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Fail safe design

Generally, electrical control systems are designed Fail-Safe. If power is temporarily lost, unnecessary shutdown of the process may occur. Thus, most safety systems such as fire and gas detectors, Nav-Aids, communications, and emergency lighting require standby D.C. power. [Pg.517]

Designing fail-safe care delivery processes that deflect system errors and system vulnerabilities before they reach a patient to create harm... [Pg.122]

MRP. andTOC systems Environmental issues related are addressed in design Fail-safe systems are implemented Internal suggestion system adivated Safety is addressed in design A quality management training program is implemented... [Pg.68]

Loss of utilities like power supply, hydraulic or pneumatic. More clearly, this may result in spurious trip when the SIF is designed fail-safe, which is generally the case in the oil and gas industry installations. [Pg.127]

Eail-Safe Design features which provide for the maintenance of safe operating conditions in the event of a malfunction of control devices or an interruption of an energy source (e.g., direction of failure of a control valve on loss of signal). A system is fail-safe if failure of a component, signal, or utility that would create a hazard initiates an action that maintains the system in a safe condition. [Pg.161]

The eddy current brake controls for the power recovery string are designed for fail-safe operation of the eddy current brake. These controls provide all of the logic required to make the eddy current brake recovery string a viable contender for recovering power from previously wasted energy. [Pg.271]

Figure 8-11 shows the effleieney variation with the tip speed ratio. This eurve also shows the runaway speed. Runaway speed is aehieved when turbine torque falls to zero at blade speeds higher than the design speed. If failure oeeurs above the tip speed, the rotor ean be defined as a fail-safe rotor design. [Pg.329]

Design not fail-safe (i.e. no indication of component failure)... [Pg.354]

Skins with bonded doublers have been used successfully on a large number of civil aircraft and are still used on new designs. The only widespread in-service problem with bonded doubler assemblies has been delamination caused by unstable surface preparation. Early fuselage skins with bonded doublers and inadequate surface preparation experienced severe delamination and subsequent corrosion. A majority of these delaminated doublers were the fail-safe tear straps (Fig. 27). Although the tear strap bond does not cany structural load, the bond... [Pg.1174]

Fail-safe Design features that provide for the maintenanee of safe operating eonditions in the event of a malfunetioning eontrol deviee or an interruption of an energy souree (e.g., direetion of failure of a motor-operated valve on loss of motor power). [Pg.1013]

Heaters and furnaces should also be designed in accordance with standards and codes. Boilers and heating units must be inspected periodically in accordance with codes, insurance requirements and state regulations. Proper controls, interlocks and fail-safe instnunentation must be provided. The heaters should also be provided with sight glasses for flame observation, monitoring devices for flame-out detection, and temperature alarms. [Pg.182]

It is virtually impossible to design a fail-safe operation of a chemical process. However, many companies have attempted to minimize liazardous conditions by developing a systematic approach to process design. Implemention of these acdons hoped to aeliieve maximmn protection to personnel, equipment, and die public. [Pg.249]

Figure 12-31. Capacity control suction valve unloaders are available in either of two designs with pneumatic operators (A) direct-acting (air to unload) (B) reverse-acting or fail safe (air to load), which automatically unloads the compressor in the event of control air failure (C) an innovation in manually operated unloaders. Here, the lever cam arrangement provides positive loading or unloading, eliminating the requirement to turn a handwheel completely in or out. (Used by permission Bui. 9-201B, 1991. Cooper-Cameron Corporation.)... Figure 12-31. Capacity control suction valve unloaders are available in either of two designs with pneumatic operators (A) direct-acting (air to unload) (B) reverse-acting or fail safe (air to load), which automatically unloads the compressor in the event of control air failure (C) an innovation in manually operated unloaders. Here, the lever cam arrangement provides positive loading or unloading, eliminating the requirement to turn a handwheel completely in or out. (Used by permission Bui. 9-201B, 1991. Cooper-Cameron Corporation.)...
Design of the product to meet the anticipated environmental stresses as well as the functional requirements. The product must have a designed-in means for reducing the possibility of failure plus either a fail-safe mode or an indication of incipient failure that can be monitored. [Pg.276]

