| Circulation Systems for Single and Multiple Seal Arrangements (Part Three) |
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| Written by Gordon Buck and Ralph Gabriel, John Crane, Inc. | |
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Page 4 of 7
Similar to Plan 53B, there is no gas pressurizing the barrier fluid so there is no chance of gas entrainment. Also, like Plan 53B flow is generated by a pumping ring through a heat exchanger. The heat exchanger can be water cooled, air cooled or can be finned tubing if the heat load is small enough. This system should be used with caution, as the reference line to the accumulator is subject to the process fluid. The process fluid may be corrosive, abrasive, or a slurry that could potentially clog the pressure reference line threatening the tracking ability of the system.
Seal Flush Plan 53CAdvantages & Disadvantages (vs. other Plan 53 systems)
Plan 54Plan 54 utilizes an external source to provide a clean pressurized barrier fluid to a dual pressurized seal. Strictly speaking, there is no "Plan 54 System" specified by API. That is, the details of the external lubrication system are not included by simply specifying Plan 54. The external lubrication system for Plan 54 can be as simple as a basic reservoir, pump/motor, heat exchanger and relief valves to a complex system per API Standard 614 system. Plan 54 can even be pressurized from a process stream (the so-called "Process Plan 54"). The more complex systems can be supplied with redundant systems for uninterrupted service, accumulators to maintain pressure in the case of a power outage, and any number of alarms to detect operational problems. The complexity of the external lubrication system should be in line with the severity of the service or importance of the equipment operation it is supplying barrier fluid to. The flush rate for a Plan 54 system must take into account not only energy from the mechanical seal (heat soak, seal generated heat, and turbulence), but also the heat added to the barrier fluid from the pump supplying the barrier fluid. On low pressure/flow systems this is minimal, but can become significant on larger systems operating at high pressures and flows. The system reservoir should be sized for a retention time of 5 minutes, so if the flow rate is 4-gpm the reservoir size should be a minimum of 20-gal. The flow rate is usually controlled by the size of the pump on the system. In applications where one system is supplying barrier fluid to multiple seal chambers, flow can be controlled with simple manually adjustable needle or globe valves to control valves utilizing a variety of mechanical or pneumatic systems. