U.S. patent application number 09/330588 was filed with the patent office on 2001-07-12 for novel formulations comprising lipid-regulating agents.
Invention is credited to LEE, DENNIS, LIU, RONG (RON), PAN, QINGHAI.
Application Number | 20010007669 09/330588 |
Document ID | / |
Family ID | 23290425 |
Filed Date | 2001-07-12 |
United States Patent
Application |
20010007669 |
Kind Code |
A1 |
LIU, RONG (RON) ; et
al. |
July 12, 2001 |
NOVEL FORMULATIONS COMPRISING LIPID-REGULATING AGENTS
Abstract
The present invention is directed to a process for preparing a
formulation comprising a lipid-regulating agent dissolved in a
supercritical fluid, spraying the solution through a nozzle to form
small particles of the lipid-regulating agent, forming a suspension
of the particles of said lipid-regulating agent in a liquid, and
collecting the particles.
Inventors: |
LIU, RONG (RON); (GURNEE,
IL) ; PAN, QINGHAI; (LAKE BLUFF, IL) ; LEE,
DENNIS; (HIGHLAND PARK, IL) |
Correspondence
Address: |
ABBOTT LABORATORIES
DEPT. 377 - AP6D-2
100 ABBOTT PARK ROAD
ABBOTT PARK
IL
60064-6050
US
|
Family ID: |
23290425 |
Appl. No.: |
09/330588 |
Filed: |
June 11, 1999 |
Current U.S.
Class: |
424/400 |
Current CPC
Class: |
A61K 9/1694 20130101;
Y10S 977/906 20130101; A61K 31/216 20130101; A61K 9/1688 20130101;
A61K 31/22 20130101 |
Class at
Publication: |
424/400 |
International
Class: |
A61K 009/00 |
Claims
1. A process for preparing a formulation comprising a
lipid-regulating agent dissolved in a supercritical fluid, spraying
the solution through a nozzle to form small particles of the
lipid-regulating agent, forming a suspension of the particles of
said lipid-regulating agent in a liquid, and collecting the
particles.
2. A process of claim 1 wherein the supercritical fluid is carbon
dioxide.
3. A process of claim 1 wherein the particle size of the
lipid-regulating agent is less than 5000 nm.
3. A process of claim 1 wherein the lipid-regulating agent is a
fibrate.
4. A process of claim 3 wherein the fibrate is fenofibrate.
5. A process of claim 1 wherein the lipid-regulating agent is a
statin.
10. A delivery system comprising a composition prepared by the
process of claim 1.
11. A delivery system of claim 1 wherein said delivery system is a
capsule.
12. A method of treating hyperlipidemia comprising the
administration of a composition prepared by the process of claim 1
to a patient.
13. A method of treating hyperlipidemia comprising the
administration of a composition prepared by the process of claim 4
to a patient.
14. A method of treating hyperlipidemia comprising the
administration of a composition prepared by the process of claim 11
to a patient.
Description
FIELD OF THE INVENTION
[0001] The present invention relates to novel formulations
comprising lipid-regulating agents.
BACKGROUND OF THE INVENTION
[0002] 2-[4-(4-chlorobenzoyl)phenoxy]-2-methyl-propanoic acid,
1-methylethylester, also known as fenofibrate, is representative of
a broad class of compounds having pharmaceutical utility as lipid
regulating agents. More specifically, this compound is part of a
lipid-regulating agent class of compounds commonly known as
fibrates, and is disclosed in U.S. Pat. No. 4,058,552.
[0003] Fenofibrate has been prepared in several different
formulations, c.f., U.S. Pat. No. 4,800,079 and U.S. Pat. No.
4,895,726. U.S. Pat. No. 4,895,726 discloses a co-micronized
formulation of fenofibrate and a solid surfactant.
[0004] U.S. Pat. No. 4,961,890 discloses a process for preparing a
controlled release formulation containing fenofibrate in an
intermediate layer in the form of crystalline microparticles
included within pores of an inert matrix. The formulation is
prepared by a process involving the sequential steps of dampening
said inert core with a solution based on said binder, then
projecting said fenofibrate microparticles in a single layer onto
said dampened core, and thereafter drying, before said solution
based on said binder dissolves said fenofibrate microparticles, and
repeating said three steps in sequence until said intermediate
layer is formed.
[0005] European Patent Application No. EP0793958A2 discloses a
process for producing a fenofibrate solid dosage form utilizing
fenofibrate, a surface active agent and polyvinyl pyrrolidone in
which the fenofibrate particles are mixed with a polyvinyl
pyrrolidone solution. The thus obtained mixture is granulated with
an aqueous solution of one or more surface active agents, and the
granulate thus produced is dried.
