Pharma Ingredients
The Choice for No. 5, October 2000 your Success Excipients & Actives for Pharma
Dear reader, Riboflavin 100 page 2–3 Y You may have known ExAct for nearly three years as a customer’s Kollicoat SR 30 D page 4–5 newsletter with its main focus on pharmaceutical excipients. Y Kollidon VA 64 page 6–7 This year the pharma active ingredients business within the BASF One Source: group has been reorganized in order to provide you with an page 8–11 intensified and integrated service fulfilling your needs. The Portfolio Preview page 12 BASF now provides a whole range of pharma ingredients from one source. By focusing on our comprehensive portfolio of News page 12 actives, excipients and vitamins and offering a complete technical New Media page 12 application and formulation support, we guarantee process safety as well as freedom in application while enhancing our customers’ long-term product and market success. Calendar The ExAct newsletter will continue to provide you with recent th nd findings, application data and experience relating to our widened 30 January to 2 February, 2001 product range for the pharmaceutical industry. Informex New Orleans*, USA th st 19 to 21 April, 2001 PIM (Fair for Pharmaceutical Ingredients) Kuala Lumpur, Malaysia th th Yours sincerely, 11 to 13 June, 2001 INTERPHEX Asia (Internat. Exposition BASF Aktiengesellschaft for the Pharmaceutical Industry) Marketing Singapur, Singapore Pharma Ingredients rd th 23 to 27 June, 2001 28th International Symposium on Controlled Release of Bioactive Materials San Diego*, USA th th 10 to 12 July, 2001 Gabriel Tanbourgi CPhI, Pharmaceutical Ingredients China Shanghai, China Imprint rd th 3 to 5 October, 2001 CPhI, Pharmaceutical Ingredients Worldwide Publisher: London*, United Kingdom BASF Aktiengesellschaft st th Editorial staff: 21 to 25 October, 2001 Dr. Volker Bühler, Valérie Filiatreau, AAPS (American Association of Pharmaceutical Dr. Hubertus Folttmann, Patrick Glaser, Scientists) Annual Meeting Klaus Kalter, Dr. Karl Kolter, Dr. Siegfried Lang Denver*, USA th th Concept/Layout: 9 to 12 November, 2001 MLW KommunikationsForm PHARMA INDIA (Internat. Congress and GmbH Werbeagentur, Mannheim Exposition for the Pharmaceutical Industry) Mumbai, India Print: Frotscher Druck, Darmstadt * BASF will be represented. BASF ExAct page 2 – No. 5, October 2000
Riboflavin 100
Vitamin B2 in a new shape. U. Sindel
Introduction In general, direct-compressible actives have gained more and more importance. Expensive and time consuming granulation steps are avoided – if possible – and replaced by direct compression. Therefore the demand for direct-compressible substances increased within the last years. This is especially the case for substances which are difficult to handle in their pure 12 crystalline form like Riboflavin. Crystalline Riboflavin shows poor flowability and bad dissolution properties. Microscope photograph of Riboflavin 100 (1) and Therefore BASF invested in new technology to synthetic Riboflavin (2); magnification: x126. produce an improved direct-compressible product specially designed for the food/pharma requests. Moreover it shows better results in the electrostatic charging test. These two factors determine the superior Direct-compressible Riboflavin formulations generally handling and processing properties of Riboflavin 100. consist of granules with a certain amount of excipients 56 to provide binding and disintegration properties. BASF Purity offers a direct-compressible 100% grade which HPLC tests prove that beside its excellent physical Flowability of Riboflavin 100 (5) and synthetic combines the advantages of improved powder prop- properties Riboflavin 100 shows also outstanding Riboflavin. (6) erties and optimized release rates with the highest quality regarding purity of the material. Whereas possible potency: Riboflavin 100. synthetic Riboflavin includes several by-products (10), Volume [%] BASF’s Riboflavin 100 has less additional peaks with 20 Manufacture remarkable lower quantity (9). Riboflavin 100 is manufactured by a natural fermenta- tion process using a non-GMO microorganism, Food fortification 10 Ashbaya gossypii. Since the soy products utilized for In addition to its excellent handling properties, Ribo- the fermentation are