The present invention relates to the field of medical technology. More specifically, the present invention relates to the preparations of taxanes for intravenous administration and the preparation method thereof.
Paclitaxel (Taxol™) and docetaxel (Taxotem™) are two sorts of taxanes anticancer drugs approved by Food & Drug Administration (FDA), wherein the paclitaxel, as a natural product, is an anticancer chemical ingredient extracted from the bark of the mountain mahogany (Taxus brevifolia Nutt.) tree, while the docetaxel is a product semi-synthesized from the precursor extracted from the needle leaves of the Taxus baccata tree.
The taxanes belong to a sort of typical cytotoxic agents with a wide spectrum of anticancer effect, having strong inhibitory effect on both primary and metastatic tumors such as breast cancer, ovarian cancer, non small lung cancer (NSCLC), head and neck squamous cell carcinoma and malignant melanoma. Its anti-tumor mechanism lies in that promoting the assembly of tubulin dimer into microtubule and further making the microtubule super-stable by stimulating polymerization of tubulin, thus inhibiting the microtubule net from kinetic recombination. Consequently, the proliferation of cancer cell is prevented at the resting stage of mitosis, and thus achieves the purpose of anti-cancer.
Due to the poor water-solubility and oil-solubility of paclitaxel and docetaxel, they can hardly dissolved in the water (4 μg/ml of water-solubility) and only have 2%-4% is absorpted after oral administration. On the other hand, paclitaxel and docetaxel can be dissolved in organic solvent such as anhydrous ethanol, but when normal saline is added, the drug is precipitated immediately from the drug solution prepared by organic solvent. This makes the intravenous drip impossible in clinical application. Hence, polyoxyethylated castor oil (Cremophor® EL), is usually used as a solubilizer in the available paclitaxel injection preparation. In the paclitaxel injection preparation, the drug solution of paclitaxel is a colorless viscous concentrated solution prepared by a mixed solvent of Cremophor® EL and anhydrous ethanol in the ratio of 50:50 (v/v). Because of the presence of the solubilizer, the drug is not precipitated immediately when normal saline is added in clinical practice. However, the preparation has short stability time, which makes it necessary to complete the intravenous drip in a short period of time; otherwise, the drug will be precipitated. But the quickened infusion rate has a potential for some patients, which is one of drawbacks for the preparation. The second drawback is the serious toxic and side effects induced by the solubilizer, the Cremophor® EL. The acute and common clinical side effects of the available paclitaxel preparation after administration are severe: dyspnea, flushing face, palpitation and allergic reaction such as skin rash etc, which brings a lot of potential safety troubles and suffering to the patients. As a result, pre-administration of anti-allergy drug is a feasible way usually adopted to alleviate the side effects, so available preparation is not an ideal one.
Similarly, there are problems in available docetaxel preparation. The solvent of the drug solution is composed of a solution of Tween 80 and 13% ethanol solution, in which the Tween 80, utilized as a solubilizer, has an effect for hemolysis to some degree. In addition, the addition of normal saline when administrating it to the patients will also have the stability time shortened, so it is needed to complete the intravenous drip in a short period of time. Therefore, the available docetaxel preparation has less drug safety in the clinical application.
Now, a lot of research works on the paclitaxel emulsion-related preparation have been reported. For example, Kan et al. had developed a paclitaxel O/W emulsion by nonionic surfactant and phospholipid (Kan P, et al., Controlled Release, 1999, 58: 271-278). However, Tween 80 is contained in this preparation, which leads to hemolysis in patients after intravenous drip, causing serious side effects. In the application entitled “Parenteral paclitaxel in a stable non-toxic preparation” filed by B. S. Anderson (Chinese Appl. No.: 97196934.5), dimethylacetamide and PEG were used in the composition of the parenteral preparation, in which dimethylacetamide, utilized as a solubilizer, had effects for inducing toxicity and hemolysis to some degree.
The present invention provides a solubilizer-free, less toxicity and more stable preparations of taxanes for intravenous administration.
The preparations of taxanes for intravenous administration of the present invention consist of two parts: a drug solution containing paclitaxel or docetaxel, and an emulsion. The solvent of said drug solution is organic solvent; and the emulsion includes fat emulsion. When used, the drug solution at the clinical dosage can be added and evenly mixed in the emulsion to perform intravenous drip directly; or the drug solution at the clinical dosage can also be firstly added into the emulsion with no less than 5 times volume of the drug solution and then a predetermined amount of normal saline or glucose solution for injection is added to perform intravenous drip.
It is well-known that the fat emulsion belongs to one kind of emulsion, and the emulsion consists of an oil phase and a water phase. The structure of the emulsion micro-particles can be divided into two parts of inner core and outside layer, the former is made up of low polar oils and hydrophobic groups of surfactant to form a non-polar hydrophobic area; and the latter is made up of polar groups of the hydrated surfactant. Furthermore, a transitional layer with increasing polarity from the inner core to the outside layer is formed in the structure. According to the theory of similarity and intermiscibility, drugs with different polarity can usually find their corresponding polar areas in this transitional polar environment of the emulsion micro-particles; hence the emulsion can be used as a drug carrier. Considering the poor water and oil solubility demonstrated by paclitaxel and docetaxel, after the drug solution is dissolved in the emulsion solution, some of the emulsion micro-particles are used as the carrier to carry the drug, and then these drug-loaded emulsion micro-particles are further dispersed homogeneously into other drug-unloaded emulsion to form a stable preparation. This is one of reasons for using emulsion in the present invention. In addition, the emulsion has a targeting effect, which can delivery drug to the tumor or other lesion site. Further, the fat emulsion can be used as a nutritional agent. Clinically, it is usually administrated intravenously to the patient in need of high calorie, such as the patients with tumor and other malignant diseases, the protein-forbidden patients due to renal injury as well as the patients unable to uptake nutrition via gastrointestinal tract for some reason. It is remarkable that, compared with long chain fatty glycerides such as soybean oil, medium chain fatty glycerides represented by octyl and decyl glycerate displays better solubility, absorption, high compatibility and anti-oxidation. This is another reason for using emulsion including fat emulsions prepared by long and medium chain triglycerides in the present invention.