[0006] PCT Publication No. WO 82/01649 discloses a fenofibrate
formulation having granules that are comprised of a neutral core
that is a mixture of saccharose and starch. The neutral core is
covered with a first layer of fenofibrate, admixed with an
excipient and with a second microporous outer layer of an edible
polymer.
[0007] U.S. Pat. No. 5,645,856 describes the use of a carrier for
hydrophobic drugs, including fenofibrate, and pharmaceutical
compositions based thereon. The carrier comprises a digestible oil
and a pharmaceutically-acceptable surfactant component for
dispersing the oil in vivo upon administration of the carrier,
which comprises a hydrophilic surfactant, said surfactant component
being such as not to substantially inhibit the in vivo lipolysis of
the digestible oil.
[0008] Sheu, M. T., et al, Int. J. Pharm. 103 (1994) 137-146,
reported that a dispersion of fenofibrate in PVP still maintains
the same crystalline form of the drug itself.
[0009] Palmieri, G. F., et al, Pharma Sciences 6 (1996) 188-194,
reported that a dispersion of crystalline fenofibrate could be
prepared in PEG 4000. However, dissolution of the composition was
poor.
[0010] Gemfibrozil is another member of the fibrate class of
lipid-regulating agents. U.S. Pat. No. 4,927,639 discloses a
disintegratable formulation of gemfibrozil providing both immediate
and sustained release, comprising a tablet compressed from a
mixture of a first and second granulation, and a disintegration
excipient operable to effect partial or complete disintegration in
the stomach. The first granulation comprises finely divided
particles of pure gemfibrozil granulated with at least one
cellulose derivative, and the second granulation comprises finely
divided particles of pure gemfibrozil granulated with a
pharmaceutically-acceptable water soluble or insoluble polymer
which are then uniformly coated with a pharmaceutically-acceptabl-
e (meth)acylate copolymer prior to admixture with the first
granulation. The first and second granulations are present in the
final composition in a ratio of from about 10:1 to about 1:10.
[0011] U.S. Pat. No. 4,925,676 discloses a disintegratable
gemfibrozil tablet providing both immediate and enteric release,
which is compressed from a mixture of a first granulation of
gemfibrozil with at least one acid-disintegratable binder, and a
second granulation formed from the first granulation, but
regranulated or coated with an alkali-disintegratable formulation
of at least one substantially alkali-soluble and substantially
acid-insoluble polymer.
[0012] Another class of lipid-regulating agents are commonly known
as statins, of which pravastatin and atorvastatin are members. U.S.
Pat. Nos. 5,030,447 and 5,180,589 describe stable pharmaceutical
compositions, which when dispersed in water have a pH of at least
9, and include a medicament which is sensitive to a low pH
environment, such as prevastatin, one or more fillers such as
lactose and/or microcrystalline cellulose, one or more binders,
such as microcrystalline cellulose (dry binder) or
polyvinylpyrrolidone (wet binder), one or more disintegrating
agents such as croscarmellose sodium, one or more lubricants such
as magnesium stearate and one or more basifying agents such as
magnesium oxide.
[0013] It is an object of the present invention to provide
formulations of lipid-regulating agents having enhanced
bioavailability when compared to commercially available
formulations.
SUMMARY OF THE INVENTION
[0014] The present invention is directed to a process for preparing
formulations comprising lipid-regulating agents with enhanced
dissolution and absorption characteristics. More particularly, the
process comprises dissolving the lipid-regulating agent in a
supercritical fluid, spraying the supercritical fluid through a
nozzle to form small particles comprising said lipid-regulating
agent, forming a suspension of said lipid-regulating agent in a
liquid in which the particles are insoluble and collecting said
particles. The particles then be spray dried or lyophilized. They
may optionally also be cooled with pharmaceutically-acceptable
excipients, such as, for example, surfactants, polymers, lipids or
other materials.
[0015] The resulting formulation results in an increase in drug
solubility and oral bioavailability, and an improved dissolution
rate.
[0016] The formulation may be administered directly, diluted into
an appropriate vehicle for administration, encapsulated into hard
gelatin capsules for administration, or administered by other means
obvious to those skilled in the art.
BRIEF DESCRIPTION OF THE DRAWINGS
[0017] FIG. 1 is a graph showing the dissolution characteristics of
fenofibrate nanocrystals or nanoparticles produced by the process
of the present invention and reference compositions.
DETAILED DESCRIPTION OF THE INVENTION
[0018] The bulk lipid-regulating agent may be prepared by any
available method, as for example the compound fenofibrate may be
prepared by the procedure disclosed in U.S. Pat. No. 4,058,552, or
the procedure disclosed in U.S. Pat. No. 4,739,101, both herein
incorporated by reference.
