JP2013231185A - Hard hydroxypropylmethyl cellulose capsule and manufacturing method - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide an aqueous composition for manufacturing hard hydroxypropylmethyl cellulose capsule and a manufacturing method.SOLUTION: A hard hydroxypropylmethyl cellulose capsule is manufactured by using a composition comprising a film forming material of hydroxypropylmethyl cellulose including a content of 27.0 to 30.0% (w/w) of methoxy and a content of 4.0 to 7.5% (w/w) of hydroxypropoxy and having a viscosity of 3.5 to 6.0 cPs at 20°C as 2 wt.% solution.

Description

The present invention relates to an aqueous composition for the production of hydroxypropylmethylcellulose (hereinafter “HPMC”) hard capsules, a method for producing HPMC hard capsules and the hard capsules obtained thereby.

Capsules are well-known dosage forms usually composed of a shell filled with one or more specific substances. The shell is a film-forming polymer (s), such as gelatin,
It may be a soft starch containing modified starch, modified cellulose or the like, or a hard stable shell as in the present invention.

Hard capsules are generally manufactured by using a dip molding method. In this method, a pin mold is immersed in a composition that forms a film. The film-forming polymer is gelled on the pins to form a film that is subsequently dried on the pins to obtain a capsule shell. The shell is then peeled from the pins and cut to the desired length. In this way, a capsule cap and body can be obtained, which can later be filled and bonded with substances,
A filled capsule is thus obtained.

When using this type of immersion molding method, once the pin is pulled out of the immersion bath, it is necessary to ensure that the immersion composition adheres to the surface of the pin and quickly gels. This avoids flowing the composition over the surface of the pin so that the desired shell or film distribution is obtained to produce the capsule.

When gelatin is used as the film-forming polymer, the soaking composition gels upon cooling. The mixture of methylcellulose and gelling agent shows the same gelation behavior. Both these types of film-forming polymers may be processed on conventional equipment for making hard gelatin capsules.

U. S. Pat. No. US Pat. No. 2,526,683 discloses a process for the production of methylcellulose pharmaceutical capsules by a dip coating method. This method involves dipping into a methylcellulose composition maintained at a temperature below the temperature at which gelation of the capsule-forming pins preheated to 40 ° C. to 85 ° C. begins, withdrawing the pins, and in an oven at a temperature above the gelling temperature. It consists of placing the pins on and drying the film. When the hot pin is immersed in the composition, the composition gels on the surface of the pin, and when the pin is withdrawn, a gelled liquid film with a certain thickness is formed on the pin. The pin is then typically rotated 180 ° to an upright position and placed in an oven for drying. This technique is customarily called “thermal gelation”. The dried capsule is then peeled off, cut to the desired size and the body and cap are combined.
However, methylcellulose is insoluble in water below 37 ° C.

U. S. Pat. No. US Pat. No. 3,493,407 discloses the use of non-thermal gelling dip molding compositions of some hydroxyalkyl methylcellulose ethers in an aqueous solvent. In order for the capsule to take a defined shape, the pin must be rotated for more than 0.5 hours.

U. S. Pat. No. 3,617,588 discloses the use of induction heaters for the gelation of cellulose ethers.
U. S. Pat. No. US Pat. No. 4,001,211 discloses an improved thermal gelling composition based on a mixture of methylcellulose and hydroxypropylmethylcellulose.

The above composition and method did not make it possible to obtain a high performance production of hard capsules both in terms of speed, dissolution properties and overall quality. Similarly, capsules made with a combination of HPMC and a gelling agent are very poor in visual quality and dissolution properties because they are sensitive to cations and pH.

There continues to be research on compositions with even better quality in terms of lack of particular disadvantages, visual appearance, high performance on filling equipment, excellent dissolution properties and energy consumption limitations. Additives should be avoided whenever possible.

U. S. Pat. No. 2,526,683 U. S. Pat. No. 3,493,407 U. S. Pat. No. 3,617,588 U. S. Pat. No. 4,001,211

The object of the present invention is in particular a new composition for the production of HPMC capsules with high quality: eg standardized dimensions, high transparency (similar to hard gelatin capsules) and excellent solubility and mechanical performance Is to provide.

This and other objects are achieved in accordance with the first aspect of the invention, which is an aqueous composition for the manufacture of hard capsules, wherein the composition is based on the total weight of the aqueous composition in an aqueous solvent. 15-25% by weight, methoxy content 27.0-30.0% (w / w), hydroxypropoxy content 4.0-7.5% (w / w) and in water at 20 ° C. Hydroxypropyl methylcellulose having a viscosity of 3.5 to 6.0 cPs as a 2 wt% solution is included.

