WO2018154538A1 - Method for encapsulating tetracyclines - Google Patents

Method for encapsulating tetracyclines Download PDF

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Publication number
WO2018154538A1
WO2018154538A1 PCT/IB2018/051227 IB2018051227W WO2018154538A1 WO 2018154538 A1 WO2018154538 A1 WO 2018154538A1 IB 2018051227 W IB2018051227 W IB 2018051227W WO 2018154538 A1 WO2018154538 A1 WO 2018154538A1
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WIPO (PCT)
Prior art keywords
doxycycline
solution
percentage
tetracycline
process according
Prior art date
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PCT/IB2018/051227
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Spanish (es)
French (fr)
Inventor
Vanessa GALLEGO LONDOÑO
Julián LONDOÑO
Santiago MONSALVE BURITICÁ
Andrés Felipe LONDOÑO BARBARÁN
Original Assignee
Corporacion Universitaria Lasallista
Gentech Biosciences S.A.S
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Publication of WO2018154538A1 publication Critical patent/WO2018154538A1/en

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    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K31/00Medicinal preparations containing organic active ingredients
    • A61K31/65Tetracyclines
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K31/00Medicinal preparations containing organic active ingredients
    • A61K31/70Carbohydrates; Sugars; Derivatives thereof
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K47/00Medicinal preparations characterised by the non-active ingredients used, e.g. carriers or inert additives; Targeting or modifying agents chemically bound to the active ingredient
    • A61K47/30Macromolecular organic or inorganic compounds, e.g. inorganic polyphosphates
    • A61K47/36Polysaccharides; Derivatives thereof, e.g. gums, starch, alginate, dextrin, hyaluronic acid, chitosan, inulin, agar or pectin
    • A61K47/38Cellulose; Derivatives thereof
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00Medicinal preparations characterised by special physical form
    • A61K9/48Preparations in capsules, e.g. of gelatin, of chocolate
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00Medicinal preparations characterised by special physical form
    • A61K9/48Preparations in capsules, e.g. of gelatin, of chocolate
    • A61K9/50Microcapsules having a gas, liquid or semi-solid filling; Solid microparticles or pellets surrounded by a distinct coating layer, e.g. coated microspheres, coated drug crystals
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61PSPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
    • A61P31/00Antiinfectives, i.e. antibiotics, antiseptics, chemotherapeutics
    • A61P31/04Antibacterial agents

Definitions

  • the present invention is in the field of chemistry, specifically in relation to encapsulation methods of antibiotics of the tetracycline group for the control of bacterial infections.
  • Tetracyclines constitute a group of antibiotics, some natural and others obtained by semisynthesis, which cover a broad spectrum in their antimicrobial activity. Despite their great antimicrobial properties, they have gastrolesive effects that are characterized by the production of nausea and vomiting when administered orally.
  • a tablet that offer an enteric coating, however to administer doses in concentrations other than the composition of the tablet, the tablet must be divided to meet the required dose, which alters the cover and enteric protection of the drug.
  • An alternative that could counteract its irritating effects in its passage through the gastric route is encapsulation, since it allows modifying biopharmaceutical characteristics of the drug, such as its release profile. In this way, two important aspects of its administration could be modified: the dosage frequency and the quantities required. Finally, this will affect the reduction of some of the gastrointestinal adverse effects described above.
  • US20090004281A1 describes a pharmaceutical composition and its method of preparation and administration.
  • the composition includes a core containing at least one drug (eg doxycycline, insulin) in combination with at least one pharmaceutically acceptable excipient.
  • the composition further includes an osmotic sub-coating surrounding the core (eg sodium chloride, sucrose, mannitol), and a release coating, together with adjuvants and binders (eg starch, pre-gelatinized starch, gelatin).
  • the manufacturing process consists of preparing individual solutions of the drug and of the osmotic subcoats, which are mixed until a homogeneous solution is fed to a spray dryer.
  • US20130196954A1 discloses a method for preparing a sustained-release doxycycline tablet.
  • the tablet comprises doxycycline (0.1-99.0%) together with binders between (5-10%), excipients and adjuvants (25-50%).
  • Doxycycline or other chemically modified tetracycline may be included in the tablet and also contains appropriate inactive ingredients, which are well known in the art, and may include bulking agents such as microcrystalline cellulose, calcium sulfate, starches, disintegrating agents, microcrystalline cellulose, gelatin and sweeteners.
  • document US8415331B2 discloses a solid dosage form of a doxycycline metal complex and a process for manufacturing a doxycycline metal complex in solid dosage form.
  • the solid dosage further includes pharmaceutically known excipients.
  • the process comprises the steps of: (i) providing an aqueous solution of doxycycline or a physiologically acceptable salt thereof; (ii) mixing a metal salt with the aqueous solution; (iii) mixing a base to increase the pH of the aqueous solution, thereby forming a metal doxycycline suspension; and (iv) drying the suspension, thereby forming a dry granulation of the doxycycline metal complex.
  • the present invention relates to a method of microencapsulating antibiotics of the tetracycline group, comprising: separately preparing a solution of gelatin, sucrose, and tetracyclines (eg tetracycline, minocycline, tigylcycline, chlortetracycline, doxycycline, oxytetracycline, demethyl ); mix the sucrose solution with the tetracycline solution; subsequently the obtained mixture is added to the gelatin solution until a homogeneous mixture is formed, characterized by a percentage of total solids between 20 and 40% and a particle size between 0.33 and 0.44 ⁇ ; finally the mix Homogeneous is dried by the spray drying method, until an oral powder formulation of encapsulated doxycycline is obtained.
  • the method is characterized by performance percentages between 40 and 60% and encapsulation efficiency between 35 and 60%.
  • FIG. L Response surface and estimated equation for: A) Size; B) Viscosity
  • FIG. 2 Release of microencapsulated doxycycline at pH between 1.0 and 3.0 and pH between 6.8 and 7.4:
  • Tta A Formulation without carboxymethyl cellulose
  • Tto B Formulation with carboxymethyl cellulose.
  • FIG. 3 Scanning electron microscopy (SEM) of the microparticles obtained by spray drying: (A) Formulation with gelatin and sucrose; (B) Formulation with gelatin, sucrose and carboxymethyl cellulose.
  • Encapsulation is defined as a packaging technology for solid, liquid or gaseous materials.
  • the sealed capsules can release their contents at controlled speeds under specific conditions, and can protect the encapsulated product from light, oxygen and pH, among others.
  • the encapsulation consists of the formation of particles formed by a porous membrane containing an active substance.
  • the material or mixtures of materials to be encapsulated is thus covered or trapped within another material or system.
