|Publication number||US3873694 A|
|Publication date||Mar 25, 1975|
|Filing date||Sep 27, 1973|
|Priority date||Sep 27, 1973|
|Publication number||US 3873694 A, US 3873694A, US-A-3873694, US3873694 A, US3873694A|
|Inventors||Joseph L Kanig|
|Original Assignee||Cpc International Inc|
|Export Citation||BiBTeX, EndNote, RefMan|
|Patent Citations (9), Referenced by (45), Classifications (25), Legal Events (3)|
|External Links: USPTO, USPTO Assignment, Espacenet|
United States Patent [1 1 Kanig 1 DIRECT COMPRESSION TABLETTING COMPOSITION AND PHARMACEUTICAL TABLETS PRODUCED THEREFROM  Inventor: Joseph L. Kanig, Westbury, NY.
 Assignee: CPC International Inc., Englewood Cliffs, NJ.
 Filed: Sept. 27, 1973  Appl. No.: 401,322
 US. Cl 424/127, 424/154, 424/155,
 Int. Cl. Cl3f 3/00  Field of Search 127/29, 30, 63; 426/214, 426/217, 213; 424/127  References Cited UNITED STATES PATENTS 3,140,201 7/1964 Reimers 127/30 X 3,169,888 2/1965 Ryan 127/30 3,305,447 2/1967 I Reimers... 127/30 3,589,909 6/1971 Godzicki 426/214 3,619,292 11/1971 Brouillard 127/29 3,627,583 12/1971 Troy 426/217 X 3,639,168 2/1972 Monti 127/29 Mar. 25, 1975 3,639,169 2/1972 Broeg 127/29 3,642,535 2/1972 Graham 127/29 FOREIGN PATENTS OR APPLICATIONS 1,286,275 23/1912 tinged Kingdom OTHER PUBLICATIONS H. David Bergman et a1., Drug and Cosmetic Industry, 109(3), 48, 50, 56, 58, 156, 157, (Sept. 1971).
Primary Examiner-Morris O. Wolk Assistant ExaminerSidney Marant; Attorney, Agent, or FirmAlbert P. l-Ialluin 57 ABSTRACT Method for producing a direct compression vehicle for tabletting which involves admixing a crystalline sugar with a maltodextrin and spraying the admixture with an aqueous solution of a maltodextrin. The resulting vehicle may be combined with a pharmaceutically active ingredient wherein the pharmaceutically active ingredient may be present in an amount of up to 80% of the weight of the vehicle. The resulting pharmaceutical composition can be compressed into a tablet having a Strong Cobb Hardness Unit (S.C.H.U.) value of at least about 6.
25 Claims, N0 Drawings DIRECT COMPRESSION TABLETTING COMPOSITION AND PHARMACEUTICAL TABLETS PRODUCED THEREFROM BACKGROUND OF THE INVENTION 1. Field of the Invention:
This invention relates to direct compression tabletting compositions and the pharmaceutical tablets produced therefrom. More particularly, this invention relates to an improved direct compression tabletting composition prepared from a uniquely granulated mixture of a crystalline sugar such as dextrose monohydrate, and a maltodextrin having a measurable dextrose equivalent value not substantially above about 20. The improved direct compression tabletting compositions are capable of being directly compressed into commercially acceptable and hard tablets with large amounts of a variety of active materials. The new direct compression tablets can be used as the sole binder disintegrant without the aid of other adjuvants ordinarily used for this purpose.
2. Description of the Prior Art:
The compressed tablet is the most popular unit dosage form for medicinal substances. The tablet as a dosage form can be traced to well over 1,000 years ago when a procedure for molding solid forms containing medicinal ingredients was recorded. As a result of the introduction of new carriers and compression vehicles, tablets are replacing all forms of pills, powders and capsules. Accordingly, tablets presently represent the largest production volume of all pharmaceuticals.
The reason for the widespread use of tablets is apparent, since tablets enable: (1) administration of medication in an accurate dose, (2) fast and accurate dispensing with less chance of error and contamination, (3) ease of administration, (4) administration in a form in which the time and area of contact between'the active ingredient and the taste buds is reduced, thus obviating the physiological problems associated with the oral administration of drugs that possess a bitter taste and, in the case of coated tablets, with drugs that possess a dis agreeable odor, (5) release of drugs at specific loca tions in the gastro-intestinal tract to: (a) prevent degradation of drugs sensitive to the low pH environment in the stomach, (b) prevent release of drugs that irritate the gastric mucosa in the stomach, (c) facilitate local action or preferential absorption at specific sites in the tract, (6) enhance stability by effecting a marked reduction in the surface of the drug exposed to the environment, (7) rapid production, and (8) economy and ease in storage, packaging and shipping.
It is well-known that in order to form a tablet of a given material, the material must possess fluidity and compressibility. lt is essential that the material must flow uniformly from the hopper to the dies of the tablet press. Any defective flow of the material will effect the weight of the tablets, content uniformity, disintegration time, hardness, friability, and also the bioavailability of the active ingredient.
There are currently three basic methods for tablettin g. They are the wet granulation method, the dry granulation method, and the direct compression method. The direct compression method is by far the desired method from the standpoint of processing procedures, equipment and materials. However, only a very limited number of pharmaceutically used substances possess enough cohesive strength and flowability to allow direct compression without previous granulation. Certain crystalline materials, such as potassium bromide and potassium chloride can be compressed without preliminary treatment. Also, aspirin, phenolthaline, chlorohydrate can be directly compressed.
It has been stated that the ideal material to compress would be composed of crystals which, at the moment of compression, behaved like clay rather than rubber. The crystals should be such that on release of pressure they should not rebound into their original shape. Generally, most materials possess both plastic and elastic deformation properties. Therefore, most materials are not suitable for direct compression without previous granulation.
It has been estimated that about 20% of the materials used for tabletting in the pharmaceutical field may be compressed directly. In order to use this method to a considerable extent, many more materials should be modified by treatment or by use of additives. Modification may be undertaken, either by treating the material in some special way during earlier stages of preparation, or by adding a binder or excipient material which will surround the active ingredient and form an easily compressible carrier.
An ideal direct compression vehicle should possess the following properties: (1) low elastic modules, (2) high dislocation density, (3) inert, non-potent and nontoxic, (4) high degree ofplastic deformation, (5) colorless, odorless, tasteless or without disagreeable taste, (6) free-flowing, (7) compatible with active ingredients and common additives like lubricants, colors, etc., (8) non-hygroscopic, or relatively low order of hygroscopicity, (9) fast disintegration properties, or should not delay the bioavailability of the drug, l0) limited range of particle size distribution, l l) stable effects of aging, and (12) reworkable and should possess high carrying capacity for active medicinal agents.
There are currently several available direct compression vehicles. They include spray-dried lactose; anhydrous lactose; microcrystalline cellulose; dicalcium phosphate dehydrate, unrnilled; Cellutab; spraycongealed mannitol; Emcompress; Magnapol', Frodex; Di Pac; and Royal-T.
Microcrystalline cellulose is a natural cellulose in a specially processed form which makes it digestible. lt normally produces good tablets with fast disintegration and drug release properties. lt has been found to give better results if stored in a dry condition before use exposure to a slightly humid atmosphere makes it compress less easily. It is quite fluffy by nature.
Spray-dried lactose has a heavy appearance when poured and is spherical in shape. It cannot be re worked, as the spherical shape is lost when ground. lt has been disclosed that spray-dried lactose with 5-10% maize starch as a disintegrant and 0.5% magnesium stearate as a lubricant forms a useful direct compression base. However, it has the tendency to get brown in the presence of moisture, amines, phosphates, lactates and acetates. Borates and the stearate lubricants tend to retard the browning.
Dicalcium phosphate dehydrate has good flow and compressibility properties. The tablets from dicalcium phosphate are also easily embossed. The increased flow is believed to be due to its high density. It cannot be re worked. Due to its alkaline pH, stability of ingredients like Vitamin C or aspirin may be effected.
The vehicle mannitol, absorbs heat from the surroundings when going into solution, and results in good mouth feel." Thus, it is commonly used in chewable tablets. It has been reported that a change in the compression characteristics of mannitol occurs when spraycongealing the product.
The vehicle known in the art as Cellutab is a spraydried dextrose product. It has excellent flow characteristics. It is relatively coarse compared to other vehicles and contains approximately 8% moisture.
The product known in the art as Encompress is essentially a blend of dicalcium phosphate dehydrate, unmilled; starch; Avacil; and magnesium stearate. It is free-flowing, self-lubricating and possesses good compression characteristics.
The vehicle known in the art as Royal-T is essentially an agglomerated mixture of a crystalline sugar such as dextrose and a maltodextrin such as Mor-Rex Code 1918. The preparation of this bold and new pioneering discovery in the direct compression vehicle art is described in British Pat. No. 1,286,275, published Aug. 23, 1972 which generally corresponds to pending U.S. application Ser. No. 485,480, filed July 3,1974, which is a continuation-in-part of abandoned U.S. application Ser. No. 254,552, filed May 18, 1972, which in turn is a continuation-in-part of abandoned U.S. application Ser. No. 141,030, filed May 6, 1971, and which in turn is a continuation-impart of abandoned U.S. application Ser. No. 767,520, filed Oct. 14, 1968.
The vehicle known in the art as Di Pac is also a mixture of a crystalline sugar and a maltodextrin. The preparation ofthis product is generally described in the aforesaid British patent and, more specifically disclosed in U.S. Pat. No. 3,642,535, granted Feb. 15, 1972.
