Bone Tissue Engineering With Mesenchymal Stem Cell Seeded Scaffold Assisted Perfusion Bioreactors
dc.contributor.advisor | Gümüşderelioğlu, Menemşe | |
dc.contributor.author | Cengiz, Alper | |
dc.date.accessioned | 2018-09-13T06:58:30Z | |
dc.date.available | 2018-09-13T06:58:30Z | |
dc.date.issued | 2017 | |
dc.date.submitted | 2017-07-04 | |
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dc.identifier.uri | http://hdl.handle.net/11655/4879 | |
dc.description.abstract | This study was financially supported by Turkish Scientific and Research Council (Tübitak) Project no: 214M100. In the present thesis study, it was aimed to investigate the potential of proliferation and osteogenic differentiation of human mesenchymal stem cells (hMSCs) in perfusion bioreactors. In the first step of this study, chitosan-hydroxyapatite superporous hydrogel (chitosan-HA SPHC) scaffolds were prepared by using sodium bicarbonate (NaHCO3) as a foaming agent and glyoxal as a cross-linking agent. The microwave assisted gas foaming technique has produced tissue scaffolds that are faster to obtain, in high yield and higher reproducibility in vitro studies. In the second step of the experimental study, the installation of the perfusion bioreactor system, in which leakage and diffusion problems can be solved and which provides sustainable sterility through long-term dynamic culture studies has been completed. At the next stage of the study, dynamic cell culture studies were carried out for 21 days using hMSCs at different flow velocities and tissue scaffolds of different sizes (P3D-6: 0.1 mL/min, P3D-6:0.2 mL/min; P3D-10: 0.27 mL/min) and media changes were made on certain days (days 3, 6, 9, 12, 15 and 18) of the culture. MTT (3-[4,5-dimethylthiazol-2-yl]-2,5 diphenyltetrazolium bromide) analysis was performed to observe viability and proliferation of cells on certain days of cell culture studies. SEM (Scanning Electron Microscopy) analysis was performed to observe cell morphologies and penetrations. At the end of the cell culture studies, RT-PCR (Real Time Polymerase Chain Reaction) analyzes were performed to determine the expression levels of Collagen1 (Col1), Runt Associated Transcription Factor 2 (RUNX2), Osteocalcin (OCN) and Osteopontin (OPN) genes in hMSCs. In the last part of the thesis study, flow and mass transfer simulation studies were carried out in the perfusion bioreactor using COMSOL software. The accuracy of the model was tested with models developed for low and high flow rates in a bioreactor without a tissue scaffold and in the presence of a non-porous tissue scaffold. Affterwards the flow model and mass transfer model in perfusion bioreactor in the presence of a permeable tissue scaffold took place. The results obtained from the Computational Fluid Dynamics (CFD) modeling studies conducted within the scope of the thesis seem to support the experimental findings. In the light of all these analyzes and findings, it has been shown that the dynamic culture approach performed with P3D-6 scaffolds at 0.1 mL/min and 0.2 mL/min flow rates support the osteogenic differentiation of hMSCs in the perfusion bioreactor. In addition, it can be seen that the CFD approach is the decisive factor in achieving successful results in vitro production of engineered bone grafts when different operating parameters are considered | tr_TR |
dc.description.abstract | This study was financially supported by Turkish Scientific and Research Council (Tübitak) Project no: 214M100. In the present thesis study, it was aimed to investigate the potential of proliferation and osteogenic differentiation of human mesenchymal stem cells (hMSCs) in perfusion bioreactors. In the first step of this study, chitosan-hydroxyapatite superporous hydrogel (chitosan-HA SPHC) scaffolds were prepared by using sodium bicarbonate (NaHCO3) as a foaming agent and glyoxal as a cross-linking agent. The microwave assisted gas foaming technique has produced tissue scaffolds that are faster to obtain, in high yield and higher reproducibility