  • the materials used for encapsulation can be gelatin, fats, oils, gum arabic, calcium alginate, waxes, wheat starch, corn starch, rice starch, potato starch, nylon, cyclodextrin, maltodextrin, sodium caseinate, sucrose and carboxymethyl cellulose.
  • Tetracyclines are broad spectrum antimicrobials, some natural and others obtained by semisynthesis, are characterized by their activity against a large group of gram-positive and gram-negative bacteria, aerobic and anaerobic and atypical microorganisms such as Chlamydia sp, Rickettsia sp, Mycoplasma sp, Borrelia sp, Treponema pallidum, Helicobacter pylori, Plasmodium sp and some mycobacteria.
  • Tetracyclines belong to a group of antibiotics with a basic tetracyclic chemical structure and common biological activity, formed by the fusion of four benzene rings with various substituents; Its chemical structure gives them an amphoteric character that allows the formation of salts, both with acids and with bases, usually using soluble hydrochlorides.
  • the present invention proposes a method of encapsulation of tetracyclines, for example selected from the group: minocycline, tigylcycline, chlortetracycline, doxycycline, oxytetracycline and demethylchlortetracycline, to obtain an oral powder composition that facilitates its dosing and reduces the gastrolesive effects produced by the irritant capacity of this.
  • tetracyclines for example selected from the group: minocycline, tigylcycline, chlortetracycline, doxycycline, oxytetracycline and demethylchlortetracycline
  • a gelatin solution, a sucrose solution and a tetracycline solution are individually prepared; optionally a carboxymethyl cellulose solution can be added.
  • the tetracycline solution and the sucrose solution are mixed until a dispersion is formed, to which the gelatin solution is added to form a suspension characterized by a percentage of total solids between 20 and 40%, preferably between 30 and 40% and a particle size between 0.30 and 0.48 ⁇ , preferably 0.35 and 0.40.
  • the suspension is dried until a powder composition of encapsulated tetracyclines is obtained. More specifically, initially each component of the formulation is individually dispersed in an aqueous medium.
  • the quantity of the component to be dispersed should be such that its percentage in total solids quantity is: for gelatin between 10 and 40% w / w, preferably between 20 and 30%; for sucrose between 60 and 90% w / w, preferably 70 and 80%; and for tetracyclines between 5 and 15% w / w, preferably 8 and 10%.
  • the suspension may contain sodium carboxymethyl cellulose between 0.2 and 1% w / w, preferably between 0.3 and 0.8% of the total solids.
  • the tetracycline used is preferably doxycycline.
  • the tetracycline solution is mixed with the sucrose solution to form a dispersion, to which the gelatin solution is added to form the suspension.
  • the suspension obtained is homogenized between 2000 and 6000 rpm for 10 cycles of one minute each to guarantee the total incorporation of the components and is characterized by the properties of Table 1.
  • the suspension is subjected to a mechanical encapsulation method such as spraying, atomization, lyophilization, fluidized bed drying and extrusion.
  • spray drying is used at an inlet temperature between 100 and 180 ° C, preferably between 120 and 140 ° C, an outlet temperature between 54 and 90 ° C, preferably between 60 and 80 ° C and a percentage of suction between 65 and 85%, preferably between 75 and 80%.
  • the encapsulation method of the present invention has a percentage of encapsulation efficiency between 35 and 60%, preferably between 40 and 50% and yields between 40 and 60%, preferably 50 and 58%.
  • the encapsulation method of the invention provides a powder composition with a tetracycline content (e.g. doxycycline) between 2 and 10 mg per 100 mg of powder and is characterized by the properties of Table 2.
  • a tetracycline content e.g. doxycycline
  • the final powder composition has a release percentage at pH between 1.0 and 3.0 of 0.10 and 0.40% w / w encapsulated tetracycline / initial tetracycline (2-10% w / w), and at pH between 6.8 and 7.4 of 0.10 and 0.20% w / w encapsulated tetracycline / initial tetracycline (2-10% w / w).
  • a composite central design was applied for the optimization of the preparation conditions, in which the parameters of percentage of total solids were evaluated (ST) between 20 to 40% and the homogenization speed between 2000 to 6000 rpm. 4 replicas were applied to the center within the design, that is, it was evaluated at 30% ST and 4000 rpm 4 times.
  • the response variables evaluated were viscosity ( ⁇ ), particle size and zeta potential (Q.
  • the design was carried out with 6 degrees of freedom and randomized order and in total 12 treatments were analyzed.
  • Table 3 YEAR variable VA response (second order model): A) Zeta potential; B) Size; C) Viscosity
  • the suspension should contain total solids between 20 and 40% to ensure greater efficiency, performance and stability during the drying process.
  • the optimal conditions of the suspension from the DCC were (ST: 33.3% and 6000 rpm) for a ⁇ : 256.0 cp, ⁇ : 18.74 mV and size: 0.44 ⁇ . These reached values are within the ranges required for spray drying.
  • the ideal proportions of the encapsulants correspond to: 13.64% w / w gelatin, 85.86% sucrose and 0.5% w / w sodium carboxymethylcellulose.
  • Example 2 Prepare stable suspension with doxycycline
  • Total 50gr of suspension were prepared, independently dispersing each of the components in an aqueous medium: 38.25 g of sucrose were added to 18.0 mL of water; 6.08 g of gelatin was dispersed in 45.5 mL of water; 0.22 gr of sodium carboxymethyl cellulose was dispersed in 23.0 mL of water; and 4.95 g of doxycycline were dispersed in 14 mL of water. Each component was suspended in distilled water at 60 ° C and homogenized with magnetic stirring at 2000 rpm.
  • the suspension for spray drying was prepared by slowly adding 14 mL of the doxycycline solution to 18 mL of the sucrose solution, with constant mechanical stirring and at a temperature of 60 ° C. To guarantee the complete dispersion of the components, the mixture obtained was homogenized with an Ultraturrax at a speed of 6000 rpm for 1 minute. Subsequently, 23.0 mL of the carboxymethyl cellulose solution and 45.5 mL of the gelatin solution were added to the previously formed mixture of doxycycline and sucrose, maintaining mechanical stirring and temperature at 60 ° C. The suspension obtained was homogenized with an Ultraturrax at 6000 rpm for 10 cycles of one minute each. The final suspension obtained is characterized by the parameters in Table 4.
  • Example 3 Doxycycline encapsulation Doxycycline encapsulation was performed by spray drying technique. For this, the suspension described in Example 2 was dried through a Spray Dryer under the following conditions: feed rate between 2 and 5 mL / min, inlet temperature between 100 and 180 ° C, an outlet temperature between 54 and 90 ° C and a percentage of aspiration between 65 and 85%.
  • an encapsulated doxycycline powder is obtained with a percentage of encapsulation efficiency between 35 and 60%, yields between 40 and 60%, encapsulated doxycycline content of 4.86 mg per 100 mg of powder and total doxycycline of 9.46 mg per 100 mg of powder.