In the present invention, the content of HPMC methoxy and hydroxypropyl is USP30-
Expressed according to NF25.
In the present invention, the viscosity of a 2 wt% solution of HPMC in water at 20 ° C. is measured according to the method of USP 30-NF25 for cellulose derivatives.

The aqueous composition preferably comprises 17-23% by weight of hydroxypropyl methylcellulose based on the total weight of the aqueous composition.
Suitable hydroxypropyl methylcellulose is commercially available. For example, suitable types are all that meet the requirements described in USP 30-NF25 for the HPMC 2906 type.

Suitable aqueous compositions can be obtained by mixing HPMCs of the same type but different viscosity grades.

In a preferred embodiment, the HPMC in the aqueous composition of the invention is 2 in water at 20 ° C.
HPMC having a viscosity of 4.0 to 5.0 cPs as a% w / w solution.
The viscosity of the HPMC solution in water can be measured by using a Ubbelohde viscometer, for example, by a common technique as disclosed in USP.

In one embodiment of the invention, the aqueous composition of the invention comprises 0% by weight and 5% based on the total weight.
It may comprise an aqueous composition of an additional non-animal derived film-forming polymer commonly used in the manufacture of hard capsules, between wt%, preferably between 0 wt% and 2 wt%. The HPMC aqueous composition of the present invention preferably contains no film-forming polymer in addition to the HPMC disclosed herein. Non-animal derived film forming polymers are, for example, polyvinyl alcohol, plant derived or bacterial derived film forming polymers. Typical plant-derived film-forming polymers are starch, starch derivatives, cellulose, cellulose derivatives other than HPMC as defined herein, and mixtures thereof. A typical bacterial film-forming polymer is an exopolysaccharide. Typical exopolysaccharides are xanthan, acetan, gellan, welan, rhamsan, furcelleran, succinoglycan (s
uccinoglycan, scleroglycan, schizophyllan, tamarind gum
, Curdlan, pullulan, dextran (de
xtran) and mixtures thereof.

In a preferred embodiment, the HPMC aqueous composition of the present invention is of animal origin commonly used in the manufacture of hard capsules of between 0% and 1% by weight, preferably 0% by weight, based on the total weight of the aqueous composition. Contains substances. A typical animal derived material is gelatin.

In a preferred embodiment, the aqueous composition of the present invention is 0% by weight based on the total weight of the aqueous composition.
And less than 1% by weight, preferably 0% by weight of the gelling system. By “gelling system” is meant one or more cations and / or one or more gelling agents. Typical cations are K ⁺ , Na ⁺ , Li ⁺ , NH ₄ ⁺ , Ca ⁺⁺ , Mg ⁺⁺ and mixtures thereof. Typical gelling agent (s) are hydrocolloids such as alginate, agar gum, guar gum, locust bean gum (carob) (loc
ust bean gum (carob)), carrageenan (carrageenan)
s), tara gum, gum arabic, ghatti gum, kaya grandifolia gum (khaya grand)
ifolia gum), tragacanth gum, karaya gum, pectin, arabian (araban) (
arabian (araban)), xanthan, gellan gum
), Konjac mannan, galactomannan (gala)
ctomannan, funoran, and mixtures thereof. Usually, the gelling agent can optionally be used in combination with cations and other components such as sequestering agents.

Since the HPMC aqueous compositions disclosed herein are suitable for producing tough and physically stable gels without a gelling system, the solubility characteristics of the HPMC capsules of the present invention are generally Unaffected by the disadvantages associated with the system, especially the cations.

In natural, i.e., no pigments or similar ingredients added to the composition, the HPMC hard capsules obtained from the aqueous composition of the present invention exhibit excellent clarity and transparency. 6
The transmittance of the capsule body (through its double shell layer) measured by 50 nm UV light is approximately 80%, which is equivalent to a hard gelatin capsule.

To obtain colored capsules, at least one inert, non-toxic pharmaceutical grade or food grade dye, such as titanium dioxide, can be mixed into the aqueous composition.
In general, 0.001 to 1.0% by weight of the dye can be included in the aqueous composition. Weight is expressed as divided by the total weight of the composition.

