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Oligonucleotide Synthesis – Overcoming Production Scale Limitations

Aug 09, 2024

Joseph Laviano

Sr. Process Engineer

The demand for oligonucleotide production facilities has increased significantly in recent years. As this trend continues, it is essential to design manufacturing facilities that are flexible enough to meet current production needs and have the foresight for future expansion.


An emerging market for patient therapeutics

Given the relative novelty of the process technologies used to manufacture chemically-synthesized oligonucleotides, the current DNA/RNA synthesis methods are primarily carried out at laboratory-scale (batches less than 100 mMol). As large-scale facility designs in the US become more prevalent, scaling up from the pilot lab environment to a full commercial-level facility (>1,000 mMol/day) presents unique infrastructure challenges that have yet to be resolved. When engaging in facility development for oligonucleotides, the outside engineering design and internal client teams should work closely together to understand equipment and material flows, scale limitations, and the intended operational philosophies of each unit operation. For novel therapy facilities, a phased approach is often considered to allow production to begin at an initial, lower throughput while leaving room to grow for future expansion in overall capacity.


Understanding limitations is essential

Arcadis has designed multiple facilities capable of manufacturing oligonucleotides at scales ranging between 150 and 16,000 mMol/day. Designing a facility for any technology is highly dependent on scalability and forecasted market trends, but oligonucleotide facility design is unique in its inherent overlap between an active pharmaceutical ingredient (API) facility (heavy solvent usage) and a biopharmaceutical facility (cleanroom environments), leading to a handful of limitations, including:


High-hazard spaces (H-spaces)

It’s inevitable that the topic of H-spaces arises when looking at a large-scale facility for a process that uses a substantial amount of flammable solvents. A ‘high hazard’ occupancy per the International Building Code (IBC) comes into play when a building generates or processes any material that constitutes a physical health hazard in quantities in excess of those allowed in control areas (also defined by IBC). Typical solvents used in oligonucleotide synthesis, like acetonitrile, toluene, and pyridine, fall under Class 1B solvents per the National Fire Protection Association (NFPA) code, meaning facilities may only store and process a limited amount of solvent before having to be characterized as a high-hazard area. Assuming the facility is designed with an NFPA-approved sprinkler system and utilizes IBC-approved storage containers, the maximum allowable quantity (MAQ) for Class 1B solvents is 480 gallons in storage and 240 gallons to be used in closed processes (less in open processes).

Nfpa Liquid Classification table


A large-scale facility may have 100 times that in storage and use thousands of gallons of solvent for a single production run, meaning it is unlikely to engineer out the possibility of designing for an H-rated facility.

Designing an H-space is unlike most other bioprocessing facility designs, as code compliance becomes much more rigorous.

For example, H-spaces require:

  Automatic fire detection and sprinkler systems that meet IBC and NFPA standards.

  Separation via rated firewalls from non-controlled spaces (i.e., office areas, warehouse storage, etc.)

  Additionally, H-rated areas that exceed 500 square feet also require:

  25% of their perimeter to be an exterior wall.

  Multiple, independent egress paths with less than 25 feet of common travel path from the most remote location within the room.

It is essential to bring an experienced and reliable code consultant on-board early in design, as early as the conceptual phase, to guide code compliance. To confirm all code requirements are sufficiently met, a qualified code consultant will review the production scale, projected chemical inventory and anticipated floor layout and comment on areas that require further evaluation. Ensuring the facility design is fully compliant up-front will remove the need for significant re-work late in the project, adding substantial engineering time and project cost (both of which are at a premium in the era of warp-speed design projects).


Operating at a variety of production scales

For the laboratory environment, equipment selection is fairly trivial; most equipment fits on benchtop spaces, can be moved fairly easily, and doesn’t require an overwhelming capital investment.

At commercial scale, depending on the flexibility required, this is less so. A pilot process producing 100 mMol/day looks quite different than one producing 10,000+ mMol/ day. Synthesis and chromatography equipment, including skids and columns, get larger, taking up valuable space on the production floor. Process skids, supporting feed vessels, distribution equipment, and utility systems must be viable across all production phases. Feed tanks are typically sized for the largest batch they are required to produce, but if they are required to support multiple production scales, they may fall short during turndown. For example, batches less than the minimum required mixing volume of the tank will either need their recipes modified or be mixed in completely separate tanks, which are significant added costs. When considering vessel sizing for both the upper and lower production limits, it will be apparent which proposed pieces of equipment can be repurposed and which will need to be segregated.