  • the doxycycline powder obtained is characterized by the parameters in Table 5.
  • FIG. 2 corresponds to the percentage of doxycycline released at pH between 1.0 and 3.0 and pH between 6.8 and 7.4 for a formulation without sodium carboxymethylcellulose (Tto A) and with sodium carboxymethylcellulose (Tto B).
  • the characterization of microparticles obtained from Spray drying was performed by scanning electron microscopy (SEM).
  • SEM scanning electron microscopy
  • the inclusion of sodium carboxymethylcellulose as an encapsulating agent softens the surface of the particles and gives them the property of having a spherical shape
  • the particles where only gelatin and sucrose were used as encapsulating agents have forms irregular, cracks and pores.

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Abstract

The invention relates to a method for encapsulating antibiotics of the tetracycline group, comprising the following steps: separately preparing solutions of gelatine, saccharose and tetracyclines; and mixing the saccharose solution with the tetracycline solution, the mixture obtained then being added to the gelatine solution to form a suspension characterised by a total solids percentage of between 20 and 40% and a particle size of between 0.33 and 0.44µm. Finally, the suspension obtained is dried by the spray drying method until an oral powder formulation is obtained. The method is characterised by yields of between 40 and 60% and an encapsulation efficiency of between 35 and 60%.

Description

MÉTODO DE ENCAPSULACION DE TETRACICLINAS  TETRACICLINE ENCAPSULATION METHOD
Campo de la invención Field of the Invention
La presente invención se encuentra en el campo de la química, específicamente en relación con métodos de encapsulacion de antibióticos del grupo tetraciclinas para el control de infecciones bacterianas. The present invention is in the field of chemistry, specifically in relation to encapsulation methods of antibiotics of the tetracycline group for the control of bacterial infections.
Descripción del estado de la técnica Description of the state of the art
Las tetraciclinas constituyen un grupo de antibióticos, unos naturales y otros obtenidos por semisíntesis, que abarcan un amplio espectro en su actividad antimicrobiana. A pesar de sus grandes propiedades antimicrobianas, presentan efectos gastrolesivos que se caracterizan por la producción de náuseas y vómito al ser administradas por vía oral. Existen algunas presentaciones comerciales en forma de tableta que ofrecen un recubrimiento entérico, sin embargo para administrar dosis en concentraciones diferentes a la composición de la tableta, se debe fraccionar la tableta para cumplir con la dosis requerida, lo cual altera la cubierta y la protección entérica del fármaco. Una alternativa que podría contrarrestar sus efectos irritantes en su paso por la vía gástrica es la encapsulacion, ya que permite modificar características biofarmacéuticas propias del fármaco, como su perfil de liberación. De esta forma, se podrían modificar dos aspectos importantes de su administración: la frecuencia de dosificación y las cantidades requeridas. Finalmente, esto repercutirá en la disminución de algunos de los efectos adversos gastrointestinales anteriormente descritos. Tetracyclines constitute a group of antibiotics, some natural and others obtained by semisynthesis, which cover a broad spectrum in their antimicrobial activity. Despite their great antimicrobial properties, they have gastrolesive effects that are characterized by the production of nausea and vomiting when administered orally. There are some commercial presentations in the form of a tablet that offer an enteric coating, however to administer doses in concentrations other than the composition of the tablet, the tablet must be divided to meet the required dose, which alters the cover and enteric protection of the drug. An alternative that could counteract its irritating effects in its passage through the gastric route is encapsulation, since it allows modifying biopharmaceutical characteristics of the drug, such as its release profile. In this way, two important aspects of its administration could be modified: the dosage frequency and the quantities required. Finally, this will affect the reduction of some of the gastrointestinal adverse effects described above.
En el documento US20090004281A1 se describe una composición farmacéutica y su método de preparación y administración. La composición incluye un núcleo que contiene al menos un fármaco (v.g. doxiciclina, insulina) en combinación con al menos un excipiente farmacéuticamente aceptable. La composición incluye además un sub- revestimiento osmótico que rodea al núcleo (v.g. cloruro de sodio, sacarosa, manitol), y un revestimiento de liberación, junto con adyuvantes y aglutinantes (v.g. almidón, almidón pre-gelatinizado, gelatina). El proceso de fabricación consiste en preparar soluciones individuales del fármaco y de los sub-revestimientos osmóticos, los cuales se mezclan hasta obtener una solución homogénea que se alimenta a un secador por aspersión. El documento US20130196954A1 divulga un método para preparar un comprimido de doxiciclina de liberación sostenida. El comprimido comprende doxiciclina (0,1 - 99,0%) junto con aglutinantes entre (5 -10%), excipientes y adyuvantes (25 - 50%). La doxiciclina u otra tetraciclina químicamente modificada puede incluirse en el comprimido y contiene además ingredientes inactivos apropiados, que son bien conocidos en la técnica, y pueden incluir agentes de volumen como celulosa microcristalina, sulfato de calcio, almidones, agentes desintegrantes, celulosa microcristalina, gelatina y edulcorantes. US20090004281A1 describes a pharmaceutical composition and its method of preparation and administration. The composition includes a core containing at least one drug (eg doxycycline, insulin) in combination with at least one pharmaceutically acceptable excipient. The composition further includes an osmotic sub-coating surrounding the core (eg sodium chloride, sucrose, mannitol), and a release coating, together with adjuvants and binders (eg starch, pre-gelatinized starch, gelatin). The manufacturing process consists of preparing individual solutions of the drug and of the osmotic subcoats, which are mixed until a homogeneous solution is fed to a spray dryer. US20130196954A1 discloses a method for preparing a sustained-release doxycycline tablet. The tablet comprises doxycycline (0.1-99.0%) together with binders between (5-10%), excipients and adjuvants (25-50%). Doxycycline or other chemically modified tetracycline may be included in the tablet and also contains appropriate inactive ingredients, which are well known in the art, and may include bulking agents such as microcrystalline cellulose, calcium sulfate, starches, disintegrating agents, microcrystalline cellulose, gelatin and sweeteners.
Por otro lado el documento US8415331B2 divulga una forma de dosificación sólida de un complejo de metal de doxiciclina y un procedimiento para fabricar un complejo de metal de doxiciclina en forma de dosificación sólida. La dosificación sólida incluye además excipientes farmacéuticamente conocidos. El procedimiento comprende las etapas de: (i) proporcionar una solución acuosa de doxiciclina o una sal fisiológicamente aceptable de la misma; (ii) mezclar una sal metálica con la solución acuosa; (iii) mezclar una base para aumentar el pH de la solución acuosa, formando de este modo una suspensión de doxiciclina metálica; y (iv) secar la suspensión, formando de este modo una granulación seca del complejo de metal de doxiciclina. On the other hand, document US8415331B2 discloses a solid dosage form of a doxycycline metal complex and a process for manufacturing a doxycycline metal complex in solid dosage form. The solid dosage further includes pharmaceutically known excipients. The process comprises the steps of: (i) providing an aqueous solution of doxycycline or a physiologically acceptable salt thereof; (ii) mixing a metal salt with the aqueous solution; (iii) mixing a base to increase the pH of the aqueous solution, thereby forming a metal doxycycline suspension; and (iv) drying the suspension, thereby forming a dry granulation of the doxycycline metal complex.