Optionally, a suitable plasticizer such as glycerin or propylene glycol can be included in the aqueous solution. In order to avoid excessive softness, the plasticizer content should be low, for example between 0% and 2% by weight divided by the total weight of the composition, more preferably 0% and 1% by weight. Must be between.

The aqueous composition of the present invention can be prepared by dispersing HPMC and other optional ingredients in one or more aqueous solvents, preferably water. The aqueous solvent can be above room temperature, preferably above 60 ° C, more preferably above 70 ° C. The optimum temperature can be determined by a technician. In a preferred embodiment, after defoaming, the dispersion is cooled to below room temperature, preferably below 15 ° C., to achieve HPMC solubilization.

The gelation temperature of the aqueous composition may be determined by gradually heating the composition and measuring the viscosity. The temperature at which the viscosity begins to increase suddenly is considered the gelation temperature. As an example, at a concentration of about 19% w / w in water, any HPMC of the present invention that meets the USP definition of HPMC type 2906 has a gel temperature between approximately 30 ° C and 40 ° C. As an additional example,
H with a hydroxypropoxy content of about 6% at a concentration between 15 and 25% w / w in water
The HPMC of the present invention that meets the USP definition of PMC has a gel temperature between approximately 30 ° C and 40 ° C. An example of how the gelation temperature can be easily measured is shown in the examples.

The aqueous composition of the present invention can be used as an immersion composition in an immersion molding method for producing HPMC hard capsules.
It has been stated that the aqueous composition of the present invention enables the production of excellent HPMC hard capsules with optimal dissolution characteristics. The dissolution profile is an important point for obtaining a complete and reproducible release of the substance contained in the capsule in therapy.

Furthermore, it has been stated that the aqueous composition of the present invention allows for the manufacture of excellent HPMC hard capsules that can be properly sealed once the body and cap are bonded together. This allows the novel HPMC hard capsules disclosed herein to be used in the manufacture of liquid-filled oral dosage forms as well as powder-filled dosage forms for inhalation, or for use in the context of double-blind trials. It is a particularly excellent and cost-effective solution for the production of pharmaceutical dosage forms that can be easily tampered with.

In a second aspect, the present invention relates to a method for the production of hydroxypropylmethylcellulose hard capsules according to the dip coating method, characterized in that the method comprises the following steps:
(A) As a 2% by weight solution in water at 20 ° C. with a methoxy content of 27.0-30.0% (w / w), a hydroxypropoxy content of 4.0-7.5% (w / w) 3.5
Preparing an aqueous composition of hydroxypropylmethylcellulose having a viscosity of ˜6.0 cPs, wherein the concentration of hydroxypropylmethylcellulose in the aqueous composition is from 10 ° C. to 1.0 ° C. at the temperature at which the aqueous composition gels; The viscosity of the aqueous composition measured at the lower temperature is 100
0 to 3000 cPs, preferably 1200 to 2500 cPs, more preferably 1600
Selected to be 2000 cPs,
(B) preheat the dip pins so that they are 55-95 ° C when they are immersed in the aqueous composition;
(C) immersing the preheated dip pin in an aqueous composition maintained at a temperature between 10 ° C. and 1.0 ° C. below the temperature at which it gels;
(D) pull the dip pin from the aqueous composition to obtain a film on the dip pin, and (e) dry the film on the dip pin at a temperature above the gelation temperature of the aqueous composition and mold it on the pin Get a capsule shell.

Steps (a) and (b) can be performed in any order. In contrast, step (c)
~ (E) should be performed in the order shown and after steps (a) and (b).
In the step (a), the aqueous composition of the present invention can be used. Adjustment of the HPMC concentration optimization can be carried out along the viscosity range indicated above.

In step (b), the temperature range of the preheated pin is 55 to 95 ° C., which means that this is the temperature of the pin when the pin is immersed. This temperature is preferably 60-90 ° C.
More preferably, it is 60-85 degreeC, More preferably, it is 65-85 degreeC, More preferably, it is 70-80 degreeC. The temperature is preferably selected according to the desired capsule size. By “according to capsule size”, the smaller the pin dimensions, the higher the temperature. For example, for HPMC type 2906 (USP classification) and within the HPMC weight range defined above for aqueous compositions, the pin temperature is between 70 and 80 for capsule size 00 (generally considered large capsule size) Preferably, for capsule size 1 (generally considered a medium capsule size), the pin temperature is preferably between 80 and 90, and capsule size 4 (typically a small capsule size and The pin temperature is preferably between 85 and 95.

