Presentation on theme: "1 Utility Systems Process Systems – ‘Direct Impact Systems’ Contact the Product Contact Materials that will Ultimately Become Part of the Product Could."— Presentation transcript:
1 Utility Systems Process Systems – ‘Direct Impact Systems’ Contact the Product Contact Materials that will Ultimately Become Part of the Product Could Otherwise Directly Impact Product Quality Examples Purified Water (Deionised) WFI Clean Steam Nitrogen Sterile Air
2 Utility Systems Process Systems – ‘Indirect Impact Systems’ Do Not Contact the product or Material that will Ultimately Become part of the product Generally Site or Building Systems (Not Tailored to Sterile Manufacturing Facilities) Deal with a Side Effect of the Manufacturing Process Examples HVAC for non classified areas Chilled Water Potable Water Floor Drains Waste Disposal
3 Exercise 3 - Direct or Indirect Utilities A: What Utilities are Direct or Indirect for the process of filling product into Mobile Vessels? Instrument Air for isolation/ control valves Glycol for temperature control of vessel jacket WFI is used for CIP (Clean in Place) CS (Clean Steam) is used to Steam in Place (SIP) the vessel before filling
4 Exercise Answers A: What Utilities are Direct or Indirect for the process of filling product into Mobile Vessels? Instrument Air for isolation/ control valves Indirect as it will never come directly in contact with product. Glycol for temperature control of vessel jacket Indirect as it will never come directly in contact with product. WFI is used for CIP (Clean in Place) Direct as it comes in contact with product path and potentially the product. Quality is critical to successful cleaning also. CS (Clean Steam) is used to Steam in Place (SIP) the vessel before filling Direct as it comes in contact with product path and potentially the product. Quality is critical to successful cleaning also.
5 Utility Systems Direct Impact Systems – Key Considerations Material of Construction in Sterile Core Should be 316L Stainless Steel Surface Finish Should be at Least 0.5 m (Preferably < 0.4 m) Utilities May Require Point-of-Use Filtration in Sterile Core Pipework in Sterile Core Should be Electropolished Materials of Construction Must be Compatible with Sterilisation Methods in Area As Many Components as Possible Should be Located Outside Sterile Core Pipework and Components in Cleanroom Must be Designed and Installed in Accordance with ASME BPE 2002 (Bio-Pharmaceutical Engineering)
6 HVAC – Heating, Ventilation & Air Conditioning Contamination From People is the Greatest Source of Contamination in an Aseptic Facility People Contribute 80% of Airborne Contamination in Cleanrooms Special Cleanroom Clothing is Worn to provide a barrier Between person and Environment High Personal Hygiene Standards Essential Minimise Number of People in Sterile Core HVAC System Must Maintain the Cleanroom Environment Requirements by Removing Airborne Contamination and Replacing it With Suitably Filtered Air Definition of Environmental Requirement Depends on Cleanroom Classification
8 HVAC Guideline on Sterile Drug Products Produced by Aseptic Processing States: Air in Critical Areas Should be Supplied at the Point-of-Use as HEPA Filtered Laminar Flow Air Having a Velocity Sufficient to Sweep Particulate Matter Away From the Filling Area. Normally a Velocity of 90 Feet Per Minute (0.46 m/sec.), Plus or Minus 20% is Adequate. Critical Areas Should Have a Positive Pressure Differential Relative to Less Clean Areas; a Pressure Differential of 0.05 inch of Water (12.5 Pascals) is Acceptable.
9 HVAC - Exercise 4 Apply Pressure Cascade Principle to Aseptic Facility Layout Below (Use Pressure of 37.5Pa for Aseptic Pressure Room 1)
14 Sterilisation Example Given: Micro-organism : Bacillus Stearothermophilus Initial Count: 1 million (10 6 ) spores D 121 Value: 1.5min (i.e. at 121 oC it will take 1.5 mins to reduce number of viable Bacillus Stearotherm – ophilus by 1 log reduction) Q1: What is the SAL? Q2: What sterilising time (t) is required to achieve an SAL of 10 - 6?
15 Sterilisation Example Answer 1 LRV = Sterilisation time D 121 LRV = 15 min 1.5 min LRV = 10 log reduction SAL = Initial bioburden count – LRV = 10 6 – 10 Logs = 10 -4
16 Sterilisation Example Answer 2 SAL = 10 -6 LRV Required = Initial Bioburden - SAL LRV = 10 6 – 10 -6 = 12 Log Reduction LRV = t/D or LRV x D 121 Value = t LRV = 12 LRV x D 121 Value = Sterilisation hold time 12 x 1.5 = 18min