Rapidly Dissolving Tablet

The present invention relates to dosage forms for providing a medication or pharmaceutical, and in particular, relates to solid dosage forms which can dissolve rapidly in the oral cavity.

The recent, current and projected growth of the elderly population in the U.S. and abroad is well recognized. Currently, 12% of the U.S. population is 65 years of age or older and receives nearly 30% of the medications prescribed. It is anticipated that there may be a 10% to 60% increase in the demand for drugs by the elderly under some new government programs.

In spite of the disproportionately large demand for prescription pharmaceuticals among the elderly, relatively little attention has been directed to meeting the unique pharmacotherapeutic needs of this age group. Drug products are currently designed for three groups of individuals: infants, pediatrics and adults. The needs of the infants are obviously different from those of children 2 to 12 years of age and the needs of children are obviously different from that of adults. However, the needs of the elderly population are being overlooked as they have special characteristics that necessitate dosage forms designed especially for them. Many older patients have difficulty swallowing tablets or capsules and yet the vast majority of dosage forms administered to the elderly are tablets or capsules. Uncoated tablets are convenient and economical to manufacture but are often difficult to swallow and often cause discomfort by "hanging" in the throat. Coated tablets and capsules are somewhat easier to swallow but with increasing age and the large number of drug products that are administered to a single individual, this is a source of apprehension. Liquid dosage forms are relatively easy to administer but are more costly, easily spilled, often do not taste good, occupy large volumes of space per dosage unit, and possess some inherent stability problems. As is evident, the needs of the elderly differ from those of other populations and deserve special attention in new drug development, product formulation, posology, product packaging, product labeling, patient information, and product marketing and sales. A practical and new dosage form would be of value for these patients.

Pediatric patients generally have difficulty swallowing until they reach the age of about 10-16 years old. Younger pediatric patients generally take either chewable tablets, crush and mix regular tablets with food/juice, or take a liquid dosage form. Chewable tablets, generally a good dosage form, do not always taste good. Crushing and mixing regular tablets with food or juice, is time-consuming, messy and not always practical. The difficulty of liquid dosage forms, i.e., syrups, is that they are bulky, do not always taste good, and drugs are not as stable in a liquid dosage form as they are in a solid dosage form, such as a tablet. A practical and new dosage form would also be of value for these patients.

Incarcerated patients often will retain their medications within the oral cavity while pretending to swallow them. These can then be accumulated and taken all at once for an enhanced drug effect. Obviously, this can be very dangerous. A dosage form which would not remain intact once placed in the oral cavity would be useful when treating these patients.

There currently are several fast-dissolving products on the market. These products have a number of drawbacks including the manufacturing methods used, taste masking, and pre- vs post-loading techniques that are required.

One commercially available dosage form is prepared by a lyophilization, or freeze-drying, technique which is slow and expensive. Because each "batch" of material must be handled in its entirety, the tablet cannot be produced using a continuous process where raw materials come in and finished product is output at the other end. This tablet can be either pre-loaded (i.e., the drug is added to the tablet matrix before the tablet is formed) or post-loaded (the drug is added after the tablet "blank" is prepared). One difficulty with a freeze-dried dosage form is that of taste-masking. To effectively mask the taste of poorly tasting drugs, it is generally necessary to microencapsulate or nanoencapsulate them. Then, if they are pre-loaded, the encapsulating shell material may dissolve during the tablet production process allowing the drug to leak into the tablet matrix, resulting in a poorly tasting product. If the tablet is post-loaded, the tablet may become disfigured causing the tablet to be disposed of or handled again, adding extra expense to the process.

Another commercially available dosage form is prepared using solid state dissolution techniques. These manufacturing methods are expensive and add additional cost to the tablet. This tablet must be post-loaded. This is necessary because drugs are generally soluble in the water and alcohol which is used in the preparation of the tablet. As with the freeze-dried dosage form discussed above, when a solution of the drug is post-loaded onto the matrix blank, often the tablets become disfigured. Another problem encountered with the solid state dissolution technique is the selection of a solvent material that will evaporate quickly but will not attack the microcapsule shell surrounding the active drug.

Effervescent dosage forms contain compounds for enhancing tablet breakup and dissolution and may also serve to mask the taste of certain medications. These tablets depend upon approximate stoichiometric quantities of sodium bicarbonate and an acid, e.g., citric acid or tartaric acid, reacting to form CO.sub.2 to break up the tablet in the mouth. The difficulty with the commercially available effervescent tablets is that the mouth tends to "foam" leaving an uncomfortable feeling to many.

The present invention comprises a solid dosage form, and method for making such, which disintegrates or dissolves in a matter of just a few seconds once placed into the oral cavity. This rapidly dissolving tablet has many of the characteristics of a regular tablet up to the point of administration, i.e., convenient size, stable, easy to dispense, easily transportable, easy to alter the dose and easy to administer. Upon placing this dosage form in the mouth, the saliva will serve to rapidly dissolve the dosage form and the patient in effect will swallow the medication in a liquid form. The rapid-dissolving tablets of the present invention will eliminate many of the problems inherent in the other forms of orally-dissolving tablets described above since the matrix and active drug powders are blended and formed into tablets in the same way as regular tablets, except that a very light compression pressure is used in forming the tablets of the present invention.