in vitro studies. In the second step of the experimental study, the installation of the perfusion bioreactor system, in which leakage and diffusion problems can be solved and which provides sustainable sterility through long-term dynamic culture studies has been completed. At the next stage of the study, dynamic cell culture studies were carried out for 21 days using hMSCs at different flow velocities and tissue scaffolds of different sizes (P3D-6: 0.1 mL/min, P3D-6:0.2 mL/min; P3D-10: 0.27 mL/min) and media changes were made on certain days (days 3, 6, 9, 12, 15 and 18) of the culture. MTT (3-[4,5-dimethylthiazol-2-yl]-2,5 diphenyltetrazolium bromide) analysis was performed to observe viability and proliferation of cells on certain days of cell culture studies. SEM (Scanning Electron Microscopy) analysis was performed to observe cell morphologies and penetrations. At the end of the cell culture studies, RT-PCR (Real Time Polymerase Chain Reaction) analyzes were performed to determine the expression levels of Collagen1 (Col1), Runt Associated Transcription Factor 2 (RUNX2), Osteocalcin (OCN) and Osteopontin (OPN) genes in hMSCs. In the last part of the thesis study, flow and mass transfer simulation studies were carried out in the perfusion bioreactor using COMSOL software. The accuracy of the model was tested with models developed for low and high flow rates in a bioreactor without a tissue scaffold and in the presence of a non-porous tissue scaffold. Affterwards the flow model and mass transfer model in perfusion bioreactor in the presence of a permeable tissue scaffold took place. The results obtained from the Computational Fluid Dynamics (CFD) modeling studies conducted within the scope of the thesis seem to support the experimental findings. In the light of all these analyzes and findings, it has been shown that the dynamic culture approach performed with P3D-6 scaffolds at 0.1 mL/min and 0.2 mL/min flow rates support the osteogenic differentiation of hMSCs in the perfusion bioreactor. In addition, it can be seen that the CFD approach is the decisive factor in achieving successful results in vitro production of engineered bone grafts when different operating parameters are considered | tr_TR |
dc.description.sponsorship | TÜBİTAK, 214M100 No'lu proje | tr_TR |
dc.description.tableofcontents | ABSTRACT …………………………………………………………………………… ……i ÖZET …………………………………………………………………………………... …..iii ACKNOWLEDGEMENT …………………………………………………………….. …...v TABLE OF CONTENTS ……………………………………………………………… …...vi SYMBOLS AND ABBREVIATIONS ………………………………………………... …...ix 1. INTRODUCTION …………………………………………………………………. ……1 2. LITERATURE REVIEW ………………………………………………………… ……5 2.1 Bone Tissue Engineering …………………………………………………………. ……5 2.2. Bioreactors in Bone Tissue Engineering …………………………………………. ……7 2.2.1. Definition, Structure and Function of Bioreactors ……………………………… ……7 2.2.1.1. The Role of Bioreactors in Cell Culture ……………………………………… ……9 2.2.1.2. Mechanical Stimulation in Bioreactors ……………………………………….. …..11 2.2.1.3. Mass Transfer in Bioreactors …………………………………………………. …..12 2.2.2. Design Requirements in Bioreactors ……………………………………………. …..13 2.2.3. Types of Bioreactors in Tissue Engineering ……………………………………. …..13 2.2.3.1. Spinner Flask Bioreactors …………………………………………………….. …..14 2.2.3.2. Rotating Wall Bioreactors …………………………………………………….. …..14 2.2.3.3. Perfusion Bioreactors …………………………………………………………. …..15 2.2.4. Bioreactor Applicatıons in Bone Tissue Engineering …………………………... …..17 2.3. Computational Fluid Dynamics in Bone Tissue Engineering …………………….. …..18 2.3.1. Computational Fluid Dynamics ………………………………………………… …..18 2.3.2. Spatial Discretization …………………………………………………………… …..20 2.3.3. Determination of Mesh Size and Asymmetrical Meshing ……………………… …..21 2.3.4. Grid Independence ……………………………………………………………… …..22 2.3.5. Periodical Discretization and Time Sequence …………………………………... …..22 2.3.6. Determination of Installation Equations ……………………………………… …..23 2.3.6.1. Flow Characteristics …………………………………………………………... …..23 2.3.6.2. Media Porosity ………………………………………………………………... …..24 2.3.6.3. Modelling of Nutrient Transport ……………………………………………… …..25 2.3.7. Computational Fluid Dynamics Applications in Fluid Dynamics………………. …..26 3. RESEARCH METHODOLOGY AND THEORY …………………………………. …..29 3.1. Materials Used in Experimental Studies ………………………............................ …..29 3.2. Production and Characterization of Chitosan-HA SPHCs ………………………... …..30 3.3. Installation of Perfusion Bioreactor System ………………………........................ …..32 3.4. Sterilization Procedures …………………...............………………….................... …..33 3.5. Cell Seeding and Cell Culture Studies …………………...............……………….. …..33 3.5.1. Static Cell Seeding …………………...............…………………......................... …..35 3.5.2. Cell Culture …………………...............…………………...............……………. …..35 3.5.2.1. Monolayer Cell Culture …………………...............…………………............... …..35 3.5.2.2. Static Cell Culture …………………...............…………………....................... …..35 3.5.2.3. Dynamic Cell Culture Using Perfusion Bioreactor …………………................ …..36 3.5.3. Characterization Tests …………………...............………………….................... …..38 3.5.3.1. MTT Analysis …………………...............…………………...............……….. …..38 3.5.3.2. SEM Analysis …………………...............………………….............................. …..38 3.5.3.3. Real-time Polymerase Chain Reaction (RT-PCR) Analysis ………………….. …..39 3.5.4. Statistical Analysis …………………...............…………………......................... …..41 3.6. Computational Fluid Dynamics Modelling Studies …………………..................... …..41 3.6.1. Method …………………...............…………………...............………………… …..41 3.6.2. Bioreactor Geometry and Meshing …………………...............………………… …..44 3.6.3. Simulation Parameters …………………...............…………………................... …..46 4. RESULTS AND DISCUSSION …………………...............………………….......... …..47 4.1. Cell Culture Studies …………………...............…………………...............……... …..47 4.1.1. Monolayer Cell Culture …………………...............………………….................. …..47 4.1.2. Static Cell Culture …………………...............………………….......................... …..49 4.1.3. Dynamic Cell Culture in Perfusion Bioreactor at 0.1 mL/min Flow Rate ……… …..51 4.1.4. Dynamic Cell Culture in Perfusion Bioreactor at 0.2 mL/min Flow Rate ……… …..53 4.1.5. Effect of Flow Rate on Perfusion Bioreactor …………………............................ …..56 4.1.6. Experimental Dynamic Cell Culture in Perfusion Bioreactor at 0.27 mL/min Flow Rate ……………………………………………………………………………… …..58 4.2. Computational Fluid Dynamics Modelling Studies ………………………………. …..60 4.2.1 Perfusion Bioreactor Flow Model without Tissue Scaffold ……………………... …..61 4.2.2. Perfusion Bioreactor Flow Model with Non-Porous Tissue Scaffold ………….. …..63 4.2.3. Perfusion Bioreactor Flow Model at Flow Rate of 0.1 mL/min in the Presence of a Permeable Tissue Scaffold ………………………………………………………... …..66 4.2.4. Perfusion Bioreactor Mass Transfer Model at Flow Rate of 0.1 mL/min in the Presence of a Pemeable Tissue Scaffold ………………………………………………. …..69 4.2.5. Perfusion Bioreactor Flow Model at Flow Rate of 0.2 mL/min in the Presence of a Permeable Tissue Scaffold ……………………………………………………… …..74 4.2.6. Perfusion Bioreactor Mass Transfer Model at Flow Rate of 0.2 mL/min in the Presence of a Permeable Tissue Scaffold ……………………………………………… …..76 4.2.7. Perfusion Bioreactor Flow Model at Flow Rate of 0.27 mL/min in the Presence of a Permeable Tissue Scaffold ………………………………………………………... …..81 5. CONCLUSION ……………………………………………………………………... …..83 6. REFERENCES ……………………………………………………………………… …..86 7. CURRICULUM VITAE ……………………………………………………………. …..96 | tr_TR |