As shown in the experiment, the preparations of taxanes for intravenous administration of the present invention completely comply with the requirements for clinical application. It offers some advantages as follows:
(1) The preparations of the present invention have excellent safety. The preparations of the present invention do not contain any solubilizer such as dimethylacetamide and Tween-80 etc., thus the toxic and side effect is reduced accordingly. The adjuvants used have good biocompatibility and tolerance in vivo.
(2) The preparations of the present invention have high stability. Within 48 hours after mixing paclitaxel or docetaxel solution with emulsion or fat emulsion, no obvious precipitation or degradation of drug is observed. Even if the addition of normal saline or glucose solution for injection is followed, many pharmaceutical parameters such as the drug content, particle size of the emulsion and pH value do not change significantly, which completely meets the clinical needs, hence solving problem of immediate precipitation of drugs caused by dispersion of drug into the normal saline or glucose solution for injection.
(3) The preparations of the present invention can be used as nutritional agents. Not only does a fat emulsion have the targeting effect when used as a drug carrier, but can provide nutritional replenisher for the tumor patient, hence, achieving a better therapeutic effect.
(4) The preparations of the present invention are cost-efficient and convenient for transportation and storage in practice. The reason is that the normal saline or glucose solution for injection can be used to replace a considerable proportion of the emulsion, thus the amount of emulsion or fat emulsion is reduced.
The preparations of taxanes for intravenous administration of the present invention are composed of two parts, a drug solution and an emulsion. The ingredients and proportions are as follows:
Wherein, the solvent for injection is an organic solvent, including one or more kinds selected from a group consisting of PEG (polyethylene glycol)-200, PEG-300, PEG-400, PEG-600, propylene glycol, glycerol and anhydrous ethanol, optionally comprising water for injection with an amount of no more than 50% of total amount of the drug solution; the pH regulator is one or more kinds selected from a group consisting of citric acid, malic acid, hydrochloric acid, acetic acid, sodium carbonate, sodium bicarbonate and sodium hydroxide.
Wherein, the oil for injection is one or more kinds selected from a group consisting of octyl and decyl glycerate, monooctanoin, dicaprylin, trioctanoin, Ganoderma lucidum spores oil, monodecanoin, didecanoin, tridecanoin, octyl and decyl monoglyceride, coix seed oil, Brucea Javanica oil, Herba Artemisiae Annuae oil, octyl and decyl diglyceride, soybean oil, fish oil, linseed oil, helianthus annuus seed oil, evening primrose oil, sea buckthorn oil, zedoary turmeric oil, safflower seed oil, sesame oil, corn oil, elemene oil and stearic acid. The emulsifier is one or more kinds selected from a group consisting of soybean phospholipid, yolk phospholipid, cholesterol, poloxamer 188 and glyceryl monooleate. The antioxidant is tocopherol. The isotonic regulator is one or more kinds selected from a group consisting of glycerol, sorbitol, mannitol, glucose and sodium chloride to adjust the osmotic pressure to that in human body. The stabilizer is one or more kinds selected from a group consisting of oleic acid, sodium oleate, cholic acid and sodium cholate. The pH regulator is one or more kinds selected from a group consisting of citric acid, malic acid, hydrochloric acid, acetic acid, sodium carbonate, sodium bicarbonate and sodium hydroxide.
According to the present invention, a method to prepare the preparations of taxanes for intravenous administration is described as follows:
a). Preparing a Drug Solution:
paclitaxel or docetaxel is added to a solvent for injection in a predetermined proportion and stirred at 50-100° C. to dissolve. The pH value of the obtained solution was adjusted to 4.0-7.0 by using a pH regulator, and 0.01%-5%(W/V) activated carbon for injection use is added to perform adsorption for 15-120 min at 25-100° C. Next, the solution is filtrated, separately packaged, sterilized and packaged using routine methods to obtain the drug solution. The obtained solution is a transparent liquid.
b). Preparing an Emulsion:
b-1). Preparing an oil phase: an emulsifier or stabilizer is added into an oil for injection in a predetermined proportion, stirred at 50-90° C. to dissolve, into which tocopherol is added and dissolved by stirring or ultrasonicating to obtain the oil phase;
b-2). Preparing a water phase: the emulsifier or stabilizer, and isotonic regulator are added into water for injection in a predetermined proportion, stirred at 50-90° C. to dissolve to obtain the water phase;
During preparing the oil phase or water phase, said emulsifier and stabilizer may be added simultaneously or separately.
b-3). Preparing the emulsion: the oil phase of step b-1) is mixed with the water phase of step b-2) at 50-90° C., and followed by emulsification by shear emulsifying machine or stirring emulsification for 5-300 min at a rotation speed of 300-8000 rpm to obtain an initial emulsion, the pH value of the initial emulsion is adjusted by the pH regulator to 4.0-9.0. The obtained initial emulsion is further emulsified and diluted to volume with water for injection, filtrated, separately packaged, charged with nitrogen and sterilized by routine method, thus the emulsion is obtained. The final emulsion looks like a white or off-white colored emulsified liquid with opalescence, and the particle size of the emulsion micro-particles ranges from 50-500 nm.