As noted, upon placing the dosage form of the present invention into the mouth, the saliva will serve to rapidly dissolve the dosage form and the patient will swallow the medication in a liquid form. If a drug entity has little or no taste, the dosage form will be prepared to be almost tasteless. If a drug product does have a characteristic, undesirable taste, the taste will either be altered by different mechanisms such as flavorings to make it acceptable, or, the drug will be micro- or nano-encapsulated with a coating that dissolves at an acidic pH and incorporated into the tablet. This rapid dissolving tablet will not only provide the geriatric, pediatric and incarcerated populations with an easy to use tablet, but may also result in long-term benefits such as enhanced patient compliance, fewer hospital admissions due to poor compliance, and enhanced health and quality of life.

Furthermore, the application of this dosage form is not limited to oral delivery as it is also applicable for use as a fast dissolving tablet when administered to other moist areas of orifices of the body, such as the rectum.

Generally, the method of the present invention comprises up to four steps. First, a porous particulate powder which will serve as the tablet support matrix is produced. In the second step, the pharmaceutical, for example an antihistamine, decongestant, or antibiotic is combined with the powder. Other additives may also be added to the mixture. In the third step the mixture is formed into a tablet. Finally, in the fourth step, a coating may be applied to the outer surface of the tablet to enhance the intactness and durability of the tablet.

More particularly, the invention comprises a process for producing a particulate support matrix for use in forming a pharmaceutical dosage form. The process comprises the steps of providing an aqueous composition which further comprises (1) an aqueous medium, (2) a support agent comprising a polymeric primary component capable of maintaining a net charge, a solubilizing component capable of maintaining a net charge of the same sign as the primary component, and a bulking agent and wherein the solubilizing component has a solubility in aqueous solution greater than that of the primary component, (3) a volatilizing agent for enhancing the rate of vaporization of the aqueous medium and for enhancing volume and porosity of the support agent during drying, and (4) a buffering agent for maintaining the net charge of the components of the support agent. The aqueous composition is then introduced as droplets into a drying chamber heated to a predetermined temperature causing evaporation of substantially all of the aqueous medium and volatilizing agent from the droplets. This results in the support agent as a dried and expanded particulate form comprising the particulate support matrix.

The resulting particulate support matrix produced may have a density within a range of about 0.03 g/ml to about 0.06 g/ml. Further, the polymeric primary component may comprise a first polypeptide and the solubilizing component may comprise a second polypeptide. More preferably, the first polypeptide may be a non-hydrolyzed gelatin and the second polypeptide may be a hydrolyzed gelatin.

The invention further comprises a rapidly dissolving solid pharmaceutical dosage form, which is made from an active ingredient such as a pharmaceutical product which is mixed and dispersed throughout the particulate support matrix described herein and then formed into a tablet. When this dosage form is introduced into an aqueous environment the support matrix is substantially completely disintegrable within less than about 20 seconds so as to release the pharmaceutical ingredient to the aqueous environment. The support matrix may be substantially completely disintegrable within less than about 10 seconds, or more preferably in from about 1 second to about 6 seconds. The dosage form may also contain an effervescing agent for aiding in the disintegration of the dosage form, a binding agent, and a flavoring agent. Further, the dosage form may have a polymeric coating of the external surface for enhancing the intactness of the dosage form. The density of the dosage form is within a range of about 0.1 g/ml to about 0.2 g/ml.

The particulate support matrix, in the preferred embodiment, is produced using standard spray-drying techniques, well known to persons of ordinary skill in the art. The components of the composition which is used to produce the matrix include a support agent which comprises in one version a gelatin and a hydrolyzed gelatin and may additionally include a bulking agent for increasing the bulk and solubility of the support matrix and tablet formed therefrom. Another component is a volatilizing agent, having a volatility which exceeds that of water, such as an alcohol, preferably ethanol. Another component is a buffering agent which functions to cause the components of the support agent to be maintained with a net charge, either positive (when the pH of the composition is below neutral) or negative (when the pH is above neutral). In a preferred version the support matrix is maintained with a net positive charge by an acidic buffering agent such as citric acid. The composition further comprises an aqueous medium such as water.