In the step (c), the immersion composition has a gelling temperature of 10 ° C. to 1.0 ° C., preferably 6
It is maintained at a temperature of from 0C to 2.0C. For example, if the dipping composition has a gelling temperature of about 36.0 ° C., it can be maintained at a temperature of about 34.0 ° C., for example.

After withdrawal from the dipping composition, the pin can be rotated from a dipping position “tip down” to a dry position “tip up” according to common capsule molding methods. In this step, the pin rotates about 180 ° around the horizontal axis with respect to the immersion position of step (c).

In drying in step (e), the objective is to reduce the water content in the capsule shell on the pin. In general, the water content in the molded capsule shell is reduced from approximately 80% by weight to approximately 7% by weight, based on the total weight of the molded capsule shell. The index of the water content in the capsule shell of the present invention is shown below.

Step (e) can be carried out according to any technique generally known for this purpose, for example by placing the pins in a typical oven for a sufficient time, generally 30-60 minutes.

In a preferred embodiment, step (e) comprises a co-pending patent application filed by the applicant on October 26, 2006 having the title “Formation of capsules” and having application number US60 / 863,040. Is performed as disclosed. According to its preferred embodiment, it has been found that excellent results are obtained when the film is placed under a special combination of temperature and relative humidity.

Accordingly, the step (e) preferably includes the step (e1), and the capsule shell formed with the dip pin in this step has a temperature of 50 to 90 ° C. at RH 20 to 90%, preferably R
T is 55 to 85 ° C at H20 to 70%, more preferably T at RH20 to 60%.
Is placed under 60-85 ° C.

In general, the period of step (e1) is 90 to 480 seconds, preferably 120 to 300 seconds, more preferably 120 to 240 seconds.
Step (e1) is preferably followed by step (e2), in which the pin is RH2
The temperature is 30 to 60 ° C. at 0 to 90%, preferably T is 35 to RH at 20 to 70%
T is placed below 35-50 ° C. at 55 ° C., more preferably RH 20-60%.

In general, the period of step (e2) is 30 to 60 minutes.
Steps (e1) and (e2) can both be performed in an oven. The oven used is preferably a tunnel that allows continuous processing.

The term “relative humidity” is used herein to mean the ratio of the actual water vapor pressure at a given temperature to the vapor pressure that would occur if air was saturated at the same temperature. There are many techniques for humidity measuring instruments known to technicians, all of which will provide substantially the same RH measurement.

In the present specification, unless otherwise indicated, “capsule” means a hard capsule composed of a body and a cap, which are two parts connected in the same fitting manner. Typically, the cap and body have side walls, open ends and closed ends. The length of each side wall of these parts is generally greater than the diameter of the capsule. Therefore, the HPMC of the present invention
Hard capsules do not depart structurally from the general definition of hard capsules. “Capsule” refers to both empty and filled capsules.

The molded capsule shell generally refers to both the body and the cap, depending on the shape of the molding pin. Thus, after step (e), the dried capsule shell on the dip pin can be processed according to a general process. This generally means that after step (e), the capsule shell (body and cap) is peeled from the pin. This step can be followed by cutting the peeled shell to the desired length.

Generally, hard capsule dip molding manufacturing methods include an additional step of lubricating the pin to facilitate peeling of the capsule shell from the pin. Lubrication is usually accomplished by applying a release agent to the surface of the pin.

In the present invention, any release agent and lubrication device generally used for HPMC capsules can be used.
After peeling and cutting, the body and cap may be combined to obtain a complete capsule. The caps and body of the capsules are preferably joined together so that their side walls partially overlap to obtain a capsule.

“Partially overlapping” means that the side wall of the cap and the body have substantially the same length so that the entire side wall of the body fits into the side wall of the cap when the cap and the body are fitted together. Including. This embodiment is particularly advantageous for the manufacture of capsules that are not tampered with, for example for use in the context of a double-blind test.

In one embodiment, the dip pin is designed to provide a means to pre-lock to the cap and body formed thereon. Suitable pin designs and means for pre-locking are disclosed, for example, in EP110500B1, in particular in the second row, lines 27-31 and for example in FIG. If the cap and body are provided with means for pre-locking, the body and cap obtained after peeling are first combined to obtain a pre-locked capsule. The pre-locked capsule is then reopened, filled and combined to its final position.

