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Flavomycin® “The original” Content 2 Content OH HO CH3 O HO CH3 CH3 HO O O CH2 CH3 O O HO H3C O O O O CH3 OH O CH3 P OH O H O O O CH3 O NH NH HN CH3 O O COOH Flavomycin O O HO OH NH2 CH3 COOH HO HO OH • Introduction • Stability Flavomycin® compared with generics - Flavomycin 40 and 80 - in feed - in premix • Conclusions 3 Introduction • • • Wallhäuser et al in 1965, designated it as moenomycin Popular names: “bambermycin”, “flavophospholipol”, Flavomycin® Initially recovered from: – Streptomyces bambergiensis – Three other Streptomyces spp. (S. ghanaensis, S. ederensis, and S. geysiriensis) are also identified • Flavophospholipol is stable in: – the pH range from 7 to 9 – the presence of a large variety of enzymes (including trypsin, amylase, lysozyme, and lipase) • • • Is a complex of five active, chemically related, compounds (A, A1/2 C1, C2 and C3), all (Huber et al 1965; Lenoir et al 1970) Characterized as very high molecular weight phosphorus containing glycolipids (1582 g/mol) Biologically, flavophospholipol had particular antibiotic activity against Gram positive bacteria: – no evidence of cross resistance to other antibiotics such as penicillin, tetracycline or macrolides (Wasielewski et al 1965) 4 Flavomycin® Specifications • Flavophospholipol content • Moisture* (2% average) • Heavy Metals o o o o Arsenic ≤ 5 ppm Lead ≤ 10 ppm Cadmium ≤ 5 ppm Mercury ≤ 0.2 ppm * H2O content bound inside the Flavomycin molecule determines heat stability. The Flavomycin molecule is compact due to intra-molecular bounds and contains less H2O molecules, compared with generics. 5 Moisture and pH Loss during drying 9 9% 8 5% 1% 7 pH G en er ic B G en er ic A en er ic G Loss of C 7,5 40 3% Fl av om yc in % 7% pH 8,5 6 Specifications cont’d • • • • • Product description Bulk density (loose) Bulk density (compacted) Flow properties Particle size distribution Visual (aspect, color) Volumetric check Volumetric check Shear cell test Laser diffraction test 7 Typical distribution of FPL components: A, A1/2, C1, C3, C4 % Components distribution % 90 80 70 60 50 40 30 20 10 0 A A1/2 C1 C3 C4 8 Typical distribution of FPL components: A, A1/2, C1, C3, C4 Not the right % spread A1/2 C1 C3 3 er ic 2 G en er ic 1 G en G en er ic 9 8 7 6 5 4 3 2 20 18 16 14 12 10 8 6 4 2 0 1 % Components without A C4 9 Stability data summary 10 Flavomycin 40 and 80 11 Flavomycin® stability data Huvepharma (for regulatory purpose) Stability Flavomycin Huvepharma 12 Fl 80 10 % 8 6 4 Fl 40 2 0 0 1 2 3 6 9 months 40°C RH 75% Moisture 40°C RH 75% Activity 25°C RH 60% Moisture 25°C RH 60% Activity 12 Stability study performed under stress conditions during 20 days at 55°C Flavomycin® vs. generics Residual stability FLP vs. Flavomycin® Evolution of FPL content in % of the claimed activity 100 95 Huvepharma % 90 Generic 1 85 Generic 2 80 Generic 3 75 70 0 5 10 20 Time lines in days 13 Stability Flavomycin® in normal storing conditions vs. generics µg/mg Stability Flavo next to generics 44 42 40 38 36 34 32 30 28 Declared Flavomycin 40 +6md Generic A +9 md Generic B +12 md Generic C 14 IN FEED 15 Stability in different extruded feeds • Flavomycin mixed into piglet and broiler feed undergoing extrusion process • temperature and pressure at head of extruder: 145°C, 50 bar • duration of passage through extruder: 5 to 10 sec. • efficiency of extruder: 300 kg of feed/h values given are the average of 4 replicates Piglet feed Content of