Although the direct compression method for preparing tablets is by far the method of choice by virtue of its simplicity, this method has several limitations which have hampered its use in the tabletting industry. These limitations include: (1) differences in the particle size, and bulk density between the diluent and the active ingredient may lead to stratification and variation in drug content of tablets, (2) unless the drug itself is easily compressible, the amount present is limited to a maximum of 25% of the tablet weight (Of course, the amount of vehicle and the weight of the tablet may be increased to reduce the percentage of active ingredient. Then there arises a question of economics and size of the tablet, a question that may be resolved only by wet granulation), (3) the drug may interact with the vehicle, such as amine compounds do with spray-dried lactose, and (4) static charges which may develop on the drug during combination and mixing may prevent uniform distribution.
In light of the limitations mentioned hereinabove, the great percentage of tabletting operations, therefore, have been forced to resort to other formulation techniques such as the wet and dry granulation methods. Thus, there is a continued search for an improved direct compression tabletting composition capable of being employed as a binder in the preparation of tablets by direct compression which are rapidly disintegrative, resistant to breakage and crumbling and compatible with the active material incorporated therein which forms the basis of the compositions utility.
SUMMARY OF THE INVENTION measurable dextrose equivalent value not substantially above about 20 to form a uniform admixture and thereafter concurrently agitating and spraying said admixture with an aqueous solution containing dissolved therein the aforesaid maltodextrin having a measurable dextrose equivalent value not substantially above about 20, said aqueous solution of dissolved maltodextrin being present in an amount sufficient to provide a damp mass of said uniform admixture and to cause binding and granulation of said uniform admixture. The granulated mixture is thereafter dried to a moisture content of less than about 10% by weight.
The preferred direct compression compositions of this invention will contain from about 15% to about 35% by weight of said maltodextrin, preferably from about 20-30% by weight of said maltodextrin. The preferred crystalline sugar utilized includes dextrose monohydrate.
It has been found that when a crystalline sugar such as dextrose monohydrate is granulated with at least about 15% by weight of a maltodextrin having a measurable dextrose equivalent value not substantially above 20, the composition has an exceptionally high carrying capacity for a large variety of pharmaceutically active compounds. This result is quite unexpected, inasmuch as the compositions described in British Pat. No. 1,286,275 have a relatively low carrying capacity for most pharmaceutically active compounds. Thus, the compositionsof this invention provide a direct compression vehicle which can be directly compressed into commercially acceptable and hard tablets with large amounts of a variety of active materials and can be used as the sole'binder disintegrant without the aid of other adjuvants ordinarily used for this purpose.
DESCRIPTION OF THE PREFERRED EMBODIMENTS The crystalline sugars employed in the practice of the present invention include any type of crystalline sugar product, examples of which include dextrose, sucrose, lactose and blends thereof. Many of these crystalline sugars are wellknown in the art and are conventional articles of commerce sold under various trade names. Such sugars are generally produced and crystallized by conventional techniques. The preferred crystalline sugar employed in the practice of the present invention is dextrose, either in its monohydrate, anhydrous or dehydrated form. Dextrose monohydrate is particularly preferred as the crystalline sugar to be utilized in the practice of the invention.
The maltodextrins having a measurable dextrose equivalent value not substantially above about 20 utilized in the practice of the present invention represent a known class of materials. The maltodextrins are also known as hydrolyzed cereal solids and such materials are commercially available under the tradenames Mor- Rex, manufactured and sold by CPC lnternational lnc., Maltrin. manufactured and sold by Grain Processing Corporation, Frodex, manufactured by American- Maize Products Company, and Star-Dry l5, manufactured by A. E. Staley Manufacturing Company.
The terms maltodextrins" and hydrolyzed cereal solids" herein refer to those starch conversion products having a relatively small amount of dextrose and maltose. Generally, the dextrose content of the maltodextrins in less than about 2.4% by weight and the amount of maltose is less than about 9% by weight. As it is wellknown in the industry, the dextrose equivalent value in a starch conversion product having a value above about 20 is generally referred to as a corn syrup solid; whereas starch conversion products having only a trace amount of dextrose are referred to as dextrins. The starch conversion products having a measurable dextrose equivalent value not substantially above about 20 and also having a trace amount of dextrose as hereinabove referred to, are known as hydrolyzed cereal solids or maltodextrins. lt is the maltodextrins described hereinabove which are employed in the practice of this invention for the preparation of the direct compression tabletting compositions. The corn syrup solids having a dextrose equivalent value greater than about 20 are not suitable in the practice of the present invention, since these products do not possess the proper properties to effectively cause granulation and thereby produce a tabletting composition having a high carrying capacity for the active material. The corn syrup solids are also extremely hygroscopic, a property undesirable from the standpoint of flowability and mixing during the direct compression procedure for preparing the tablets.
The preferred maltodextrins or hydrolyzed cereal solids employed in the practice ofthe present invention are characterized as having a descriptive ratio of at least about 2. The descriptive ratio is the sum of the percentages (dry basis) of saccharides of the maltodextrin with a degree of polymerization of l to 6 divided by the dextrose equivalent value. An especially preferred class of maltodextrins employed in the practice of the present invention are derived from waxy starch hydrolysates and have a dextrose equivalent value in the range of from about 9 to about 13 and a descriptive ratio of at least about 2. These starch hydrolysates or maltodextrins are prepared by the method disclosed in British Pat. No. 1,203,048, particularly Examples 111 and IV, and the corresponding disclosure and claims in U.S. application Ser. No. 181,566, filed Sept. 17, 1971, US. Pat. No. 3,849,194, granted Nov.- 19, 1974 the disclosure of which is incorporated herein by reference. These waxy starch hydrolysates or maltodextrins are commercially available under the tradename of Mor- Rex Code 1918, manufactured and sold by CPC lnternational Inc.
The term measurable dextrose equivalent value (D.E,) referred to herein, is defined as the reducing value of the hydrolysate material compared to the re as percent, dry basis, i.e.,
Reducing Value of Hydrolysate Material Reducing Value of Dextrose x In the above equation, an equal Weight of each of dextrose and the hydrolysate material is involved. The term dextrose equivalent value of a starch hydrolysate is a common expression in the art for describing the total reducing sugars content of a material calculated as dextrose and expressed as percent, dry basis.
An essential aspect of the invention comprises admixing (e.g., by spraying or by any other convenient means) an aqueous solution containing from about 5 to about 60 weight/volume percent of the abovedescribed maltodextrin with a uniform mixture of a crystalline sugar and 10 to about 50% by weight of the above-described maltodextrin. The admixing of the aqueous solution of the maltodextrin should be conducted while the uniform mixture of the crystalline sugar and the maltodextrin is being agitated to achieve uniform and homogeneouscontact of the crystalline sugar particles and the maltodextrin with the aqueous solution containing the maltodextrin. Preferably, the aqueous solution will contain from about 10 to about 30% weight/volume of the maltodextrin.
The solution containing the maltodextrin is preferably admixed with the uniform mixture of the crystalline sugar and maltodextrin at ambient temperatures and pressures. Slight deviations may be imposed, provided that such conditions do not adversely affect the compositions.
The amount of the solution containing the maltodex trin utilized may vary, depending on the characteristics of the crystalline sugar, the amount of moisture in the homogeneous mixture of the crystalline sugar and/or the maltodextrin, etc. Generally, the amount of the aqueous solution containing the maltodextrin utilized will be an amount such that its admixture with all of the materials provides a thoroughly admixed damp mass. Such amounts will generally be in the range of from about 20 ml. to about ml.' of the aqueous solution per one kilogram (kg) of the uniform mixture of the crystalline sugar and the maltodextrin. A suitable damp mass can be obtained under ordinary conditions utilizing from about 40 ml. to about 60 ml. of the aqueous solution per one kilogram (kg) ofthe uniform mixture.
After the aqueous solution containing the maltodextrin is added to the uniform mixture of the crystalline sugar and the maltodextrin, the entire admixture is thoroughly mixed to cause granulation. The granulated product is thereafter dried to a moisture content of less than about 10% by weight, preferably less than about 5% by weight moisture. The dried granulated product may be screened to provide a more homogeneous screen size. The final dried and screened product can be used as is as a direct compression tabletting composition whereupon it can simply be admixed with the desired active material and directly compressed into tablets.
The crystalline sugar hereinabove described may be admixed in either dry or wet form with the maltodextrin. Preferably, the crystalline sugar, e.g., dextrose monohydrate, is employed in its centrifuge cake form following crystallization, which cake has been washed and centrifuged so that the water content in the cake (excluding water of hydration, which, if present, comprises l-l6% of the cake weight) will be sufficient to provide the necessary amount of water to initially granulate the crystalline sugar with the maltodextrin. In this respect, the amount of water necessary to initially granulate the above-described composition of this invention, excluding water of hydration, is preferably from 1-8% by weight of the total composition. The initially granulated admixture may be dried, providing the amount of maltodextrin exceeds about 10% by weight of the total mixture. However, it has been found that in order to provide a direct compression vehicle having a high carrying capacity, it is necessary to spray the admixture of the crystalline sugar and maltodextrin with an aqueous solution containing dissolved therein at least about 5% weight/volume of the maltodextrin.
As stated hereinabove, the amount of maltodextrin employed in the direct compression compositions of this invention is critical. The final composition will generally contain more than about by weight of the maltodextrin which is introduced into the matrix of the crystalline sugar composition, either by the initial blending of the maltodextrin with the crystalline sugar and/or by the admixture treatment with the aqueous solution containing the maltodextrin which follows the blending of the crystalline sugar and the maltodextrin. Preferably, the tabletting composition will contain from about to about 35% by weight of the maltodextrin based on the total amount of the direct compression vehicle. Particularly good results are obtained when the level of maltodextrin in the tabletting composition is in the range of from about to about by weight.
In one typical example of the above-described process of preparing the direct compression tabletting compositions of the present invention, a premix is formed by admixing 80 parts by weight of dextrose monohydrate crystals and 20 parts by weight of maltodextrin having a dextrose equivalent value in the range of from about 9 to about 13, the water content of the mixture being in the range of from about 2 to about 15 by weight. The mixture is thereafter thoroughly agitated and sprayed with an aqueous solution containing the above-described maltodextrin in an amount such that a damp mass is formed. The amount of maltodextrin dissolved in the aqueous solution is preferably l0 to about 40% weight/volume. In a typical example, 50 ml. of a 20% weight/volume aqueous solution contain ing the aforedescribed maltodextrin is sprayed onto 1 kg. of the dextrosemaltodextrin admixture (800 grams of dextrose and 200 grams of maltodextrin). The sprayed mixture is thereafter dried to a moisture content of less than about 10%, preferably less than about 5% by weight. Alternatively, the granulated mixture may be wet screened through a number 6 sieve prior to drying to the final desired moisture content. However, satisfactory results are obtained by drying the granulated mixture prior to screening.
The particle size of the direct compression tabletting composition of the present invention is rather impor tant. Most pharmaceutical compounds have a particle size of less than 100 mesh. Accordingly, the carrier must be coarser or have a particle size larger than the pharmaceutical compound. If the particle size of the direct compression tabletting composition or vehicle is v broadly dispersed, stratification will occur and uniform amounts of ingredients in the respective tablets will not be successfully accomplished. Therefore, it is important that the particle size of the direct compression tabletting compositions of the present invention have a relatively narrow particle size distribution. The particle size distribution found to be most desirable should be such that the particles of the composition fall within the range of 20 to about +200. However, better results are obtained wherein the composition has a particle size in the range from about 30 to about and, more preferably, in the range of from about -40 to about +100.
In the preferred preparation of pharmaceutical tablets by the present invention, an active material ingredient is thoroughly mixed by any suitable dry blending technique with the above-described direct compression tabletting composition in relative amounts required to provide a resultant superficially dry, free-flowing formulation directly compressible into tablets, and the formulation is then tabletted by direct compression.
Active ingredients contemplated to be employed in the preparation of tablets by the present invention constitute all active ingredients compatible with the abovedescribed direct compression tabletting compositions. The present invention is particularly suitable for the use in preparing tablets containing the well-known pharmaceutically active materials. Specific examples of pharmaceutically active ingredients which advantageously may be tabletted by the present invention include ascorbic acid, sodium salicylate, acetaminophen, sodium bicarbonate, aluminum hydroxide, magnesium trisilicate, Vitamin E acetate, calcium lactate, ferrous sulfate and mixtures thereof.
Particularly preferred pharmaceutically active mate rials include ascorbic acid (Vitamin C), acetaminophen (APAP), aluminum hydroxide in combination with sodium bicarbonate (an antacid); citric acid in combination with sodium bicarbonate (an antacid), and magnesium trisilicate in combination with aluminum hydroxide (in a ratio of 2:1, respectively, as another antacid).
The pharmaceutically active materials may be present at relatively high levels in the tablets produced from the vehicles of the present invention. These tablets, even when they contain a high level of the active material, possess acceptable hardness and friability values, not possessed by other sugar-based tablets such as those described in British Pat. No. 1,286,275. The tablets of the present invention may be prepared by direct compression utilizing relatively small amounts of pressure in high speed tabletting machines. Due to the unusual structural integrity of the direct compression tabletting vehicles of the present invention, the vehicles may be simply dry mixed with the desired active materials, and, alternatively with conventional tabletting aids such as fillers, lubricants and the like, to obtain ac tive ingredient-containing formulations which are directly compressible into tablets in conventional tabletting equipment. These directly compressed tablets exhibit the desired hardness and friability even though they are sugar-based compositions. The fact that the tablets are sugar-based and also contain the new relatively tasteless maltodextrins renders the tablets quite suitable for chewable type formulations. In other words, the sugar in the tablets masks the undesirable flavor of many active materials. Thus, the present invention provides pleasant tasting chewable tablets which may contain a high level of active material therein and still have the appropriate hardness and friability necessary for commercial manufacture and shipping of these tablets.
The novel tabletting vehicles of the present invention are also characterized as having properties which satisfy the requirements of a binder for the active material and a disintegrant for the tablet in an aqueous medium. Thus, the compositions of the present invention are capable of being directly compressible into tablets having commercially acceptable hardness, friability and disintegration properties merely by blending the compositions of the present invention with an active material and compressing the mixture with conventional tabletting equipment.
The actual reason why the novel tabletting vehicles of the present invention are capable of carrying relatively high levels of active materials and still maintain commercially acceptable hardness. friability and disintegration properties when directly compressed at low pressures is not fully understood. These unusual properties are not as evident in the agglomerated" dextrose-maltodextrin tabletting compositions described in British Pat. No. 1,286,275. Not wishing to be bound by any theory, it is believed, however, that the addition of the aqueous solution containing the maltodextrin dissolved therein to the uniform mixture of the crystalline sugar and maltodextrin achieves a form of granulation which provides a unique structural integrity in the vehicle. This structural integrity, it is believed, provides a matrix whereby the active material can be locked therein and the resulting composition thereby uniquely possesses a low elastic modules, a high dislocation density and a high degree of plastic deformation. Since the vehicles of the invention are free-flowing, nonhygroscopic and compatible with active ingredients and common additives, as well as having fast disintegration properties, they are excellent direct compression vehicles.
The unique structural integrity of the direct compression vehicles of the invention which makes it possible for the granulated mixture ofa crystalline sugar such as dextrose and from about to about 50% by weight of a water soluble maltodextrin having a measurable dextrose equivalent value not substantially above about 20, wherein said granulated mixture contains less than about 10% by weight moisture, to be capable of being formed into hard, substantially non-friable tablets by direct compression when in admixture with up to 80% by weight of at least one pharmaceutically active ingredient, said tablets have a Strong Cobb Hardness Unit Value (S.C.H.U.) of about 6 or more, and are substantially non'friable.
ln many instances, the tablets of the invention which contain the aforesaid active ingredients will have a hardness value greater than about 7 S.C.H.U. and quite often greater than about 9 S.C.H.U. The hardness values referred to herein are generally obtainable by compressing the dry blended vehicle of the present invention with the active material at pressures as low as 2,000 pounds and, more consistently, such hardness values are obtained when the dry mix is compressed at pressures of 3,000 5,000 pounds (as is generally the case in some commercially available tabletting machines). The hardness and friability properties are further improved when the level of maltodextrin is increased to a value of from -35%, the most preferred levels being in the range of from about 30% by weight.
A preferred embodiment of the invention comprises 21 directly compressed pharmaceutical composition in tablet form, comprising a dry-blended mixture of up to about 80% by weight of a pharniaceutically active ingredient such as ascorbic acid or acetaminophen and at least about 20% by weight of a granulated mixture of dextrose and about 15 to about 35% by weight of a water soluble maltodextrin having a measurable dextrose equivalent value not substantially above about 20, said granulated mixture containing less than about 10% by weight moisture, said directly compressed pharmaceutical composition having a Strong Cobb Hardness Unit (S.C.H.U.) value of at least about 6. Typically, the preferred tablets of the invention will contain from about 15 to about 35% by weight of the pharmaceuti cally active ingredient. Of course, the level of active ingredient in the tablet having the desired hardness value will vary from one active ingredient to another. For example, higher levels of ascorbic acid can be tolerated as compared to Vitamin E acetate to attain the desired hardness values with the vehicles of the present invention at comparable pressures of preparation. In any event, it is quite unexpected that a crystalline sugar such as dextrose based vehicle is capable of providing substantially non-friable, hard tablets when directly compressed with high levels of active ingredients.
As mentioned hereinabove, various known additives such as lubricants, fillers, colors and disintegrants may be added to the novel vehicles of the present invention for their known purposes. Such additives include magnesium stearate, talc, CabO-Sil, Cellutab, Sta-Rx 1500, Magnapol, etc. These additives may be present in amounts ranging from about 0.25% by weight to about 10% by weight or more. The amount of additive, such as the suitable libricant, will generally depend on the active material employed, and the speed and pressure of the tabletting machine utilized.
Because of the plethora of terms that are in common use in the art, a few definitions are made to simplify the present application and permit it to be more concise.
The terms tablet hardness", tablet friability, weight variation, tablet disintegration, and accelerated stability study are defined as follows:
Tablet Hardness A measure of the strength of tablets (average of ten or more tablets) and their ability to retain their physical integrity, expressed in terms of Strong Cobb Hardness Units (S.C.H.U.), as determined by conventional procedure using a Strong Cobb Hardness tester of the Strong-Cobb-Arner Company, Cleveland, Ohio, and the average of these readings is reported herein as mean hardness. The hardness tester was actuated by hand at 60i 5 strokes per minute.
