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Vpliv zasnove in velikosti vrtinčnoslojne opreme na od velikosti delcev odvisen trend debeline obloge in profil sproščanja iz pelet s podaljšanim sproščanjem
ID Gošek, Tjaša (Author), ID Dreu, Rok (Mentor) More about this mentor... This link opens in a new window, ID Brezovar, Teja (Comentor)

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Abstract
Pelete predstavljajo osnovo za večenotne farmacevtske oblike. Polnimo jih v kapsule ali stisnemo v tablete. Nanje pogosto nanesemo filmsko oblogo, ki ima med drugim lahko funkcijo zagotavljanja prirejenega sproščanja. Ker pelete nimajo povsem enake velikosti, pač pa imajo določeno porazdelitev velikosti, lahko pri rokovanju z njimi pride do njihove segregacije, torej ločitve v plasti, najpogosteje zaradi njihovih razlik v velikosti. Med oblaganjem pelet lahko pride do razlik v debelini obloge med peletami različnih velikosti. To je še posebej neugodno, kadar ima filmska obloga funkcijo podaljšanega sproščanja, saj imata največji vpliv na hitrost sproščanja učinkovine debelina tovrstne obloge in specifična površina pelet. V nalogi smo preučevali, kako velikost vhodnih pelet v primeru različnih konfiguracij in velikostne ravni oblagalnikov vpliva na končno debelino filmske obloge. Primerjali smo vpliv dveh različic Wursterjevega oblagalnika, ki ustvarjata različen tok zraka in s tem gibanje pelet v sami komori, ter dveh nastavitev višine valja na profil podaljšanega sproščanja modelne učinkovine iz pelet širše velikostne porazdelitve. Pelete smo po oblaganju ločili glede na velikost in vsaki frakciji določili vsebnost ter izvedli preskus sproščanja. Pri oblaganju z različico z generatorjem vrtinčenja zraka (SW) na pilotnem nivoju smo pri višji nastavitvi valja dosegli, da je bil profil sproščanja enak za vse pelete, ne glede na njihovo velikost, pri nižji nastavitvi višine valja pa so manjše pelete prejele še nesorazmerno več obloge, kar je celo upočasnilo profil sproščanja najmanjših pelet. Na laboratorijskem nivoju so razlike med izidi poskusov oblaganja med SW in klasično različico procesne opreme majhne. Zaradi številčno večje zastopanosti najmanjših pelet so te v klasični različici oblagalnika prejele enako količino obloge, v primeru SW različice pa celo nekoliko več obloge kot večje velikostne frakcije pelet. V drugem, komplementarnem vsebinskem sklopu smo na pelete nanesli oblogo z barvilom in iz obarvanosti sklepali na debelino obloge posameznih pelet. Iz naklonov na diagramu odvisnosti debeline obloge od premera pelet smo ugotovili, da je od velikosti pelet odvisno pozitivno preferenčno oblaganje (večje pelete prejmejo več obloge) izraženo pri vseh poskusih na laboratorijski skali, nekoliko nižja naklona smo dobili pri SW različici oblagalnika. Generalno lahko zaključimo, da je v primeru SW procesa, neodvisno od njegove ravni pri izbranih vrednostih procesnih spremenljivk, količini pelet ter porazdelitvi velikosti začetnih pelet profil nanosa obloge podaljšanega sproščanja na pelete različnih velikosti ustrezen z vidika kompenzacije razlik v specifični površini velikostnih frakcij pelet in tako kakovost končnega izdelka ne bo problematična niti v primeru morebitne segregacije zmesi pelet.

Language:Slovenian
Keywords:debelina obloge, filmsko oblaganje, generator vrtinčenja zraka, pelete, Wursterjeva komora
Work type:Master's thesis/paper
Organization:FFA - Faculty of Pharmacy
Year:2022
PID:20.500.12556/RUL-134666 This link opens in a new window
Publication date in RUL:25.01.2022
Views:890
Downloads:149
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Secondary language

Language:English
Title:The effect of design and size of the fluid-bed equipment on the particle size-dependent trend of coating thickness and the release profile from prolonged release pellets
Abstract:
Pellets are basis for multiple unit dosage forms and can be filled into hard capsules or pressed into tablets. They are often film coated with polymer film that can, among other functions, enable modified release of an active ingredient. Pellets do not have exactly the same size, but certain size distribution width. During manufacturing process differences in their size can lead to segregation, which means that pellets are separated into layers. During coating process differences in amount of received coating among pellets of different size can appear. This is especially unwanted, if the purpose of coating is to enable prolonged release of active pharmaceutical ingredient (API). In this case coating thickness and particles specific area have the biggest impact on release rate of API. In this master thesis we studied how the size of initial pellets affects final depth of coating in case of different design and size of fluid-bed coating equipment. We compared two versions of Wurster chamber that create different airflows and pellets movement and two heights of partition column. We evaluated their effect on release profiles of API from pellets with wider size distribution. After coating experiments we separated pellets by their size, determined the amount of incorporated API and carried out dissolution tests. When coating on pilot scale with swirl distribution plate and higher position of partition column, we managed to achieve that all pellet fractions yielded comparable release profiles; in case of lower position smaller pellets received disproportionally more coating than bigger ones, which even slowed down the release profile of the smallest pellets. On laboratory scale the differences in release profiles between classic and swirl distribution plates are small. Because of higher number of smaller pellets in the coating batch they received the same amount of coating compared to bigger pellets in case of classic coating chamber and even a little bit more in case of swirl version. In the second, complementary part of experiments we coated pellets with colouring agent and from particles coloring we extracted the coating thickness of individual pellets. From the slopes in coating thickness vs. pellet diameter diagram we found out that positive size dependent preference coating (bigger pellets receive more coating) is expressed in each series on laboratory scale, with a little bit lower slopes determined in experiments with swirl generator. From the obtained results we can generally conclude, that on both scales of swirl generator equipped coaters and in combination with selected process parameters, amount of pellets and particle size distribution the profile of deposited film coating on pellets of different size will be adequate regarding the compensation of differences in specific area of differently sized pellets, therefore quality of final product will not vary even in the case of potential segregation of pellet mixture.

Keywords:coating thickness, film coating, swirl generator, pellets, Wurster chamber

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