Si bien en el estado de la técnica se encuentran divulgados procesos de encapsulación de tetraciclinas, es necesario el desarrollo de nuevos métodos de encapsulación de antibióticos del grupo tetraciclina en diferentes presentaciones y dosificaciones, que optimicen la acción farmacológica y reduzcan la incidencia o intensidad de las lesiones gastrointestinales al ser administrados por vía oral y que así mismo posibiliten una administración cómoda que favorezca el mantenimiento del régimen farmacéutico. Although tetracycline encapsulation processes are disclosed in the state of the art, it is necessary to develop new methods of encapsulating antibiotics of the tetracycline group in different presentations and dosages, which optimize the pharmacological action and reduce the incidence or intensity of Gastrointestinal lesions when administered orally and that also allow a comfortable administration that favors the maintenance of the pharmaceutical regimen.
Breve descripción de la invención La presente invención se refiere a un método de microencapsulacion de antibióticos del grupo tetraciclinas, que comprende: preparar separadamente una solución de gelatina, sacarosa, y tetraciclinas (v.g. tetraciclina, minociclina, tigilciclina, clortetraciclina, doxiciclina, oxitetraciclina, demetilclortetraciclina); mezclar la solución de sacarosa con la solución de tetraciclina; posteriormente la mezcla obtenida se adiciona a la solución de gelatina hasta formar una mezcla homogénea, caracterizada por un porcentaje de sólidos totales entre 20 y 40% y un tamaño de partícula entre 0,33 y 0,44μπι; finalmente la mezcla homogénea se seca por el método de secado por aspersión, hasta obtener una formulación oral en polvo de doxiciclina encapsulada. El método se caracteriza por porcentajes de rendimiento entre 40 y 60 % y eficiencia de encapsulacion entre 35 y 60 %. BRIEF DESCRIPTION OF THE INVENTION The present invention relates to a method of microencapsulating antibiotics of the tetracycline group, comprising: separately preparing a solution of gelatin, sucrose, and tetracyclines (eg tetracycline, minocycline, tigylcycline, chlortetracycline, doxycycline, oxytetracycline, demethyl ); mix the sucrose solution with the tetracycline solution; subsequently the obtained mixture is added to the gelatin solution until a homogeneous mixture is formed, characterized by a percentage of total solids between 20 and 40% and a particle size between 0.33 and 0.44μπι; finally the mix Homogeneous is dried by the spray drying method, until an oral powder formulation of encapsulated doxycycline is obtained. The method is characterized by performance percentages between 40 and 60% and encapsulation efficiency between 35 and 60%.
Breve descripción de las figuras Brief description of the figures
FIG.l Superficie de respuesta y ecuación estimada para: A) Tamaño; B) Viscosidad FIG. L Response surface and estimated equation for: A) Size; B) Viscosity
FIG. 2 Liberación de doxiciclina microencapsulada a pH entre 1,0 y 3,0 y pH entre 6,8 y 7,4: (Tta A). Formulación sin carboximetilcelulosa; (Tto B) Formulación con carboximetilcelulosa. FIG. 2 Release of microencapsulated doxycycline at pH between 1.0 and 3.0 and pH between 6.8 and 7.4: (Tta A). Formulation without carboxymethyl cellulose; (Tto B) Formulation with carboxymethyl cellulose.
FIG. 3 Microscopía electrónica de barrido (SEM) de las micropartículas obtenidas por secado por aspersión: (A) Formulación con gelatina y sacarosa; (B) Formulación con gelatina, sacarosa y carboximetilcelulosa. FIG. 3 Scanning electron microscopy (SEM) of the microparticles obtained by spray drying: (A) Formulation with gelatin and sucrose; (B) Formulation with gelatin, sucrose and carboxymethyl cellulose.
Descripción detallada de la invención Detailed description of the invention
La encapsulacion es definida como una tecnología de empaquetamiento de materiales sólidos, líquidos o gaseosos. Las cápsulas selladas pueden liberar sus contenidos a velocidades controladas bajo condiciones específicas, y pueden proteger el producto encapsulado de la luz, el oxígeno y el pH, entre otros. La encapsulacion consiste en la formación de partículas conformadas por una membrana porosa contenedora de una sustancia activa. El material o mezclas de materiales a encapsular es así cubierto o atrapado dentro de otro material o sistema. Los materiales empleados para el encapsulamiento pueden ser gelatina, grasas, aceites, goma arábiga, alginato de calcio, ceras, almidón de trigo, almidón de maíz, almidón de arroz, almidón de papa, nylon, ciclodextrina, maltodextrina, caseinato de sodio, sacarosa y carboximetilcelulosa. Encapsulation is defined as a packaging technology for solid, liquid or gaseous materials. The sealed capsules can release their contents at controlled speeds under specific conditions, and can protect the encapsulated product from light, oxygen and pH, among others. The encapsulation consists of the formation of particles formed by a porous membrane containing an active substance. The material or mixtures of materials to be encapsulated is thus covered or trapped within another material or system. The materials used for encapsulation can be gelatin, fats, oils, gum arabic, calcium alginate, waxes, wheat starch, corn starch, rice starch, potato starch, nylon, cyclodextrin, maltodextrin, sodium caseinate, sucrose and carboxymethyl cellulose.