Tablet Friability A measure of the tendency of tablets (average of 10 or more tablets) to crumble and dust, expressed in terms of percent weight loss, as determined by the R0- che test described in the Journal of the American Pizarmaceutical Association, Scientific Edition, Vol. 45, pages 114-116 (1956). This is conducted by sampling ten or more tablets from each batch by first de-dusting the tablets and weighing the same. The tablets are then subjected to the friability test in a Roche Friabilator at 20 revolutions per minute. The tablets are allowed to roll and fall for 4 minutes and thereafter de-dusted and weighed again. The loss of weight is reported as percentage loss from the original weight. lt is well-known that an active ingredient-containing tablet displaying a weight loss of less than about 1% generally is considthe mean of these two limits is taken.
ered to have acceptable friability. Such a tablet characteristic is herein defined as substantially non-friable.
Weight Variation This test is conducted by accurately weighing or more tablets from a batch on a Mettler Balance and the high and low limits of the tablet weights are noted and The time observed for tablets (range of six tablets) to disintegrate in water, as determined by a modification, in which the use of this is eliminated, of the procedure for uncoated tablets described in Pharmucopeia of the United States ofAmerica, 16th. Edition, pages 934-936 I960).
The pressure-hardness profiles were obtained from several dextrose products and Royal-T (agglomerated" mixture of dextrose monohydrate wet filter cake and about 5% by weight Mor-Rex Code 1918) on a Carver Press. This test was strictly comparative.
Prior to the experiment, the die walls and punch faces of the Carver Press, which was utilized to measure the pressure-hardness profiles, were swabbed with 5% solution of stearic acid in chloroform and allowed to dry. One-half gram of the test material was placed in the die and compressed on the Carver Press at various pressures, maintaining a constant dwell time of 10 seconds in all cases. The compressed tablet was ejected from the die by pushing out with the upper punch and its hardness (breaking strength) was determined on the Strong Cobb Hardness tester. Five tablets were compressed at each pressure level, and their average hardness value determined. Table 1 indicates the pressurehardness values of dextrose monohydrate. dehydrated dextrose, anhydrous dextrose and Royal-T.
TABLE 1 Pressure-Hardness Comparison Expressed in S.C.H.U.
HARDNESS VALUE IN S.C.H.U. AT:
"N.T. Not Tested "'35. Beyond Scale Accelerated Stability Study This test is conducted by taking tablets from each batch and packing the same in a wide-mouthed bottle which is tightly stoppered and storing the same in a tray-type dryer at 50C for 7 days. The tablets are then removed and subjected to tests for hardness, disintegration, and friability. Any change in physical appearance is thereafter noted.
The following examples further illustrate the present invention and will enable others skilled in the art to understand it more completely. It should be understood, however, that the invention is not limited solely to the particular examples given below. The parts are parts by weight, unless otherwise indicated.
EXAMPLE 1 Evaluation of Pressure-Hardness Profile on Dextrose Monohydrate, Dehydrated Dextrose, Anhydrous Dextrose, And Royal-T Obtained on Carver Press The above data are indicative that all of the dextrose exhibit poor compressibility and. therefore, they are not suitable as direct compression vehicles. The Royal- T product without any active ingredient exhibited a satisfactory compressibility profile.
EXAMPLE 2 Evaluation of Mixtures of Various Ratios of Dextrose Monohydrate and Maltodextrin Prepared by Different Methods, on Carver Press a. Dry Blends of Dextrose Monohydrate and Maltodextrin:
Four 1 killogram batches of a dry blend of dextrose monohydrate and a maltodextrin (Mor-Rex Code 1918) were prepared in ratios of 95/5, 80/20, /35 and 50/50, respectively, in 21 Hobart Bowl Mixer. Each of the blends was mixed for 7 minutes, and subjected to a pressure-hardness profile evaluation on a Carver r s tThsxssa tsera e forth in T b ""85. Beyond Scale Based upon the data in Table 2, it is quite evident that dry blends of a crystalline sugar such as dextrose and a maltodextrin would not be suitable as a vehicle for carrying high levels of a pharmaceutically active in- This experiment illustrates the granulation of various levels of a mixture ofdextrose monohydrate and maltodextrin with various solutions containing inaltodextrin dissolved therein.
g sgzf smlcc hurdnessnlullucs t: g mlxtum about 3 A calculated quantity of dextrose monohytlrate was 7OL111LS are enera ess an l k screened through a No. 20 sieve (to remove any lumps! b. Dextrose Monohydrate Granulated with Aqueous and mixed with varying amounts otmaltodextrin (Mon Solutions Containing a Maltodextrin: Rex Code 1918) in a Hobart Bowl Mixer for -7 min Five 1 killogram batches of dextrose monohydrate 10 utes- Welght i m eilch Mich l were each granulated with 30 ml. ot'a solution containlogmmeach mlxwre there was added 50 of 5, 10 Q0 30 d 40% W/\ Qffl l l r i (M solution containing dissolved therein the maltodextrin Rex Code 1918, a waxy starch hydrolysate having a (Mor-Rex Code 1918) to obtain a damp mass. The DE. of about 9l3 which readily dissolves in water in damp mass was mixed an additional 7 minutes follow- ConCentrations of up 0 0 he granulation ing the addition of the maltodextrin solution to cause P y ildflllllg the multodexmn granulation, whereupon the granulated damp mass was solution to the dextrose to obtain a damp mass. The Wm SCI-gelled through 3 6 Sic. and dried in an m ll f l i thoroughly mlxcd l g N fi oven to a final moisture content of 8.2 to 8.0%. The M u m f W 1 0 dried, granulated products were evaluated on a arvcr sieve and dried in an oven to a final moisture content I Press to ascertain their ability to foini commercially acot 5.2 to 5.8 /r. lhe moisture content was determined 4 ceptable tablets. lhe details of the preparation and the on an ()haus Moisture Determination Balance. The H hcmilm Clcmum was Set at a point currcsponding to results of the hardness profile evaluation me set loith 100C. and the timer was set for 60 minutes. The loss m Table in weight was noted every 15 minutes until there was no further loss. The percentage moisture lost was read [ABLE 4 otl the scale directly. All the granulations were dry screened to obtain a particle size such that 100% passed through a No. 16 screen and 4992 passed through a No. 80 screen. tThejscieening" described Quantity g herein and throughout this specification was conducted Quantity ()t (iranulate HARDNESS \'.\i.iiis on a Syntron Test Sieve Shaker. Model: TSSZSB. man 01 Maltot\ ilb 510k ufacturcd by the Syntron Company. Homer City. Pa, Dextrose d xtrin M soil. of zltliiio 4|(li00 0:100 and U.S. Standard Sieves (A.S.T.M. specifications). (11mm) lgrmm maiuifactured by Fisher Scientific Company. New 900 30% N York. New York.) All the granulations were sub ected s50 150 20 14.3 Isa its. to the pressure-hardness profile evaluation on the Car- H i /1 .i \ci l css. The details of the amounts of the solvents 8W 200 30% um :12 B5. used in each batch and the results of the pressurehardness profile are set forth in Table 3. 40 as. iittma scat TABLE 3 Quantity Quantity ()l Of HARDNESS VALUE lN S.C.H.U. AT: Dextrose (W/V Aq. Solvent 2000 4000 6000 8000 10.000
(grams) Sol. No. IHtt) Used lhs. lbs. lbs. lbs. lbs.
i) 10 30 ml. 5.0 12.2 16.6 17.0 17.2
1000 20% 30 ml. 5.0 14.6 l8.4 22.8 25.0
I000 30% 30 mi. 5.0 14.x 23.6 28.0 23.2
I000 40) 30 ml. 0.0 14.4 22.8 26.4 9.6
EXAMPLE 3 Granulation of Dextrose Monohydrate-Maltodextrin Mixture with Aqueous Solutions Containing Maltodextrin The above data are indicative that the granulation of a mixture of a crystalline sugar such as dextrose and at least about 10% by weight of a maltodextrin with an aqueous solution containing dissolved therein a maltodextrin provides a tabletting composition having excellent hardness profiles at commercially utilized pressures. Based upon the above hardness profile values of the foregoing granulations. these compositions can be used as direct compression tabletting compositions. whereas the compositions described in Examples 1 and 2 (with the exception of Royal-T. which has limited capacity to carry high levels ofpharmaeeutical materials) are not acceptable as direct compression vehicles.
EXAMPLE 4 Evaluation ot'Compressibility and Carrying Capacity of Dextrose-Maltodextrin Granulated Direct Compression Vehicles 16 per to the dies under operating conditions was observed and noted.
Each of the active ingredients (ascrobic acid (granular), as supplied by Hoffman-LaRoche Inc. and ace1- aminophen (APAP), special power. supplied by S. B.