[0019] As used herein, the term "supercritical fluid" means a
substance, such as for example carbon dioxide, which becomes a
liquid state when its pressure and temperature are greater than its
critical pressure and critical temperature, respectively.
[0020] As used herein, the term "nozzle" means a device through
which a liquid is forced out under high pressure to become very
fine (micronized) droplets.
[0021] The composition comprising the lipid-regulating agent may be
prepared by using a SFX 220 supercritical particle generator, which
consists of an ISCO extractor, controller, one or more D series
syringe pumps, and a temperature controlled variable restrictor.
The extractor incorporated six motor actuated valves that are
controlled by the controller. The controller executes the process
program and displays real-time data. The fluid source for the
extractor is supplied by a unique syringe-type pump that maintains
a constant process pressure in the extractor and up to the
restrictor.
[0022] The lipid-regulating agent nanocrystals or nanoparticles are
prepared by a process in which the drug is solubilized in the
extractor at 50.degree. C. and 2000 psi with carbon dioxide for a
period of one to five minutes. The solutions are then released
through a temperature controlled restrictor. Drug particles form
when the carbon dioxide is vaporized. Particle size can be
controlled by varying the concentration of the solution and/or by
the process flow rate.
[0023] Sub-micron particle size can be achieved either by using a
very dilute solution or by adding additional liquid carbon dioxide
through a second syringe pump to the outlet and before the
restrictor.
[0024] Surface coating meterials, such as phospholipids,
surfactants, and/or polymers, may also be added either before or
after particle formation to change properties of the surface of the
sub-micron particles, as desired. The materials can be coated on
the surface of these tiny particles in the process to become coated
nanocrystals or nanoparticles, which can prevent from the growth or
aggregation of particles. Representative particle size stabilizers
include, for example, sodium lauryl sulfate (SLS) or sodium
dodecylsufate (SDS) (BDH Laboratory Supplies), gelatin (Sigma),
casein (Aldrich), lecithin (Sigma) and any phospholipids, gum
acacia (TIC Gums), cholesterol (Aldrich), tragacanth (Sigma),
stearic acid (Sigma), benzalkonium chloride (Sigma), calcium
sterarate (Penta Manufacturing Company), glyceryl monostearate
(ABITEC), cetostearyl alcohol (Croda), cetomarogol emulsifying wax
(Croda), sorbitan esters (Uniqema), polyethylene glycols (Union
Carbide), polyoxyethylene stearates (Uniqema), colloidal silicon
dioxide (Cabot), phosphates (Sigma), caboxylmethylcellulose calcium
(Kraft), carboxymethylcellulose sodium (Aldrich), methyl cellulose
(Sigma), hydroxypropylmethycellulose phthaltate (Sigma),
Microcrystalline cellulose (FMC), magnesium aluminum silicate (R.
T. Vanderbilt), triethanolamine (Sigma), polyvinyl alcohol
(Aldrich), PEG-2 stearate (Goldschmidt Chemical), PEG-stearate and
gylcol stearate (Uniqema), PEG-6-32 stearate (Gattefosse), Gelucire
53/10 (Gattefosse), PEG-6 stearate (Protameen Chemicals), PEG-6
stearate and glyceryl stearate and ceteth-20 (Gattefosse), glyceryl
stearate and PEG-75 stearate (Goldschmidt Chemical), hydrogenated
palm oil/palm kernel oil PEG-6 complex (California Oils
Corporation), glyceryl stearate and PEG-100 stearate (Uniqema),
isoceteth-20 (Uniqema), PEG-6 sorbitan beeswax (Nikko Chemical),
PEG 20 sorbitan beeswax (Nikko Chemical), Ceteth-10 (Protameen
Chemicals), Cetech-20(Protameen Chemicals), Ceteareth-20 (Protameen
Chemicals), Stearate-2 (Protameen Chemicals), Steareth-10
(Protameen Chemicals), Stearate-20 (Protameen Chemicals),
stearate-100 (Uniqema), Pluronic F127 (BASF) and
polyvinylpyrrolidone (BASF).
[0025] Other optional ingredients which may be included in the
compositions of the present invention are those which are
conventionally used in oil-based drug delivery systems, e.g.
antioxidants such as tocopherol, tocopherol acetate, ascorbyl
palmitate; ascorbic acid, butylhydroxytoluene, butylhydroxyanisole
and propyl gallate; pH stabilisers such as citric acid, tartaric
acid, fumaric acid, acetic acid, glycine, arginine, lysine and
potassium hydrogen phosphate; thickeners/suspending agents such as
hydrogenated vegetable oils, beeswax, colloidal silicon diocide,
gums, celluloses, silicates, bentonite; flavouring agents such as
cherry, lemon and aniseed flavours; sweeteners such as aspartame,
saccharin and cyclamates; etc.
