{"title":"使用Ambr®250高通量平行生物反应器生产单克隆抗体的CHO细胞培养工艺图和优化研究。","authors":"A Bordoloi, F Talebnia Rowshan","doi":"10.1007/s00449-025-03229-y","DOIUrl":null,"url":null,"abstract":"<p><p>The demand to accelerate monoclonal antibody (mAbs) process development timelines using Chinese hamster ovary (CHO) host cells to bring therapies to patients sooner is gaining momentum. The applicability of single use high-throughput (HTP) bioreactor system such as Ambr<sup>®</sup>250 facilitating precise and automated control is very promising. This entails optimizing process parameters through design of experiments (DoE) using less resources and time, compared to traditionally employed large-scale bench top reactors (2-5L). It is imperative to improve mAb productivity through robust process development to mitigate current manufacturing challenges. In this study, a systematic mapping approach was employed to identify critical process parameters (CPP) and improve process efficacy. A central composite design (CCD) was used in Ambr<sup>®</sup>250 bioreactors to investigate the impact of initial seeding density (SD) and feeding rate (FR) on mAb production. Variance in the SD and FR impacted the cell performance and mAb titer profile based on which parameter optimization was done using response surface methodology. Significant impact of FR and SD was identified leading to improved mAb titer. Bioreactors operated at SD > 1 × 10<sup>6</sup> cells/mL and FR of > 2% Vc/day were more productive, and respective optimal FR and SD were estimated at 2.68% Vc/day and 1.1 × 10<sup>6</sup> cells/mL. Cell viability and productivity were well-maintained at optimal conditions allowing extended cultivation time to reach higher mAb titer of up to 5 g/L. These findings, which optimize the operating range of critical process parameters (CPPs) using the high-throughput Ambr® 250 scaled-down platform, provide a framework for accelerated early-phase process development and enable reliable scalability to commercial manufacturing. Improving productivity and providing robust estimates for manufacturing scale would significantly cut costs and reduce timelines for biologics development and facilitate patient access.</p>","PeriodicalId":9024,"journal":{"name":"Bioprocess and Biosystems Engineering","volume":" ","pages":""},"PeriodicalIF":3.6000,"publicationDate":"2025-08-30","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Process mapping and optimization study of CHO cell cultures for mAb production using Ambr<sup>®</sup> 250 high-throughput parallel bioreactors.\",\"authors\":\"A Bordoloi, F Talebnia Rowshan\",\"doi\":\"10.1007/s00449-025-03229-y\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<p><p>The demand to accelerate monoclonal antibody (mAbs) process development timelines using Chinese hamster ovary (CHO) host cells to bring therapies to patients sooner is gaining momentum. The applicability of single use high-throughput (HTP) bioreactor system such as Ambr<sup>®</sup>250 facilitating precise and automated control is very promising. This entails optimizing process parameters through design of experiments (DoE) using less resources and time, compared to traditionally employed large-scale bench top reactors (2-5L). It is imperative to improve mAb productivity through robust process development to mitigate current manufacturing challenges. In this study, a systematic mapping approach was employed to identify critical process parameters (CPP) and improve process efficacy. A central composite design (CCD) was used in Ambr<sup>®</sup>250 bioreactors to investigate the impact of initial seeding density (SD) and feeding rate (FR) on mAb production. Variance in the SD and FR impacted the cell performance and mAb titer profile based on which parameter optimization was done using response surface methodology. Significant impact of FR and SD was identified leading to improved mAb titer. Bioreactors operated at SD > 1 × 10<sup>6</sup> cells/mL and FR of > 2% Vc/day were more productive, and respective optimal FR and SD were estimated at 2.68% Vc/day and 1.1 × 10<sup>6</sup> cells/mL. Cell viability and productivity were well-maintained at optimal conditions allowing extended cultivation time to reach higher mAb titer of up to 5 g/L. These findings, which optimize the operating range of critical process parameters (CPPs) using the high-throughput Ambr® 250 scaled-down platform, provide a framework for accelerated early-phase process development and enable reliable scalability to commercial manufacturing. Improving productivity and providing robust estimates for manufacturing scale would significantly cut costs and reduce timelines for biologics development and facilitate patient access.</p>\",\"PeriodicalId\":9024,\"journal\":{\"name\":\"Bioprocess and Biosystems Engineering\",\"volume\":\" \",\"pages\":\"\"},\"PeriodicalIF\":3.6000,\"publicationDate\":\"2025-08-30\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Bioprocess and Biosystems Engineering\",\"FirstCategoryId\":\"5\",\"ListUrlMain\":\"https://doi.org/10.1007/s00449-025-03229-y\",\"RegionNum\":3,\"RegionCategory\":\"生物学\",\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"Q2\",\"JCRName\":\"BIOTECHNOLOGY & APPLIED MICROBIOLOGY\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Bioprocess and Biosystems Engineering","FirstCategoryId":"5","ListUrlMain":"https://doi.org/10.1007/s00449-025-03229-y","RegionNum":3,"RegionCategory":"生物学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q2","JCRName":"BIOTECHNOLOGY & APPLIED MICROBIOLOGY","Score":null,"Total":0}
Process mapping and optimization study of CHO cell cultures for mAb production using Ambr® 250 high-throughput parallel bioreactors.