The main danger in the operation of a nuclear power plant is potential loss of control over the nuclear reaction. If the core overheats, it may either explode or melt down. In either event, radioactive materials escape Irom the reactor to contaminate the environment. Designers attempt to make nuclear reactors fail-safe by providing mechanisms that automatically shut the core down on overheating. One way this has been done is to design the control rods to fall into the core if their control mechanism fails. [Pg.1587]

An important safety feature is provided by the spring in an actuator. It can be designed to position a control valve in a safe position if a loss of supply air occurs. On a loss of supply air, the actuator in Figure 36 will fail open. This type of arrangement is referred to as "air-to-close, spring-to-open" or simply "fail-open." Some valves fail in the closed position. This type of actuator is referred to as "air-to-open, spring-to-close" or "fail-closed." This "fail-safe" concept is an important consideration in nuclear facility design. [Pg.164]

The principles of operation of a hydraulic actuator are like those of the pneumatic actuator. Each uses some motive force to overcome spring force to move the valve. Also, hydraulic actuators can be designed to fail-open or fail-closed to provide a fail-safe feature. [Pg.166]

Simpler plants are friendlier than complex plants because they provide fewer opportunities for error and because they contain less equipment that can cause problems. Often, the reason for complexity in a plant is the need to add equipment and automation to control the hazards. Simplification reduces the opportunities for errors and misoperation. For example, (1) piping systems can be designed to minimize leaks or failures, (2) transfer systems can be designed to minimize the potential for leaks, (3) process steps and units can be separated to prevent the domino effect, (4) fail-safe valves can be added, (5) equipment and controls can be placed in a logical order, and (6) the status of the process can be made visible and clear at all times. [Pg.23]

Fail-safe designs All controls need to be designed to fail safely. Add safeguards for automated and safe shutdowns during emergencies. [Pg.346]

The filling method (See Figure 2) is essentially a fail-safe system in that controls are designed to prevent double-cycling. The filling valve and the reservoir valve are electrically interlocked so... [Pg.169]

An example for the design of fail-safe systems for the continuous sulfonation of an aromatic compound has been described [229]. This investigation was undertaken because a thermal explosion had occurred in a pump and circulation line. The total exothermic decomposition energy of the reaction mass is 500 kcal/kg, which is large. [Pg.169]

The SIS is normally designed to fail-safe on loss of power and takes action only when the process demands that it do so. These demands often occur when safe operating limits are exceeded due to BPCS failures. Therefore, the SIS is designed and managed to be independent of the BPCS in terms of its hardware and software and its user interfaces, such as operator, maintenance, and engineering interfaces. [Pg.104]

Failures can either be fail-safe or fail dangerously. Fail safe incidents may be initiated by spurious trips that may result in accidental shutdown of equipment or processes. Fail dangerously incidents are initiated by undetected process design errors or operations, which disable the safety interlock. The fail dangerously activation may also result in accidental process liquid or gas releases, equipment damage, or fire and explosions. [Pg.118]

ESD systems should be designed to be sufficiently reliable and fail safe that a (1) accidental initiation of the ESD is reduced to acceptable low levels or as low as reasonably practical, (2) availability is maximized as a function of the frequency of system testing and maintenance, and (3) the fractional MTBF of the system is sufficiently large to reduce the hazard rate to an acceptable level, consistent with the demand rate of the system. [Pg.118]

Fail Safe - A system design or condition such that the failure of a component, subsystem or system or input to it, will automatically revert to a predetermined safe static condition or a state of least critical... [Pg.285]

Fail-safe design of valves and instrumentation, including entire cooling or heating loop... [Pg.49]


See other pages where Fail safe design is mentioned: [Pg.222]    [Pg.258]    [Pg.42]    [Pg.580]    [Pg.222]    [Pg.258]    [Pg.42]    [Pg.580]    [Pg.234]    [Pg.98]    [Pg.440]    [Pg.396]    [Pg.1130]    [Pg.388]    [Pg.86]    [Pg.561]    [Pg.85]    [Pg.270]    [Pg.396]    [Pg.277]    [Pg.461]    [Pg.239]    [Pg.117]    [Pg.119]    [Pg.240]    [Pg.289]   
See also in sourсe #XX -- [ Pg.194 ]




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