also not genetically modified we flavin 100 shows good mixing behavior with reduced are able to supply our customer with a GMO-free tendency to subsequent segregation. A typical example product. The fermentation process guarantees a in food fortification is the flour test. A flour mixture con- 0 product of highest quality and purity. taining three percent of Riboflavin is mixed thoroughly 0.1 1.0 10.0 100.0 1000.0 Particle Diameter [µm] and sieved. The less flour mixture remains upon sieve Technical advantages of Riboflavin 100 250 µm the better the mixture. As can be seen in Particle size distribution of Riboflavin 100. (7) picture (11), BASF’s Riboflavin 100 has considerably Volume [%] Outstanding product properties: better mixing and sieving properties. These results 20 homogeneous particle size can also be expected in the fortification of other food good flowability products like instant powders. The fortification of soft high purity drinks or other liquids in the range of typical pH values
reduced dusting with Riboflavin 100 results in the same color as with 10 good compressibility synthetic Riboflavin. excellent dissolution
Particle form 0 0.1 1.0 10.0 100.0 1000.0 Many of the disadvantages in handling synthetic Particle Diameter [µm] Riboflavin result from its particle form (2). Particles in form of needles show poor flow properties (6) and low Particle size distribution of synthetic Riboflavin. (8) bulk density (4). Especially the production of high potency Riboflavin tablets becomes difficult or even Tabletting properties impossible. BASF’s Riboflavin 100 however consists Identical coloration compared to synthetic Riboflavin is of round particles (1) with a smooth surface leading also achieved for the use of Riboflavin 100 in pharma to a higher bulk density (3). applications like tablets. Good flowability and homo- geneous particle size distribution result in excellent Flowability tabletting properties. Even formulations containing 50 34 Due to the round particle form and its slightly coarser mg and more of Riboflavin per tablet are easily com- particle size (7, 8), Riboflavin 100 has an improved Bulk density of Riboflavin 100 (3) [0.35 g/ml] and pressible and show excellent dissolution. The dissolu- flowability compared to the synthetic material (5). synthetic Riboflavin (4) [0.12–0.18 g/ml]. tion in water has been improved compared to synthetic page 3–No.5,October2000 mAU mAU 100 released rate [%] 100 20 20 40 60 80 40 60 80 100 0 0 20 40 60 80 0 06 01010 8 20 4 20 0 30 360 330 300 270 240 210 180 150 120 90 60 30 0 0 5 2 5 min 25 20 15 10 5 0 5 2 5 min 25 20 15 10 5 minutes 100. 50 mgofRiboflavin of tabletscontaining Dissolution profile 100. of syntheticRiboflavin HPLC chromatogram of Riboflavin 100. HPLC chromatogram (12) (10) (9) regarding dissolutionspeedintabletformulations. after 30minutesindicatesclearlyahighreliability even Riboflavin 100tablets.Thereleaserateof75% (12) within45min.Figure containing Riboflavinis75% The USPrequirementforthedissolutionoftablets resulting inabout70Nhardnesswithoutanyfriability. manufactured atalowcompressionforceof4kN A tabletcontaining50mgofRiboflavin 100 was a highperformancedissolutionisrequired. Riboflavin. Thisgivesbenefitsinapplicationswhere synthetic Riboflavin. Flour testwithRiboflavin 100 incomparisonwith Dissolution Tablet mass Aerosoil 200 Magnesium stearate Avicel PH 102 Ludipress Kollidon CL Riboflavin 100 Table 1: loss: 20–40% Riboflavin 100
powder properties arerequired. choice fordifficultformulationswhere excellent tions. Thereforeitshouldbethe productof properties forfoodaswellpharma applica- product ofhighqualitywithgood handling Riboflavin 100hasdemonstrated tobea Conclusions showsthedissolutionprofileofhigh-potency loss: 1–4% Vitamin B Vitamin B Riboflavin Synthetic
Composition pertablet 2 2 upon sieve 250 (11) BASF µ m through sieve 50 Ex 307 mg 160 mg µ 50 mg 80 mg m 2 mg 9 mg 6 mg Act BASF ExAct page 4 – No. 5, October 2000
KollicoatY SR 30 D
Influence of additives on the properties of films and coated dosage forms. K. Kolter, T. Rock