Critical physical factors in the spray drying process have to do with net charge and solubility of the support agent (for example, of proteins) and the evaporation characteristics of the volatilizing agent (for example, ethanol). In the preferred embodiment, the support agent is comprised of a primary support component and a solubilizing component and a bulking agent. The solubilizing component contributes to the support function of the support matrix when in the dried particulate but also serves to enhance the rate of dissolution of the support matrix once the tablet is introduced into an aqueous environment such as the salivary environment of the oral cavity. In one example of the preferred embodiment, the primary and solubilizing components of the support agent comprise two different forms of gelatin, an unmodified form (the primary support component), and a hydrolyzed form (the solubilizing component), and act together to form a support matrix in the dried particles. Both of these forms of gelatin are commercially available. The hydrolyzed gelatin assists the unmodified gelatin as a structural component of the matrix but it also functions to increase the solubility of the matrix in some cases by a factor of two. For example, when the particulate matrix was formed only from gelatin, water and alcohol, the powder dissolved in approximately 25 seconds. When gelatin hydrolysate was added to the formula, the powder produced therefrom dissolved in about 15 seconds. In the preferred version of the invention, the solution of the protein and protein hydrolysate is made acidic, preferably in the pH range of about 4-5.5. This acidity causes the protein components of the composition to have a net positive charge. Together with or in lieu of gelatins, the primary support component and/or solubilizing component may be comprised of polymers, including cellulose derivatives, polyethylene glycol derivatives and sugar derivatives.

The effect of the net positive charge of the protein molecules is to cause individual protein molecules to be repellent to each other when in solution thereby reducing the tendency for the protein molecules to "cling" to each other. As a result, the protein molecules tend to remain repelled in the solution and during the spray drying process while the droplets of the composition are drying into particles. As a result, the powder formed will be of relatively low bulk density, generally in the range of from about 0.03 g/ml to about 0.06 g/ml. The bulking agent contributes to the bulk and stability of the support matrix and increases the rate at which the support matrix will dissolve. Examples of bulking agents are carbohydrates such as mannitol, sorbitol, sucrose and xylitol, and acacia.

The incorporation of the ethanol (or another volatilizing agent) into the solvent system functions to decrease the vaporization temperature of the solvent and contributes to the production of a more porous particle having a lesser bulk density and thus a greater bulk volume. It has been discovered that if water alone is used as the aqueous solvent, when the composition is introduced as droplets into the spray drying chamber, the droplets will have a tendency to contract in size thus increasing in density, as they traverse from the spray nozzle, through the drying chamber, to the collecting chamber of the spray-drier unit. By incorporating into the solvent a volatilizing agent such as ethanol, numerous pores and channels are formed within the structure of the droplet as the solvent mixture volatilizes from the droplet during the drying process. The particle formed from the droplet retains a higher porosity and low density and even experiences expansion resulting in a powder having a larger bulk volume.

In one experiment, a control comprising a quantity of a formula excluding ethanol produced a dried particulate support matrix powder having a bulk density of 0.077 g/ml (porosity was about 13 ml/g) and a bulk volume of 180 ml. The treatment comprised a comparable initial quantity of the formula with ethanol added produced a dried particulate support matrix powder having a bulk density of 0.049 g/ml (porosity was about 20.4 ml/g) and a bulk volume of 450 ml. ›The formula comprised, mannitol (10 g), sorbitol (5 g), citric acid (0.4 g), sucrose (0.15 g), Explotab (0.15), gelatin G8-275 (1 g), gelatin hydrolysate (1 g), and a quantity of water sufficient to produce a volume of 500 ml. The amount of ethanol added to the treatment was 150 ml!.

This result of a product having a greater bulk volume when ethanol is added is apparently obtained by the lowering of the vaporization temperature of the solvent thus increasing the rate at which the solvent is vaporized. The retention of the porous nature of the particle is critical to the speed with which a tablet constructed of the material dissolves. The porosity enhances the capillary movement of saliva into the interior of the tablet thereby increasing the dissolution rate of the support matrix of the tablet.

The presence of the buffering agent in the composition serves to maintain the net charge of the molecules of the support matrix. For example, in the preferred embodiment, the net positive charge of the protein components is maintained by an acidifying agent such as citric acid. When the support matrix makes contact with an aqueous solution the proteins comprising the support matrix will have a positive charge and immediately repel each other as soon as they dissolve, thus causing the particles of the tablet to repel each other, enhancing the rapidness of disintegration of the tablet. A similar phenomenon may be effected by using an alkalizing agent such as sodium bicarbonate as the buffering agent (causing the polypeptide components of the support matrix to be negatively charged).

In the present invention, the primary and solubilizing components of the support matrix together generally comprise from 2-20% of the dry components of the aqueous composition (percentage by weight), when the composition comprises the primary and solubilizing components, the bulking agent and the buffering agent used to form the particulate support matrix. More preferably, the range is from 3-18% and more preferably is from 6-16%. Most preferably the primary and solubilizing components of the support matrix together comprise from 10-14% of dry portion of the aqueous composition.

In addition, the bulking agent of the support matrix generally comprises from 60-96% of the dry components of the aqueous composition (percentage by weight) used to form the particulate support matrix. More preferably, the range is from 75-92% and more preferably is from 80-90%. Most preferably the bulking agent of the support matrix comprises from 82-88% of the dry portion of the aqueous composition. In addition, the buffering agent of the support matrix generally comprises from 0-30% of the dry components of the aqueous composition (percentage by weight) used to form the particulate support matrix. More preferably, the range is from 1-16% and more preferably is from 1-6%. Most preferably the buffering agent of the support matrix comprises from 1-3% of the dry portion of the aqueous composition.

