The influence of input material properties on hot melt granules prepared using a counter-rotating batch mixer
The objective of this study was to develop a method that enabled granulation in a counter-rotating batch mixer to emulate large scale dry twin screw granulation trials. Four granulations were prepared using counter rotating batch mixing for formulations containing a mixture of different particle siz...
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Veröffentlicht in: | Pharmaceutical development and technology 2023-01, Vol.28 (1), p.1-17 |
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creator | Pafiakis, Afstathios Armenante, Piero Gogos, Costas G. |
description | The objective of this study was to develop a method that enabled granulation in a counter-rotating batch mixer to emulate large scale dry twin screw granulation trials.
Four granulations were prepared using counter rotating batch mixing for formulations containing a mixture of different particle sizes of the API (70% w/w) and polymer (30% w/w). Milled theophylline (MTHF; fine API) was blended with coarse hydroxypropyl cellulose (HPC MF; coarse polymer), theophylline (THF; coarse API) with fine hydroxypropyl cellulose (HPC EXF, fine polymer), and the other two formulations consisted of both components in the blend being fine or coarse.
The formulations selected for granulation had the lowest friction coefficient, f, as a function of drug load determined by the iShear
®
powder flow rheometer. Despite the non-uniform chaotic and random nature of thermal granulation, each formulation granulated reproducibly, though the evolution for each was different.
This work highlighted that, firstly it is possible to measure plastic and frictional energy dissipation as product temperature. Secondly, granule growth and density were found to be proportional to the onset of polymer molecular mobility activated by the heat liberated from interparticle velocity differences via mechanical work (torque) required to move agglomerates through the mixer for the duration of each run. |
doi_str_mv | 10.1080/10837450.2022.2156539 |
format | Article |
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Four granulations were prepared using counter rotating batch mixing for formulations containing a mixture of different particle sizes of the API (70% w/w) and polymer (30% w/w). Milled theophylline (MTHF; fine API) was blended with coarse hydroxypropyl cellulose (HPC MF; coarse polymer), theophylline (THF; coarse API) with fine hydroxypropyl cellulose (HPC EXF, fine polymer), and the other two formulations consisted of both components in the blend being fine or coarse.
The formulations selected for granulation had the lowest friction coefficient, f, as a function of drug load determined by the iShear
®
powder flow rheometer. Despite the non-uniform chaotic and random nature of thermal granulation, each formulation granulated reproducibly, though the evolution for each was different.
This work highlighted that, firstly it is possible to measure plastic and frictional energy dissipation as product temperature. Secondly, granule growth and density were found to be proportional to the onset of polymer molecular mobility activated by the heat liberated from interparticle velocity differences via mechanical work (torque) required to move agglomerates through the mixer for the duration of each run.</description><identifier>ISSN: 1083-7450</identifier><identifier>EISSN: 1097-9867</identifier><identifier>DOI: 10.1080/10837450.2022.2156539</identifier><identifier>PMID: 36533900</identifier><language>eng</language><publisher>England: Taylor & Francis</publisher><subject>agglomeration ; Drug Compounding - methods ; frictional energy dissipation ; Hot melt granulation ; Particle Size ; plastic energy dissipation ; Powders ; sintering ; Technology, Pharmaceutical - methods ; Temperature ; Theophylline ; Twin screw granulation ; viscous energy dissipation</subject><ispartof>Pharmaceutical development and technology, 2023-01, Vol.28 (1), p.1-17</ispartof><rights>2022 Informa UK Limited, trading as Taylor & Francis Group 2022</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><cites>FETCH-LOGICAL-c314t-78caa6cc547acb648b8853f95b1acf276bd128fe42c760710ed47543740983b3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,780,784,27924,27925</link.rule.ids><backlink>$$Uhttps://www.ncbi.nlm.nih.gov/pubmed/36533900$$D View this record in MEDLINE/PubMed$$Hfree_for_read</backlink></links><search><creatorcontrib>Pafiakis, Afstathios</creatorcontrib><creatorcontrib>Armenante, Piero</creatorcontrib><creatorcontrib>Gogos, Costas G.</creatorcontrib><title>The influence of input material properties on hot melt granules prepared using a counter-rotating batch mixer</title><title>Pharmaceutical development and technology</title><addtitle>Pharm Dev Technol</addtitle><description>The objective of this study was to develop a method that enabled granulation in a counter-rotating batch mixer to emulate large scale dry twin screw granulation trials.
Four granulations were prepared using counter rotating batch mixing for formulations containing a mixture of different particle sizes of the API (70% w/w) and polymer (30% w/w). Milled theophylline (MTHF; fine API) was blended with coarse hydroxypropyl cellulose (HPC MF; coarse polymer), theophylline (THF; coarse API) with fine hydroxypropyl cellulose (HPC EXF, fine polymer), and the other two formulations consisted of both components in the blend being fine or coarse.
The formulations selected for granulation had the lowest friction coefficient, f, as a function of drug load determined by the iShear
®
powder flow rheometer. Despite the non-uniform chaotic and random nature of thermal granulation, each formulation granulated reproducibly, though the evolution for each was different.