Introduction Table 2: Composition and preparation was first added to the given amount of water. Then Controlled release film coatings generally do not of the spray suspension Kollidon SR 30 D was stirred in. The pigment disper- consist only of the controlled release polymer but also sion was homogenized using a corundum mill and contain various excipients such as plasticizers, added slowly to the polymer dispersion while stirring. Parts by Compo- coloring agents, antitack additives, pore formers or Polymer dispersion suspension stabilizers. These additives have differing weight (g) sition (%) Table 3: Coating process degrees of influence on a variety of film properties, the The coating was applied on 0.5 kg caffeine dissolution rate and the film coating process. Kollicoat pellets in a fluidized bed coater (Aeromatic Kollicoat SR 30 D 190.00 47.0 SR 30 D is a new polyvinyl acetate based polymer Strea 1) under the following conditions: (dry polymer) (57.00) (14.1) dispersion for the manufacture of controlled release 1,2 Propylene glycol 5.66 1.4 coated dosage forms [1]. While the influence of Water 147.97 36.6 Inlet air temperature 60°C plasticizers on the mechanical film properties has Outlet air temperature 35°C already been described [2], no data are yet available Pigment dispersion Atomizing pressure 1.0 bar concerning the other excipients. Talc 14.15 3.5 Spraying rate 11.5 g/min Titanium dioxide 2.02 0.5 Drying 40°C/3 min Purpose SicovitY Red 30 2.02 0.5 Coating level 3 mg/cm2 This study was performed to determine the influence Water 42.45 10.5 Spraying time about 35 min of additives commonly used in coating formulations Solids content of on the coating process and film properties. This Total 404.30 100 the spray suspension 20% knowledge can be used to optimize coating formula- tions and to improve and expedite their development.
Materials and Methods 10% Propylene glycol 10% Triethyl citrate ■ 5% Triethyl citrate Materials ● 5% Triacetin 5% Acetyl tributyl citrate Kollicoat SR 30 D is a polyvinyl acetate dispersion 80 stabilized with polyvinylpyrrolidone and sodium lauryl 70 Dissolution of caffeine 2 Coating level 3mg/cm pellets coated with sulfate (BASF AG); caffeine (Knoll AG), Pharsil 60 Kollicoat SR 30 D and (dimethicone, Wacker); Aerosil 200 (Degussa), 50 Granulac 230 (lactose, Meggle). different plasticizers 40 without further Table 1: Composition and 30 additives. released drug [%] preparation of the pellets 20 (Figure 1)
10 Ingredient (%) 0 Caffeine powder 10 04812162024 time [h] Avicel PH 101 43.75 Granulac 230 43.75 Kollidon VA 64 2.5 ● 0% Talc ■ 25% Talc 50% Talc 75% Talc Total 100 100 Influence of talc on the 90 All ingredients were blended in a Diosna-mixer for 5 Coating level 3mg/cm2 release rate of caffeine 80 minutes, moistened with water until a readily mould- pellets. able mass was obtained (approx. 48% water). The 70 (Figure 2) mass was then mixed thoroughly for another 3 minutes 60 extruded in an Alexanderwerk apparatus with a vertical 50
1.5 mm sieve and the resulting granules were trans- 40 ferred to a spheronizer (Heller) and rounded for 10 released drug [%] 30 minutes. The still moist pellets were dried in a fluidized 20 bed granulator and then sieved to obtain the required particle size (0.7–1.4 mm). 10 0 The recommended addition rate of 1,2 Propylene gly- 04812162024 col is 10% referred to the dry polymer. Propylene glycol time [h] page 5 – No. 5, October 2000 BASF ExAct
Dissolution Dissolution tester (Pharmatest PTW-S), medium: 25% Aerosil 25% Magnesium stearate 50% Magnesium stearate 890 ml 0.08M HCl (0–2 h) and phosphate buffer 25% Tricalcium phosphate 50% Tricalcium phosphate 10% Aerosil pH 6.8 (2–24 h), paddle with 50 rpm. 100 Influence of finely 90 dispersed additives Results and Discussion 80 on drug release of The use of different plasticizers resulted in very similar 70 caffeine pellets. dissolution rates (Figure 1). No differences were (Figure 3) 60 apparent between propylene glycol 10% and triethyl citrate (5% and 10%), while triacetin (5%) and ATBC 50 (5%) produced slightly slower dissolution rates. 40
released drug [%] 30 The excipient talc – widely used in coating preparations 20 – accelerated dissolution with increasing concentration Coating level 3mg/cm2 10 (Figure 2) at constant coating level. It should be noted, however, that especially at very high talc con- 0 04812162024 centrations the polymer content was much lower and time [h] was no longer sufficient to completely bind the solids.