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    As equipment sizes increase, the design becomes less mobile. A compromise between dedicated equipment for increased capacity and mobile equipment for flexibility must be met to fulfil the manufacturing needs. Small, portable equipment has a cheaper capital expenditure but requires more manual operation, limiting throughput and repeatability in product quality. Fixed equipment allows for (in many cases) a primarily automated and integrated closed system with little operator intervention but also limits the operable range in production and requires dependable preventative maintenance and cleaning procedures. It is never a one-size-fits-all solution, and this balance can only be achieved with a thorough understanding of the facility’s key process parameters and master operational philosophy.


Other Considerations

There are many other considerations that are no less important than those discussed above to consider in the design phases. A few questions to keep in mind:

 

Logistics

Aside from production capability, supply chain logistics need to be clearly understood. For a facility potentially using millions of liters of hazardous material per week:

  Has the solvent distribution equipment been sufficiently specified? Is it robust to keep up with downstream demand at its highest need requirement as well as the ability to turn down appropriately for slower production phases?

  Has waste segregation and management been fully developed? Is there a sound strategy for recovering and disposing of hazardous wastes?

  Has a cleaning philosophy been developed to maximize throughput and efficiency? This includes not only scheduling downtime between batches but also equipment movement and utility consumption requirements. Smaller equipment can be sent to a dedicated washing station, but large skids and tanks will likely need to be cleaned in place.

 

Input from manufacturing

Operability is one of the most critical parameters to evaluate when reviewing a new facility design. Far too often, design projects begin solely with engineering/leadership teams and a goal in mind while not looking at it from a day-to-day perspective. Operations groups (manufacturing, facilities, and maintenance), always bring relevant context to efficiency and safety issues in existing facilities that could easily be mitigated early in the conceptual phases of a new design. Still, this key input is sometimes not highlighted or thought about until design transfers into construction.

  Has the manufacturing team been consulted early in the design on major layout and operational considerations? The layout may look great on paper, but the manufacturing team can sniff out equipment and process issues that others may not see.

  Are all pieces of equipment maintainable? Is there adequate clearance and access around equipment for service and replacement?

  Are there pieces from previous facilities that are primed to be optimized if given a chance rather than replicated in a new facility?

 

Future expansion

Sure, the design may be adequate for current short-term plans, but if the oligonucleotide market rapidly expands in five or ten years, the facility may quickly become obsolete if it is not designed adequately to meet the required capacity. Instead of pursuing an entirely new capital project to catch up, why not build the potential for market expansion in now? Ideally, flexibility is built into the current footprint to allow for future growth, allowing for major early site work to be completed once, while deferring additional process equipment costs and effort until the future demand becomes apparent. “Shell” spaces are unfinished rooms built within the given footprint to be used for an intended purpose later and are a great way to provide flexibility to a facility that may not have the current capacity requirement but is expected to reach market forecasts throughout its lifetime. Consider the following for future design options:

  How does this design affect the infrastructure above the ceiling? HVAC is one of the least flexible areas once a building is constructed, as the airflow requirements and ductwork layout are typically finalized in the early stages of the project for the proper room classifications.

  How much would future expansion affect the current production in place? Can interference with existing operations be minimized so construction on future phases can occur in parallel with the normal facility schedule, eliminating a long shut down phase where no product (and therefore no revenue) is being made?

  Are supporting process and mechanical utility equipment (air compressors, chillers, etc.) large enough to meet this expansion?


The right solution

The demand for oligonucleotide production facilities has increased significantly in the past year and is likely to continue. Designing a manufacturing facility that is flexible enough to meet the current production need and has the foresight toward future expansion requires partnering with the right A/E/C firm to turn that vision into reality. Whether designing for a pilot- or commercial-scale oligonucleotide facility, Arcadis is committed to developing an engineering solution that works for you.

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