Before forming the particulate support matrix into a tablet, a quantity of the drug, medication, or pharmaceutical and any necessary flavoring agent is added to a quantity of the particulate support matrix. The optional addition of a small amount of effervescent material serves to assist in the initial stage of the disintegration of the particles of the tablet. The tablet may be formed by methods known to those of ordinary skill in the art. For example, the tablet may be formed by direct compression. Or, it may be formed by first adding a moistening agent such as alcohol, then compressing or molding the composition. Or, it may be formed by first adding a binding agent such as polyvinylpyrrolidone, then compressing or molding the composition into a tablet. The dosage form described herein may include one or more adjuvants which can be chosen from those known in the art including flavors, diluents, colors, binders, fillers, compaction vehicles, effervescent agents, and non-effervescent disintegrants, such as those disclosed in U.S. Pat. No. 5,178,878, issued to Wheling et al. on Jan. 12, 1993, and in U.S. Pat. No. 5,215,756, issued to Gole et al., on Jun. 1, 1993, the specifications of which are hereby incorporated herein by reference. More specifically, the tablets may be composed of, but not limited to, the following: gelatin (commercially available Pharmagel A and B, Type A, 275 Bloom, and Type B, 100 Bloom), hydrolyzed gelatin, sugars (mannitol, sucrose), organic acid (citric acid, succinic acid), sodium bicarbonate, ethyl alcohol, disintegrants such as Explotab (starch glycolate) and AcDiSol, starch, polyvinylpyrrolidone polymers, alginic acid, bulking and electrical charge agents such as acacia, and polyethylene glycol polymers.

Following the formation of the mixture into a tablet, it may be desired to apply a very thin coating to the external surface of the tablet. The function of the coating, when applied, is to enhance the intactness of the tablet. Due to the porous nature of the tablet, the tablet tends to be rather fragile and breakable and generally benefits from the added protection afforded by the coating. The coating may comprise a polymer, such a polyvinyl alcohol or a polyvinylpyrrolidol, which, when applied forms a polymeric "net" over and into the tablet. This "net" maintains the tablet intact but does not inhibit the capillary uptake by the tablet once placed in the aqueous environment of the oral cavity although dissolution time may be slightly increased when a coating is applied to the tablet (see Example 17).

In preparation for forming the tablets, a tablet blend is produced by combining a quantity of the particulate support matrix with a quantity of the pharmaceutical or drug and optionally with a quantity of an effervescent blend, a binding solution and/or a flavoring.

The pharmaceutical composition can be added at several different stages of the formulation of the dosage form depending on the circumstances. The pharmaceutical can be added directly to the liquid composition before or during the spray drying process at the inlet nozzle. The resulting product can then be incorporated into the tablets. Alternatively, the pharmaceutical, in untreated or encapsulated form, is mixed with the particulate support matrix (after the spray drying process, before or after adding the binder, if a binder is added) and then formed into tablets. Alternatively, the pharmaceutical could be added by direct application to the preformed tablet by spray coating or drop coating.

As noted, the addition of the effervescent blend, the binding solution (also referred to herein as the binding agent) and the flavoring are optional. When present, the binding solution and the effervescent blend may be added to the support matrix powder in a ratio of about 20:10:1 (support matrix:binding solution:effervescent blend). The effervescent blend consists of an approximately stoichiometric ratio of citric/tartaric acids with sodium bicarbonate in a powder form. In various versions, the effervescent blend may comprise the following ratios of components:

(1) citric acid:sodium bicarbonate, 1:1.2

(2) tartaric acid:sodium bicarbonate, 2:2.24

(3) citric acid:tartaric acid:sodium bicarbonate, 1:2:3.4

The blend is slightly acidic so there will be a slight tartness in the mouth upon dissolution of the product. As is indicated above, the amount of effervescent blend present is minimal and almost non-detectable in the mouth. Its presence enhances the separation of the porous particles and enhances capillarity during dissolution of the tablet within the oral cavity thereby decreasing dissolution time of the tablet (see Example 15). The effervescent blend also enhances salivation in the oral cavity.

The binding solution in one version of the invention consists of 1% PVP-40 in ethanol (e.g., see Example 14). Other binding solutions may consist of mixtures of PEG 1000 and PEG 4000 in Alcohol, PEG 1000 and PVP 1000 in Alcohol. The binding solution may further comprise a quantity of a surface active agent such as sodium lauryl sulfate for further increasing the dissolution rate of the dosage form. The binding solution, when used, is mixed slowly with the spray dried powder, then dried at about 40.degree.-50.degree. C.

In one method used for forming the tablets, a quantity of the tablet blend is lightly compressed. The tablets thus produced are then coated with a very thin coating of an organic solution of a polymer, which rapidly evaporates leaving a polymeric "net" on the surface of the tablet. This thin external "net" aids in keeping the tablets intact during handling. Polymers may include, but not be limited to PVP and PVA. The coating may be applied by passing the tablet into a chamber having a saturated atmosphere of the coating material. Alternatively, the coating may be applied by lightly spraying the coating material onto the surface of the tablet.