Wherein, in the step of further emulsifying the initial emulsion, emulsifying methods used in the present invention include but are not limited to emulsification by high-pressure homogenizer, mechanical stirring, ultrasound or colloid mill, the preferred method is emulsification by high-pressure homogenizer under a pressure of 5000-25000 psi. In the step of preparing the drug solution and emulsifier, sterilization methods used in the present invention include but are not limited to using rotary high-pressure steam sterilizer, circulating vapor or micro-porous filter membrane etc. The preferred method is using rotary high-pressure steam sterilizer carried out at 100-121° C. for 20-60 min. The filtrating equipments include but are not limited to micro-porous filter membrane, sand filtrating bar, sintered filter funnel or bladder-type filter etc.
According to the present invention, the preparations of taxanes for intravenous administration can be administered in two ways: the drug solution at the clinical dosage can be added and evenly mixed in the emulsion to perform intravenous drip directly; or the drug solution at the clinical dosage can also be firstly added into the emulsion with no less than 5 times volume of the drug solution and then a predetermined amount of normal saline or glucose solution for injection is added to perform intravenous drip.
According to the present invention, the preparations of taxanes for intravenous administration are solubilizer-free and have advantages of safety, effectiveness, stability and economy. The fat emulsion is also used as a nutritional replenisher for the patients, thus achieving a better therapeutic effect. In addition, the normal saline or glucose solution for injection can be used to replace a considerable proportion of the emulsion, thus makes the preparations of the present invention more cost-efficient and convenient for transportation and storage in practice. The present invention also can be used to prepare the preparations of other poorly water or oil soluble medicinal compounds for intravenous administration.
The following examples are described to demonstrate preferred embodiments of the present invention.
Preparing the drug solution: 2.5 g paclitaxel was added to 100 ml PEG-400, and stirred at 70° C. to dissolve. The pH value of the solution was adjusted to 5.5 by using hydrochloric acid and sodium bicarbonate, and 0.2 g activated carbon for injection use was added to perform adsorption at 25° C. for 30 min. Next, the solution was filtrated by 0.45 μm micro-porous filter membrane, separately packaged, sterilized by high-pressure steam at 115° C. for 30 min, and the drug solution is obtained;
a) Preparing the Emulsion
b-1) Preparing the oil phase: 200 g octyl and decyl glycerate for injection was heated to 70° C. in water bath, into which 12 g soybean phospholipid for injection was added to dissolve by stirring, and then 0.5 g tocopherol was added to stir well to obtain the oil phase;
b-2) Preparing the water phase: 22.5 g glycerol and 10 g poloxamer 188 were added into 640 ml water for injection , stirred at 70° C. to dissolve to obtain the water phase;
b-3) Preparing the emulsion: the oil phase was mixed with the water phase at 70° C., and followed by emulsification using shear emulsifying machine for 12 min at a rotation speed of 1500 rpm to obtain an initial emulsion. The pH value of the initial emulsion was adjusted to 6.0 by sodium carbonate solution. The initial emulsion was further emulsified by a high-pressure homogenizer under a pressure of 20000 psi. The emulsion was diluted to 1000 ml with water for injection, filtrated by 0.45 μm micro-porous filter membrane, the filtrate was separately packaged, charged with nitrogen, capped and sterilized by a rotary high-pressure steam sterilizer at 121° C. for 20 min to obtain the emulsion. By measurement, the average particle size of the emulsion micro-particles was 168nm with the pH value of 5.80.
Preparing the drug solution: 3.0 g docetaxel was added to 100 ml PEG-300, and stirred at 70° C. to dissolve. The pH value of the solution was adjusted to 6.0 by using hydrochloric acid and sodium hydroxide, and 0.2 g activated carbon for injection use was added to perform adsorption at 25° C. for 30 min. Next, the solution was filtrated by 0.45 μm micro-porous filter membrane, separately packaged, sterilized by high-pressure steam at 115° C. for 30 min, and the drug solution is obtained;
a) Preparing the Emulsion
b-1) Preparing the oil phase: 200 g soybean oil for injection was heated to 70° C. in water bath, into which 12 g soybean phospholipid for injection was added to dissolve by stirring, and then 0.5 g tocopherol was added to stir well to obtain the oil phase;
b-2) Preparing the water phase: 22.5 g glycerol and 10 g poloxamer 188 were added into 640 ml water for injection , stirred at 70° C. to dissolve to obtain the water phase;
b-3) Preparing the emulsion: the oil phase was mixed with the water phase at 70° C., and followed by emulsification using shear emulsifying machine for 10 min at a rotation speed of 1000 rpm to obtain an initial emulsion. The pH value of the initial emulsion was adjusted to 6.0 by sodium carbonate solution. The initial emulsion was further emulsified by a high-pressure homogenizer under a pressure of 10000 psi. The emulsion was diluted to 1000 ml with water for injection, filtrated by 0.45 μm micro-porous filter membrane, the filtrate was separately packaged, charged with nitrogen, capped and sterilized by a rotary high-pressure steam sterilizer at 121° C. for 20 min to obtain the emulsion. By measurement, the average particle size of the emulsion micro-particles was 177 nm with the pH value of 5.77.