dc.description.tableofcontents | ABSTRACT ................................................................................................................................. i ÖZET ......................................................................................................................................... iii ACKNOWLEDGEMENT ........................................................................................................... v TABLE OF CONTENTS ........................................................................................................... vi LIST OF TABLES ..................................................................................................................... ix LIST OF FIGURES ..................................................................................................................... x SYMBOLS AND ABBREVIATIONS .................................................................................... xiv 1. INTRODUCTION ................................................................................................................... 1 2. LITERATURE REVIEW ........................................................................................................ 5 2.1. Bone Tissue Engineering ...................................................................................................... 5 2.2. Bioreactors in Bone Tissue Engineering .............................................................................. 7 2.2.1. Definition, Structure and Function of Bioreactors ............................................................ 7 2.2.1.1. The Role of Bioreactors in Cell Culture ......................................................................... 9 2.2.1.2. Mechanical Stimulation in Bioreactors ........................................................................ 11 2.2.1.3. Mass Transfer in Bioreactors ........................................................................................ 12 2.2.2. Design Requirements in Bioreactors ............................................................................... 13 2.2.3. Types of Bioreactors in Tissue Engineering.................................................................... 13 2.2.3.1. Spinner Flask Bioreactors ............................................................................................. 14 2.2.3.2. Rotating Wall Bioreactors ............................................................................................ 14 2.2.3.3. Perfusion Bioreactors ................................................................................................... 15 2.2.4. Bioreactor Applications in Bone Tissue Engineering ..................................................... 17 2.3. Computational Fluid Dynamics in Bone Tissue Engineering ............................................ 18 2.3.1. Computational Fluid Dynamics ....................................................................................... 18 2.3.2. Spatial Discritization ....................................................................................................... 20 2.3.3. Determination of Mesh Size and Asymmetrical Meshing ............................................. 21 2.3.4. Grid Independence ........................................................................................................... 22 2.3.5. Periodic Discritization and Time Sequence..................................................................... 22 2.3.6. Determination of Installation Equations .......................................................................... 23 2.3.6.1. Flow Characteristics ..................................................................................................... 23 2.3.6.2. Porous Media ................................................................................................................ 24 2.3.6.3. Modelling of Nutrient Transport .................................................................................. 25 2.3.7. Computational Fluid Dynamics Applications in Tissue Engineering ............................. 26 3. RESEARCH METHODOLOGY AND THEORY ............................................................... 29 3.1. Materials Used in Experimental Studies ............................................................................ 29 3.2. Production and Characterization of Chitosan-HA SPHCs ................................................. 