Penick & Co.) were mixed with the granulated direct In this experiment, the compressibility and carrying compressionvehicle in a proportion of 50 50% in a capacity ofthe dextrose-maltodextrin granulated direct Hobart Bowl Mixer for 57 minutes. Then. 0.5% to compression vehicle was evaluated. The granulated ve- 0.75% by weight of magnesium stearate was mixed with hicle used herein was prepared in the same manner dethe vehicle and active ingredient as a lubricant. The scribed in Example 3 by admixing 80% by weight of mixture was then fed into the tablet press. described dextrose monohydrate with 20% by weight of the malabove in this Example. In the event that tablets were todextrin (Mot-Rex Grade I918, a waxy starch hydronot formed with a given mixture of active ingredients ly having it DB of and thereafter g fln and granulated direct compression vehicle, the ratio ing the admix ure ith a 2 qu SOIUIiOn 0f 15 was altered to increase the amount of vehicle while the maltodextrin (50 ml. ofsolution per 1,000 grams of lowering the level of the active ingredient. This procedextrose monohydrate and maltodextrin admixture). dure was followed until the ratio which produced ac- The particle size otthe direct compression vehicles uticeptabletablets under identical operating conditions lized in this experiment was such that they passed was produced. through a No. sieve. 20 Acceptable tablets are defined as those which pos- The vehicles with and without the active ingredient sess minimum friability, effective hardness and rapid were formed into tablets in a Stokes Model 8-2, 16 stadisintegration time. Samples of tablets produced at diftion rotary tablet machine which had been set up with ferent pressures were taken and subjected to tests for four inch s.c. tooling and a standard feed frame to hardness, weight variation, friability. disintegration and enable gravity feed. All samples of the granulation were 5 stability. The details of these experiments and their refirst inspected for physical appearance. In each insults are tabulated in Table 5.
TABLE 5 EVALUATION Tablet Formulation 71 Disinte- "/1 Active Lubricant Tahlet gration Ascorbic Magnesium Hardness In Time Friahility Acld' APAPI Stearate S.C.H.U. In Min /1 0.5 a. 24.l a. 7.5 a. 0.l2 b. 17.3 b. 7.5 b. 0.22 c. 8.8 c. 7.0 e. 0.21 0.5 t 7.5 10.5 0.46 25 0.75 10.0 10.5 0.00
stance, 0.5% concentration of magnesium stearate was used as a tablet lubricant. The tablets were prepared at the maximum load obtainable, which was determined by gradually increasing the press pressure until a distinct knocking sound caused by a pressure overload was heard. and then easing off on the pressure until the knocking sound ceased. The hardness values for tablets produced at maximum pressure were obtained and recorded. The operating press pressure was then reduced to produce tablets with hardness values approximately one-third of the maximum and two-thirds of the maximum readings. In this manner, tablets were obtained with three different hardness values, ranging from onethird to maximum hardness for each material evaluated. The tablets were evaluated for weight variation, hardness, friability, disintegration and stability. The die till in all cases was adjusted so as to produce tablets weighing 0.5 gram. The flow of the base from the hopges of these readings were reported as Mean Hardnessin Strong Cobb Hardness L' nits. The hardness lL'SItilVItS actuated by hand at 5 strokes per minute.
In each instance, the granulated direct compression composition was indicated as having excellent cornpressibility characteristics and carrying capacity. The granulated direct compression composition exhibited excellent flowtl'rom the hopper to the dies of the tablet press. However. the flow properties of the APAP compositions were not quite as good as the ascorbic acid containing compositions. The weight variation of the TABLE 6 FORMULATION ACCELERATED STABILITY STUDY /1 Active 70 Lubricant Hardness Disintegration Physical Ascorbic Magnesium S.C.H.U. Time In Min. 7: Friability Appearance" Acid APAP Stearate Before After Before After Before After Before After 0.5 24.1 8.5. 7% 8% 0.12 0.10 White A 17.3 8.5. 7% 7% 0.22 0.06 White A 8.8 B.S. '7.0 7% 0.21 0 White A 30 0.5 7.5 8.5. 10% 11.0 0.46 0.08 White A 25 0.75 10.0 20.4 16.0 16.0 0.9 006 White A "Stored at 50"C for 7 days. 'Ascorbic acid granular. APAP (special powder, 5. B. Penick 8:. Co.).
w s. m.-. h
The results tabulated in Table 6 clearly reveal that the granulated direct compression vehicles of the invention provide excellent tablets. The Accelerated Stability Studies indicate that there is a substantial increase in tablet hardness with a noticeable decrease in friability and no change in the disintegration time of the tablets. All of the tablets had an excellent white appearance.
EXAMPLE 5 In this experiment, the ilowability, compressibility, and carrying capacity of granulations of different particle sizes are compared.
In each of the tests, the vehicle was prepared by the granulation process of Example 3, wherein 80% by weight of dextrose monohydrate was admixed with 2071.11 weight of the maltodextrin (Mor-Rex Code 1918. a waxy starch hydrolysate having a DB. 019-1 3) bonate, aluminum hydroxide gel, dried; magnesium trisilicate, dried; (all three supplied by Rugar Chemical Co, New York), acetaminophen (APAP) regular powder, (as supplied by S. B. Penick & Co.) as indicated in Table 7. Each of the samples tested contained a lubricant. The mixtures of the vehicle and the active ingredient were placed in a Colton Model No. 204. 4 Station Rotary tablet machine which had been set up with /8 inch S.C. tooling and a standard feed frame to enable gravity feed. The die fill in all cases was adjusted so as to produce tablets weighing 0.5 gram. The flow of the base from the hopper to the dies under operating conditions was observed and noted. Also, each of the mix- TABLE 7 DETAILS OF EXPERIMENTS ON CAPACITIES OF DIFFERENT PARTICLE SIZE RANGES OF GRANULATED VEHICLE Granu- FORMULATION lation 70 ACTIVE LUBRICANT EVALUATION [particle sodium Aluminum size Magnesium Hydroxide Magnesium Hardness In Disintegration range) carbonate APAP Trisilicate Gel. Dried Stearate Talc S.C.H.U. in Min. Friability +200 0.75 19.0 12.0 0.05 9.5 12.0 0.14 30 1.0 5.0 20 0.29 15 2.0 5.0 14 Caps 20 2.0 1.0 6.0 62 0.2 20 1.0 1.0 8.5 79 0.19
and thereafter the admixture was granulated with a 20% W/V aqueous solution of the maltodextrin (50ml. of the solution per 1.000 grams of dextrose monohydrate and maltodextrin admixture). Each of the granulations tested was passed through a Fitz Mill using a suitable screen (No. 2A or No. 1) with knives forward at medium speed. The comminuted granulations were then hand sieved so as to obtain three particle size ranges, viz.: 20 +60. 40 +100, and -100 +200. The granulations (except the controls which did not contain active ingredient) were dry blended with sodium bicar weight variation (U.S.P.) test was also good to excel 19 lent. However, the 20 +60 and 40 +100 particle size ranges illustrated the best uniformity.
' EXAMPLE 7 This experiment compares the vehicles of the present invention alone or in combination with various actives TABLE 8 DETAILS OF EXPERIMENTS ON CAPACITY OF GRANULATED VEHICLE AT DIFFERENT MOISTURE CONTENT LEVELS FORMULATION Granulated ACTIVE LUBRICANT EVALUATION Vehicle Sodium Magnesium Aluminum Hardness Disin- Moisture Tri- Hydroxide Magnesium Capping, In tegration Content carbonate APAP silicate Gel, Dried Stearate Talc If Any S.C.H.U. In Min. Friability 4.2 0.75 10.2 9.0 0.06 (i 0.2%) 0.75 8.7 13.0 0.93 15 1.25 Slight 8.2 18.0 0.63 25 2.0 1.0 6.5 79 0.11 25 1.0 1.0 8.2 89 0.2
r 4 r at various moisture content levels. EXAMPLE 8 The vehicle used in this experiment was prepared in I the same manner as previously described in Examples 3 6. The vehicle was a granulated admixture of 80% by weight of dextrose monohydrate and 20% by weight of the maltodextrin granulated with a 20% W/V solution of a maltodextrin. The final granulated admixture was screened to a particle size range of +100. The granulation was dried in an oven at different temperatures and for different lengths of time so as to obtain at least three different moisture content levels, 8.0, 4.0 and 2.0%. by weight. The tablets were prepared on a Colton Model No. 204, 4 station rotary tablet machine in the same manner described in the previous examples. The tablets were evaluated for weight variation, hardness. friability and disintegration. All four active medicinal ingredients (described in Table 8) which had been dry blended with the vehicle of the invention were selected to evaluate the capacities of the granulations in the same manner previously described. The details of the experiment are set forth in Table 8.
As it can be seen from the data in Table 8, there was no significant difference in the compressibility and carrying capacity of the granulation at higher and lower moisture content levels. The tablets made from the granulations with lower moisture content were checked for capping and capping of the tablets was not ob- This experiment was performed to evaluate the carrying capacities of the granulations of the present invention with additional active medicinal agents.
Each of the active ingredients (ascrobic acid (type S); calcium salicylate; ferrous sulfate (exicated); and Vitamin E acetate; 50% SD.) were mixed with the granulated vehicle of Example 3 and tested in exactly the same way as described in Example 4. Each of the blended mixtures of granulated vehicle and active medicinal ingredient had excellent flow characteristics from the hopper to the tablet die. The tablets also had a very narrow weight variation. All of the active ingredients were carried very well and the resulting tablets were of extremely high quality, having a friability of less than 2%. Sodium salicylate was carried the least and it required a larger amount (2%) oflubricant. Vitamin E acetate (111) was carried up to 55%. The addition of 0.25% Cab-O-Sil as a glidant was extremely helpful in aiding the flow characteristics of the blend from the hopper to the tablet die. Calcium lactate and ferrous sulfate, exicated, were carried up to 35% and had excellent hardness .and friability characteristics. Ascrobic acid (type S) at the 20% level produced excellent tablets having less than 1% friability and a hardness value of about 6. The details of the experiments and results are tabulated in Table 9.