active ingredient Broiler feed Mg/kg % Mg/kg % 20 100 20 100 before conditioning 21 105 19 95 after conditioning 19 95 18.8 94 after extrusion, before cooling 21.3 106.5 20.3 101.5 after extrusion and cooling 20.8 104 20.5 102.5 Nominal Actual Ref.: Trial report no. 1358 of International Institute of Feed Technology, Braunschweig, Germany 16 Broiler Feed Stability under Expansion Conditions • Production line consisted of mixer, conditioner, expander, pellet press and cooler; expander yielded 1t / hour • two approaches were run: •one using commercially practiced conditions • the other using maximum conditions technically possible with equipment employed in heat, pressure and energy. Commercial conditions maximum conditions parameters temperature during expansion after expansion after pelleting pressure in expander specific energetic input 90 - 112 ° 95 ° 97 ° 52 bar 33.7 kWh/t 124 - 135 ° 100 ° 100 ° 70 bar 40.8 kWh/t results site of measurement after mixing after conditioning after expansion after pelleting/cooling inclusion, ppm % 28.7 100 25.7 89.5 26.3 91.6 29.3 102.1 inclusion, ppm 28.3 26.0 27.0 28.3 % 100 91.9 95.4 100 Feed contained 5.2 % fat; dosage used for FLAVOMYCIN is not a recommendation, but was used to minimize random variation Ref.: Trial report no. 1457 of “Research Institute for Feed Technology”, IFF, Braunschweig, Germany 17 In Premix 18 Comparison of Flavomycin and Flaveco* under different storage conditions Storage conditions: 25 °C / 50 % h 40 °C / 75 % h Premix: Flavomycin Flaveco Flavomycin Flaveco Batch; Prod. D ate: U 023; 8/98 098051038; 5/98 U 023; 8/98 098051038; 5/98 Expected content; mg/ kg: 40.000 40.000 40.000 40.000 Initial content 1/ 99: 44.200 33.300 44.200 33.300 After 4 weeks storage: 48.133 34.567 42.250 30.000 After 8 weeks storage: 44.050 31.350 40.050 24.950 After 12 weeks storage: 42.500 31.300 37.700 23.000 After 21 weeks storage: 39.800 29.200 36.600 15.600 *Flaveco is based on Chinese FPL 19 Comparison of Flavomycin and Flaveco under different storage conditions Storage condition: 25 °C / 50 % h 50.000 Flavomycin 48.133 45.000 40.000 Flaveco 44.200 44.050 42.500 expected level 39.800 35.000 30.000 33.300 34.567 31.350 31.300 29.200 25.000 20.000 start 4 weeks 8 weeks 12 weeks 21 weeks 20 Comparison of Flavomycin and Flaveco under different storage conditions Storage condition: 40 °C / 75 % h 50.000 Flavomycin Flaveco 45.000 40.000 44.200 expected level 42.250 35.000 30.000 40.050 37.700 36.600 33.300 30.000 25.000 24.950 20.000 23.000 15.000 15.600 10.000 start 4 weeks 8 weeks 12 weeks 21 weeks 21 Conclusions 22 Conclusion Flavomycin, the original o Better stability vs. generics of the additive itself, in feed and in premix which is related to: – – – – Compacter molecule, low nr of H2O molecules bound Fermentation technology and knowledge Fermentation medium composition Quality of carrier and additives used in its composition o Superior formulation – Available as dust free powder or as granule – Standardization technology – Spray dry technology o Strict compliance of the specs of the different components – Five different components (e.g. component A between 40 and 80% of the FLP complex) – Percentage of components is calculated in accordance to the detected potency (relative) – Water content, pH o Investments in technology & Quality – Modern EU fermentation sites with the most important certifications: HACCP,GMP, GMP+, FDA, ISO. 23 Flavomycin® “ADDING PERFORMANCE TO YOUR BUSINESS” 24