
A Look at the HAZOP Worksheet Format
A Hazard and Operability (HAZOP) study is a systematic and structured examination of a planned or existing process or operation, designed to identify and evaluate potential hazards that may represent risks to personnel, equipment, or the environment. At the heart of this critical safety assessment lies the HAZOP worksheet, a comprehensive document that meticulously records the analysis. This article provides a detailed breakdown of the typical format of a HAZOP worksheet.
A standard HAZOP worksheet is designed to be a clear and logical record of the team’s brainstorming and analysis. While the specific layout can vary slightly between organizations, the core components remain consistent. The worksheet is typically structured as a table with several key columns, each serving a distinct purpose in the hazard identification and mitigation process.
Node/Section | Design Intent | Guideword | Deviation | Possible Causes | Consequences | Safeguards | Recommendations | Action Party | Due Date |
PL-101 | Transfer of flammable liquid from Tank A to Reactor B at 50 L/min. | No | No Flow | Pump P-101 failure; Blockage in the line; Valve V-1 closed in error. | Reactor B starves, potentially leading to an off-spec product. Potential for pump damage. | Low-flow alarm (FAL-101); Regular pump maintenance schedule. | Install a redundant pump. Develop a specific checklist for valve line-up before transfer. | Engineering Dept. | 31-Oct-2025 |
More | More Flow | Pump P-101 control failure; Incorrect pump speed setting. | Overfilling of Reactor B, leading to a potential spill of flammable liquid and a fire hazard. | High-level alarm on Reactor B (LAL-201); Emergency shutdown system. | Review and validate the calibration of the pump speed controller. | Maintenance Dept. | 15-Sep-2025 |
Core Elements of a HAZOP Worksheet
The following columns are fundamental to a comprehensive HAZOP worksheet:
Column | Description |
Node/Section | This identifies the specific part of the process or system being analyzed. For example, a particular pipeline, a reactor vessel, or a heat exchanger. |
Design Intent | A concise description of how the node is intended to operate under normal conditions. This sets the baseline for identifying deviations. |
Guideword | A short, simple word (e.g., “No,” “More,” “Less,” “Reverse”) used to prompt the team to consider deviations from the design intent. |
Deviation | A potential departure from the design intent, created by combining a guideword with a process parameter (e.g., “No Flow,” “More Pressure,” “Less Temperature”). |
Possible Causes | The potential reasons why the deviation might occur. This could include equipment failure, human error, or external events. |
Consequences | The potential effects of the deviation if it were to occur, including impacts on safety, environment, and operability. |
Safeguards | Existing protective measures that are in place to prevent the cause or mitigate the consequences of the deviation. This can include alarms, relief valves, and interlocks. |
Risk Ranking (Optional) | An assessment of the likelihood and severity of the consequence, often using a risk matrix to prioritize hazards. |
Recommendations | Actions proposed by the HAZOP team to reduce the identified risk. This could involve adding new safeguards, modifying procedures, or conducting further analysis. |
Action Party/Due Date | The individual or department responsible for implementing the recommendation and the target completion date. |
Remarks | Any additional notes or comments from the team. |