Preparing the drug solution: 8.0 g paclitaxel was added to 100 ml anhydrous ethanol, and stirred at 55° C. to dissolve. The pH value of the solution was adjusted to 4.5 by using hydrochloric acid, and 4.5 g activated carbon for injection use was added to perform adsorption at 45° C. for 60 min. Next, the solution was filtrated by 0.45 μm micro-porous filter membrane to remove carbon, then filtrated by 0.22 μm micro-porous filter membrane to remove bacteria, separately packaged under a sterile condition, and the drug solution is obtained;
a) Preparing the Emulsion
b-1) Preparing the oil phase: a mixture of 10 g elemene oil, 45 g monodecanoin, 58 g didecanoin, 47 g helianthus annuus seed oil and 20 g evening primrose oil was heated to 75° C. in water bath, into which 65 g soybean phospholipid for injection, 5 g glyceryl monooleate and 3 g cholic acid were added to dissolve by stirring, and then 3.0 g tocopherol was added to stir well to obtain the oil phase;
b-2) Preparing the water phase: 50 g sorbitol and 16 g sodium cholate were added into 590 ml water for injection and stirred at 75° C. to dissolve to obtain the water phase;
b-3) Preparing the emulsion: the oil phase was mixed with the water phase at 75° C., and followed by emulsification using shear emulsifying machine for 170 min at a rotation speed of 2300 rpm to obtain an initial emulsion. The initial emulsion was further emulsified by a high-pressure homogenizer under a pressure of 12000 psi. The emulsion was diluted to 1000 ml with water for injection, and the pH value of the initial emulsion was adjusted to 7.1 by sodium hydroxide solution. The solution was filtrated by sintered filter funnel, and the filtrate was separately packaged, charged with nitrogen, capped and sterilized by performing high-pressure sterilization at 121° C. for 20 min to obtain the emulsion. By measurement, the average particle size of the emulsion micro-particles was 250.7nm with the pH value of 6.80.
Preparing the drug solution: 0.1 g docetaxel was added into a mixed solvent of 60 ml propylene glycol and 40 ml PEG-200, and stirred at 95° C. to dissolve. The pH value of the solution was adjusted to 6.5 by using a proper amount of citric acid and sodium carbonate, and 1.5 g activated carbon for injection use was added to perform adsorption at 100° C. for 30 min. Next, the solution was filtrated by 0.45 μm micro-porous filter membrane, separately packaged, sterilized by high-pressure steam at 117° C. for 55 min, and the drug solution is obtained;
a) Preparing the Emulsion
b-1) Preparing the oil phase: a mixture of 25 g soybean oil for injection and 1.2 g oleic acid was heated to 58° C. in water bath, into which 10 g yolk phospholipid for injection was added to dissolve by stirring, and then lg tocopherol was added to stir well to obtain the oil phase;
b-2) Preparing the water phase: 22.5 g glycerol and 20 g poloxamer 188 were added into 820 ml water for injection, stirred at 58° C. to dissolve to obtain the water phase;
b-3) Preparing the emulsion: the oil phase was mixed with the water phase at 58° C., and followed by emulsification using shear emulsifying machine for 22 min at a rotation speed of 750 rpm to obtain an initial emulsion. The initial emulsion was further emulsified by colloid mill. The emulsion was diluted to 1000 ml with water for injection, and the pH value of the initial emulsion was adjusted to 5.6 by citric acid solution. The solution was filtrated by sand filtrating bar, and the filtrate was separately packaged, charged with nitrogen, capped and sterilized by performing high-pressure steam sterilization at 105° C. for 45 min to obtain the emulsion. By measurement, the average particle size of the emulsion micro-particles was 63.2 nm with the pH value of 5.20.
Preparing the drug solution: 4.0 g paclitaxel was added to a mixed solvent of 95 ml PEG-300 and 5 ml water for injection, and stirred at 60° C. to dissolve. The pH value of the solution was adjusted to 5.8 by using malic acid, and 0.8 g activated carbon for injection use was added to perform adsorption at 30° C. for 115 min. Next, the solution was filtrated by 0.45 μm micro-porous filter membrane, separately packaged, sterilized by circulating steam at 100° C. for 30 min, and the drug solution is obtained;
a) Preparing the Emulsion
b-1) Preparing the oil phase: a mixture of 42 g fish oil, 60 g sesame oil, 2 g tridecanoin, 18 g safflower seed oil, 5 g octyl and decyl monoglyceride and 23 g octyl and decyl diglyceride was heated to 60° C. in water bath, stirred until dissolution. 2.1 g tocopherol was added to stir well to obtain the oil phase;
b-2) Preparing the water phase: 50 g soybean phospholipid, 22.5 g glycerol, 7 g sodium cholate and 3 g sodium oleate were added into 700 ml water for injection, and stirred at 60° C. to dissolve to obtain the water phase;
b-3) Preparing the emulsion: the oil phase was mixed with the water phase at 60° C., and followed by emulsification using shear emulsifying machine for 80 min at a rotation speed of 1600 rpm to obtain an initial emulsion. The initial emulsion was further emulsified by a high-pressure homogenizer under a pressure of 10000 psi. The emulsion was diluted to 1000 ml with water for injection, and the pH value of the initial emulsion was adjusted to 6.7 by sodium carbonate solution. The solution was filtrated by sintered filter funnel, then filtrated by 0.22 μm micro-porous filter membrane to remove bacteria and the filtrate was separately packaged, charged with nitrogen, capped to obtain the emulsion. By measurement, the average particle size of the emulsion micro-particles was 128 nm with the pH value of 6.42.