30 3.3. Installation of Perfusion Bioreactor System ....................................................................... 32 3.4. Sterilization Procedures ...................................................................................................... 33 3.5. Cell Seeding and Cell Culture Studies ............................................................................... 33 3.5.1. Static Cell Seeding Studies .............................................................................................. 35 3.5.2. Cell Culture Studies ......................................................................................................... 35 3.5.2.1. Monolayer Cell Culture Studies ................................................................................... 35 3.5.2.2. Static Cell Culture Studies ............................................................................................ 35 3.5.2.3. Dynamic Cell Culture Studies Using Perfusion Bioreactor ......................................... 36 3.5.3. Characterization Tests ..................................................................................................... 38 3.5.3.1. MTT Analysis ............................................................................................................... 38 3.5.3.2. SEM Analysis ............................................................................................................... 38 3.5.3.3. Real-time Polymerase Chain Reaction (RT-PCR) Analysis ........................................ 39 3.5.4. Statistical Analysis .......................................................................................................... 41 3.6. Computational Fluid Dynamics Modelling Studies ........................................................... 41 3.6.1. Method ............................................................................................................................. 41 3.6.2. Bioreactor Geometry and Meshing ................................................................................. 44 3.6.3. Simulation Parameters ..................................................................................................... 46 4. RESULTS AND DISCUSSION ............................................................................................ 47 4.1. Cell Culture Studies ............................................................................................................ 47 4.1.2. Static Cell Culture Studies ............................................................................................... 49 4.1.3. Dynamic Cell Culture Studies in Perfusion Bioreactor at 0.1 mL/min Flow Rate ......... 51 4.1.4. Dynamic Cell Culture Studies in Perfusion Bioreactor at 0.2 mL/min Flow Rate ......... 53 4.1.5. Effect of Flow Rate on Perfusion Bioreactor .................................................................. 56 4.1.6. Dynamic Cell Culture Studies in Perfusion Bioreactor at 0.27 mL/min Flow Rate ....... 58 4.2. Computational Fluid Dynamics Modelling Studies ........................................................... 60 4.2.1. Perfusion Bioreactor Flow Model Without a Tissue Scaffold ........................................ 61 4.2.2. Perfusion Bioreactor Flow Model with Non-Porous Tissue Scaffold ............................. 63 4.2.3. Perfusion Bioreactor Flow Model at Flow Rate of 0.1 mL/min in the Presence of a P3D-6 Permeable Tissue Scaffold ............................................................................................. 66 4.2.4. Perfusion Bioreactor Mass Transfer Model at Flow Rate of 0.1 mL/min in the Presence of a Pemeable Tissue Scaffold................................................................................................... 69 4.2.5. Perfusion Bioreactor Flow Model at Flow Rate of 0.2 mL/min in the Presence of a P3D- 6 Pemeable Tissue Scaffold ....................................................................................................... 