Manufacturing, Aseptic Processing

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Recent problems with food and pharmaceutical ingredients sourced from China highlight a major disadvantage of our complex international supply chains for food and drug ingredients. A global supply chain offers more opportunities for accidental contamination as well as intentional adulteration and counterfeiting. Sticking to minimal requirements may not be enough.

The US Pharmacopeia (Rockville, MD, USP, www.usp.org) recently announced that the implementation period for its USP­–NF general notices statement requiring all manufacturers to conform to recently revised residual solvent standards in General Chapter <467> has been extended from July 1, 2007 to July 1, 2008.

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NovAseptic mixers from Millipore (www.millipore.com/bioprocess) are designed for a variety of mixing applications in the pharmaceutical and biotechnology industries and are magnetically driven, which minimizes contamination risk.

Steam traps are part of a steam-in-place system. The current design allots 18 in. of vertical leg for condensate backup. A design with a sensitive bellows has been proven in laboratory tests to need only 6 in. of vertical leg during the 15 min. of 121?C sterilization. Loads of 1 to 27 lb/h are covered by the capability of the new trap, equivalent to required steam for vessels 20 to 40,000 L.

In the pharmaceutical industry, ultrafiltration (UF) membranes are used extensively in the downstream purification of recombinant proteins or monoclonal antibodies. However, the fouling of membranes after a unit operation?especially when recombinant proteins or monoclonal antibodies are highly concentrated?is a common problem. Typically, normalized water permeability (NWP) of a membrane can be reduced to about 20 percent of its original permeability at the end of an ultrafiltration-diafiltration (UF-DF) operation.