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I&C Safety Guide DRAFT 20110803.doc
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7.185. Trip setpoints used to initiate safety actions should be selected to ensure that required mitigating actions occur before the monitored variable reaches the analytical limit.

FIG. 5. Setpoint terminology and errors to be considered in setpoint determination

Operational identification of items important to safety

7.186. A consistent and coherent method of naming and identifying all I&c components should be determined and followed throughout the design, installation and, operation phases of the plant.

7.187. Such identification ought not require frequent reference to drawings, manuals, or other reference material.

7.188. Coherent and easily understood naming and identification of systems and components is important for engineering, maintenance, and construction staff as well as for use to label the controls, displays and indications.

7.189. Components or modules mounted in equipment or assemblies that are clearly identified do not themselves need identification. Configuration management is generally sufficient for maintaining the identification of such components, modules and embedded computer software. Chapter 2 discusses configuration management.

7.190. I&c components in the plant should be marked with their identifying information.

7.191. Safety systems and their components should be uniquely identified and marked to differentiate them from non-safety systems and to differentiate the different redundancy groups from each other.

7.192. Clear identification of components is necessary to reduce the likelihood of inadvertently performing maintenance, tests, repair or calibration on an incorrect channel.

7.193. Identification may, for example, take the form of tagging or colour coding.

8. SYSTEM AND EQUIPMENT SPECIFIC DESIGN GUIDELINES

SENSING DEVICES

8.1. Measurements of plant variables should be consistent with the requirements of the design basis.

8.2. Measurement of plant variables includes both detection of the present value of a variable within a range, and detection of a discrete state such as are detected by limit switches, auxiliary relay contacts, and temperature, pressure, flow or level switches.

8.3. Measurement of plant variables may be made by direct measurement of a plant variable, or indirect measurements such as calculation of the value of a variable based upon multiple measurements, or determination of the value of a variable based upon measurement of other data with a known relationship to the desired variable.

8.4. To the extent practicable, the plant conditions of concern should be monitored by direct measurement rather than being inferred from indirect measurements.

8.5. The sensor for each monitored variable and its range should be selected on the basis of the accuracy, speed of response, and range needed to monitor the variable in normal, accident, and design extension conditions.

8.6. CCF affecting sensing devices should not result in unacceptable consequences for people and environment.

8.7. No identified CCF vulnerability of sensing devices should have the potential of denying operators the information and parameters that they need to control and mitigate accident conditions.

8.8. If more than one sensor is necessary to cover the entire range of the monitored variable, a reasonable amount of overlap from one sensor to another should be provided at each transition point to ensure that saturation or foldover effects do not prevent the required function from being performed.

8.9. If the monitored variables have a spatial dependence (i.e., the measured value of variable depends upon sensor location), the minimum number and locations of sensors should be identified.

THE PROTECTION SYSTEM

8.10. SSR 2/1 Requirement 61 states:

A protection system shall be provided at the nuclear power plant that has the capability to detect unsafe conditions and automatically to initiate safety actions to actuate the safety systems necessary for achieving and maintaining safe plant conditions.

Automatic and manual safety actions

8.11. The protection system should monitor plant variables and detect deviations from their specified limits so that protection system functions can be initiated and performed.

8.12. SSR 2/1 Paragraph 6.33(2) states:

The design (of the protection system) shall … automate various safety actions to actuate safety systems so that operator action is not necessary within a justified period of time from the onset of anticipated operational occurrences or accident conditions.

8.13. Means should be provided to automatically initiate and control all safety actions except those for which manual action alone has been justified.

8.14. Typically automatic initiation will be necessary for most protection system functions.

8.15. Examples of situations in which manual action alone might be justified include:

  • Initiation of certain safety tasks after completion of automatic sequences;

  • Control actions to bring the plant to a safe state in the long term after an accident; and

  • Initiation of safety actions that are not required until a considerable time after the PIE.

8.16. In order to justify that manual action alone is acceptable it should be shown that:

  1. The operator has sufficient and clearly presented information from sensors and equipment of the safety system to make reasoned judgments on the need to initiate the required safety actions;

  2. The operator is provided with written procedures and training for the safety tasks;

  3. The operator is allowed sufficient time to evaluate the status of the plant and to complete the required actions;

For new designs many Member States consider that it is inadvisable to require that operators take any safety action in less than 30 minutes.

  1. The operator is provided with sufficient means of plant control to perform the required actions; and

  2. The communication links between operators carrying out the actions are adequate to ensure the correct performance of these actions.

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