Once filled, the capsules can be tampered with fraudulently by using any solution commonly used to make the bond permanent in the hard capsule field. Banding or sealing is a suitable technique. Sealing is a technique well known in the field of hard shell capsules. Various alternative techniques are currently used for this purpose. Suitable methods are disclosed for example in US 4,539,060 and US 4,656,066. Many improved sealing methods are currently available.

According to one known sealing method, the capsule is contacted with (i) sealing liquid, (ii) excess sealing liquid is removed from the surface, and (iii) the capsule is dried to cause hardening and make the seal permanent.

For the HPMC capsules obtained according to the invention, an alcohol / water mixture, for example an ethanol / water mixture, can be used as the sealing liquid.
The excellent sealing quality obtained makes the sealed capsules of the invention particularly suitable for the production of leak-proof dosage forms, particularly for use in the administration of substances in liquid form. By “sealing quality” is meant either the visual quality of the seal and / or the adhesive strength.

The above aqueous compositions and methods are particularly suitable for the production of HPMC hard capsules that dissolve at a rate comparable to common gelatin capsules. The capsules can be produced at processing speeds comparable to gelatin capsules on an industrial scale. Because they are less brittle, especially under extremely dry atmospheres, their mechanical properties are superior to that of common gelatin capsules. Their visual appearance is similar to that of gelatin capsules.

In a third aspect, the present invention relates to a methoxy content of 27.0 to 30.0% (w / w), a hydroxypropoxy content of 4.0 to 7.5% (w / w), and water at 20 ° C. For HPMC hard capsule shells containing HPMC having a viscosity of 3.5-6.0 cPs as a 2% by weight solution, where the content of methoxy and hydroxypropoxy is USP30-NF
The viscosity is measured according to the USP method for cellulose derivatives.

In a preferred embodiment, the capsule shell can be obtained by the aqueous composition and / or method disclosed above.
In a preferred embodiment, the capsule shell comprises HPMC in an amount between 70 and 99% by weight, preferably between 80 and 99% by weight, based on the weight of the shell. In the absence of other film-forming polymers, HPMC is preferably 92 and 9 based on the weight of the shell.
Between 9% by weight, more preferably between 93 and 98% by weight, even more preferably 94%
And between 97% by weight.

In a preferred embodiment, the capsule shell is 0% by weight and 25% based on the weight of the shell.
Including, by weight, preferably between 0% and 10% by weight of additional non-animal derived film-forming polymer as defined above.

In a preferred embodiment, the capsule shell is between 1-8% by weight, based on the weight of the shell,
Preferably it contains between 7 and 2% by weight, more preferably between 6 and 3% by weight of water.
In a preferred embodiment, the capsule shell is 0 and 10% by weight based on the weight of the shell
Between one and more dyes, such as those discussed above, preferably between 0.001 and 5% by weight, more preferably between 0.01 and 3% by weight.

In a preferred embodiment, the capsule shell is between 0 and 5% by weight, preferably between 0.001 and 3% by weight, more preferably 0.01 and 2% by weight, based on the weight of the shell.
One or more dyes in between.

In a preferred embodiment, the capsule shell is 0 and 10% by weight based on the weight of the shell
Between one and more plasticizers such as those discussed above, preferably between 0.001 and 5% by weight, more preferably between 0.01 and 3% by weight.

In a preferred embodiment, the capsule shell is one type between 0 and 2% by weight, preferably between 0.001 and 1% by weight, more preferably between 0.01 and 0.5% by weight, based on the weight of the shell. Contains the above antibacterial agents.

In a preferred embodiment, the capsule shell is one type between 0 and 2% by weight, preferably between 0.001 and 1% by weight, more preferably between 0.01 and 0.5% by weight, based on the weight of the shell. Including the above flavoring.

In preferred embodiments, the HPMC hard capsule shells disclosed herein can be used for the manufacture of pharmaceutical dosage forms that are not tampered with. For this purpose, it is particularly advantageous if the capsule shell is as disclosed in EP110500B1.
In this preferred embodiment, the HPMC hard capsule shell includes a co-axial cap and body, each of the cap and body having a generally cylindrical sidewall, an open end and a closed end portion, each side wall of this portion being substantially Larger than the diameter of the capsule shell,
The cap and body are adapted for coupling in a telescoping relationship, where when the cap and body are fully coupled in a telescoping relationship, the only exposed portion of the body is a closed end portion, where The closed end portion has an outer surface that is difficult to grasp and thereby prevents separation of the cap and body, wherein when the cap and body are fully connected in a snap-fit relationship, the inner side wall of the cap is external to the body. Substantially completely overlaps the sidewall. In other words, when the cap and the body are fully connected in a snap-fit relationship, the entire side wall of the body fits in the side wall of the cap. In this way, only the closed end of the body is exposed in use,
Provides a minimal surface for grasping and pulling the body out of the cap, thereby preventing separation of the capsule shell.