74 4.2.6. Perfusion Bioreactor Mass Transfer Model at Flow Rate of 0.2 mL/min in the Presence of a Pemeable Tissue Scaffold................................................................................................... 76 4.2.7. Perfusion Bioreactor Flow Model at Flow Rate of 0.27 mL/min in the Presence of a P3D-10 Pemeable Tissue Scaffold ............................................................................................ 81 5. CONCLUSION ..................................................................................................................... 83 6. REFERENCES ...................................................................................................................... 86 7. CURRICULUM VITAE........................................................................................................ 96 | tr_TR |
dc.language.iso | en | tr_TR |
dc.publisher | Fen Bilimleri Enstitüsü | tr_TR |
dc.rights | info:eu-repo/semantics/openAccess | tr_TR |
dc.subject | bone tissue engineering | |
dc.subject | human mesenchymal stem cells | |
dc.subject | dynamic cell culture | |
dc.subject | chitosan-hydroxyapatite superporous hydrogels | |
dc.subject | P3D-6 and P3D-10 scaffolds | |
dc.subject | perfusion bioreactor | |
dc.subject | computational fluid dynamics. | |
dc.title | Bone Tissue Engineering With Mesenchymal Stem Cell Seeded Scaffold Assisted Perfusion Bioreactors | tr_TR |
dc.title.alternative | Mezenkimal Kök Hücre Ekilmiş Doku İskelesi Destekli Perfüzyon Biyoreaktörlerle Kemik Doku Mühendisliği | tr_TR |
dc.type | info:eu-repo/semantics/masterThesis | tr_TR |
dc.description.ozet | Bu çalışma, Türkiye Bilimsel ve Teknolojik Araştırma Kurumu (Tübitak) Projesi No: 214M100 tarafından maddi olarak desteklenmiştir. Bu tez çalışmasında, durağan hücre kültürü ve dinamik yaklaşım olan perfüzyon biyoreaktörlerinde farklı ebat ve farklı boyuttaki doku iskelelerine dayanan hücre kültürü çalışmalarının insan mezenkimal kök hücreleri (hMSC) üzerindeki üreme ve osteojenik farklılaşmanın potansiyelinin araştırılması amaçlanmıştır. Deneysel çalışmaların ilk aşamasında, kitosan-hidroksiapatit süpergözenekli hidrojel (kitosan-HA SGPH) doku iskeleleri, köpükleşme ajanı olarak sodyum bikarbonat (NaHCO3) ve çapraz bağlayıcı olarak glioksal kullanılarak hazırlanmıştır. Mikrodalga destekli gaz köpükleşme tekniği, in vitro çalışmalarda yüksek verim ve daha yüksek tekrarlanabilirlik elde etmenin yanında doku iskelelerinin üretiminin hızlandırılmasını desteklediğinden tercih edilmiştir. Deneysel çalışmanın ikinci aşamasında, olası bir sızıntının önlendiği ve besin maddeleri / atık madde difüzyon sorunlarının çözülebildiği, uzun vadeli dinamik kültür çalışmaları ile sürdürülebilir sterilite sağlayan perfüzyon biyoreaktör sisteminin kurulumu gerçekleştirilmiştir. Çalışmanın bir sonraki safhasında, hMSC’ler kullanılarak farklı akış hızlarında ve farklı boyutlarda doku iskeleleriyle (P3D-6: 0.1 mL/dk, P3D-6: 0.2 mL/dk; P3D-10: 0.27 mL/dk) 21 gün süreyle dinamik hücre kültürü çalışmaları gerçekleştirilmiş ve kültürün 3, 6, 9, 12, 15 ve 18. günlerinde ortam değişiklikleri yapılmıştır. Hücre kültürü çalışmalarının 7, 14 ve 21. günlerinde hücre canlılığı ve çoğalmasını gözlemlemek için MTT (3-[4,5-Dimethylthiazol-2-yl]-2,5-Diphenyltetrazolium Bromide) analizi gerçekleştirilmiş ve SEM (Taramalı Elektron Mikroskopisi) analizi ile hücre morfolojileri ve penetrasyonları gözlemlenmiştir. Hücre kültürü çalışmalarının sonunda insan mezenkimal kök hücrelerinin Kolajen1 (COL1), Runt İlişkili Transkripsiyon Faktörü 2 (RUNX2), Osteokalsin (OCN) ve Osteopontin (OPN) ekspresyon düzeylerini belirlemek için RT-PCR (Gerçek Zamanlı Polimeraz Zincir Reaksiyonu) analizi yapılmıştır. Tez çalışmasının son bölümünde, perfüzyon biyoreaktörde akış ve kütle transferi simülasyon çalışmaları COMSOL yazılımı kullanılarak gerçekleştirilmiştir. Modelin doğruluğu, doku iskelesi olmayan bir biyoreaktörde düşük ve yüksek akış hızı uygulamaları için geliştirilen modellerle test edilmiştir. Ardından, farklı akış hızlarında ve farklı boyutlarda üretilmiş olan geçirgen doku iskeleleri varlığında