La encapsulacion en el área de medicamentos permite modificar el perfil de liberación de un principio activo. Uno de los grupos de fármacos susceptibles a tratamientos de encapsulacion por sus efectos gastrolesivos son las tetraciclinas. Las tetraciclinas son antimicrobianos de amplio espectro, unos naturales y otros obtenidos por semisíntesis, se caracterizan por su actividad contra un gran grupo de bacterias gram-positivas y gram- negativas, aerobios y anaerobios y microorganismos atípicos como Chlamydia sp, Rickettsia sp, Micoplasma sp, Borrelia sp, Treponema pallidum, Helicobacter pylori, Plasmodium sp y algunas micobacterias. Las tetraciclinas pertenecen a un grupo de antibióticos con una estructura química tetracíclica básica y actividad biológica común, formadas por la fusión de cuatro anillos bencénicos con diversos sustituyentes; su estructura química les otorga un carácter anfotérico que permite la formación de sales, tanto con ácidos como con bases, utilizándose usualmente los clorhidratos solubles. Encapsulation in the area of medications allows modifying the release profile of an active substance. One of the groups of drugs susceptible to encapsulation treatments due to their gastrolesive effects are tetracyclines. Tetracyclines are broad spectrum antimicrobials, some natural and others obtained by semisynthesis, are characterized by their activity against a large group of gram-positive and gram-negative bacteria, aerobic and anaerobic and atypical microorganisms such as Chlamydia sp, Rickettsia sp, Mycoplasma sp, Borrelia sp, Treponema pallidum, Helicobacter pylori, Plasmodium sp and some mycobacteria. Tetracyclines belong to a group of antibiotics with a basic tetracyclic chemical structure and common biological activity, formed by the fusion of four benzene rings with various substituents; Its chemical structure gives them an amphoteric character that allows the formation of salts, both with acids and with bases, usually using soluble hydrochlorides.
La presente invención propone un método de encapsulación de tetraciclinas, por ejemplo selecciondas del grupo: minociclina, tigilciclina, clortetraciclina, doxiciclina, oxitetraciclina y demetilclortetraciclina, para obtener una composición oral en polvo que facilite su dosificación y disminuya los efectos gastrolesivos producidos por la capacidad irritante de éstas. The present invention proposes a method of encapsulation of tetracyclines, for example selected from the group: minocycline, tigylcycline, chlortetracycline, doxycycline, oxytetracycline and demethylchlortetracycline, to obtain an oral powder composition that facilitates its dosing and reduces the gastrolesive effects produced by the irritant capacity of this.
De acuerdo con método de la invención, se preparan individualmente una solución de gelatina, una solución de sacarosa y una solución de tetraciclinas; opcionalmente puede adicionarse una solución de carboximetilcelulosa. Posteriormente se mezcla la solución de tetraciclina y la solución de sacarosa hasta formar una dispersión, a la cual se adiciona la solución de gelatina hasta formar una suspensión caracterizada por un porcentaje de sólidos totales entre 20 y 40%, preferiblemente entre 30 y 40% y un tamaño de partícula entre 0,30 y 0,48 μπι, preferiblemente 0,35 y 0,40. La suspensión se seca hasta obtener una composición en polvo de tetraciclinas encapsuladas. Más específicamente, inicialmente cada componente de la formulación es dispersado de manera individual en un medio acuoso. La cantidad del componente a dispersar debe ser tal, que su porcentaje en cantidad de sólidos totales sea: para gelatina entre 10 y 40 %p/p, preferiblemente entre 20 y 30%; para sacarosa entre el 60 y 90 %p/p, preferiblemente 70 y 80%; y para tetraciclinas entre 5 y 15 %p/p, preferiblemente 8 y 10%. Adicionalmente la suspensión puede contener carboximetilcelulosa sódica entre 0,2 y l%p/p, preferiblemente entre 0,3 y 0,8% de los sólidos totales. En una modalidad de la invención la tetraciclina empleada es preferiblemente doxiciclina. According to the method of the invention, a gelatin solution, a sucrose solution and a tetracycline solution are individually prepared; optionally a carboxymethyl cellulose solution can be added. Subsequently, the tetracycline solution and the sucrose solution are mixed until a dispersion is formed, to which the gelatin solution is added to form a suspension characterized by a percentage of total solids between 20 and 40%, preferably between 30 and 40% and a particle size between 0.30 and 0.48 μπι, preferably 0.35 and 0.40. The suspension is dried until a powder composition of encapsulated tetracyclines is obtained. More specifically, initially each component of the formulation is individually dispersed in an aqueous medium. The quantity of the component to be dispersed should be such that its percentage in total solids quantity is: for gelatin between 10 and 40% w / w, preferably between 20 and 30%; for sucrose between 60 and 90% w / w, preferably 70 and 80%; and for tetracyclines between 5 and 15% w / w, preferably 8 and 10%. Additionally, the suspension may contain sodium carboxymethyl cellulose between 0.2 and 1% w / w, preferably between 0.3 and 0.8% of the total solids. In one embodiment of the invention, the tetracycline used is preferably doxycycline.
Se mezcla la solución de tetraciclinas con la solución de sacarosa hasta formar una dispersión, a la que se le adiciona la solución de gelatina para formar la suspensión. La suspensión obtenida se homogeniza entre 2000 y 6000 rpm por 10 ciclos de un minuto cada uno para garantizar la total incorporación de los componentes y se caracteriza por las propiedades de la Tabla 1. The tetracycline solution is mixed with the sucrose solution to form a dispersion, to which the gelatin solution is added to form the suspension. The suspension obtained is homogenized between 2000 and 6000 rpm for 10 cycles of one minute each to guarantee the total incorporation of the components and is characterized by the properties of Table 1.
Tabla 1. Características suspensión estable de tetraciclinas Table 1. Features stable suspension of tetracyclines
Figure imgf000006_0001
Figure imgf000006_0001
Finalmente la suspensión se somete a un método de encapsulacion mecánica como aspersión, atomización, liofilización, secado por lecho fluidizado y extrusión. En una modalidad se emplea secado por aspersión a una temperatura de entrada entre 100 y 180°C, preferiblemente entre 120 y 140°C, una temperatura de salida entre 54 y 90°C, preferiblemente entre 60 y 80°C y un porcentaje de succión entre 65 y 85%, preferiblemente entre 75 y 80%. El método de encapsulacion de la presente invención presenta un porcentaje de eficiencia de encapsulacion entre el 35 y 60%, preferiblemente entre 40 y 50% y rendimientos entre 40 y 60%, preferiblemente 50 y 58%.  Finally, the suspension is subjected to a mechanical encapsulation method such as spraying, atomization, lyophilization, fluidized bed drying and extrusion. In one embodiment, spray drying is used at an inlet temperature between 100 and 180 ° C, preferably between 120 and 140 ° C, an outlet temperature between 54 and 90 ° C, preferably between 60 and 80 ° C and a percentage of suction between 65 and 85%, preferably between 75 and 80%. The encapsulation method of the present invention has a percentage of encapsulation efficiency between 35 and 60%, preferably between 40 and 50% and yields between 40 and 60%, preferably 50 and 58%.
El método de encapsulacion de la invención proporciona una composición en polvo con un contenido de tetraciclinas (v.g. doxiciclina) entre 2 y 10 mg por cada 100 mg de polvo y se caracteriza por las propiedades de la Tabla 2. The encapsulation method of the invention provides a powder composition with a tetracycline content (e.g. doxycycline) between 2 and 10 mg per 100 mg of powder and is characterized by the properties of Table 2.