In another method for forming the tablets, a quantity of the tablet blend is moistened with ethanol then passed through a #40 mesh screen and immediately compressed into tablets and dried overnight at about 50.degree. C. The tablets thus produced may be then coated with a very thin coating of an organic solution of a polymer, which rapidly evaporates leaving a "net" on the surface of the tablet.

The present invention contemplates a tablet which is much lighter (for example 50 mg) than a comparable typical commercially available tablet (for example 400-500 mg).

The present invention further contemplates a tablet which will disintegrate within the oral cavity in less than about 20 seconds. More preferably, the tablet will disintegrate within less than about 10 seconds. More preferably, the tablet will disintegrate within the oral cavity in less than about 6 seconds. Still more preferably, the tablet will disintegrate in from about 1 second to about 4 seconds. The bulk density of the formed tablet is preferably in a range of from abut 0.1 g/ml to about 0.2 g/ml, but may be either less than or greater than the bounds of this range. Porosity may be in a range of from about 50 to 75% in a preferred embodiment.

The following examples further illustrate compositions of the dosage form of the present invention including preferred versions and methods of making the same; however these examples are not to be construed as limitations of this invention.

The testing method used to determine the dissolution of the tablet material is a modification of the USP disintegration method which involves the agitation of tablets in purified water at 37.degree. C. The present testing conditions included used a 600 mL glass beaker with water at about 37.degree. C. The surface of the water was motionless. The water was not agitated. A fresh beaker of water was used for each test. To test the dissolution rate of the particulate matrix in powder form, the tip of a 4" stainless steel spatula was dipped into the powder and a quantity of powder equivalent to approximately 100 mg was removed from the container and dropped onto the surface of the water from a distance of approximately 1 inch. To test the dissolution rate of the support matrix in tablet form, a tablet was removed from its container and placed on the tip of a 4" stainless steel spatula. The tip of the spatula was held approximately 1 inch above the surface of the water and the tablet allowed to slide off the spatula tip onto the water. The testing method is an approximation of the in vitro use of the tablet. In actual practice, of course, the tablet will be placed on the tongue and a combination of the saliva dissolving the tablet and the tongue action aiding in its breakup will occur.

The following components were added to a quantity of purified water sufficient to produce a mixture with a volume of 500 ml. pH was 2.8.

The mixture was introduced into a Buchi model 190 spray drier with a heat setting of 10, an aspirator setting of 5, a flow rate setting of 4.27, an initial flow control setting of 700 (changing to 650 after the first time interval), and a vacuum setting of -20. Chamber temperatures were measured at approximately 5 minute consecutive intervals during the drying process. The temperatures at the flow inlet point were 156.degree. F., 156.degree. F., 159.degree. F., 154.degree. F., and 157.degree. F. The temperatures at the flow outlet point (the point where the dried product exits the drying chamber to product collector) were measured as 115.degree. F., 111.degree. F., 86.degree. F., 109.degree. F., and 108.degree. F. The mixture was introduced into a spray drier yielding a particulate support matrix product having a bulk volume of about 140 ml and a porosity of 5.6 ml/g. The resulting matrix had a dissolution time of from 5 to 15 seconds.

The following components were added to a quantity of purified water sufficient to produce a mixture with a volume of 500 ml. pH was 6.4.

The mixture was introduced into a Buchi model 190 spray drier with a heat setting of 10, an aspirator setting of 5 (which was changed to 7 after the second time interval), a flow rate setting of 4.27, a flow control setting of 700, and a vacuum setting of -20. Chamber temperatures were measured at approximately 5 minute consecutive intervals during the drying process. The temperatures at the flow inlet point were 154.degree. F., 154.degree. F., 133.degree. F., 143.degree. F., and 143.degree. F. The temperatures at the flow outlet point (the point where the dried product exits the drying chamber to product collector) were measured as 104.degree. F., 104.degree. F., 90.degree. F., 93.degree. F., 93.degree. F., and 93.degree. F. The mixture was introduced into a spray drier yielding a particulate support matrix product having a bulk volume of about 100 ml and a porosity of 2.3 ml/g. Dissolution time of the support matrix was 5-15 seconds.

The following components were added to a quantity of purified water sufficient to produce a mixture with a volume of 400 ml. pH was 8.4.

The mixture was introduced into a Buchi model 190 spray drier with a heat setting of 10, an aspirator setting of 5, a flow rate setting of 4.27, an initial flow control setting of 700 (changing to 550 after the first time interval), and a vacuum setting of -20. Chamber temperatures were measured at approximately 5 minute consecutive intervals during the drying process. The temperatures at the flow inlet point were 154.degree. F., 157.degree. F., 157.degree. F., 157.degree. F., and 157.degree. F. The temperatures at the flow outlet point (the point where the dried product exits the drying chamber to product collector) were measured as 107.degree. F., 108.degree. F., 108.degree.0 F., 108.degree. F., and 108.degree. F. The mixture was introduced into a spray drier yielding a particulate support matrix product having a bulk volume of about 60 ml and a porosity of 3.7 ml/g. Dissolution time of the matrix was about 5 seconds.