Preparing the drug solution: 5 g docetaxel was added to a mixed solvent of 10 ml PEG-600, 40 ml propylene glycol and 50 ml anhydrous ethanol, and stirred to dissolve at 65° C. The pH value of the solution was adjusted to 5.7 by using a proper amount of acetic acid, and 4 g activated carbon for injection use was added to perform adsorption at 60° C. for 100 min. Next, the solution was filtrated by 0.45 μm micro-porous filter membrane, separately packaged, sterilized by high-pressure steam at 121° C. for 30 min to obtain the drug solution;
a) Preparing the Emulsion
b-1) Preparing the oil phase: 15 g octyl and decyl glycerate was heated to 55° C. in water bath, into which 7 g soybean phospholipid for injection was added and stirred to dissolve well to obtain the oil phase;
b-2) Preparing the water phase: 9 g sodium chloride was added into 950 ml water for injection, and stirred at 55° C. to dissolve to obtain the water phase;
b-3) Preparing the emulsion: the oil phase was mixed with the water phase at 55° C., and followed by emulsification by shear emulsifying machine for 8 min at a rotation speed of 375 rpm to obtain an initial emulsion. The initial emulsion was further emulsified by ultrasound. The emulsion was diluted to 1000 ml with water for injection, and the pH value of the initial emulsion was adjusted to 4.5 by hydrochloric acid solution. The solution was filtrated by 0.22 μm micro-porous filter membrane, and the filtrate was separately packaged, charged with nitrogen, capped to obtain the emulsion. By measurement, the average particle size of the emulsion micro-particles was 86.3 nm with the pH value of 4.37.
Preparing the drug solution: 0.5 g paclitaxel was added to a mixed solvent of 25 ml glycerol and 75 ml anhydrous ethanol, and stirred to dissolve at 60° C. The pH value of the solution was adjusted to 5.8 by using malic acid, and 0.8 g activated carbon for injection use was added to perform adsorption at 30° C. for 115 min. Next, the solution was filtrated by 0.45 μm micro-porous filter membrane to remove carbon, separately packaged, sterilized by circulating steam at 100° C. for 30 min to obtain the drug solution;
a) Preparing the Emulsion
b-1) Preparing the oil phase: a mixture of 120 g linseed oil and 130 g sea buckthorn oil was heated to 80° C. in water bath, stirred to dissolve, into which 3.5 g tocopherol and 35 g cholic acid were added and stirred to dissolve well to obtain the oil phase;
b-2) Preparing the water phase: 30 g poloxamer (F68) for injection and 50 g yolk phospholipid were added into 550 ml water for injection and stirred to dissolve, into which 35 g sorbitol and 15 g mannitol were added, stirred at 80° C. to dissolve to obtain the water phase;
b-3) Preparing the emulsion: the oil phase was mixed with the water phase at 80° C., and followed by emulsification by shear emulsifying machine for 200 min at a rotation speed of 6000 rpm to obtain an initial emulsion. The initial emulsion was further emulsified by a high-pressure homogenizer under a pressure of 20000 psi. The pH value of the initial emulsion was adjusted to 8.5 by sodium hydroxide solution or hydrochloric acid solution and diluted to 1000 ml with water for injection. The solution was filtrated by 0.45 μm micro-porous filter membrane, and the filtrate was separately packaged, charged with nitrogen, capped, and sterilized by high-pressure steam at 115° C. for 30 min to obtain the emulsion. By measurement, the average particle size of the emulsion micro-particles was 320 nm with the pH value of 8.10.
Preparing the drug solution: 0.5 g docetaxel was added to a mixed solvent of 90 ml PEG-400 and 10 ml anhydrous ethanol, and stirred to dissolve at 55° C. The pH value of the solution was adjusted to 6.8 by using a proper amount of sodium hydroxide, and 1.0 g activated carbon for injection use was added to perform adsorption at 40° C. for 60 min. Next, the solution was filtrated by 0.45 μm micro-porous filter membrane, separately packaged, sterilized by circulating steam at 100° C. for 30 min to obtain the drug solution;
a) Preparing the Emulsion
b-1) Preparing the oil phase: a mixture of 15 g Ganoderma lucidum spores oil, 92 g corn oil, 90 g monooctanoin, 100 g dicaprylin and 100 g linseed oil was heated to 85° C. in water bath, into which 4.5 g tocopherol and 42 g oleic acid were added and stirred to mix well to obtain the oil phase;
b-2) Preparing the water phase: 50 g soybean phospholipid, 43 g poloxamer (F68) and 50 g glucose were added into 400 ml water for injection and stirred at 85° C. to dissolve to obtain the water phase;
b-3) Preparing the emulsion: the oil phase was mixed with the water phase at 85° C., and followed by emulsification by shear emulsifying machine for 269 min at a rotation speed of 7200 rpm to obtain an initial emulsion. The initial emulsion was further emulsified by a high-pressure homogenizer under a pressure of 24700 psi. The pH value of the initial emulsion was adjusted to 9.0 by sodium hydroxide solution and hydrochloric acid solution and diluted to 1000 ml with water for injection. The solution was filtrated by 0.45 μm micro-porous filter membrane, and the filtrate was separately packaged, charged with nitrogen, capped, and sterilized by high-pressure steam at 115° C. for 30 min to obtain the emulsion. By measurement, the average particle size of the emulsion micro-particles was 472.4 nm with the pH value of 8.54.