The closed end portion of either the body or the cap is, for example, generally hemispherical, pyramidal,
It may have a conical or flat shape.
For added safety, the body and cap preferably further include interlocking means including one or more circumferentially extending ridges and / or grooves. Thus, depending on the situation, the capsule shell may have a cap and one side wall of the body either (i) radially inward from the inner surface of the cap side wall or (ii) radially outward from the outer surface of the body side wall , One or more circumferentially extending ridges may be included to provide a combined means.

Alternatively or in addition, the cap and the other side wall of the body can be (i)
One or more circumferentially extending grooves that extend either radially inward from the outer surface of the body or (ii) radially outward from the inner surface of the cap and engage with each ridge. Have.

The capsule shell further includes venting means for allowing air to escape from within the capsule when joined, wherein the or each circumferentially extending ridge is between the segments. Preferably, the space between them includes two or more segments that function as vents to allow air to escape from within the capsule when joining the cap and body.

Depending on the situation, one side wall of the cap and body extends either (i) radially inward from the inner surface of the cap side wall or (ii) radially outward from the outer surface of the body side wall. Preferably has a notch defining a portion of the opposite pair of diameters;
The spacing along the notch diameter is in the case of (i) outside the open end of the body so that the body can enter the cap so that air can escape from inside the capsule when the cap and body are joined. It is smaller than the diameter, and in the case of (ii) it is larger than the diameter inside the open end of the cap.

For storage and / or transport purposes, the capsule shell also includes means for pre-locking the cap and body partially bonded in a stable predetermined relative position prior to filling and final bonding. It may be preferable. This embodiment is particularly advantageous when it is desired to include step [l-1] of the method of the present invention.

To avoid contact when the body is snapped into the cap,
The diameter is preferably reduced at the open end.
Alternatively, or in addition, as additional resistance to tampering with the cap, the caps are reduced in diameter at their open end portions, thereby providing a portion of the body sidewall adjacent to them and the closed end portion of the body. And improved meshing.

In a fourth aspect, the present invention provides a capsule shell as defined above and 1 filled therein
It relates to a HPMC hard capsule containing more than one kind of substance.
All kinds of suitable compounds may be filled in the capsules of the present invention, including pharmaceuticals, vitamins or nutrients, plant powder extracts, etc., especially containing hygroscopic ingredients.

When used as a dosage form for a medicament, the capsules of the invention generally comprise from 0.001 g to 2.0 g of active ingredient, for example optionally mixed with one or more pharmaceutically acceptable excipients.

In one embodiment, the optionally sealed HPMC hard capsules disclosed herein can be used in the context of dry powder inhalation (also commonly known as DPI with the acronym). In this aspect, the superiority of the capsules disclosed herein over common HPMC capsules can be based, for example, on the following points:
・ Capsule has improved color / transparency,
-The stickiness of the inner surface of the side wall of the cap and the main body is reduced, for example, by reducing the amount of release agent required in the capsule manufacturing process,
-The sealing quality of the capsule is improved.

All of the capsule embodiments disclosed above can be produced on a typical capsule making machine utilizing dip molding techniques. The technician can find additional background information on dip molding methods for gelatin capsules in US 4,893,721.

In a fifth aspect, the invention relates to hydroxypropyl methylcellulose hard capsule shells and capsules as defined above for use in the administration of substances in liquid or solid form, in particular pharmaceutical substances, to a subject.

In a sixth aspect, the invention relates to the use of a hydroxypropylmethylcellulose hard capsule shell and capsule as defined above for the manufacture of a pharmaceutical dosage form suitable for administration to a subject of a pharmaceutical substance in liquid or solid form. .

“Solid form” preferably means powder form, substance (may be more than one type)
The administration of may preferably involve the use of a dry powder inhaler.
By "subject" is preferably meant a human or animal subject, more preferably a human subject.

Preferred conditions for providing the above composition also apply to other objects of the invention discussed above, such as methods and capsules.
The scope of the invention can be better understood with reference to the following examples, the purpose of which is to illustrate the advantages of the invention. Unless otherwise noted, all parts and percentages are by weight. The viscosity of the composition was measured with a Brookfield viscometer.

