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88<br />

Rush<br />

type of soil include fermenters or bioreactors that have been thermally inactivated<br />

prior to cleaning; especially challenging is the air–liquid interface where media<br />

and cell mass agglomerates and dries during the cell growth phase. Spray dryers<br />

and evaporators also present acleaning challenge as the equipment surfaces are<br />

coated with ahighly concentrated soil, often comprised primarily of denatured<br />

protein and mineral content.<br />

Protein denaturation in these examples can result in acarbohydrate-proteinfat-mineral<br />

matrix, which can be very difficult to attack with an alkaline cleaner<br />

alone. The acid override program is amore extensive treatment than any of the<br />

previously described programs, and can be effective in removing the soils noted<br />

above. The program uses a strong, hot acid solution in recirculation for an<br />

extended wash period to attack the tenacious protein and mineral soils. The<br />

concentrated alkaline is introduced after the acid wash duration to “override” the<br />

acid solution and continue recirculation, without discharge of solution. The alkaline<br />

wash phase to attack the fat and carbohydrate components of the soil. This<br />

approach conserves water usage, and minimizes discharge of concentrated acids<br />

to waste.<br />

The CIP program begins with atraditional rinse operation to send all freerinsing<br />

soil to drain prior to establishing a recirculated chemical wash phase<br />

using ahot acid solution. The CIP circuit is next subjected to ahot acid wash to<br />

attack the protein component of the matrix, breaking down peptide bonds and<br />

minerals, exposing the fat and carbohydrates trapped within the denatured<br />

protein matrix. The acid solution may be recirculated for a period of 25 to<br />

30 minutes prior to introducing concentrated alkaline cleaner to override the acid<br />

solution, the alkaline solution then working to remove the remaining exposed<br />

soils. The alkaline solution may be recirculated for aperiod 30 to 45 minutes<br />

prior to being flushed out with asubsequent rinse phase. The remainder of the<br />

program concludes in the same manner as the traditional alkaline-based<br />

wash program.<br />

Solvent-Based Cleaning Programs<br />

The application of a solvent-based cleaning program is primarily to bulk<br />

pharmaceutical chemical or API facilities, with organic and inorganic solvents<br />

employed for both process operations and cleaning the equipment. As noted in<br />

chapter 16, the process equipment and piping may not be hygienic in design or<br />

fully susceptible to CIP technology. The process cleaning is often performed in a<br />

contained manner to protect personnel from potent compounds and solvent<br />

exposure, as well as solvent release to atmosphere. The application of CIP cleaning<br />

can improve cleaning reliability while minimizing the operator exposure to potent<br />

compounds and reduce manual cleaning required to restore this equipment for<br />

process use.<br />

These CIP operations typically occur between process campaigns, and<br />

cleaning frequency may vary as acampaign may be one week or one year in<br />

duration. However, between process lots, aprocess solvent flush may be used to<br />

prevent build up of process soil. The soils noted may not be susceptible to<br />

dissolution, suspension and removal by aqueous cleaning solutions. Organic<br />

process solvents rely primarily on solubility for the removal of the soil residue,<br />

and can perform their cleaning duty without introducing an external contaminant

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