Continuous Production of Viral Vectors using membraneless Perfusion Culture of Host Cells

Information

  • Research Project
  • 10414312
  • ApplicationId
    10414312
  • Core Project Number
    R01FD007480
  • Full Project Number
    1R01FD007480-01
  • Serial Number
    007480
  • FOA Number
    RFA-FD-21-034
  • Sub Project Id
  • Project Start Date
    9/1/2021 - 2 years ago
  • Project End Date
    8/31/2024 - 3 months from now
  • Program Officer Name
    OSORIO, MANUEL
  • Budget Start Date
    9/1/2021 - 2 years ago
  • Budget End Date
    8/31/2022 - a year ago
  • Fiscal Year
    2021
  • Support Year
    01
  • Suffix
  • Award Notice Date
    9/9/2021 - 2 years ago

Continuous Production of Viral Vectors using membraneless Perfusion Culture of Host Cells

Project Summary Abstract Continuous Bioproduction of Viral Vectors via High Cell Density, Membrane-less Perfusion Culture In this project, we propose to intensify the viral vector production process by the membrane-less perfusion bioreactor system, which was developed by our team at MIT. Based on the inertial microfluidics and fully validated in CHO cell cultivation, this system has many critical advantages over existing perfusion bioreactors, including high product recovery and avoiding membrane fouling, continuous removal of dead cells, cell debris, and cell aggregates, and easy maintenance and automation. As a result, our bioreactors can maintain high cell density reliably even when the cell viability and culture conditions change significantly, ideally suited for controlling viral vector production processes. Teaming with experts in HEK293 and Sf9 based production systems, we will implement long-term, high cell density cultures of host cells and explore and validate several innovative vector production platforms that provide more accurate control over fresh cell growth, transfection, incubation/production, and recovery of the products. Inertial microfluidic cell manipulation processes allow many novel controls over host cells in bioreactors, including selective separation of transfected from untransfected host cells. Finally, a continuous bioprocessing system will be optimized to maximize the quantity and quality of the finished viral vector products. For this, we will employ novel microfluidic electrokinetic separation of empty from filled viral capsid, which can provide near real-time determination of the quality of the product. In contrast to fed-batch or batch cultures, continuous monitoring of vector quality and quantity enables rapid adjustment of the culture protocols to restore/maintain optimal conditions for vector production over an extended period. This project is expected to have a broader impact on the bioproduction of viral vectors, but especially on rare and ultra-rare diseases where low disease prevalence requires relatively small production volumes. Such diseases do not justify the biopharmaceutical industry?s large investment needed for vector manufacturing.

IC Name
FOOD AND DRUG ADMINISTRATION
  • Activity
    R01
  • Administering IC
    FD
  • Application Type
    1
  • Direct Cost Amount
  • Indirect Cost Amount
  • Total Cost
    600000
  • Sub Project Total Cost
  • ARRA Funded
    False
  • CFDA Code
    103
  • Ed Inst. Type
    ORGANIZED RESEARCH UNITS
  • Funding ICs
    FDA:600000\
  • Funding Mechanism
    Non-SBIR/STTR RPGs
  • Study Section
    ZFD1
  • Study Section Name
    Special Emphasis Panel
  • Organization Name
    MASSACHUSETTS INSTITUTE OF TECHNOLOGY
  • Organization Department
    MISCELLANEOUS
  • Organization DUNS
    001425594
  • Organization City
    CAMBRIDGE
  • Organization State
    MA
  • Organization Country
    UNITED STATES
  • Organization Zip Code
    021421029
  • Organization District
    UNITED STATES