The following components were added to a quantity of purified water sufficient to produce a mixture with a volume of 400 ml. pH was 3.0.

The mixture was introduced into a Buchi model 190 spray drier with a heat setting of 10, an aspirator setting of 5, a flow rate setting of 4.27, an initial flow control setting of 700 (changing to 600 after the first time interval and to 550 after the second time interval), and a vacuum setting of -20. Chamber temperatures were measured at approximately 5 minute consecutive intervals during the drying process. The temperatures at the flow inlet point were 155.degree. F., 150.degree. F., and 155.degree. F. The temperatures at the flow outlet point (the point where the dried product exits the drying chamber to product collector) were measured as 114.degree. F., 109.degree. F. and 108.degree. F. The mixture was introduced into a spray drier yielding a particulate support matrix product having a bulk volume of about 70 ml and a porosity of 5.11 ml/g. Dissolution time of the support matrix was from 2-10 seconds.

The following components were added to a quantity of purified water sufficient to produce an acidic mixture "Part A" with a volume of 100 ml.

The following components were added to a quantity of purified water to produce a basic mixture "Part B" with a volume of 100 ml.

The two mixtures were mixed as introduced into a Buchi model 190 spray drier with the heat settings shown below, aspirator settings shown below, a flow rate setting of 4.27, a flow control setting of 700, and a vacuum setting of -20, as shown below. Chamber temperatures were measured at approximately 5 minute consecutive intervals during the drying process. These temperatures are shown as inlet and outlet readings below. The mixture was introduced into a spray drier yielding a particulate support matrix product having a bulk volume of about 50 ml.

The following components were added to a quantity of purified water sufficient to produce an acidic mixture "Part A" with a volume of 100 ml.

The following components were added to a quantity of purified water to produce a basic mixture "Part B" with a volume of 200 mL.

The mixture was introduced into a Buchi model 190 spray drier with heat settings shown below, aspirator settings shown below, a flow rate setting of 4.27, a flow control setting of 700, and a vacuum setting of -30. Chamber temperatures were measured at approximately 5 minute consecutive intervals during the drying process. The temperatures at the flow inlet point and outlet point are shown below. The mixture was introduced into a spray drier yielding a particulate support matrix product having a bulk volume of about 70 ml. The resulting particulate support matrix had a dissolution time of from 6-10 seconds.

The following components were added to a quantity of purified water sufficient to produce a mixture with a volume of 300 ml. pH was 3.0.

The mixture was introduced into a Buchi model 190 spray drier with a heat setting of 10, an aspirator setting of 5, a flow rate setting of 4.27, an initial flow control setting of 700 (changing to 650 after the first time interval), and a vacuum setting of -20. Chamber temperatures were measured at approximately 5 minute consecutive intervals during the drying process. The temperatures at the flow inlet point were 156.degree. F., 156.degree. F., 156.degree. F., 156.degree. F., and 155.degree. F. The temperatures at the flow outlet point (the point where the dried product exits the drying chamber to product collector) were measured as 114.degree. F., 108.degree. F., 92.degree. F., 89.degree. F., and 84.degree. F. The mixture was introduced into a spray drier yielding a particulate support matrix product having a bulk volume of about 150 ml and a porosity of about 6.3 ml/g. Dissolution time of the support matrix was about 5-15 seconds.

The following components were added to a quantity of purified water sufficient to produce a mixture with a volume of 500 ml. pH was 8.7.

The mixture was introduced into a Buchi model 190 spray drier with a heat setting of 10, an aspirator setting of 5, a flow rate setting of 4.27, an initial flow control setting of 700 (changing to 650 after the first time interval), and a vacuum setting of -20. Chamber temperatures were measured at approximately 5 minute consecutive intervals during the drying process. The temperatures at the flow inlet point were 160.degree. F., 157.degree. F., 157.degree. F., 156.degree. F., and 155.degree. F. The temperatures at the flow outlet point (the point where the dried product exits the drying chamber to product collector) were measured as 115.degree. F., 108.degree. F., 107.degree. F., 108.degree. F., and 108.degree. F. The mixture was introduced into a spray drier yielding a particulate support matrix product having a relatively small bulk volume of 70 ml and having a porosity of about 3.9 ml/g. Dissolution time was about 5-20 seconds.

The following components were added to a quantity of purified water sufficient to produce a mixture with a volume of 500 ml. pH was 3.5.

The mixture was introduced into a Buchi model 190 spray drier with a heat setting of 10, an aspirator setting of 7, a flow rate setting of 4.27, an initial flow control setting of 700 (changing to 670 after the third time interval), and a vacuum setting of -20. Chamber temperatures were measured at approximately 5 minute consecutive intervals during the drying process. The temperatures at the flow inlet point were 156.degree. F., 155.degree. F., 156.degree. F., 155.degree. F., and 155.degree. F. The temperatures at the flow outlet point (the point where the dried product exits the drying chamber to product collector) were measured as 117.degree. F., 113.degree. F., 106.degree. F., 108.degree. F., and 107.degree. F. The mixture was introduced into a spray drier yielding a particulate support matrix product having a bulk volume of about 175 ml with a porosity of 6.6 ml/g. Dissolution time was 3-4 seconds.

