SPRAY DRIED N-ACETYL-P-AMINOPHENOL COMPOSITIONS AND METHOD FOR MANUFACTURE THEREOF

Abstract: Spray dried compositions are disclosed comprising agglomerates of N-acetyl-p-aminophenol in a gelatinized starch matrix; said compositions prepared by spray drying a slurry including N-acetyl-p-aminophenol and gelatinized starch and optionally including other active ingredients such as codeine salts; said spray dried compositions having good compressibility and flow properties facilitating the formation of tablets, capsules and other dosage forms.

Description: SPRAY DRIED N-ACETYL-p-AMINOPHENOL COMPOSITIONS AND METHOD FOR MANUFACTURE THEREOF The invention relates to spray dried compositions comprising agglomerates of N-acetyl-p-aminophenol in a gelatinized starch matrix and to a method for manufacture thereof. Unlike N-acetyl-p-aminophenol, aspirin can be dry mixed with starch and is easily compressible into tablets. Since N-acetyl-p-aminophenol and aspirin are sold competitively as analgesics and antipyretics, it would be desirable if N-acetyl-p-aminophenol could be provided in a form which is easily compressible into tablets. In the past, most N-acetyl-p-aminophenol tablets have been prepared from a wet granulation including a binder with the N-acetyl-p-aminophenolwhich is dried, mixed with lubricants and disintegrating agents and compressed into tablets. This process involves many processing steps, each of which is subject to operator error. Less commonly, N-acetyl-p-aminophenol tablets have been prepared from spray dried particles of N-acetyl-paminophenol coated with gelatin; this material is simply mixed with lubricants, disintegrating agents and auxiliary binders and compressed, e.g. British Patent No. 1,287,431. Compared to the products of the present invention, such spray dried formulations as are commercially available are lacking in bulk density and are less free flowing, while tablets made therefrom are excessively friable. Such com mere'ally available formulations also tend to be dusty and hygroscopic. Gelatine, unlike starch, is an animal product and chemically varies with its origin. This variation has a eleterious effect on the compression characteristics of the spray dried N-acetyl-p-aminophenol product. The present invention accordingly seeks to provide a spray dried N-acetyl-p-aminophenol composition which is compressible into tablets and can be used for filling capsules or the lie. It also seeks to provide for the manufacture of such compositions. The invention accordingly comprises the compositions and methods hereinafter described, the scope of the invention being indicated in the subjoined claims. Spray dried compositions of the present invention comprise N-acetyl-p-aminophenol in a gelatinized starch matrix; such compositions are formed by spray-drying a slurry containing N-acetyl-p-aminophenol and starch, said starch being present in a matrix forming amount such that when the composition is spray dried as described hereinafter, particles of general spherical shape are formed. Generally the gelatinized starch does not comprise more than 25 percent by weight of'the aforementioned composition but less than 1.5 percent by weight in most cases will not form an effective matrix. If the spray dried composition is to be tabletted, the gelatinized starch is effectively present in an amount from 7 to 12 percent by weight and more preferably from 7 to 10 percent by weight If the spray dried composition is to be used for filling capsules or the like, the gelatinized starch may be present in a lesser amount. Although pregelatinized starch USP is preferred as the binder, nongelatizined starch in other forms may be used as long as it is gelatinized before spray drying is complete. For exampie, starch USP, modified starches and so forth may all be used. The N-acetyl-p-aminophenol, in the form of a finely divided powder, may be added to a solution or. dispersion of the starch. For ease of incorporation, however, the starch is pre-blended with an equal amount of N-acetyl-p-aminophenol and charged into a suitable high shear mixing device prefilled with water in an amount sufficient to provide a smooth slurry. With continued mixing, the remaining N-acetyl-p-aminophenol is added and mixing further continued until a smooth slurry is formed. The minimum amount of water should be used such that the slurry is pumpable. For this purpose, the slurry should have a solids content from 40 to 60 percent by weight and preferÅably no more than 50 percent. Greater amounts of water can be used of course, but the process becomes less economic since substantialiy all of the water must be removed during spray drying and if lesser amounts are used such that the solids content is greater than 60 percent by weight, -the slurry is not easily handled with commonly available equipment. The particle size of the N-acetyl-p-aminophenol has an. effect on the spray dried product. For example, it has been found that if more than 50 percent by weight of the N-dcetyl-p-aminophenol particles are larger than 200 mesh (U.S. Standard Sieve), then the spherical conformation of the spray dried particles is adversely effected. For use in the present invention, preferably all of the N-acetyl-paminophenol particles will pass through a 200 