances % (1)(2)
Specified
Related
Substances
GlutamicNDNDNDNDNDNDND
acid
RRT 0.47
IMP 6 RRTNDNDNDNDNDNDND
1.20
IMP 1 RRT<0.10<0.10<0.10<0.10<0.10<0.10<0.10
1.93(0.011)(0.012)(0.029)(0.017)(0.030)(0.050)(0.055)
IMP 2 RRT<0.10<0.10<0.10<0.10<0.10<0.10<0.10
2.21(0.003)(0.004)(0.011)(0.005)(0.007)(0.011)(0.015)
IMP 5a RRT<0.10<0.10<0.10<0.10<0.10<0.10<0.10
2.34(0.015)(0.022)(0.021)(0.021)(0.021)(0.019)(0.021)
IMP 5b RRTNDNDNDNDNDND<0.10
2.77(0.012)
Each Other
Indiv.
Relat.
Substance
UNK RRTNDNDNDND<0.10<0.10<0.10
0.63(0.050)(0.046)(0.051)
UNK RRTNDNDNDND<0.10<0.10<0.10
0.87(0.044)(0.059)(0.050)
UNK RRTNDNDNDND<0.10<0.10<0.10
1.15(0.032)(0.050)(0.082)
Total<0.10<0.10<0.10<0.10<0.10<0.10<0.10
Related
Substances
Water1.4%1.4%1.3%1.3%1.3%1.4%1.3%
Content
Reconstituted solution in Sterile Water for Injections
Results
2 Months3 Months6 Months6 Months12 Months
TestT0 (3)1 Month (3)(3)(4)(4)(4)(4)
Reconstitution≈1 min≈1 min≈1 min≈1 min≈1 min≈1 min≈1 min
Time
AppearanceClearUnchangedUnchangedUnchangedUnchangedUnchangedUnchanged
ofsolution
Reconstitutedfree from
Solutionvisible
particles
pH Recon.6.36.36.36.36.36.36.3
Sol.
Note (1):
The results <0.10% (LOQ) are reported in brackets only for information.
Note (2):
The Total Related Substances % is the sum of the reportable (≥0.10%) specified and unspecified impurities.
Note (3):
The reconstitution volume is 20 ml
Note (4):
The reconstitution volume is 25 ml
TABLE 8
Shelves TSet TimeActual time
Lyophilization CycleSet point (° C.)(hrs:min)(hrs:min)
Freezing (shelves cooling)−42° C.01:0003:00
Freezing (shelves holding)−42° C.06:0006:00
Annealing (shelves heating)−5° C.01:2001:00
Annealing (shelves holding)−5° C.04:0004:00
Freezing (shelves cooling)−40° C.00:3502:00
Freezing (shelves holding)−40° C.02:0003:00
Primary drying (shelves heating)−10° C.05:0005:00
Primary drying (shelves holding)−10° C.48:0055:00*
Secondary drying (shelves heating)+35° C.03:4504:00
Secondary drying (shelves holding)+35° C.10:0010:00
Secondary drying (shelves heating)+45° C.00:1001:00
Secondary drying (shelves holding)+45° C.10:0010:00
Secondary drying (shelves cooling)+25° C.00:2001:00
Secondary drying (shelves holding)+25° C.24:00**15:00
Chamber pressure: 200 μbar
Stoppering under partial vacuum: 700 mbar——
Total cycle duration121
*= time needed for the product to reach set up T ° C. = −23° C. to start secondary drying
**= time adjustable (min 2 hours) to unload the freeze drier during working hours
TABLE 9
MobileMobile
TIME (min)phase A %phase B %
01000
81000
149010
289010
301000
401000
Run Time 40 minutes
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IPC · International Patent Classification
Section A — Human necessities
  • A61K31/198
  • A61K9/19
  • A61K47/18
  • A61K47/26
  • A61K9/08
  • A61K9/00

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