TABLE 9 DETAILS OF EXPERIMENTS ON CARRYING CAPACITIES OF GRANULATED VEHICLE WITH ACTIVE MEDICINAL INGREDIENTS FORMUATION Active Active Carried "/1 LUBRICANT EVALUATION Medicinal By Granulated Magnesium Hardness Disintegration "/1 Agent Vehicle Stearate Talc Cab-O-Sil In S.C.H.U. In Min. Friability Ascorbic 20 0.5 5.8 8.5 0.21 Acid Vitamin E Acetate 55 0.5 0.25 4.0 16.0 0.04
DETAILS OF EXPERIMENTS ON CARRYING CAPACITIES OF GRANULATED VEHICLE WITH ACTIVE MEDICINAL INGREDIENTS Ascorbic Acid (type S), Hoffmunla Roche. New Jersey. Vitamin F. Acctatc (50% SD). Hoffman-La Roche. New Jersey.
EXAMPLE 9 This experiment was performed to determine the effect of Sta-Rx 1500 (available from A. E. Staley Mfg. Co., Decatur, III.) on the disintegration time ofthe tablets of the granulations per se, as well as in combination with various active medicinal agents.
The same granulated vehicle used in the previous Example 3 was employed. which was an admixture of 80% by weight dextrose monohydrate and of the water soluble maltodextrin granulated with a 20% W/V solu- FORMUATION Active Active Carried 7r LUBRICANT EVALUATION Medicinal By Granulated Magnesium Hardness Disintegration 7r Agent Vehicle Stearate Talc Cab-O-Sil In S.C.H.U. In Min. Friability Calcium '35 1.0 12.5 12.0 0.14 I Lactate 1 Ferrous Sulfate. 0.5 7.6 25 0.31 Exicated Sodium 10 2.0 5.0 23 1.4 Salicylate ments measured less than 1%. All of the tablets had good hardness values. The hardness value for Vitamin E acetate tablets ranged from 3.8 to 4.0, simply because of the reference pressure for the control tablets to produce a hardness value of 10.8. The hardness value of these tablets could be increased to about 6 or TABLE 10 EFFECT OF STA-RX 1500 AS A DISINTEGRANT ON GRANULATED VEHICLE WITH AND WITHOUT ACTIVE MEDICINAL INGREDIENTS FORMULATION 7c ACTIVE Vitamin E 7c LUBRICANT EVALUATION Acetate Calcium Magnesium Capping, Hardness Disintegration 7t (509? SD.) Lactate Stearate Talc Cab-O-Sil Sta-Rx 1500 If Any In S.C.H.U. In Min. Friability 0.75 10.8 8.5 0.07 0.75 10% Slight 11.9 5.0 0.24 55 0.5 0.25 4.0 16.0 0.04 55 0.5 025 10% 3.8 12.0 0.08 1.0 12.5 12.0 0.14 35 1.0 10% Slight 12.4 8.0 021 tion of the maltodextrin. The dried granulated vehicle EXAMPLE 1() was screened to obtain a mesh size in the range of +100. The screened granulated vehicle (except the control) was blended with Sta-Rx 1500 to obtain 10% by weight of Sta-Rx of the total mixture. The Sta-Rx 1500 was also added to the formulations containing the active medicinal ingredients, displacing the granulated direct compression vehicle. The tablets were prepared in the same manner as described in Example 4, keeping the hardness the same as the tablets without Sta-Rx The tablets were evaluated for their weight variation, hardness, friability and disintegration. The addition of the directly compressible starch, Sta-Rx 1500, did not effect the carrying capacity of the granulated vehicle of the invention. However. very slight capping was observed in the case of the calcium lactate formulation] This result was expected. since tablets containing starches have a tendency to cap. There was a decrease in disintegration time for the tablets containing Sta-Rx 1500, as compared to those tablets without it. The reduction of time was about one-third of the original time. The flow from the hopper to the tablet die for all samples was excellent. The friability in all ofthe experi- This experiment was conducted to evaluate the rate of moisture pick-up by the granulations of the present invention per se, and in combination with active medicinal agents at a given relative humidity to ascertain the stability of the active medicinal agents with the granulated vehicle and the performance of the formulations containing the granulated vehicle under industrial working conditions, where a whole batch runs for eight hours or more, when moisture pick-up is possible.
The experiment was performed using the same granulated vehicle used in the previous Examples which had been prepared by admixing by weight of dextrose monohydrate with 20% by weight of the maltodextrin. and thereafter granulating the admixture with a 20% W/V aqueous solution of the maltodextrin (50 ml. of solution per 1,000 grams of dextrose monohydrate and maltodextrin admixture). Vitamin C and Vitamin E acetate were blended with several samples to provide 20 and 55% by weight of the active medicinal agent in the total blend, respectively. The rate of moisture pick-up of the granulated vehicle. per se. and in ct'imbination with the active medicinal agents was studied at 50%, 70 and 90% relative humidity at room temperature.
The moisture pick-up of the samples tested was determined using the below-described procedure.
The Rosano Surface Tensiometer, Model: LG, manufactured by the Federal Pacific Electric Company, N.J., was employed in conjunction with Scheibler Desiccators, containing constant relative humidity solutions.
One gram of the test material which was placed in an aluminum pan (supported by a wire ring) was hooked onto the Surface Tensiometer with a thread passing through a 2-inch length of rubber tubing partly slipped over a 3-inch length of plastic tubing. The glass tubing was fitted into the tubulature of the desiccator top through a one-hole rubber stopper. The test material, the aluminum pan with the ring, the nylon thread were counterbalanced by necessary weights to produce a tensiometer reading of 0.00 mg. Readings were taken at the end of each hour and the increase in weight was noted.
All of the samples exhibited very little moisture pickup. The samples subjected to 50% relative humidity ex hibited a maximum moisture pick-up after 4-5 hours of less than 2.8%, by weight (increase in weight attributed to moisture pick-up). The samples subjected to 70% relative humidity exhibited a maximum moisture pickup after about 5 hours of less than 6%, by weight. The samples subjected to 90% relative humidity exhibited a maximum moisture pick-up after ll hours of less than by weight. Based upon the results of the above moisture pickup tests, it is apparent that the granulated vehicles, per se, or in combination with the active medicinal agents are not troubled by moisture pick-up when exposed to relative humidities of less than about 75%. This desired result is quite unexpected in light of the propensity of dextrose containing compounds to be hygroscopic, i.e., they tend to pick-up moisture upon standing.
EXAMPLE ll This experiment demonstrates the excellent density and fluff characteristics possessed by the granulated vehicles of the present invention, which characteristics enable the vehicle to have the good flow properties from the hopper to the tablet die. As it is well-known, the tablet thickness actually depends on the volume occupied by the vehicle in the die cavity. Tablet thickness is related to the density of the granulation as volume and is inversely proportional to the density. Thus, the denser the granulation, the less volume will be occupied at a given weight, producing thinner tablets. The thickness of the tablets determines the choice of a given packaging unit and even the toolings to be used in their manufacturing. This Example determines the fluff and top densities of the granulations; first, the weight of the material at a given volume, and secondly, the volume is evaluated at a given weight of material. In each test, the granulated vehicle was prepared as previously described in Example 3, using 80% by weight of dextrose monohydrate and 20% by weight of the maltodextrin.
The details of the procedure employed to determine the fluff density and top density of the granulated vehicle of the invention are as follows:
Fluff Density Each granulated vehicle sample was poured down a gentle slope into a tarred l0-ml. cylinder. The weight was reported as Fluff Density in grams/ml.
Top Density Each granulated vehicle sample (50 grams) was accurately weighed and transferred to a .l00-ml. cylinder. The cylinder was gently topped on a thick layer of cloth, until no further perceptible decrease in volume was observed. The weight of the granulations was divided by the volume obtained, and the result was reported as Top Density" in grams/ml.
The results of the tests revealed that the granulated vehicle tested had a Fluff Density of 0.65 gram/ml. and a Top Density of 0.71 gram/ml. These values are indicative of excellent characteristics of the granulated vehicles of the present invention.
EXAMPLE 12 Several granulated vehicles were prepared utilizing the unique procedure described in Example 3, except that in place of Mor-Rex Code 1918, an acid hydrolysate having a DB of about 15 (Frodex, available from American Maize-Products), an enzyme hydrolysate having a E.E. of about 5 (Mor-Rex P908), and two dextrins (Globe Dextrin and Excello Dextrin, available from CPC International Inc.) were employed in amounts of l0, 20 and 30% by weight in the initial blend with the dextrose monohydrate. The respective maltodextrin or dextrin was placed in water and the solution or dispersion (containing 20% W/V of the maltodextrin or dextrin) was used to granulate the blend. The blends were dried to a moisture content of 3-5% and screened of oversize granules above a No. 14 mesh. Each of the granulated vehicles was mixed with 1.0% magnesium stearate for lubrication and was formed into tablets on a Model F single stroke tabletting machine set at a ratio of 45 strokes per minute and at 1% tons of pressure.
In all instances, the granulated vehicles were freeflowing and had acceptable compressibilities. Slight scoring of tablets was observed in the vehicles prepared from the acid hydrolysate (Frodex) and Mor-Rex P908, therefore, necessitating a higher amount of lubricant or inclusion of an anti-adherent. From a hardness and friability standpoint, all blends made acceptable tablets. All of the granulated vehicles demonstrated very little hygroscopicity at 50, and 90% relative humidity. The acid hydrolysate (Frodex) containing vehicles. However, the acid hydrolysate containing vehicles were slightly more hygroscopic than the other vehicles tested. The dextrin containing vehicles, while they provided suitable tablets, were not acceptable because the tablets possessed a yellow color and had a burnt flavor. Thus, it is necessary to employ the maltodextrins to product commercially acceptablegranulated vehicles for use in the pharmaceutical industry.