[0026] The particles comprising the lipid-regulating agent produced
by the process of the present invention are preferable less than
5000 nm in diameter, more preferably less than 1000 nm in
diameter.
[0027] The delivery system of the present invention results in an
increased dissolution rate which improves bioavailability of the
lipid-regulating agent.
[0028] The resulting composition comprising the lipid-regulating
agent may be dosed directly for oral administration, diluted into
an appropriate vehicle for oral administration, filled into hard
gelatin capsules for oral administration, or delivered by some
other means obvious to those skilled in the art. The said
composition may be used to improve the dissolution rate, and the
oral bioavailability, and increase the half-life of said
lipid-regulating agent.
[0029] The invention will be understood more clearly from the
following non-limiting representative examples:
EXAMPLE 1
[0030] Fenofibrate (100 mg) was added into a 10 mL cartridge in a
critical fluid extractor. The cartridge was processed with 50 mL
liquid carbon dioxide, which was heated and pressurized above its
critical temperature and pressure. Fenofibrate was dissolved/finely
dispersed in the supercritical carbon dioxide fluid. The outlet
restrictor was adjusted to deliver the desire flow rate. The
supercritical fluid containing solubilized/finely dispersed
fenofibrate was filtered through a submicron pore sized filter, and
then sprayed out through a nozzle. Liquid carbon dioxide became gas
and submicron particles or nanoparticles dropped out. The particle
size was determined using a API Particle Sizer. The particles may
optionally be filled into capsules in a quantity appropriate to
obtain the desired dose.
[0031] The equipment used in the experiment included:
[0032] 1. Isco Controller, Model SFX 200
[0033] 2. Isco Supercrtical Fluid Extractor, Model SFX 220
[0034] 3. Isco Syringe pump, Model 260D
[0035] 4. Isco Restrictor Temperature Controller
[0036] 5. Lauda Chiller, Model K2/RD
[0037] 6. Mettler Balcance, Model AE 100
[0038] 7. API Particle Sizer, Model Aerosizer LD
[0039] The process parameters were:
1 Static Parameters: 1. Time 1 minutes (range 1 to 10 minutes)
(based on solubility) 2. Pressure 2000 psi 3. Temperature
50.degree. C. Dynamic Parameters: 1. Pressure 2000 psi 2.
Temperature 50.degree. C. 3. Time 10 minutes 4. Volume 50 mL 5.
Flow rate 10 mL/min (range 1 to 20 mL/min)
EXAMPLE 2
[0040] Pravastatin 100 mg
[0041] Carbon dioxide (Liquid) 50 mL
[0042] Applying the general procedure of Example 1 one may obtain
Pravastatin nanoparticles.
EXAMPLE 3
[0043] The method used in Example 1 to generate fenofibrate
nanoparticles was limited to a small scale because of equipment
capability.
[0044] The following formulations were used to generate larger
quantity of fenonfibrate nanocrystals/nanoparticles using a milling
process.
[0045] Formulations:
2 Formulation 1: Fenofibrate 10 g Sodium Lauryl Sulfate 1 g
Formulation 2: Fenofibrate 10 g Pluronic F127 1 g Formulation 3:
Fenofibrate 10 g Gelucire 53/10 1 g
[0046] These three formulations were prepared using three different
particle size stabilizers--Sodium Lauryl Sulfate, Pluronic F127 and
Gelucire 53/10. Each formulation was milled in water to the desire
particle size and each suspension was filtered through a 1 micron
filter to remove large particles. Each formulation was further
processed using either a lyophilizing process or sprayed drying
procedure to remove the milling media. The collected particles may
optionally be filled into capsules in a quantity appropriate to
obtain the desired dose.
[0047] The equipment used in the milling process including:
[0048] 1. DYNO-MILL, model KDL
[0049] 2. Peristaltic Pump
[0050] 3. 0.6 L Jacked Glass Chamber
[0051] 4. Lead Free Glass beads 0.5 mm (GlenMills Inc.)
[0052] The process parameters in the milling are listed below
3 Mill Speed 2000-4500 rpm Temperature 5-25.degree. C. Pump Rate
20-200 ml/min
EXAMPLE 4
[0053] A dissolution study was conducted to observe the dissolution
rates of three types of nanoparticles/nanocrystal formuolations
generated in Example 3 and with that of a commercial formulation,
Lipanthyl (Fournier SA). The results are illustrated in FIG. 1
below.
* * * * *