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ERT 312 SAFETY & LOSS PREVENTION IN BIOPROCESS HAZARDS IDENTIFICATION

ERT 312 SAFETY & LOSS PREVENTION IN BIOPROCESS HAZARDS IDENTIFICATION. Prepared by: Pn. Hairul Nazirah Abdul Halim. OBJECTIVES. To evaluate hazard and operability studies methods To synthesis HAZOP session. What is hazard?. How to reduce the possibility of hazard?

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ERT 312 SAFETY & LOSS PREVENTION IN BIOPROCESS HAZARDS IDENTIFICATION

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  1. ERT 312SAFETY & LOSS PREVENTION IN BIOPROCESSHAZARDS IDENTIFICATION Prepared by: Pn. Hairul Nazirah Abdul Halim

  2. OBJECTIVES • To evaluate hazard and operability studies methods • To synthesis HAZOP session

  3. What is hazard?

  4. How to reduce the possibility of hazard? 1. Remove hazard (use public transport) 2. Reduce the frequency (follow rules, car in good conditions, physically alert, route selection) 3. Consequence – prepare for hazard (airbag, seat belt)

  5. Hazard Identification (HAZID) • Can be performed during initial design or ongoing operation of the process. • Hazard identification (HAZID) methods: 1. Process hazard checklist 2. Hazard surveys 3. Hazard and operability (HAZOP) studies 4. Safety review

  6. Process Hazard Checklists • List of possible problems and areas to be checked. • Checklist should be applied only during the preliminary stages of HAZID. • Example: Automobile checklist: • Check oil in engine • Check air pressure in tires • Check air filter • Refer to Figure 10-2.

  7. Hazards Surveys • 2 most popular forms of hazard survey: 1. Dow Fire and Explosion Index (F&EI) 2. Dow Chemical Exposure Index (CEI) 1. Dow Fire and Explosion Index (F&EI) • Is designed for rating the relative hazards with storage, handling and processing of explosive and flammable materials. • Apply to units with high potential of hazards. • Refer to Dow Index Documentation for penalty factor. • Refer to Figure 10-3 and 10-4.

  8. Procedure: • Select Material Factor (MF) - MF is function of the type of chemical used. - Table 10-1 list the MF - Higher MF indicates more flammable/explosive the material • Give penalty for various unsafe situations. 3. Total up F1 and F2. F3 = F1 x F2 • Fire & Explosion Index, F&EI = F3 x MF • Determine the degree of hazard, refer Table 10-2.

  9. Example 10-1 Your plant is considering the installation of a new railcar tank unloading facility. The facility will unload nominal 25,000-gal tank cars containing either pure butadiene or cyclohexane. The unloading system will be equipped with an emergency shutdown system with remotely operated block valves. The unloading operation will be done by computer control. The railcars are inerted with nitrogen to a pressure of 40 psig, and the railcar relief system has a set pressure of 75 psig. The unloading operating instructions are written and have been reviewed by the corporate technical staff. A reactive chemicals review has already been completed on the proposed facility. Combustible gas detectors will be located at the unloading station. A deluge system will be installed at the unloading site with an excellent water supply. A diking system will surround three sides of the facility, with any spills directed to a covered impounding area. Determine the Dow F&EI for this operation, and determine the minimum spacing from adjacent units.

  10. F&EI value = 106 • Refer to Table 10.2, which means this unloading station is an intermediate hazard. • By refering to Dow index booklet, for this case, the radius is 90ft • Thus, the unloading station must be located a minimum of 90ft from any other equipment or process.

  11. Hazard & Operability Studies (HAZOP) The HAZOP procedure: • Begin with a detailed flow sheet. Break the flow sheet into a number of process units. Thus the reactor area might be one unit, and the storage tank another. Select a unit for study. 2. Choose a study node (vessel, line, operating instruction). 3. Describe the design intent of the study node. For example, vessel V-1 is designed to store the benzene feedstock and provide it on demand to the reactor. 4. Pick a process parameter: flow, level, temperature, pressure, concentration, pH, viscosity, state (solid, liquid, or gas), agitation, volume, reaction, sample, component, start, stop, stability, power, inert.

  12. 5. Apply a guide word to the process parameter to suggest possible deviations. 6. If the deviation is applicable, determine possible causes and note any protective systems. 7. Evaluate the consequences of the deviation (if any). 8. Recommend action (what? by whom? by when?) 9. Record all information.

  13. Example 10-2 Consider the reactor system shown in Figure 10-8. The reaction is exothermic, so a cooling system is provided to remove the excess energy of reaction. In the event that the cooling function is lost, the temperature of the reactor would increase. This would lead to an increase in reaction rate, leading to additional energy release. The result would be a runaway reaction with pressures exceeding the bursting pressure of the reactor vessel. The temperature within the reactor is measured and is used to control the cooling water flowrate by a valve. Perform a HAZOP study on this unit to improve the safety of the process. Use as study nodes the cooling coil (process parameters: flow and temperature) and the stirrer (process parameter: agitation).

  14. SAFETY REVIEWS • 2 types of safety review: the formal and the informal • The informal safety review is used for small changes to existing process • The formal safety review is used for new processes, substantial changes in existing process and process that need an updated review. • The formal report includes the following sections: 1. Introduction 2. Raw material & products 3. Equipment setup 4.Procedures 5. Safety checklist 6. MSDS

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