As it can be seen from the foregoing evidence, the present invention has now provided a unique granulated vehicle having an unusual structural integrity and density. The structural integrity and density of the granulated vehicles provides a tabletting composition having excellent flowability and capability of forming strong, hard and substantially non-friable tablets, even when the tablet contains up to about by weight of the tablet, a pharmaceutically active material. By referring to a substantially non-friable tablet, it is meant a tablet which loses less than about 1% by weight, as determined by the Roche test described hereinabove.
While the invention has been described in connection with specific embodiments thereof, it will be understood that it is capable of further modification, and this application is intended to cover any variations, uses, or adaptations of the invention following, in general, the principles of the invention and including such departures from the present disclosure as come within known or customary practice in the art to which the invention pertains and as may be applied to the essential features hereinbefore set forth, and as fall within the scope of the invention.
1. A method for producing a direct compression ve hicle for tabletting comprising:
a. admixing a crystalline sugar with from about 10 to about 50% by weight, based upon the weight of said vehicle, ofa maltodextrin having a measurable dextrose equivalent value not substantially above about 20 to form a uniform admixture,
b. concurrently agitating and spraying said admixture with an aqueous solution containing dissolved therein a maltodextrin having a measurable dextrose equivalent value not substantially above about 20, said aqueous solution of dissolved maltodextrin being present in an amount sufficient to provide a damp mass of said uniform admixture and to cause granulation of said uniform admixture, and
c. drying said granulated uniform admixture to a moisture content ofless than about l% by weight, based upon the weight of said vehicle.
2. The process of claim 1, wherein said crystalline sugar is dextrose.
3. The process of claim 2, wherein the dextrose is a centrifuge cake containing up to about l6% by weight moisture, based upon the weight of the centrifuge cake.
4. The process of claim 1, wherein said crystalline sugar is admixed with from about 15 to about 35% by weight of said maltodextrin, based upon the weight of said vehicle.
5. The process of claim 1, wherein said aqueous solution contains from about to about 40% weight- /\'olume solution of said maltodextrin.
6. The process of claim 1, wherein said maltodextrin is a waxy starch hydrolysate having a dextrose equivalent value in the range of from about 9 to about 13 and a descriptive ratio of at least about 2, said descriptive ratio being the sum of the percentages (dry basis) of saccharides of the maltodextrin with a degree of polymerization of 1 to 6 divided by the dextrose equivalent value.
7. A method for producing a direct compression vehicle for tabletting comprising:
a. admixing a crystalline dextrose having a moisture content of up to about 16% by weight with from about to about 35% by weight, based upon the weight of said vehicle, of a maltodextrin having a measurable dextrose equivalent value not substantially above about 20 to form a uniform admixture,
b. concurrently agitating and spraying said uniform admixture with an aqueous solution containing dissolved therein from about l()% to about 40% weight/volume of a maltodextrin having a measur' able dextrose equivalent value not substantially above about 20. said aqueous solution of dissolved maltodextrin being present in an amount sufficient to provide a damp mass of said uniform admixture,
c. agitating said sprayed uniform admixture to uniformly intermingle said crystalline dextrose and maltodextrin with said aqueous solution to cause granulation of said admixture, and
d. drying said granulated uniform admixture to a moisture content of less than about 10% by weight.
8. The method of claim 7, wherein the crystalline dextrose is admixed with from about 20 to about 30% by weight, based upon the weight of said vehicle, of said maltodextrin.
9. A directly compressible tabletting vehicle comprising a granulated mixture of a crystalline sugar and from about 10 to about 50% by weight, based upon the weight of said vehicle, of a water soluble maltodextrin having a measurable dextrose equivalent value not substantially above about 20, said granulated mixture containing less than about 10% by weight moisture, based upon the weight of said vehicle, said directly compressible tabletting vehicle in admixture with up to about by weight, based upon the weight of said vehicle, of at least one pharmaceutically active ingredient, being characterized as capable of being formed by direct compression at a pressure as low as about 2000 pounds into hard, substantially non-friable tablets having a Strong Cobb Hardness Unit (S.C.H.U.) value of at least about 6.
10. The directly compressible tabletting vehicle of claim 9, wherein said crystalline sugar is dextrose.
11. The directly compressible vehicle of claim 9, wherein said water soluble maltodextrin is present in an amount ranging from about 15 to about 35% by weight, based upon the weight of said vehicle.
12. The directly compressible vehicle of claim 9, wherein the moisture content of said vehicle is less than about 5% by weight, based upon the weight of said vehicle.
13. A method for preparing tablets comprising forming an admixture of the product of claim 9 and an active material, said product comprising at least about 20% by weight of said vehicle, and compressing the mixture into tablets.
14. A method for preparing tablets comprising forming an admixture of the product of claim 10 and an active material, said product comprising at least 20% of said vehicle, and compressing the mixture into tablets.
15. The method of claim 14, wherein said active material is a pharmaceutically active material.
16. The method of claim 15, wherein said pharmaceutically active material is a member selected from the group consisting of ascorbic acid, sodium salicylate, acetaminophen, sodium bicarbonate, aluminum hydroxide, magnesium trisilicate, Vitamin E acetate, calcium lactate, ferrous sulfate and mixtures thereof.
17. A directly compressed pharmaceutical composition in tablet form, comprising a dry-blended mixture comprising:
a. at least one pharmaceutically active ingredient present in an amount up to about 80% by weight, based upon the weight of said directly compressed pharmaceutical composition; and Y b. a directly compressible vehicle comprising a granulated mixture of a crystalline sugar and at least about 10% by weight. based upon the weight of the directly compressible vehicle, of a water soluble maltodextrin having a measurable dextrose equivalent value not substantially above about 20, said directly compressible vehicle containing less than about by weight moisture, said directly compressible vehicle being present in an amount of at least about 20% by weight, based upon the weight of said directly compressed pharmaceutical composition, said directly compressed pharmaceutical composition being characterized as being hard and substantially non-friable, and being further characterized as having a Strong Cobb Hardness Unit (S.C.H.U.) value of at least about 6.
18. The directly compressed pharmaceutical composition of claim 17, wherein said crystalline sugar is dextrose.
19. The directly compressed pharmaceutical composition of claim 17, wherein said directly compressible vehicle comprises a granulated mixture of dextrose monohydrate granulated with to about 35% by weight, based upon the weight of the vehicle, of a maltodextrin having a measurable dextrose equivalent value not substantially above about 20.
20. The directly compressed pharmaceutical composition of claim 17, wherein said pharmaceutically active ingredient is a member selected from the group consisting of ascorbic acid, sodium salicylate, acetaminophen, sodium bicarbonate, aluminum hydroxide, magnesium trisilicate, Vitamin E acetate, calcium lactate, ferrous sulfate and mixtures thereof.
21. The directly compressed pharmaceutical composition of claim 17, which additionally includes a small but effective amount of materials selected from the group consisting of lubricants, coloring aids, disintegrants, binders and mixtures thereof.
22. A directly compressed pharmaceutical composition in tablet form, comprising a dry-blended mixture comprising:
a. ascorbic acid in an amount of up to about 80% by weight. based upon the weight of said pharmaceutical composition; and
b. a directly compressible vehicle comprising a granulated mixture of dextrose and about 15% to about 35% by weight, based upon the weight of said vehicle, of water soluble maltodextrin having a measurable dextrose equivalent value not substantially above about 20, said vehicle containing less than about 10% by weight moisture.
said directly compressed pharmaceutical tablet being characterized as being hard and substantially nonfriable such that the tablet has a Strong Cobb Hardness Unit (S.C.H.U.) value of at least about 6.
23. The composition in accordance with claim 22, wherein said composition contains ascorbic acid in an amount from about 15 to about 35% by weight, based upon the weight of the tablet.
24. A directly compressible tabletting vehicle comprising a granulated mixture of dextrose and from about l5 to about 35% by weight, based upon the weight of the vehicle, of a water soluble maltodextrin having a measurable dextrose equivalent value not substantially above about 20, said granulated mixture containing less than about 5% by weight moisture, based upon the weight of said vehicle, said directly compressible tabletting vehicle in admixture with at least one pharmaceutically active ingredient in an amount of from about l5 to about 35% by weight, based upon the weight of the total composition, being characterized as capable of being formed by direct compression at a pressure as low as 2000 pounds into hard, substantially non-friable tablets having a Strong Cobb Hardness Unit (S.C.H.U.) value of at least about 6, said vehicle being further characterized as having a particle size in the range of from about 40 to about mesh screen.