Example 1: Aqueous composition for the production of hydroxypropylmethylcellulose hard capsules HPMC type 2906 with a concentration of 2% (w / w) and a viscosity of 4.4 cPs (methoxy content 28.7%, hydroxypropoxy content) Composition 5k containing 18.8%)
g was prepared as follows:
Disperse HPMC powder in hot water stirring at 75 ° C. Foam formation is observed. After the powder is completely dispersed, it is kept at 75 ° C. with very gentle stirring to degas the dispersion. The dispersion is then cooled to 10 ° C. with gentle stirring to dissolve the HPMC. After keeping the composition at 10 ° C. for 30 minutes or more, a dipping composition ready for use in capsule production is obtained.

The gelation temperature of the HPMC composition was determined by gradually heating the composition and measuring the viscosity. The gelation temperature found was 34 ° C.

Example 2: Production of hard capsules The composition produced in Example 1 is poured into a dipping pan of a pilot device for the production of hard capsules.
A size 0 dipping pin is preheated at 75 ° C, while the dipping composition is maintained at 32 ° C. At this temperature, the viscosity of the dipping composition is 2000 cPs. Size 0 capsules are manufactured by conventional dipping methods, but use preheated pins. After soaking, the capsule is placed in the oven for 60
Dry with hot air at 0 ° C. and 40% RH for 3 minutes, then dry with hot air at 40 ° C. and 40% RH.

The resulting capsule is of high quality: good quality and standardized dimensions (top wall thickness is 1
Greater than 40 μm), high transparency (similar to hard gelatin capsules), excellent solubility and mechanical performance.

Example 3 Preheating Temperature Optimal for Pins Example 2 was performed again, but using immersion pins preheated at 60 ° C. instead of 75 ° C. Note that pin size 0 is considered a medium to large size.

Gelation on the pins after immersion was not optimal to obtain a commercially acceptable capsule. During drying, the solution partially flows out of the pin so that the apex wall thickness is 50
It became less than μm.

Conclusion: 60 ° C. as the preheating temperature for the pins was less preferred than 75 ° C. for the production of size 0 capsules.

Example 4: Mechanical properties of Example 2 capsules under stress conditions The mechanical properties of the capsules of Example 2 were tested under the following stress conditions:
A stainless steel cylinder weighing 100 g was dropped onto an empty capsule one by one from a height of 8 cm. The percentage of capsules broken is reported below.

  result:

RH = relative humidity Conclusion: The capsule of Example 2 does not show any brittleness even at extremely low relative humidity.

Example 5: In vitro dissolution performance of capsules of Example 2 The capsules of Example 2 were tested according to the USP monograph method for dissolution of acetaminophen capsules.

  result:

Example 6: Determination of Gelation Temperature A 18.8% w / w solution of HPMC Model 2906 in water was prepared as described in Example 1. Viscosity is measured at different temperatures using a Brookfield DV-II viscometer by increasing the temperature of the measuring cell stepwise (equilibrated for 10 minutes at each step). Results are reported in the graph below. It can be readily seen that the gelation temperature is approximately 34 ° C.

Comparative Example 1: Manufacture of capsules using HPMC 2910 type As in Examples 1 and 2, 2% HPMC 2910 type 2% viscosity 3cPs
5 kg of a composition containing 6.3% was produced. The gelling temperature is found to be 47 ° C while the soaking composition is maintained at 45 ° C. Under the same processing conditions as in Example 2 above (
The immersion composition at 45 ° C. had a viscosity of 2000 cPs), and a size 0 capsule was produced.

Result: Acceptable dimensions were obtained (top wall thickness exceeds 140 μm). However, almost all capsules broke during the peeling of the dip pins, resulting in capsules that were too brittle.

Comparative Example 2: Production of capsules using HPMC type 2910 As in Examples 1 and 2, HPMC type 2910 with a viscosity of 2 c and a viscosity of 6 cPs was used.
5 kg of a composition containing 7.9% was produced. The gelling temperature is found to be 50 ° C, while the soaking composition is maintained at 48 ° C. Under the same processing conditions as in Example 2 above (
Viscosity of the immersion composition at 48 ° C. was 2000 cPs), and a size 0 capsule was produced.

Results: Unacceptable dimensions were obtained (insufficient gelation behavior, the composition on the pins partially shed and the apex wall thickness was less than 80 μm). Thus, there was an advantage in the use of HPMC 2906 over the use of other HPMCs such as HPMC 2910.