Very fine particulate solids like Aerosil 200, magne- 5% glycerol monostearate 50% glycerol monostearate sium stearate or tricalcium phosphate in higher con- 25% dimethicone 50% dimethicone without additive centrations interfere greatly with film formation, since 100 Influence of glycerol dissolution occurs very rapidly (Figure 3). 90 monostearate and Lipophilic antitack additives like glycerol monostearate 80 dimethicone on drug or dimethicone slow down dissolution in the lower concentration range and accelerate it at higher 70 release of caffeine concentrations (Figure 4). 60 pellets. (Figure 4) 50 The additives had no impact on the curing behavior of 40 the pellets. Even after high thermal stress (24 h/60°C)
released drug [%] 30 dissolution was almost unchanged. Coating formula-
20 tions with several additives also showed the same Coating level 3mg/cm2 behavior (Figure 5). 10
0 Conclusions 04812162024 The type of plasticizer used has almost no time [h] influence on dissolution. Antitack additives in low to medium concentra- 10% Propylene glycol (uncured) 10% Propylene glycol (cured 24h/60°C) tions also hardly affect dissolution. 5% Triethyl citrate (uncured) 5% Triethyl citrate (cured 24h/60°C) 10% Propylene glycol Fine particulate solids markedly accelerate + pigments (uncured) 10% Propylene glycol + pigments (cured 24h/60°C) dissolution, especially at higher concentrations. 5% Triethyl citrate + pigments (uncured) 5% Triethyl citrate + pigments (cured 24h/60°C) Curing effect of 90 caffeine pellets with 80 and without additives. Coating level 3mg/cm2 References (Figure 5) 70 [1] Technical Information KollicoatY SR 30 D 60 June 1999, BASF AG. 50 [2] K. Kolter and F. Ruchatz
40 Proceedings AAPS Congress New Orleans, November 1999, 4225. 30 released drug [%] 20
10
0 04812162024 time [h] BASF ExAct page 6 – No. 5, October 2000
KollidonY VA 64
An excellent dry binder. D. Flick, K. Kolter
Purpose Table 1 (A) (B) (C) Dry binders are intended to improve tablet formation Formulations % % % by direct compression with the main emphasis on improving the mechanical properties [1], i.e. the hardness and friability of the tablets. Apart from mi- Di-Tab 90, 85, 80 – – crocrystalline cellulose and the cellulose ethers, Ascorbic Acid – 40.0 – polyvinylpyrrolidone is probably the best-known dry Ludipress – 51.3, 46.3, 41.3 – binder. An almost unknown dry binder is Kollidon VA Dry Binder 5, 10, 15 5, 10, 15 99.5 64 (copovidone), a vinylpyrrolidone vinyl acetate- Kollidon CL 4.5 3.0 – copolymer (Figure 1)[2]. Aerosil 200 – 0.24 – Magnesium Stearate 0.5 0.5 0.5 (Figure 1) Total 100.0 100.0 100.0
H––––––CH –CH 2–––––––CH –CH 2––––––H N O O O rpm, 12 mm, beveled edge) and (C) with a weight binder content is increased from 25 to 50 to 75 mg, n C m of 500 mg on a Korsch EK0 single punch press Kollidon VA 64 gives the steepest increase in hardness. (30 tablets/min, 12 mm, beveled edge) with varied CH3 Ratio: 6 : 4 compression forces (10, 18, 25 kN). Vitamin C powder (B) was selected as a substance that is very difficult to compress into tablets and in The objective of this study was to investigate the Tablet properties mix-tures with excipients, also greatly reduces effectiveness of different dry binders and to correlate it Hardness, weight and dimensions were determined compressibility. The compression force-hardness with physicochemical properties. using a Kraemer tablet tester (HT-TMB). curves (Figure 4) are similar in appearance to those for the tablets of formulation A: Experimental Methods Results and Discussion Materials The dry binders tested exhibited considerable without dry binder: low hardness Dry Binder: Kollidon 30 (povidone), Kollidon VA 64 differences in their powder properties (Table 2) with HPMC 2910, (copovidone) (BASF AG); Avicel PH 101 (microcrystal- which are of interest with reference to tabletability. Kollidon 30 and line cellulose (FMC); Pharmacoat 606 (hydroxypropyl- MC PH 101: slight improvements methylcellulose 2910) (Shin Etsu); Maldex 18 (malto- The particle size determinations clearly show that with Kollidon VA 64: exceptional hardness dextrin) (Amylum). Kollidon VA 64 is the finest product and should, with its shell like structure (Figure 2), be able to coat drug Because of the polymerized vinyl acetate component, Ingredients and filler particles and bind them together under com- Kollidon VA 64 is a softer and more plastic material Di-Tab (Rhône-Poulenc); ascorbic acid powder, pression. than the other dry binders. This is confirmed by the Ludipress, Kollidon CL (BASF AG); magnesium low glass transition temperature (103°C). stearate (Bärlocher); Aerosil 200 (Degussa). The hardness of the tablets (A) made with Kollidon VA 64 places them in a class of their own (Figure 3). The plasticity values of the products (Figure 5) were Methods determined from the force-displacement curves (C). The dry binders were tested in several formulations At a compression force of 18 kN and a dry binder Kollidon VA 64 possesses a high plasticity of over (Table 1). A dicalcium phosphate tablet (A), with content of 50 mg, the hardness of the tablets exceeds 90% that remains constant from 10 to 18 to 25 kN. excipients which are not soluble in water and a vitamin that of tablets without a dry binder by 120%. If the same C tablet (B), with water-soluble constituents. To obtain compression force is used in each case and the dry detailed information on their compression properties, the pure dry binders were compressed (C). Mean Bulk Hausner Flowability Table 2 Particle Size Density Ratio Angle of Flow time D [4,3] Repose Powder properties bulk and tap density (Erweka volumeter) angle of repose (Pfrengle funnel) [ m] [g/ml] [°] [s] particle size (Malvern Mastersizer) Kollidon 30 50 0,389 1,24 28 7, 5 Tableting Kollidon VA 64 43 0,241 1,37 35 block The ingredients (Table 1) were passed through an MC PH 101 65 0,326 1,40 41 block 800-µm sieve and blended for 10 min in a Turbula HPMC 2910 82 0,367 1,37 42 block mixer. The tablets (A) and (B) with a weight of 500 mg Maltodextrin DE 18 74 0,522 1,34 44 block were produced on a Korsch PH 106 rotary press (30 page 7 – No. 5, October 2000 BASF ExAct
Compression Force: 18 kN Conclusions without dry binder 25 mg dry binder Kollidon VA 64 possesses unique properties as 50 mg dry binder 75 mg dry binder Hardness of a dry binder, irrespective of the formulation, Dicalcium Phoshate which far exceed those of all other materials tablets with tested. 100 increasing amounts Important information can be derived on the of dry binders. 80 effectiveness of dry binders from force displace- (Figure 3) ment curves. 60 The dry binding properties of a substance can
hardness [N] 40 be attributed to various physical properties like particle shape and plasticity. 20
0 without Kollidon 30 Kollidon MC PH 101 HPMC 2910 Maldex 18 References dry binder VA 64 [1] Lieberman, Lachman and Schwartz, Pharmaceutical Dosage Forms, Marcel Dekker (1998). [2] V. Bühler, Kollidon – Polyvinylpyrrolidone for Kollidon VA 64 Kollidon 30 HPMC 2910 the pharmaceutical industry, BASF AG (1996). MC PH 101 without dry binder Maldex 18 140 Compression force – 120 hardness profile of Vitamin C tablets. 100 (Figure 4)
80
60 hardness [N]
40
20 Scanning electron micros- 50 mg dry binder copy Kollidon VA 64. 0 (Figure 2)
5 10 15 20 25 30 compression force [kN]