Tabla 2. Características de estabilidad composición en polvo Table 2. Powder composition stability characteristics
Figure imgf000006_0002
Figure imgf000006_0002
La composición final en polvo presenta un porcentaje de liberación a pH entre 1,0 y 3,0 del 0,10 y 0,40%p/p de tetraciclina encapsulada/tetraciclina inicial (2-10% p/p), y a pH entre 6,8 y 7,4 del 0,10 y 0,20%p/p de tetraciclina encapsulada/tetraciclina inicial (2-10% p/p). The final powder composition has a release percentage at pH between 1.0 and 3.0 of 0.10 and 0.40% w / w encapsulated tetracycline / initial tetracycline (2-10% w / w), and at pH between 6.8 and 7.4 of 0.10 and 0.20% w / w encapsulated tetracycline / initial tetracycline (2-10% w / w).
Los siguientes Ejemplos ilustran la invención, sin que el concepto inventivo se restrinja a los mismos. The following Examples illustrate the invention, without the inventive concept being restricted thereto.
EJEMPLOS EXAMPLES
Ejemplo 1: Optimización de las condiciones de la suspensión: Example 1: Optimization of suspension conditions:
Para la obtención de una suspensión estable que permita un óptimo desempeño durante el proceso de secado por aspersión, se aplicó un diseño central compuesto (DCC) para la optimización de las condiciones de preparación, en el cual se evaluó los parámetros de porcentaje de sólidos totales (ST) entre 20 a 40 % y la velocidad de homogenización entre 2000 a 6000 rpm. Se aplicó 4 réplicas al centro dentro del diseño, es decir que se evaluó a 30% de ST y 4000 rpm 4 veces. Las variables respuesta evaluadas fueron la viscosidad (μ), el tamaño de partícula y el potencial zeta (Q. El diseño se llevó a cabo con 6 grados de libertad y orden aleatorizado y en total fueron analizados 12 tratamientos. Tabla 3. ANO VA variables de respuesta (modelo segundo orden): A) Potencial zeta; B) Tamaño; C) Viscosidad To obtain a stable suspension that allows optimum performance during the spray drying process, a composite central design (DCC) was applied for the optimization of the preparation conditions, in which the parameters of percentage of total solids were evaluated (ST) between 20 to 40% and the homogenization speed between 2000 to 6000 rpm. 4 replicas were applied to the center within the design, that is, it was evaluated at 30% ST and 4000 rpm 4 times. The response variables evaluated were viscosity (μ), particle size and zeta potential (Q. The design was carried out with 6 degrees of freedom and randomized order and in total 12 treatments were analyzed. Table 3. YEAR variable VA response (second order model): A) Zeta potential; B) Size; C) Viscosity
A) Potencial zeta A) Zeta potential
Figure imgf000007_0001
C) Viscosidad
Figure imgf000007_0001
C) Viscosity
Figure imgf000008_0001
Figure imgf000008_0001
La ANOVA para cada una de las variables respuesta, permite identificar que el potencial zeta no se ve afectado estadísticamente en los rangos estudiados de los factores ni por las interacciones entre estos, ya que ningún dato arrojó un valor-P menor a 0,05. Por tanto dicha variable no se tuvo en cuenta para la optimización por superficie de respuesta. Para el tamaño se observa que a mayor porcentaje de sólidos y velocidad de homogenización baja, el tamaño de la partícula es superior (FIG.1 A). En cuanto a la viscosidad, a medida que se va aumentando la velocidad de homogenización y el porcentaje de sólidos, esta respuesta va aumentando en valor (FIG. IB), tal vez sea que al aumentar el área de contacto se aumente las interacciones entre los agentes encapsulantes y el sistema se hace más viscoso; a excepción de tratamiento a 2000 rpm y 40 % de ST, donde esa velocidad es tan baja que no es capaz de homogenizar el sistema y por eso su valor de viscosidad es tan alto. A partir de la optimización realizada, se estableció que la suspensión debía contener sólidos totales entre 20 y 40% para garantizar una mayor eficiencia, rendimiento y estabilidad durante el proceso de secado. Las condiciones óptimas de la suspensión a partir del DCC fueron (ST: 33,3 % y 6000 rpm) para una μ: 256,0 cp, ζ: 18,74 mV y tamaño: 0,44 μπι. Dichos valores alcanzados se encuentran dentro de los rangos requeridos para el secado por aspersión.  The ANOVA for each of the response variables, allows to identify that the zeta potential is not statistically affected in the studied ranges of the factors or by the interactions between them, since no data showed a P-value less than 0.05. Therefore, this variable was not taken into account for the optimization by response surface. For the size it is observed that at a higher percentage of solids and low homogenization rate, the particle size is larger (FIG. 1 A). As for viscosity, as the homogenization rate and the percentage of solids increase, this response is increasing in value (FIG. IB), it may be that increasing the contact area increases the interactions between the encapsulating agents and the system becomes more viscous; with the exception of treatment at 2000 rpm and 40% ST, where that speed is so low that it is not able to homogenize the system and therefore its viscosity value is so high. From the optimization carried out, it was established that the suspension should contain total solids between 20 and 40% to ensure greater efficiency, performance and stability during the drying process. The optimal conditions of the suspension from the DCC were (ST: 33.3% and 6000 rpm) for a μ: 256.0 cp, ζ: 18.74 mV and size: 0.44 μπι. These reached values are within the ranges required for spray drying.
Finalmente, para la inclusión del componente carboximetilcelulosa sódica (CMC), se realizó un diseño de mezclas D-optimal con arreglo cuadrático y con las siguientes restricciones: gelatina (9,5 - 34,5% p/p), sacarosa (65 - 90% p/p) y carboximetilcelulosa sódica (0,1 - 0,5% p/p). Las variables respuesta tomadas en cuenta en el diseño de mezclas fueron las mismas del DCC (viscosidad, potencial zeta y tamaño). Finally, for the inclusion of the sodium carboxymethylcellulose (CMC) component, a design of D-optimal mixtures was carried out with quadratic arrangement and with the following restrictions: gelatin (9.5 - 34.5% w / w), sucrose (65 - 90% w / w) and sodium carboxymethylcellulose (0.1-0.5% w / w). The response variables taken into account in the design of mixtures were the same as the DCC (viscosity, zeta potential and size).