mesh screen, more preferably 75 percent will pass through a 325 mesh screen and most preferably all will pass through a 325 mesh screen. The slurry is then spray dried under spray drying conditions such that particles of N-acetyl-p-aminophenol in a starch matrix are formed. The size of the spray dried particles is tailored to the particular application. If the spray dried product is to be compressed into tablets, preferably 80 percent of the particles are coarser than 200 mesh while 95 percent are finer than 40 mesh. The water content of the spray dried particles also has an effect on the product. If the product is to be compressed into tablets, it is preferred that it have a moisture content in the range of 0.3 to 1.5 percent by weight water. If more than 1.5 percent by weight water is left in the product, then it is too wet to be free flowing and may support bacterial growth and if less than 0.3 percent is left, the compressibility of the product is adversely effected and the fri:hility of tablets rade from this material increases. If the product is to be used for filling capsules or the like, the spray dried product may contain less than 0.3 percent water but, even then, sufficient water must be left in the product to prevent the build up of a static charge which must be prevented to provide good flow. Moisture retaining agents can be added to the slurry before it is spray dried to maintain the moisture content. Higher levels of starch will also aid in retaining moisture. Suitable spray drying conditions depend upon the nature of the spray drying equipment, whether cocurrent or countercurrent, its size and configuration, the mode of atomization and like factors. Necessary atomization pressure, inlet and outlet temperature and air flow will also depend on the solids content of the slurry and the particle size and moisture content wanted in the spray dried product. Balancing Of the several variables can be accomplished by those skilled in the art in view of the following examples. In general, however, it is preferred that the outlet temperature be kept below 1500C to avoid yellowing the product and is preferably maintained as low as possible. Other active ingredients can be added to the slurry containing N-acetyl-p-aminophenol before it is spray dried as long as they are compatible witii the starch binder and with N-acetyl-p-aminophenol and can withstand spray drying conditions. Suitable materials satisfying these conditions include alkaloids and ';heir salts such as codeine phosphate. Alternatively, other active ingredients may be dry blended with the spray dried particles of N-acetyl-p aminophenol and formed into dosage units. One advantage in adding the other active ingredients to the N-acetyl-p-aminophenol before it is spray dried is that the active ingred ients are bonded together in-the spray dried particles so that the active ingredients do not separate on shipping. The spray dried particles of the present inven tion may be combined with still other pharmaceutically acceptable materials and made into the desired dosage form. The product may be used, as is, for filling capsules but if it is to be compressed into tablets, it is preferred that lubricants, disintegrants and the like be added before the material is tabletted. Typical lubricants include polyethylene glycols, stearic acid, magnesium stearate, calcium stearate, zinc stearate, hydrogenated vegetable oils, talc or the like. Suitable disintegrants include alginic acid, sodium alginate, starch, sodium carboxymethyl starch and so forth. The following exanples illustrate the invention. EXAliPLE 1 Pregelatinized starch in the amount indicated in Table I was mixed with an equal quantity of N-acetyl-p aminophenol powder and charged to a high shear mixer containing the indicated amount of water. The N-acetyl-paminophenol powder had a particle size such that all of it passed through a 200 mesh screen and 75 percent passed through a 325 mesh screen. Additional N-acetyl-paminophenol powder was added such that the resultant mixture contained the indicated amount of N-acetyl-p-aminophenol and mixing continued until a smooth slurry was formed. Table I Composition Ingredients Parts by Weight Pregelatinized Starch, USP 1.5 5 7 10 N-acetyl-p-aminophenol 98.5 95 93 90 H20 100 122 122 122 The resultant slurry was spray dried under the conditions shown in Table II. TABLE II SPRAY DRYER TYPE Countercurrent: Disc Atomizer Inlet Temperature 2200C. Outlet Temperature 9000. Atomization Pressure 600 psi Nozzle Atomizer Inlet Temperature 2200cm Outlet Temperature 85 C. Atomization Pressure 600 psi Cocurrent: Nozzle Atomizer Inlet Temperature 5000F Outlet Temperature 1500F Atomization Pressure 1450 psi Satisfactory countercurrent conditions were found for disc atomizers with an atomization pressure between 600-900 psi, an inlet temperature between 170-2600C; and an outlet temperature between 60-1200C. Corresponding conditions for nozzle atomizers were between 180-2600C. for the inlet temperature and 70-1200C. for the outlet temperature. Suitable cocurrent conditions were found for nozzle atomizers with an atomization pressure between 1300 - 1700 psi, an inlet temperature between 460-5700F and an outlet temperature between 140-180 F. Spray dried product was