Preparing the drug solution: 0.05 g paclitaxel was added to a mixed solvent of 80 ml PEG-300 and 20 ml propylene glycol, and stirred to dissolve at 50° C. The pH value of the solution was adjusted to 6.0 by using hydrochloric acid, and 0.2 g activated carbon for injection use was added to perform adsorption at 30° C. for 30 min. Next, the solution was filtrated by 0.45 μm micro-porous filter membrane, and then filtrated by 0.22 μm micro-porous filter membrane to remove bacteria, separately packaged to obtain the drug solution;
a) Preparing the Emulsion
b-1) Preparing the oil phase: 100 g soybean oil for injection was heated to 60° C. in water bath, into which 12 g soybean phospholipid for injection and 0.1 g oleic acid were added, and stirred to dissolve well to obtain the oil phase;
b-2) Preparing the water phase: 50 g glucose was added into 740 ml water for injection and stirred to dissolve at 60° C. to obtain the water phase;
b-3) Preparing the emulsion: the oil phase was mixed with the water phase at 60° C., and followed by emulsification by shear emulsifying machine for 20 min at a rotation speed of 5500 rpm to obtain an initial emulsion. The pH value of the initial emulsion was adjusted to 6.2 by using sodium hydroxide and hydrochloric acid solution. The initial emulsion was further emulsified by a high-pressure homogenizer under a pressure of 15000 psi and diluted to 1000 ml with water for injection. The solution was filtrated by 0.45 μm micro-porous filter membrane, and the filtrate was separately packaged, charged with nitrogen, capped, and sterilized by a rotary high-pressure steam sterilizer at 105° C. for 45 min to obtain the emulsion. By measurement, the average particle size of the emulsion micro-particles was 160 nm with the pH value of 6.0.
Preparing the drug solution: 2.0 g docetaxel was added to a mixed solvent of 50 ml PEG-400 and 50 ml propylene glycol, and stirred to dissolve at 80° C. The pH value of the solution was adjusted to 6.5 by using hydrochloric acid, and 0.4 g activated carbon for injection use was added to perform adsorption at 30° C. for 60 min. Next, the solution was filtrated by 0.45 μm micro-porous filter membrane, separately packaged, and sterilized by high-pressure steam at 100° C. for 60 min to obtain the drug solution;
a) Preparing the Emulsion
b-1) Preparing the oil phase: 150 g soybean oil for injection was heated to 70° C. in water bath, into which 12 g yolk phospholipid for injection was added and stirred to dissolve well to obtain the oil phase;
b-2) Preparing the water phase: 22.5 g glycerol and 0.2 g sodium oleate were added into 700 ml water for injection and stirred at 70° C. to dissolve to obtain the water phase;
b-3) Preparing the emulsion: the oil phase was mixed with the water phase at 70° C., and followed by emulsification by shear emulsifying machine for 20 min at a rotation speed of 4500 rpm to obtain an initial emulsion. The pH value of the initial emulsion was adjusted to 7.0 by using sodium hydroxide and hydrochloric acid solution. The initial emulsion was further emulsified by a high-pressure homogenizer under a pressure of 12000 psi and diluted to 1000 ml with water for injection. The solution was filtrated by 0.45 μm micro-porous filter membrane, and the filtrate was separately packaged, charged with nitrogen, capped, and sterilized by a rotary high-pressure steam sterilizer at 100° C. for 60 min to obtain the emulsion. By measurement, the average particle size of the emulsion micro-particles was 240 nm with the pH value of 7.0.
Preparing the drug solution: 2.5 g paclitaxel was added to a mixed solvent of 80 ml PEG-400 and 20 ml anhydrous ethanol, and stirred at 80° C. to dissolve. The pH value of the solution was adjusted to 5.2 by using hydrochloric acid, and 0.3 g activated carbon for injection use was added to perform adsorption at 40° C. for 20 min. Next, the solution was filtrated by 0.45 μm micro-porous filter membrane, separately packaged, and sterilized by high-pressure steam at 115° C. for 45 min to obtain the drug solution;
a) Preparing the Emulsion
b-1) Preparing the oil phase: 200 g soybean oil for injection was heated to 80° C. in water bath, into which 12 g yolk phospholipid for injection, 0.2 g oleic acid and 0.5 g tocopherol were added and stirred to dissolve well to obtain the oil phase;
b-2) Preparing the water phase: 20 g poloxamer and 22.5 g glycerol were added into 650 ml water for injection and stirred at 80° C. to dissolve to obtain the water phase;
b-3) Preparing the emulsion: the oil phase was mixed with the water phase at 80° C., and followed by emulsification by shear emulsifying machine for 20 min at a rotation speed of 6000 rpm to obtain an initial emulsion. The pH value of the initial emulsion was adjusted to 7.8 by using sodium carbonate solution. The initial emulsion was further emulsified by a high-pressure homogenizer under a pressure of 20000 psi and diluted to 1000 ml with water for injection. The solution was filtrated by 0.45 μm micro-porous filter membrane, and the filtrate was separately packaged, charged with nitrogen, capped, and sterilized by a rotary high-pressure steam sterilizer at 115° C. for 45 min to obtain the emulsion. By measurement, the average particle size of the emulsion micro-particles was 220 nm with the pH value of 7.8.