Las proporciones idóneas de los encapsulantes, según el diseño, corresponden a: 13,64% p/p de gelatina, 85,86% de sacarosa y 0,5%p/p de carboximetilcelulosa sódica. Los valores de las variables respuesta obtenidos con la mezcla óptima, μ: 325,5 cp, ζ: 21,30 mV y tamaño: 0,33 μπι, indican que la suspensión presenta características que le brindan estabilidad y que son adecuadas para mejorar parámetros tecnológicos (eficiencia y rendimiento) durante el proceso de secado por aspersión. Ejemplo 2: Preparar suspensión estable con doxiciclina The ideal proportions of the encapsulants, according to the design, correspond to: 13.64% w / w gelatin, 85.86% sucrose and 0.5% w / w sodium carboxymethylcellulose. The values of the response variables obtained with the optimal mixture, μ: 325.5 cp, ζ: 21.30 mV and size: 0.33 μπι, indicate that the suspension has characteristics that provide stability and are suitable for improving technological parameters (efficiency and performance) during the spray drying process. Example 2: Prepare stable suspension with doxycycline
Se prepararon 50gr totales de suspensión, dispersando de forma independiente en un medio acuoso cada uno de los componentes así: a 18,0 mL de agua se añadieron 38,25 gr de sacarosa; 6,08 gr de gelatina se dispersaron en 45,5 mL de agua; 0,22 gr de carboximetilcelulosa sódica se dispersaron en 23,0 mL de agua; y 4,95 gr de doxiciclina fueron dispersados en 14 mL de agua. Cada componente fue suspendido en agua destilada a 60°C y homogenizado con agitación magnética a 2000 rpm. Total 50gr of suspension were prepared, independently dispersing each of the components in an aqueous medium: 38.25 g of sucrose were added to 18.0 mL of water; 6.08 g of gelatin was dispersed in 45.5 mL of water; 0.22 gr of sodium carboxymethyl cellulose was dispersed in 23.0 mL of water; and 4.95 g of doxycycline were dispersed in 14 mL of water. Each component was suspended in distilled water at 60 ° C and homogenized with magnetic stirring at 2000 rpm.
La suspensión para el secado por aspersión se preparó adicionando lentamente 14 mL de la solución de doxiciclina a 18 mL de la solución de sacarosa, con agitación mecánica constante y a una temperatura de 60 °C. Para garantizar la completa dispersión de los componentes la mezcla obtenida se homogeneizó con un Ultraturrax a una velocidad de 6000 rpm por 1 minuto. Posteriormente se adicionaron 23,0 mL de la solución de carboximetilcelulosa y 45,5 mL de la solución de gelatina a la mezcla previamente formada de doxiciclina y sacarosa, manteniendo la agitación mecánica y la temperatura a 60°C. La suspensión obtenida se homogeneizó con un Ultraturrax a 6000 rpm por 10 ciclos de un minuto cada uno. La suspensión final obtenida se caracteriza por los parámetros de la Tabla 4. The suspension for spray drying was prepared by slowly adding 14 mL of the doxycycline solution to 18 mL of the sucrose solution, with constant mechanical stirring and at a temperature of 60 ° C. To guarantee the complete dispersion of the components, the mixture obtained was homogenized with an Ultraturrax at a speed of 6000 rpm for 1 minute. Subsequently, 23.0 mL of the carboxymethyl cellulose solution and 45.5 mL of the gelatin solution were added to the previously formed mixture of doxycycline and sucrose, maintaining mechanical stirring and temperature at 60 ° C. The suspension obtained was homogenized with an Ultraturrax at 6000 rpm for 10 cycles of one minute each. The final suspension obtained is characterized by the parameters in Table 4.
Tabla 4. Parámetros suspensión estable con doxiciclina Table 4. Parameters stable suspension with doxycycline
Figure imgf000009_0001
Figure imgf000009_0001
Ejemplo 3: Encapsulación de doxiciclina La encapsulacion de doxiciclina se realizó por medio de la técnica de secado por aspersión. Para esto, la suspensión descrita en el ejemplo 2 se secó a través de un Spray Dryer bajo las siguientes condiciones: velocidad de alimentación entre 2 y 5 mL/min, temperatura de entrada entre 100 y 180°C, una temperatura de salida entre 54 y 90°C y un porcentaje de aspiración entre 65 y 85%. Example 3: Doxycycline encapsulation Doxycycline encapsulation was performed by spray drying technique. For this, the suspension described in Example 2 was dried through a Spray Dryer under the following conditions: feed rate between 2 and 5 mL / min, inlet temperature between 100 and 180 ° C, an outlet temperature between 54 and 90 ° C and a percentage of aspiration between 65 and 85%.
Finalmente se obtiene un polvo de doxiciclina encapsulada con un porcentaje de eficiencia de encapsulacion entre 35 y 60 %, rendimientos entre 40 y 60 %, contenido de doxiciclina encapsulada de 4,86 mg por cada 100 mg de polvo y doxiciclina total de 9,46 mg por cada 100 mg de polvo. El polvo de doxiciclina obtenido se caracteriza por los parámetros de la Tabla 5. Finally, an encapsulated doxycycline powder is obtained with a percentage of encapsulation efficiency between 35 and 60%, yields between 40 and 60%, encapsulated doxycycline content of 4.86 mg per 100 mg of powder and total doxycycline of 9.46 mg per 100 mg of powder. The doxycycline powder obtained is characterized by the parameters in Table 5.
Tabla 5. Parámetros de estabilidad composición en polvo de doxiciclina  Table 5. Stability parameters doxycycline powder composition
Figure imgf000010_0001
Figure imgf000010_0001
Ejemplo 4: Ensayos de liberación a diferentes valores de pH  Example 4: Release tests at different pH values
Para determinar el porcentaje de doxiciclina liberado a diferentes valores de pH se dispersaron 40mg de la composición en polvo obtenida de acuerdo con el Ejemplo 3 en 5ml de una solución de HCL 0,1N y pH 1,2 con agitación mecánica de 50rpm durante dos horas a 37°C, el porcentaje de liberación obtenido fue de 0,35%p/p de doxiciclina liberada por la cantidad inicial de doxiciclina en el polvo (2-10% p/p). El mismo análisis se realizó pero esta vez empleando una solución amortiguadora de fosfato a pH 7,4, el porcentaje de liberación obtenido fue de 0,18% %p/p de doxiciclina liberada por la cantidad inicial de doxiciclina en el polvo (2-10% p/p). To determine the percentage of doxycycline released at different pH values, 40mg of the powder composition obtained according to Example 3 was dispersed in 5ml of a 0.1N HCL solution and pH 1.2 with mechanical stirring of 50 rpm for two hours. at 37 ° C, the percentage of release obtained was 0.35% w / w of doxycycline released by the initial amount of doxycycline in the powder (2-10% w / w). The same analysis was performed but this time using a phosphate buffer solution at pH 7.4, the percentage of release obtained was 0.18% w / w% of doxycycline released by the initial amount of doxycycline in the powder (2- 10% w / w).