The demand to accelerate monoclonal antibody (mAbs) process development timelines using Chinese hamster ovary (CHO) host cells to bring therapies to patients sooner is gaining momentum. The applicability of single use high-throughput (HTP) bioreactor system such as Ambr®250 facilitating precise and automated control is very promising. This entails optimizing process parameters through design of experiments (DoE) using less resources and time, compared to traditionally employed large-scale bench top reactors (2-5L). It is imperative to improve mAb productivity through robust process development to mitigate current manufacturing challenges. In this study, a systematic mapping approach was employed to identify critical process parameters (CPP) and improve process efficacy. A central composite design (CCD) was used in Ambr®250 bioreactors to investigate the impact of initial seeding density (SD) and feeding rate (FR) on mAb production. Variance in the SD and FR impacted the cell performance and mAb titer profile based on which parameter optimization was done using response surface methodology. Significant impact of FR and SD was identified leading to improved mAb titer. Bioreactors operated at SD > 1 × 106 cells/mL and FR of > 2% Vc/day were more productive, and respective optimal FR and SD were estimated at 2.68% Vc/day and 1.1 × 106 cells/mL. Cell viability and productivity were well-maintained at optimal conditions allowing extended cultivation time to reach higher mAb titer of up to 5 g/L. These findings, which optimize the operating range of critical process parameters (CPPs) using the high-throughput Ambr® 250 scaled-down platform, provide a framework for accelerated early-phase process development and enable reliable scalability to commercial manufacturing. Improving productivity and providing robust estimates for manufacturing scale would significantly cut costs and reduce timelines for biologics development and facilitate patient access.
期刊介绍:
Bioprocess and Biosystems Engineering provides an international peer-reviewed forum to facilitate the discussion between engineering and biological science to find efficient solutions in the development and improvement of bioprocesses. The aim of the journal is to focus more attention on the multidisciplinary approaches for integrative bioprocess design. Of special interest are the rational manipulation of biosystems through metabolic engineering techniques to provide new biocatalysts as well as the model based design of bioprocesses (up-stream processing, bioreactor operation and downstream processing) that will lead to new and sustainable production processes.
Contributions are targeted at new approaches for rational and evolutive design of cellular systems by taking into account the environment and constraints of technical production processes, integration of recombinant technology and process design, as well as new hybrid intersections such as bioinformatics and process systems engineering. Manuscripts concerning the design, simulation, experimental validation, control, and economic as well as ecological evaluation of novel processes using biosystems or parts thereof (e.g., enzymes, microorganisms, mammalian cells, plant cells, or tissue), their related products, or technical devices are also encouraged.
The Editors will consider papers for publication based on novelty, their impact on biotechnological production and their contribution to the advancement of bioprocess and biosystems engineering science. Submission of papers dealing with routine aspects of bioprocess engineering (e.g., routine application of established methodologies, and description of established equipment) are discouraged.