Preparing the drug solution: 1.5 g docetaxel was added to a mixed solvent of 60 ml PEG-400, 35 ml propylene glycol and 5 ml water, and stirred at 70° C. to dissolve. The pH value of the solution was adjusted to 4.8 by using hydrochloric acid, and 0.6 g activated carbon for injection use was added to perform adsorption at 45° C. for 20 min. Next, the solution was filtrated by 0.45 μm micro-porous filter membrane, separately packaged, and sterilized by high-pressure steam at 121° C. for 30 min to obtain the drug solution;
a) Preparing the Emulsion
b-1) Preparing the oil phase: 250 g soybean oil for injection was heated to 70° C. in water bath, into which 12 g soybean phospholipid for injection and 0.8 g tocopherol were added and stirred to dissolve well to obtain the oil phase;
b-2) Preparing the water phase: 10 g poloxamer, 0.2 g sodium oleate and 9 g sodium chloride were added into 550 ml water for injection and stirred at 70° C. to dissolve to obtain the water phase;
b-3) Preparing the emulsion: the oil phase was mixed with the water phase at 70° C., and followed by emulsification by shear emulsifying machine for 10 min at a rotation speed of 7000 rpm to obtain an initial emulsion. The pH value of the initial emulsion was adjusted to 8.8 by using sodium hydroxide solution. The initial emulsion was further emulsified by a high-pressure homogenizer under a pressure of 16000 psi and diluted to 1000 ml with water for injection. The solution was filtrated by 0.45 μm micro-porous filter membrane, and the filtrate was separately packaged, charged with nitrogen, capped, and sterilized by a rotary high-pressure steam sterilizer at 121° C. for 30 min to obtain the emulsion. By measurement, the average particle size of the emulsion micro-particles was 260 nm with the pH value of 8.5.
Preparing the drug solution: 3.5 g paclitaxel was added to 100 ml PEG-200, and stirred at 70° C. to dissolve. The pH value of the solution was adjusted to 6.2 by using hydrochloric acid and sodium hydroxide, and lg activated carbon for injection use was added to perform adsorption at 30° C. for 30 min. Next, the solution was filtrated by 0.45 μm micro-porous filter membrane, separately packaged, and sterilized by high-pressure steam at 105° C. for 45 min to obtain the drug solution;
a) Preparing the Emulsion
b-1) Preparing the oil phase: 300 g soybean oil for injection was heated to 70° C. in water bath, into which 12 g soybean phospholipid for injection was added and stirred to dissolve well to obtain the oil phase;
b-2) Preparing the water phase: 5 g poloxamer and 22.5 g glycerol were added into 600 ml water for injection and stirred at 80° C. to dissolve to obtain the water phase;
b-3) Preparing the emulsion: the oil phase was mixed with the water phase at 80° C., and followed by emulsification by shear emulsifying machine for 30 min at a rotation speed of 4000 rpm to obtain an initial emulsion. The pH value of the initial emulsion was adjusted to 8.2 by using sodium hydroxide solution. The initial emulsion was further emulsified by a high-pressure homogenizer under a pressure of 15000 psi and diluted to 1000 ml with water for injection. The solution was filtrated by 0.45 μm micro-porous filter membrane, and the filtrate was separately packaged, charged with nitrogen, capped, and sterilized by a rotary high-pressure steam sterilizer at 105° C. for 45 min to obtain the emulsion. By measurement, the average particle size of the emulsion micro-particles was 310 nm with the pH value of 8.1.
Preparing the drug solution: 3 g docetaxel was added to 100 ml PEG-300, and stirred at 70° C. to dissolve. The pH value of the solution was adjusted to 4.5 by using hydrochloric acid, and 0.15 g activated carbon for injection use was added to perform adsorption at 45° C. for 60 min. Next, the solution was filtrated by 0.45 μm micro-porous filter membrane, separately packaged, and sterilized by circulating steam at 100° C. for 60 min to obtain the drug solution;
a) Preparing the Emulsion
b-1) Preparing the oil phase: a mixture of 100 g soybean oil for injection and 100 g octyl and decyl glycerate was heated to 80° C. in water bath, into which 0.8 g tocopherol were added and stirred to dissolve to obtain the oil phase;
b-2) Preparing the water phase: 12 g soybean phospholipid for injection use, 10 g poloxamer, 0.2 g sodium oleate and 22.5 g glycerol were added into 550 ml water for injection and stirred at 80° C. to dissolve to obtain the water phase;
b-3) Preparing the emulsion: the oil phase was mixed with the water phase at 80° C., and followed by emulsification by shear emulsifying machine for 25 min at a rotation speed of 8000 rpm to obtain an initial emulsion. The pH value of the initial emulsion was adjusted to 7.8 by using sodium hydroxide solution. The initial emulsion was further emulsified by a high-pressure homogenizer under a pressure of 16000 psi and diluted to 1000 ml with water for injection. The solution was filtrated by 0.45 μm micro-porous filter membrane, and the filtrate was separately packaged, charged with nitrogen, capped, and sterilized by circulating steam at 100° C. for 60 min to obtain the emulsion. By measurement, the average particle size of the emulsion micro-particles was 280 nm with the pH value of 7.9.