La FIG.2 corresponde al porcentaje de doxiciclina liberado a pH entre 1,0 y 3,0 y pH entre 6,8 y 7,4 para una formulación sin carboximetilcelulosa sódica (Tto A) y con carboximetilcelulosa sódica (Tto B). La caracterización de micropartículas obtenidas del secado por aspersión se realizó por microscopía electrónica de barrido (SEM). Como se observa en la FIG.3 la inclusión de carboximetilcelulosa sódica como agente encapsulante suaviza la superficie de las partículas y les da la propiedad de tener forma esférica, por otro lado las partículas donde sólo se empleó gelatina y sacarosa como agentes encapsulantes, tienen formas irregulares, grietas y poros. Estas características están relacionadas con el perfil de liberación, siendo mayor para las partículas de gelatina y sacarosa a pH entre 1,0 y 3,0, que con aquellas que tienen en su formulación carboximetilcelulosa, por tanto este agente encapsulante otorga mayor protección a pH bajos. FIG. 2 corresponds to the percentage of doxycycline released at pH between 1.0 and 3.0 and pH between 6.8 and 7.4 for a formulation without sodium carboxymethylcellulose (Tto A) and with sodium carboxymethylcellulose (Tto B). The characterization of microparticles obtained from Spray drying was performed by scanning electron microscopy (SEM). As seen in FIG. 3, the inclusion of sodium carboxymethylcellulose as an encapsulating agent softens the surface of the particles and gives them the property of having a spherical shape, on the other hand the particles where only gelatin and sucrose were used as encapsulating agents, have forms irregular, cracks and pores. These characteristics are related to the release profile, being greater for the gelatin and sucrose particles at pH between 1.0 and 3.0, than with those that have in their carboxymethyl cellulose formulation, therefore this encapsulating agent grants greater protection at pH low.

Claims

REIVINDICACIONES
1) Un método de encapsulación de tetraciclinas que comprende las siguientes etapas: a) preparar una solución de gelatina; 1) A tetracycline encapsulation method comprising the following steps: a) preparing a gelatin solution;
b) preparar una solución de sacarosa:  b) prepare a sucrose solution:
c) preparar una solución de un antibiótico del tipo tetraciclina;  c) preparing a solution of an antibiotic of the tetracycline type;
d) mezclar la solución del antibiótico tetraciclina y la solución de sacarosa; e) adicionar la solución de gelatina a la mezcla obtenida en la etapa (d) y formar una mezcla homogénea caracterizada por un porcentaje de sólidos totales entre 20 y 40% y un tamaño de partícula entre 0,33 y 0,44μπι;  d) mixing the tetracycline antibiotic solution and the sucrose solution; e) add the gelatin solution to the mixture obtained in step (d) and form a homogeneous mixture characterized by a percentage of total solids between 20 and 40% and a particle size between 0.33 and 0.44μπι;
f) Secar la mezcla homogénea de la etapa (e).  f) Dry the homogeneous mixture from step (e).
2) El proceso según la Reivindicación 1 , donde la cantidad de cada componente debe ser tal que su porcentaje en la cantidad de sólidos totales sea: para gelatina entre 10 y 40 % p/p, para sacarosa entre el 60 y 90 %p/p y para tetraciclinas entre 5 y 15 %p/p. 2) The process according to Claim 1, wherein the amount of each component must be such that its percentage in the amount of total solids is: for gelatin between 10 and 40% w / w, for sucrose between 60 and 90% w / py for tetracyclines between 5 and 15% w / w.
3) El proceso según la Reivindicación 1, donde la tetraciclina es preferiblemente doxiciclina. 4) El proceso según la Reivindicación 1 , donde la mezcla de la etapa (e) adicionalmente contiene carboximetilcelulosa entre 0,2 y l%p/p de sólidos totales. 3) The process according to Claim 1, wherein the tetracycline is preferably doxycycline. 4) The process according to Claim 1, wherein the mixture of step (e) additionally contains carboxymethyl cellulose between 0.2 and 1% w / w total solids.
5) El proceso según la Reivindicación 1, donde la mezcla de la etapa (e) se realiza con agitación entre 2000 y 6000 rpm por 10 ciclos de un minuto cada uno. 5) The process according to Claim 1, wherein the mixing of step (e) is carried out with stirring between 2000 and 6000 rpm for 10 cycles of one minute each.
6) El proceso según la Reivindicación 1 , donde el método de secado de la etapa (f) es preferiblemente secado por aspersión, con a una temperatura de entrada entre 100 y 180°C, una temperatura de salida entre 54 y 90°C, un porcentaje de succión entre 65 y 85%. 6) The process according to Claim 1, wherein the drying method of step (f) is preferably spray dried, with an outlet temperature between 54 and 90 ° C at an inlet temperature between 100 and 180 ° C, a percentage of suction between 65 and 85%.
7) El proceso según la Reivindicación 1, con un porcentaje de eficiencia de encapsulación entre 35 y 60 % y rendimientos entre 40 y 60 %. 7) The process according to Claim 1, with a percentage of encapsulation efficiency between 35 and 60% and yields between 40 and 60%.
8) Una composición en polvo de doxiciclina encapsulada obtenida según el proceso de la Reivindicación 1 a 7. 8) An encapsulated doxycycline powder composition obtained according to the process of Claim 1 to 7.
9) Una composición en polvo de doxiciclina encapsulada según la Reivindicación 8, con un contenido de doxiciclina entre 2 y 10 mg por cada 100 mg de polvo. 9) An encapsulated doxycycline powder composition according to Claim 8, with a doxycycline content between 2 and 10 mg per 100 mg of powder.
10) Una composición en polvo de doxiciclina según la Reivindicación 8, caracterizada por un tamaño de partícula entre 0,30 y 0,80 μπι y un potencial z entre 19,00 y 23,00 mV. 11) Una composición en polvo de doxiciclina según la Reivindicación 8, con un porcentaje de liberación a pH entre 1,0 y 3,0 del 0,10 y 0,40 p/p y un porcentaje de liberación y a pH entre 6,8 y 7,4 del 0,10 y 0,20 p/p de doxiciclina encapsulada/doxiciclina inicial. 10) A doxycycline powder composition according to Claim 8, characterized by a particle size between 0.30 and 0.80 μπι and a z potential between 19.00 and 23.00 mV. 11) A doxycycline powder composition according to Claim 8, with a percentage of release at pH between 1.0 and 3.0 of 0.10 and 0.40 p / p and a percentage of release and at pH between 6.8 and 7.4 of 0.10 and 0.20 w / w encapsulated doxycycline / initial doxycycline.
PCT/IB2018/051227 2017-02-27 2018-02-27 Method for encapsulating tetracyclines WO2018154538A1 (en)

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EP1383508B1 (en) * 2001-04-05 2006-06-21 Collagenex Pharmaceuticals, Inc. Doxycycline for the treatment of acne
US20050019396A1 (en) * 2003-07-25 2005-01-27 Galen (Chemicals) Limited Doxycycline metal complex in a solid dosage form
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