Comparative Example 3: Manufacture of capsules using an immersion solution whose viscosity is too low Example 2 was performed again, but an immersion solution having a viscosity of 900 cPs measured at 32 ° C was used. This decrease in viscosity was obtained by adding water to the composition.

Gelation on the pins after immersion was not sufficient and the solution flowed down during drying, which resulted in a peak wall thickness of less than 50 μm, which was too small to tolerate. Results: The viscosity of 900 cPs for the dipping solution is too small to have acceptable gelling ability and apex wall thickness.

Claims (17)

3. Methoxy content 27.0-30.0% (w / w), hydroxypropoxy content 4.
3.5-6.0 as a 2 wt% solution in water at 0-7.5% (w / w) and 20 ° C
An aqueous composition for the production of hard capsules, characterized in that it comprises 15-25% by weight of hydroxypropylmethylcellulose (HPMC) having a viscosity of cPs in an aqueous solvent, based on the total weight of the aqueous composition. 4.0% as a 2 wt% solution of hydroxypropylmethylcellulose in water at 20 ° C
The composition according to claim 1, characterized in that it has a viscosity of ˜5.0 cPs. 3. Composition according to claim 1 or 2, characterized in that it comprises 17-23% by weight of hydroxypropylmethylcellulose, based on the total weight of the aqueous composition. The composition according to claim 1, wherein the aqueous solvent is water. Method for the production of hydroxypropylmethylcellulose hard capsules according to the dip coating method, characterized in that it comprises the following steps:
(A) As a 2% by weight solution in water at 20 ° C. with a methoxy content of 27.0-30.0% (w / w), a hydroxypropoxy content of 4.0-7.5% (w / w) 3.5
Preparing an aqueous composition of hydroxypropylmethylcellulose having a viscosity of ˜6.0 cPs, wherein the concentration of hydroxypropylmethylcellulose in the aqueous composition is from 10 ° C. to 1.0 ° C. at the temperature at which the aqueous composition gels; The viscosity of the aqueous composition measured at the lower temperature is 100
Selected to be 0-3000 cPs,
(B) preheat the dip pins so that they are 55-95 ° C when they are immersed in the aqueous composition;
(C) immersing the preheated dip pin in an aqueous composition maintained at a temperature between 10 ° C. and 1.0 ° C. below the temperature at which it gels;
(D) pull the dip pin from the aqueous composition to obtain a film on the dip pin, and (e) dry the film on the dip pin at a temperature above the gelation temperature of the aqueous composition and mold it on the pin Get a capsule shell. The method according to claim 5, characterized in that the aqueous composition of step (a) is the aqueous composition as defined in any one of claims 1-5. The method according to claim 5 or 6, characterized in that the temperature of the preheated pin is 60-90 ° C. The method according to any one of claims 5 to 7, characterized in that the aqueous composition of step (b) is maintained at a temperature below its gelling temperature of 4 ° C to 1.0 ° C. The method according to any one of claims 5 to 8, characterized in that step (e) comprises the following steps:
(E1) Place the pin under a temperature of 50-90 ° C. and a relative humidity of 20-90%. 10. A method according to claim 9, characterized in that the temperature is 55 to 85 [deg.] C and the relative humidity is 20 to 70%, preferably 60 to 85 [deg.] C and the relative humidity is 20 to 60%. The method according to any one of claims 8 to 10, wherein the period of step (e1) is 90 to 480 seconds. The process according to any one of claims 8 to 11, comprising the following process downstream of the process (e1).
Method described in section:
(E2) Place the pin under a temperature of 30-60 ° C. and a relative humidity of 20-90%. The method of claim 12, wherein the period of step (e2) is between 30 and 60 minutes. 3. Methoxy content 27.0-30.0% (w / w), hydroxypropoxy content 4.
3.5-6.0 as a 2 wt% solution in water at 0-7.5% (w / w) and 20 ° C
A hydroxypropylmethylcellulose hard capsule shell, characterized in that it comprises hydroxypropylmethylcellulose having a viscosity of cPs. Capsule shell according to claim 14, characterized in that it comprises hydroxypropylmethylcellulose in an amount between 70% and 99% by weight, based on the weight of the shell. A capsule shell obtained by the method defined in any one of claims 5 to 13. A hydroxypropyl methylcellulose hard capsule comprising the capsule shell as defined in any one of claims 14 to 16.