Preparing the drug solution: 4 g paclitaxel was added to 100 ml PEG-400, and stirred at 70° C. to dissolve. The pH value of the solution was adjusted to 6.0 by using hydrochloric acid and sodium carbonate, and 0.3 g activated carbon for injection use was added to perform adsorption at 25° C. for 45 min. Next, the solution was filtrated by 0.45 μm micro-porous filter membrane, separately packaged, and sterilized by high-pressure steam at 121° C. for 30 min to obtain the drug solution;
a) Preparing the Emulsion
b-1) Preparing the oil phase: a mixture of 75 g soybean oil for injection and 75 g octyl and decyl monoglyceride was heated to 80° C. in water bath, into which 2 g tocopherol was added and stirred to dissolve well to obtain the oil phase;
b-2) Preparing the water phase: 12 g yolk phospholipid for injection, 5 g poloxamer and 22.5 g glycerol were added into 600 ml water for injection and stirred at 80° C. to dissolve to obtain the water phase;
b-3) Preparing the emulsion: the oil phase was mixed with the water phase at 80° C., and followed by emulsification by shear emulsifying machine for 20 min at a rotation speed of 8000 rpm to obtain an initial emulsion. The pH value of the initial emulsion was adjusted to 6.8 by using sodium hydroxide and hydrochloric acid solution. The initial emulsion was further emulsified by a high-pressure homogenizer under a pressure of 11000 psi and diluted to 1000 ml with water for injection. The solution was filtrated by 0.45 μm micro-porous filter membrane, and the filtrate was separately packaged, charged with nitrogen, capped, and sterilized by a rotary high-pressure steam sterilizer at 121° C. for 30 min to obtain the emulsion. By measurement, the average particle size of the emulsion micro-particles was 320 nm with the pH value of 6.6.
1. Taking the preparation prepared in accordance with the method of example 1 as the example, the drug solution was mixed homogenously with the emulsion in the ratio of 1:25. The change of drug contents, particle sizes of the emulsion micro-particles and pH values of these preparations were detected at different time-points.
Method:
4 ml of the drug solution was added to 100 ml of the emulsion, and stirred well. The drug contents, particle sizes and pH values of the preparations were determined at different time-points by HPLC, a particle size analyzer and a pH meter. When determining the drug content at the different time-points, all of tested samples should be filtrated firstly by 0.22 μm micro-porous filter membrane so as to remove the precipitated drugs crystals, and then the drug contents were determined. The change in the drug content was used to judge whether the drug was precipitated or not. In addition, the average particle sizes and pH values were determined directly. The average results were summarized in Table 1.
2. Taking the preparation prepared in accordance with the method of example 1 as the example, the drug solution was mixed with the emulsion in the ratio of 1:5, shaken up homogenously, diluted with 10-fold volume of normal saline for injection and shaken up. The change of drug contents, particle sizes of the emulsion micro-particles and pH values of these preparations were detected at different time-points.
Method:
4 ml of the drug solution was added to 20 ml of the emulsion, and stirred well. Then the solution obtained was added into 200 ml normal saline for injection and shaken up homogenously. The drug contents, the particle sizes and pH values of the preparations were determined at different time-points by HPLC, a particle size analyzer and a pH meter. When determining the drug content at the different time, all of tested samples should be filtrated firstly by 0.22 μm micro-porous filter membrane so as to remove the precipitated drugs crystals, and then the drug contents were determined. The change in the drug content was used to judge whether the drug was precipitated or not. In addition, the average particle sizes and pH values were determined directly. The average results were summarized in Table 2.
It can be seen from tables 1 and 2 that the drug contents in the filtrate of the paclitaxel preparation for intravenous administration are almost unchanged within 48 h, showing that no precipitation of paclitaxel. Besides, the particle size and pH value did not show any significant change. All of these findings suggested that the paclitaxel preparations for intravenous administration were stable within 48 hours. At 60th hour, the drug content in the filtrate dropped slightly, indicating that a small amount of the drugs was precipitated. Meanwhile, the particle size of the emulsion micro-particles was slightly increased, and the change in the particle size also can be used to determine whether drug precipitation occurs or not. As shown in the above results, the preparations of the present invention are stable and comply with the requirements of clinical application.
This application is a continuation of U.S. patent application Ser. No. 15/274,452, filed on Sep. 23, 2016, which is a continuation of U.S. patent application Ser. No. 14/059,347, filed Oct. 21, 2013, now abandoned, which is a continuation of U.S. patent application Ser. No. 12/571,176, filed Sep. 30, 2009, now abandoned, the contents of which are each incorporated herein by reference in its entirety.
Number | Date | Country | |
---|---|---|---|
Parent | 15274452 | Sep 2016 | US |
Child | 16360860 | US | |
Parent | 14059347 | Oct 2013 | US |
Child | 15274452 | US | |
Parent | 12571176 | Sep 2009 | US |
Child | 14059347 | US |