evaluated for particle size, flow properties and bulk density as shown in Table III. Table III Particle Size Percent by eight X Cumulative Pregelatinized Stzrch/-acetyl-p-aminophenol 1.5/98.5 5/95 7/93 10/90 +60 4.9 20.5 -- - +80 39.6 63.1 15.5 56.5 +100 56.2 80.9 -36.2 73.5 +140 -- 95.6 71.1 94.6 +200 94.7 98.9 86.6 99.6 +325 -- -- -- -- +400 -- -- -- -- -400 100.0 100.0 100.0 100.0 Flow Properties gm/sec 17.3i good good good Bulk Density gm/cc 0.346 0.382 b.415 0.417 particle size was measured with a Sonic Sifter, Model L3P sold by ATM Corporation of Milwaukee, Wisconsin. good. The spray dried material was tabletted and compared with naterial prepared by conventional procedures as shown in Table IV. Table IV Percent by Weight Pregelatinized Starch/ Compressive Max Fri N-acetyl-p-aminoPhenol Force (kg) Hardness(kg) ability() Spray Drying 5/95 560 5.6 -7/93 950 10.11 0.28 10/90 1150 14.8 0.2 Glatt Fluid Bed Granulation 5/95 1070 1.7 -10/90 1200 8.1 - Conventional Wet Granulation 10/90 950 5.1 1.0 EXAMPLE 2 Spray dried product as described in Example 1 comprising 7% pregelatinized starch and 93% N-acetyl-paminophenol was dried to the moisture content indicated in Table V and compressed into tablets. The effect of moisture on tablet hardness and friability is also indicated. Table V Sample Moisture . Compressive Tablet Hard- . Fria No. Content(%) Force (kg) ness (g) bility(%) Control 0.72 670 8.1 0.96 0.72 970 11.3 0.27 1 0.60 555 6.0 1.55 0.60 960 9.8 . 2.10 2 0.54 560 5.1 1.71 0.54 930 8.8 0.60 3 0.43 565 4.7 1.97 0.43 750 6.5 1.03 4 0.26 560 4.6 2.70 0.26 935 7.5 3.80 EXAMPLE 3 Spray dried product as described in Example 1 comprising 10% pregelatinized starch and 90% N-acetyl-paminophenol was dried to the moisture content indicated in Table VI and compressed into tablets. The effect of moisture on tablet hardness and friability is also indicated. Table VI Sample Moisture Compressive Tablet Hard- Fria No. Content(%) Force (kg) ness (kg) bility(%) Control 0.75 560 6.6 0.74 0.75 950 -10.9 0.29 1 0.66 570 6.3 - 1.41 0.66 940 10.2 '0.32 2 0.57 565 5.7 1.60 0.57 935 9.5 0.48 3 0.48 565 4.7 1.28 0.48 945 7.9 0.66 4 0.29 560 4.8 2.40 0.29 935 8.3 0.80 EXAMPLE 11 Following the procedure of Example 1, when a codeine salt is added to the N-acetyl-p-aminophenol and the slurry is spray dried and the dried product then mixed with suitable tabletting excipients, tablets having the following cOmDositiOn ranges can be prepared: N-acetyl-p-aminophenol 300-550 mg, codeine salt 15-60 mg and pregelatinized starch 2-25 percent by weight. In view of the above, it will be seen that the several objects of the invention are achieved and other advantageous results attained. As various changes could be made in the above compositions and methods without departing from the scope of the invention, it is intended that all matter contained in the above description shall be interpreted as illustrative and not in a limiting sense.

Claims: CLAIMS 1. A method for preparing a spray dried N-acetyl-p-aminophenol composition, said method comprising: (a) forming a slurry of finely divided N-acetyl-paminophenol and starch; (b) spray drying said -slurry under spray drying conditions such that the spray dried particles have a moisture content between 0.3 and 1.5 percent by weight, said starch being gelatinized either prior to said spray drying step or during said step. 2. The method of claim 1 wherein the gelatinized starch comprises 7 to 12 percent by weight of said composition. 3. The method of claim 1 or claim 2 wherein the slurry contains no more than 60 percent by weight solids and wherein said solids comprise 98.5 to 75 percent by weight of N-acetyl-p-aminophenol and 1.5 to 25 percent by weight of starch. 4. The method of any one of claims 1 to 3 wherein another compatible active ingredient is substituted for part of the N-acetyl-p-aminophenol. 5. The method of claim 4 wherein the active ingredient is an alkaloid or salt thereof. 6. The method of claim 5 wherein the alkaloid salt is codeine phosphate. 7. The method of any one of claims 1 to 6 wherein 100 percent of the finely divided N-acetyl-p-aminophenol will pass through a 200 mesh screen and 75 percent will pass through a 325 mesh screen. 8. The method of any one of claims 1 to 7 wherein the gelatinized starch is pregelatinized starch. 9. The method of any one of claims 1 to 8 wherein at least 80 percent of the spray dried particles are coarser than 200 mesh, while 95 percent are finer than 40 mesh. 10. A composition comprising spray dried particles of N-acetyl-p-aminophenol in a starch matrix wherein the moisture content is between 0.3 and 1.5 percent by weight, said starch being gelatinized. 11. The composition of claim 10 wherein the gelatinized starch comprises between 1.5 and 25 percent by weight of the solids content. 12. The composition of claim 10 or claim 11 wherein another compatible active ingredient is substituted for part of the N-acetyl-p-aminophenol. 13. The composition of claim 12 wherein the active ingredient is an alkaloid or salt thereof. 14. The composition of claim 13 wherein the alkaloid salt is codeine phosphate.

Inventors: SALPEKAR, ANIL M.
Applicants: MALLINCKRODT, INC.
Application year: 1981
Main classification: A61K9
IPC codes: A61K9, A61P25, A61P29, A61K31