Annex I: Methods & Tools prepared by some members of the ICH Q9 EWG for example only; not an official policy/guidance July 2006, slide 1 ICH Q9 QUALITY.

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Annex I: Methods & Tools prepared by some members of the ICH Q9 EWG for example only; not an official policy/guidance July 2006, slide 1 ICH Q9 QUALITY RISK MANAGEMENT Annex I.6 Hazard Operability Analysis (HAZOP)

Annex I: Methods & Tools prepared by some members of the ICH Q9 EWG for example only; not an official policy/guidance July 2006, slide 2 ICH Q9 QUALITY RISK MANAGEMENT I.6: Hazard Operability Analysis (HAZOP) (IEC 61882)  A theory that assumes that risk events are caused by deviations from the design or operating intentions  Identify potential deviations from normal use How to perform? A systematic brainstorming technique for identifying hazards using so-called “guide-words” applied to relevant parameters: >No, More, Other Than, None ICH Q9

Annex I: Methods & Tools prepared by some members of the ICH Q9 EWG for example only; not an official policy/guidance July 2006, slide 3 ICH Q9 QUALITY RISK MANAGEMENT I.6: Hazard Operability Analysis (HAZOP) Concept  Focus team discussions by applying “ deviations ” to specific nodes  Deviations are generated by applying Guidewords to process parameters  Examine the process by discussing causes of each deviation >Identify consequences >Evaluate risk and safeguards >Make recommendations, if necessary  Include all parts of the process Source: Hazard and Operability Studies in Solid Dosage Manufacture. Nail L. Maxson. (2004).

Annex I: Methods & Tools prepared by some members of the ICH Q9 EWG for example only; not an official policy/guidance July 2006, slide 4 ICH Q9 QUALITY RISK MANAGEMENT I.6: Hazard Operability Analysis (HAZOP) Potential Areas of Use(s)  Manufacturing processes  Equipment and facilities  Evaluating process safety hazards  Primarily as starter of a HACCP  Operator error (“use error”) ICH Q9

Annex I: Methods & Tools prepared by some members of the ICH Q9 EWG for example only; not an official policy/guidance July 2006, slide 5 ICH Q9 QUALITY RISK MANAGEMENT I.6: Hazard Operability Analysis (HAZOP) GuidewordsExplanationRemarks NO 、 NOT 、 NONE The total absence of the function No part of the function is active, but also nothing else happens MORE LESS Quantitative increase or Quantitative decrease This applies to quantities & properties such as flow, temperature, and also for functions such as heating and reacting. AS WELL AS PARTIALLY Qualitative increase or Qualitative decrease All desired functions & operations are achieved. Additionally, something else happens. Only a few functions are achieved, some not. REVERSEThe logical reverse of the desired function This applies mainly to functions, e.g., reverse flow or reversible chemical reaction. It can also be applied to materials, e.g., poison instead of antidote, or D- instead of L- optical isomer. OTHERTotal exchangeThe original function is not performed. Something totally different happens. Nail L. Maxson. (2004).

Annex I: Methods & Tools prepared by some members of the ICH Q9 EWG for example only; not an official policy/guidance July 2006, slide 6 ICH Q9 QUALITY RISK MANAGEMENT I.6: Hazard Operability Analysis (HAZOP) DeviationCausesConsequencesSafeguardsRecommend High temperature in blender Steam heating control malfunction Feed material #1 reaches decomposition temperature Violent reaction with toxic gas generation Personnel exposure/ injury Equipment damage Diverse high temp. interlock on blender Blender vented Test interlock on quarterly basis Add steam heating control to monthly PM EXAMPLE Nail L. Maxson. (2004).

Annex I: Methods & Tools prepared by some members of the ICH Q9 EWG for example only; not an official policy/guidance July 2006, slide 7 ICH Q9 QUALITY RISK MANAGEMENT I.6: Hazard Operability Analysis (HAZOP) Experiences  Ease of applicability of the model? >Simplifies decision making >Allows uniformity of analysis across sites >Process steps guided (“guide words”, if available)  Limitations of the model >Applies to specific situations only >May need to use other models for quantifying risk >Not a structured approach >Not designed for quantifiable risk assessment >Complex output