perfüzyon biyoreaktörün akış modeli ve kütle transferi modeli ortaya konulmuştur. Tez kapsamında yapılan hesaplamalı akışkanlar dinamiği (CFD) modelleme çalışmalarından elde edilen sonuçların deneysel bulguları desteklediği görülmüştür. Tüm analizler ve bulgular ışığında perfüzyon biyoreaktöründe 0.1 ve 0.2 mL/dk akış hızı ve 3mm çapında ve 6mm yüksekliğindeki doku iskeleleri ile yapılan dinamik kültür yaklaşımının insan mezenkimal kök hücrelerinin osteojenik farklılaşmasını desteklediği gösterilmiştir. Buna ek olarak, CFD yaklaşımının, farklı çalışma parametreleri göz önüne alındığında, mühendislik ürünü kemik yamalarının in vitro üretiminde başarılı sonuçlar elde edilmesinde belirleyici faktör olduğu sonucuna varılmıştır. | tr_TR |
dc.description.ozet | Bu çalışma, Türkiye Bilimsel ve Teknolojik Araştırma Kurumu (Tübitak) Projesi No: 214M100 tarafından maddi olarak desteklenmiştir. Bu tez çalışmasında, durağan hücre kültürü ve dinamik yaklaşım olan perfüzyon biyoreaktörlerinde farklı ebat ve farklı boyuttaki doku iskelelerine dayanan hücre kültürü çalışmalarının insan mezenkimal kök hücreleri (hMSC) üzerindeki üreme ve osteojenik farklılaşmanın potansiyelinin araştırılması amaçlanmıştır. Deneysel çalışmaların ilk aşamasında, kitosan-hidroksiapatit süpergözenekli hidrojel (kitosan-HA SGPH) doku iskeleleri, köpükleşme ajanı olarak sodyum bikarbonat (NaHCO3) ve çapraz bağlayıcı olarak glioksal kullanılarak hazırlanmıştır. Mikrodalga destekli gaz köpükleşme tekniği, in vitro çalışmalarda yüksek verim ve daha yüksek tekrarlanabilirlik elde etmenin yanında doku iskelelerinin üretiminin hızlandırılmasını desteklediğinden tercih edilmiştir. Deneysel çalışmanın ikinci aşamasında, olası bir sızıntının önlendiği ve besin maddeleri / atık madde difüzyon sorunlarının çözülebildiği, uzun vadeli dinamik kültür çalışmaları ile sürdürülebilir sterilite sağlayan perfüzyon biyoreaktör sisteminin kurulumu gerçekleştirilmiştir. Çalışmanın bir sonraki safhasında, hMSC’ler kullanılarak farklı akış hızlarında ve farklı boyutlarda doku iskeleleriyle (P3D-6: 0.1 mL/dk, P3D-6: 0.2 mL/dk; P3D-10: 0.27 mL/dk) 21 gün süreyle dinamik hücre kültürü çalışmaları gerçekleştirilmiş ve kültürün 3, 6, 9, 12, 15 ve 18. günlerinde ortam değişiklikleri yapılmıştır. Hücre kültürü çalışmalarının 7, 14 ve 21. günlerinde hücre canlılığı ve çoğalmasını gözlemlemek için MTT (3-[4,5-Dimethylthiazol-2-yl]-2,5-Diphenyltetrazolium Bromide) analizi gerçekleştirilmiş ve SEM (Taramalı Elektron Mikroskopisi) analizi ile hücre morfolojileri ve penetrasyonları gözlemlenmiştir. Hücre kültürü çalışmalarının sonunda insan mezenkimal kök hücrelerinin Kolajen1 (COL1), Runt İlişkili Transkripsiyon Faktörü 2 (RUNX2), Osteokalsin (OCN) ve Osteopontin (OPN) ekspresyon düzeylerini belirlemek için RT-PCR (Gerçek Zamanlı Polimeraz Zincir Reaksiyonu) analizi yapılmıştır. Tez çalışmasının son bölümünde, perfüzyon biyoreaktörde akış ve kütle transferi simülasyon çalışmaları COMSOL yazılımı kullanılarak gerçekleştirilmiştir. Modelin doğruluğu, doku iskelesi olmayan bir biyoreaktörde düşük ve yüksek akış hızı uygulamaları için geliştirilen modellerle test edilmiştir. Ardından, farklı akış hızlarında ve farklı boyutlarda üretilmiş olan geçirgen doku iskeleleri varlığında perfüzyon biyoreaktörün akış modeli ve kütle transferi modeli ortaya konulmuştur. Tez kapsamında yapılan hesaplamalı akışkanlar dinamiği (CFD) modelleme çalışmalarından elde edilen sonuçların deneysel bulguları desteklediği görülmüştür. Tüm analizler ve bulgular ışığında perfüzyon biyoreaktöründe 0.1 ve 0.2 mL/dk akış hızı ve 3mm çapında ve 6mm yüksekliğindeki doku iskeleleri ile yapılan dinamik kültür yaklaşımının insan mezenkimal kök hücrelerinin osteojenik farklılaşmasını desteklediği gösterilmiştir. Buna ek olarak, CFD yaklaşımının, farklı çalışma parametreleri göz önüne alındığında, mühendislik ürünü kemik yamalarının in vitro üretiminde başarılı sonuçlar elde edilmesinde belirleyici faktör olduğu sonucuna varılmıştır. | tr_TR |
dc.contributor.department | Biyomühendislik | tr_TR |