The following components were added to a quantity of purified water sufficient to produce a mixture with a volume of 1000 ml. pH was 4.5.

The mixture was introduced into a Buchi model 190 spray drier with a heat setting of 9, an aspirator setting of 6 (changing to 7 after the first time interval), a flow rate setting of 5, an initial flow control setting of 700 (changing to 600 after the first time interval and to 500 after the fourth time interval), and a vacuum setting of -20. Chamber temperatures were measured at approximately 5 minute consecutive intervals during the drying process. The temperatures at the flow inlet point were 139.degree. F., 143.degree. F., 144.degree. F., 144.degree. F., and 142.degree. F. The temperatures at the flow outlet point (the point where the dried product exits the drying chamber to product collector) were measured as 102.degree. F., 94.degree. F., 97.degree. F., 104.degree. F., and 94.degree. F. The mixture was introduced into a spray drier yielding a particulate support matrix product having a bulk volume of about 150 ml and a porosity of 8.7 ml/g. Dissolution time was about 5-15 seconds.

The following components were added to a quantity of purified water sufficient to produce a mixture with a volume of 500 ml. pH was 4.3.

The mixture was introduced into a Buchi model 190 spray drier with a heat setting of 9, an aspirator setting of 6, a flow rate setting of 5, a flow control setting of 620, and a vacuum setting of -20. Chamber temperatures were measured at approximately 5 minute consecutive intervals during the drying process. The temperatures at the flow inlet point were 148.degree. F., 147.degree. F., 147.degree. F., 147.degree. F., and 147.degree. F. The temperatures at the flow outlet point (the point where the dried product exits the drying chamber to product collector) were measured as 116.degree. F., 105.degree. F., 103.degree. F., 102.degree. F., and 102.degree. F. The mixture was introduced into a spray drier yielding a particulate support matrix product having a bulk volume of about 100 ml and a porosity of about 7.5 ml/g. Dissolution time was 5-10 seconds.

The following components were added to a quantity of purified water sufficient to produce a mixture with a volume of 500 ml. pH was 4.10.

The mixture was introduced into a Buchi model 190 spray drier with a heat setting of 9, an aspirator setting of 6, a flow rate setting of 5, an initial flow control setting of 700 (changing to 650 after the second time interval), and a vacuum setting of -20. Chamber temperatures were measured at approximately 5 minute consecutive intervals during the drying process. The temperatures at the flow inlet point were 154.degree. F., 148.degree. F., 145.degree. F., 145.degree. F., 145.degree. F. and 147.degree. F. The temperatures at the flow outlet point (the point where the dried product exits the drying chamber to product collector) were measured as 104.degree. F., 104.degree. F., 98.degree. F., 95.degree. F., 95.degree. F. and 98.degree. F. The mixture was introduced into a spray drier yielding a very hygroscopic particulate support matrix product having a bulk volume of about 100 ml and a porosity of about 4.05 ml/g. Dissolution time was 5-15 seconds.

The following components were added to a quantity of purified water sufficient to produce a mixture with a volume of 500 ml. pH was 4.0.

The mixture was introduced into a Buchi model 190 spray drier with a heat setting of 8, an aspirator setting of 6, a flow rate setting of 5, an initial flow control setting of 700 (changing to 600 after the first time interval), and a vacuum setting of -20. Chamber temperatures were measured at approximately 5 minute consecutive intervals during the drying process. The temperatures at the flow inlet point were 131.degree. F., 131.degree. F., 131.degree. F., 131.degree. F., 131.degree. F. and 131.degree. F. The temperatures at the flow outlet point (the point where the dried product exits the drying chamber to product collector) were measured as 94.degree. F., 94.degree. F., 94.degree. F., 95.degree. F., 95.degree. F. and 95.degree. F. The mixture was introduced into a spray drier yielding a granular particulate support matrix product having a bulk volume of about 250 ml and a porosity of about 6.8 ml/g. Dissolution time was about 2-3 seconds.

The following components were added to a quantity of purified water sufficient to produce a mixture with a volume of 1000 ml. pH was 4.5.

The mixture was introduced into a Buchi model 190 spray drier with a heat setting of 8, changing to 8.5 after the second time interval, an aspirator setting of 6, a flow rate setting of 5, a flow control setting of 700, and a vacuum setting of -20. Chamber temperatures were measured at approximately 5 minute consecutive intervals during the drying process. The temperatures at the flow inlet point were 139.degree. F., 131.degree. F., 141.degree. F., 138.degree. F., 137.degree. F., 136.degree. F. and 137.degree. F. The temperatures at the flow outlet point (the point where the dried product exits the drying chamber to product collector) were measured as 96.degree. F., 89.degree. F., 93.degree. F., 92.degree. F., 93.degree. F., 93.degree. F. and 93.degree. F. The mixture was introduced into a spray drier yielding a particulate support matrix product having a bulk volume of about 300 ml and a porosity of about 12.7 ml/g. Dissolution time was 1-5 seconds. When a binding agent (PVP-40, 0.3 g) was added to a particulate matrix produced from this mixture, the dissolution time was 2-5 seconds in tablet form.