This work highlighted that, firstly it is possible to measure plastic and frictional energy dissipation as product temperature. Secondly, granule growth and density were found to be proportional to the onset of polymer molecular mobility activated by the heat liberated from interparticle velocity differences via mechanical work (torque) required to move agglomerates through the mixer for the duration of each run.</description><subject>agglomeration</subject><subject>Drug Compounding - methods</subject><subject>frictional energy dissipation</subject><subject>Hot melt granulation</subject><subject>Particle Size</subject><subject>plastic energy dissipation</subject><subject>Powders</subject><subject>sintering</subject><subject>Technology, Pharmaceutical - methods</subject><subject>Temperature</subject><subject>Theophylline</subject><subject>Twin screw granulation</subject><subject>viscous energy dissipation</subject><issn>1083-7450</issn><issn>1097-9867</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2023</creationdate><recordtype>article</recordtype><sourceid>EIF</sourceid><recordid>eNp9kMtOxCAUhonReH8EDUs3HbmUQnca4y0xcTN7QumpU0NLBRr17aWZ0aUbLofvP4d8CF1QsqJEkeu8cFkKsmKEsRWjohK83kPHlNSyqFUl95ez4sUCHaGTGN8Joaom4hAd8QzzmpBjNKw3gPuxczOMFrDv8mWaEx5MgtAbh6fgJwiph4j9iDc-P4FL-C2YcXa5OAWYTIAWz7Ef37DB1s9jzhbBJ5OWUmOS3eCh_4Jwhg464yKc7_ZTtH64X989FS-vj893ty-F5bRMhVTWmMpaUUpjm6pUjVKCd7VoqLEdk1XTUqY6KJmVFZGUQFtKUWYfpFa84afoats2f_5jhpj00EcLzpkR_Bw1k0IoQplQGRVb1AYfY4BOT6EfTPjWlOhFtP4VrRfReic65y53I-ZmgPYv9Ws2AzdbIMv1YTCfPrhWJ_PtfOiyPNtHzf-f8QM_ao4R</recordid><startdate>20230102</startdate><enddate>20230102</enddate><creator>Pafiakis, Afstathios</creator><creator>Armenante, Piero</creator><creator>Gogos, Costas G.</creator><general>Taylor & Francis</general><scope>CGR</scope><scope>CUY</scope><scope>CVF</scope><scope>ECM</scope><scope>EIF</scope><scope>NPM</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7X8</scope></search><sort><creationdate>20230102</creationdate><title>The influence of input material properties on hot melt granules prepared using a counter-rotating batch mixer</title><author>Pafiakis, Afstathios ; Armenante, Piero ; Gogos, Costas G.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c314t-78caa6cc547acb648b8853f95b1acf276bd128fe42c760710ed47543740983b3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2023</creationdate><topic>agglomeration</topic><topic>Drug Compounding - methods</topic><topic>frictional energy dissipation</topic><topic>Hot melt granulation</topic><topic>Particle Size</topic><topic>plastic energy dissipation</topic><topic>Powders</topic><topic>sintering</topic><topic>Technology, Pharmaceutical - methods</topic><topic>Temperature</topic><topic>Theophylline</topic><topic>Twin screw granulation</topic><topic>viscous energy dissipation</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Pafiakis, Afstathios</creatorcontrib><creatorcontrib>Armenante, Piero</creatorcontrib><creatorcontrib>Gogos, Costas G.</creatorcontrib><collection>Medline</collection><collection>MEDLINE</collection><collection>MEDLINE (Ovid)</collection><collection>MEDLINE</collection><collection>MEDLINE</collection><collection>PubMed</collection><collection>CrossRef</collection><collection>MEDLINE - Academic</collection><jtitle>Pharmaceutical development and technology</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Pafiakis, Afstathios</au><au>Armenante, Piero</au><au>Gogos, Costas G.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>The influence of input material properties on hot melt granules prepared using a counter-rotating batch mixer</atitle><jtitle>Pharmaceutical development and technology</jtitle><addtitle>Pharm Dev Technol</addtitle><date>2023-01-02</date><risdate>2023</risdate><volume>28</volume><issue>1</issue><spage>1</spage><epage>17</epage><pages>1-17</pages><issn>1083-7450</issn><eissn>1097-9867</eissn><abstract>The objective of this study was to develop a method that enabled granulation in a counter-rotating batch mixer to emulate large scale dry twin screw granulation trials.
Four granulations were prepared using counter rotating batch mixing for formulations containing a mixture of different particle sizes of the API (70% w/w) and polymer (30% w/w). Milled theophylline (MTHF; fine API) was blended with coarse hydroxypropyl cellulose (HPC MF; coarse polymer), theophylline (THF; coarse API) with fine hydroxypropyl cellulose (HPC EXF, fine polymer), and the other two formulations consisted of both components in the blend being fine or coarse.
The formulations selected for granulation had the lowest friction coefficient, f, as a function of drug load determined by the iShear
®
powder flow rheometer. Despite the non-uniform chaotic and random nature of thermal granulation, each formulation granulated reproducibly, though the evolution for each was different.
This work highlighted that, firstly it is possible to measure plastic and frictional energy dissipation as product temperature. Secondly, granule growth and density were found to be proportional to the onset of polymer molecular mobility activated by the heat liberated from interparticle velocity differences via mechanical work (torque) required to move agglomerates through the mixer for the duration of each run.</abstract><cop>England</cop><pub>Taylor & Francis</pub><pmid>36533900</pmid><doi>10.1080/10837450.2022.2156539</doi><tpages>17</tpages></addata></record> |
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source | MEDLINE; EBSCOhost Business Source Complete |
subjects | agglomeration Drug Compounding - methods frictional energy dissipation Hot melt granulation Particle Size plastic energy dissipation Powders sintering Technology, Pharmaceutical - methods Temperature Theophylline Twin screw granulation viscous energy dissipation |
title | The influence of input material properties on hot melt granules prepared using a counter-rotating batch mixer |
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