25. The directly compressible tabletting vehicle of claim 24, wherein said vehicle additionally contains a tabletting lubricant.
|Cited Patent||Filing date||Publication date||Applicant||Title|
|US3140201 *||Jan 9, 1962||Jul 7, 1964||American Sugar||Dry pulverulent sugar products and process for producing same|
|US3169888 *||Mar 5, 1962||Feb 16, 1965||American Sugar||Pressed crystal sugar tablet and method of manufacturing same|
|US3305447 *||Jun 12, 1963||Feb 21, 1967||American Sugar||Tabletting sugar and method of preparing same|
|US3589909 *||Oct 31, 1968||Jun 29, 1971||Corn Products Co||Gum confections containing dextrose and 5-15 d. e. starch hydrolysate|
|US3619292 *||Jul 15, 1968||Nov 9, 1971||Penick & Ford Ltd||Tablets and method of forming|
|US3627583 *||Apr 29, 1969||Dec 14, 1971||Sucrest Corp||Direct compression vehicles|
|US3639168 *||Apr 29, 1969||Feb 1, 1972||Sucrest Corp||Direct compression vehicles|
|US3639169 *||Apr 29, 1969||Feb 1, 1972||Sucrest Corp||Direct compression vehicles and method therefor|
|US3642535 *||Jan 21, 1970||Feb 15, 1972||American Sugar||Tabletting sugar, method of preparing compositions containing same|
|Citing Patent||Filing date||Publication date||Applicant||Title|
|US4262017 *||May 11, 1979||Apr 14, 1981||Basf Aktiengesellschaft||Preparation of a vitamin E dry powder|
|US4349542 *||May 5, 1980||Sep 14, 1982||National Research Development Corporation||Mixture containing active ingredient and dendritic crystalline sugar for tableting|
|US4465667 *||Jan 11, 1982||Aug 14, 1984||Aktiebolaget Hassle||Process for the preparation of gastric acid neutralizing agents, gastric acid neutralizing agents, and a method for treating hyperacidity and disorders related thereto|
|US4495177 *||Jan 17, 1983||Jan 22, 1985||Shaklee Corporation||Gel tableting agent|
|US4639458 *||Jan 22, 1985||Jan 27, 1987||Merck & Co., Inc.||Tablet and formulation|
|US4643894 *||Jul 24, 1984||Feb 17, 1987||Colorcon, Inc.||Maltodextrin coating|
|US4684534 *||Feb 19, 1985||Aug 4, 1987||Dynagram Corporation Of America||Quick-liquifying, chewable tablet|
|US4711894 *||Jan 16, 1986||Dec 8, 1987||Henkel Corporation||Stabilized tocopherol in dry, particulate, free-flowing form|
|US4725441 *||Oct 1, 1986||Feb 16, 1988||Colorcon, Inc.||Maltodextrin coating|
|US4894236 *||Jan 12, 1988||Jan 16, 1990||Choong-Gook Jang||Direct compression tablet binders for acetaminophen|
|US4985252 *||Apr 4, 1988||Jan 15, 1991||R. I. Ph. Recherche Informatique Et Pharmacie (S.A.R.L.)||Medication, dietetic product and hygienic product in the form of a powered composition obtained by adsorption of active ingredients on a rapidly dissolving sugar and process for obtaining said composition|
|US5037658 *||Sep 14, 1989||Aug 6, 1991||Hoechst-Roussel Pharmaceuticals, Inc.||Direct dry compressible acetaminophen composition|
|US5047246 *||Sep 9, 1988||Sep 10, 1991||Bristol-Myers Company||Direct compression cyclophosphamide tablet|
|US5130140 *||May 15, 1991||Jul 14, 1992||Hoeschst-Roussel Pharmaceuticals Inc.||Method of making direct dry compressible acetaminophen composition|
|US5164192 *||Jan 28, 1991||Nov 17, 1992||Duphar International Research B.V.||Effervescent composition for oral rehydration|
|US5198228 *||May 15, 1991||Mar 30, 1993||Hoechst-Roussel Pharmaceuticals Inc.||Direct dry compressible acetaminophen tablet|
|US5384130 *||Jan 12, 1993||Jan 24, 1995||Asahi Kasei Kogyo Kabushiki Kaisha||Spherical seed cores, spherical granules and process for production thereof|
|US5470581 *||Dec 15, 1992||Nov 28, 1995||Berwind Pharmaceutical Services, Inc.||Aqueous maltodextrin and cellulosic polymer film coatings|
|US5505983 *||Oct 17, 1994||Apr 9, 1996||Asahi Kasei Kogyo Kabushiki Kaisha||Spherical seed cores, spherical granules and process for production thereof|
|US5531983 *||Sep 13, 1994||Jul 2, 1996||Purac Biochem B.V.||Oral hygiene preparation|
|US5804217 *||Apr 14, 1994||Sep 8, 1998||Pharmacia & Upjohn Aktiebolag||Manufacturing matrices|
|US5939459 *||Mar 18, 1998||Aug 17, 1999||Cellular Sciences Inc.||Method and composition for treating mammalian disease caused by inflammatory response|
|US6008187 *||May 12, 1995||Dec 28, 1999||Alza Corporation||Peptide formulation|
|US6080427 *||Mar 17, 1998||Jun 27, 2000||Bristol-Myers Squibb Company||Cefadroxil monohydrate tablet formulation|
|US6348264||May 9, 2000||Feb 19, 2002||Roquette Freres||Process for producing low de starch hydrolysates by nanofiltration fractionation, products obtained thereby, and use of such products|
|US6432448||Jan 27, 2000||Aug 13, 2002||Fmc Corporation||Edible coating composition|
|US6500462||Oct 26, 2000||Dec 31, 2002||Fmc Corporation||Edible MCC/PGA coating composition|
|US6699315||Nov 26, 2001||Mar 2, 2004||Fmc Corporation||Edible PGA coating composition|
|US6716453 *||May 22, 2000||Apr 6, 2004||Verion, Inc.||Method for increasing the active loading of compressible composition forms|
|US6723342||Aug 4, 2000||Apr 20, 2004||Fmc Corporation||Edible coating composition|
|US6932861||Feb 15, 2002||Aug 23, 2005||Fmc Corporation||Edible PGA coating composition|
|US7282217||Aug 30, 2004||Oct 16, 2007||Kv Pharmaceutical Company||Rapidly disintegrable tablets|
|US7425341||Sep 11, 2007||Sep 16, 2008||K.V. Pharmaceutical Company||Rapidly disintegrable tablets|
|US20030129238 *||Nov 27, 2002||Jul 10, 2003||Michael Augello||Edible MCC/PGA coating composition|
|US20050095272 *||Dec 2, 2004||May 5, 2005||Fmc Corporation||Edible PGA coating composition|
|US20050143343 *||Dec 30, 2003||Jun 30, 2005||Nerenberg Arnold P.||Nutritional supplement for enhancing the production and effect of natural human growth hormone|
|US20080069936 *||Sep 18, 2006||Mar 20, 2008||ISON Renny||Cohesive non-free flowing sweeetener compositions containing a hygroscopic gluing agent and a desiccant|
|US20120034302 *||Feb 5, 2010||Feb 9, 2012||Liangping Yu||Particulate composition and the method of making the same|
|DE202015004009U1||Jun 9, 2015||Jan 11, 2016||Hermes Arzneimittel Gmbh||Schnell zerfallende Tabletten ohne Zerfallsbeschleuniger|
|EP0100168A2 *||Jul 6, 1983||Feb 8, 1984||Alan George Rogerson||Processes for preparing tablets by a modified 'wet-granulation' technique|
|EP0745382A1 *||Jan 27, 1995||Dec 4, 1996||Yamanouchi Pharmaceutical Co. Ltd.||Intraorally soluble compressed molding and process for producing the same|
|EP0909824A1 *||Oct 12, 1998||Apr 21, 1999||Saint-Louis Sucre S.A.||Water-repellent granule based on saccharose|
|EP2395972A1 *||Feb 5, 2010||Dec 21, 2011||Liangping Yu||Particulate composition and the method of making the same|
|WO2008036230A2 *||Sep 17, 2007||Mar 27, 2008||Mcneil Nutritionals, Llc||Cohesive non-free flowing sweetener compositions containing a hygroscopic gluing agent and a desiccant|
|WO2012019266A1 *||Aug 12, 2011||Feb 16, 2012||Filho Jose Raimundo||Method and composition for reducing the color of sugar|
|U.S. Classification||424/648, 127/63, 424/722, 127/29, 264/122, 424/717, 514/626, 514/557, 514/458, 424/690, 514/161, 424/683, 514/474|
|International Classification||C13B50/00, C13B50/02, A61K47/36, A61K9/20|
|Cooperative Classification||A61K9/2059, C13B50/02, C13B50/002, A61K9/2018|
|European Classification||C13B50/02, C13B50/00B, A61K9/20H6F4, A61K9/20H4B|
|May 25, 1990||AS||Assignment|
Owner name: GRAIN PROCESSING CORPORATION
Free format text: CHANGE OF NAME;ASSIGNOR:OREGON STREET ENTERPRISE, INC.;REEL/FRAME:005371/0489
Effective date: 19900523
Owner name: OREGON STREET ENTERPRISES, INC., A CORP. OF IA, IO
Free format text: MORTGAGE;ASSIGNOR:GRAIN PROCESSING CORPORATION;REEL/FRAME:005371/0501
Effective date: 19900404
Owner name: VARIED INVESTMENTS, INC.
Free format text: CHANGE OF NAME;ASSIGNOR:GRAIN PROCESSING CORPORATION;REEL/FRAME:005371/0494
|May 25, 1990||AS01||Change of name|
Owner name: GRAIN PROCESSING CORPORATION
Effective date: 19900523
Owner name: OREGON STREET ENTERPRISE, INC.
|Sep 18, 1980||AS02||Assignment of assignor's interest|
Owner name: CPC INTERNATIONAL INC.
Owner name: GRAIN PROCESSING CORPORATION, A CORP. OF IOWA
Effective date: 19800909