The following components were added to a quantity of purified water sufficient to produce a mixture with a volume of 1000 ml. pH was 4.0.

The mixture was introduced into a Buchi model 190 spray drier with a heat setting of 8.8 which increased to 9.0 after the third time interval, an aspirator setting of 2 which changed to 3 after the second time interval, a flow rate setting of 5, a flow control setting of 700, and a vacuum setting of -20. Chamber temperatures were measured at approximately 5 minute consecutive intervals during the drying process. The temperatures at the flow inlet point were 141.degree. F., 140.degree. F., 137.degree. F., 144.degree. F., 144.degree. F. and 145.degree. F. The temperatures at the flow outlet point (the point where the dried product exits the drying chamber to product collector) were measured as 107.degree. F., 94.degree. F., 96.degree. F., 97.degree. F., 99.degree. F., and 92.degree. F. The mixture was introduced into a spray drier yielding a particulate support matrix product having a bulk volume of about 275 ml and a porosity of about 21 ml/g. Dissolution time was 1-5 seconds. A tablet produced from this matrix dissolved in about 3-5 seconds. When a quantity of an effervescent agent was added to the matrix prior to forming the tablet, the dissolution time was reduced to 1-5 seconds.

The following components were added to a quantity of purified water sufficient to produce a mixture with a volume of 1000 ml. pH was 4.10.

The mixture was introduced into a Buchi model 190 spray drier with a heat setting of 8.9, an aspirator setting of 2 which changed to 1 after the third time interval, a flow rate setting of 5, a flow control setting of 600, and a vacuum setting of -20 which changed to -15 after the second time interval. Chamber temperatures were measured at approximately 5 minute consecutive intervals during the drying process. The temperatures at the flow inlet point were 143.degree. F., 144.degree. F., 145.degree. F., 145.degree. F., 145.degree. F. and 145.degree. F. The temperatures at the flow outlet point (the point where the dried product exits the drying chamber to product collector) were measured as 96.degree. F., 95.degree. F., 94.degree. F., 94.degree. F., 94.degree. F. and 94.degree. F. The mixture was introduced into a spray drier yielding a particulate support matrix product having a coarse texture and a bulk volume of about 200 ml and a porosity of about 20.5 ml/g. Dissolution time was 2-3 seconds.

The following components were added to a quantity of purified water sufficient to produce a mixture with a volume of 1000 ml. pH was 4.0.

The mixture was introduced into a Buchi model 190 spray drier with a heat setting of 8.9, an aspirator setting of 2 which was changed to 1 after the second time interval, a flow rate setting of 5, an initial flow control setting of 700 (changing to 650 after the second time interval), and a vacuum setting of -20. Chamber temperatures were measured at approximately 5 minute consecutive intervals during the drying process. The temperatures at the flow inlet point were 141.degree. F., 145.degree. F., 143.degree. F., 144.degree. F., 144.degree. F. and 144.degree. F. The temperatures at the flow outlet point (the point where the dried product exits the drying chamber to product collector) were measured as 92.degree. F., 93.degree. F., 91.degree. F., 87.degree. F., 87.degree. F. and 87.degree. F. The mixture was introduced into a spray drier yielding a particulate support matrix product having a bulk volume of about 300 ml and a porosity of about 23 ml/g. Dissolution time was about 2-3 seconds. A tablet formed from this mixture (except for Explotab) had a dissolution time of from 1-5 seconds. When the tablet was coated with 0.5% PVP-10 in chloroform, dissolution time was 2-5 seconds.

The following components were added to a quantity of purified water sufficient to produce a mixture with a volume of 1000 ml. pH was 4.2.

The mixture was introduced into a Buchi model 190 spray drier with a heat setting of 8.9, an aspirator setting of 1, a flow rate setting of 5, a flow control setting of 650, and a vacuum setting of -15. Chamber temperatures were measured at approximately 5 minute consecutive intervals during the drying process. The temperatures at the flow inlet point were 152.degree. F., 142.degree. F., 145.degree. F., and 145.degree. F. The temperatures at the flow outlet point (the point where the dried product exits the drying chamber to product collector) were measured as 90.degree. F., 81.degree. F., 86.degree. F., and 87.degree. F. The mixture was introduced into a spray drier yielding a particulate support matrix product having a rather small bulk volume of about 150 ml and a porosity was about 15 ml/g. Dissolution time was about 5 seconds.

The following are examples of coating compositions which can be used to coat the formed tablets. Coating agents can be applied by dropping, by spraying or by passing the tablet through an environment saturated with the coating agent.

Both formulas VI and VII are preferred coating compositions due to their tendency to leave tablet volume unaffected. Solvents other than ether, alcohol and chloroform may be used. These include ethyl acetate and other types of organic solvents.

Changes may be made in the construction and the operation of the various components, elements and assemblies described herein or in the steps or the sequence of steps of the methods described herein without departing from the spirit and scope of the invention as defined in the following claims.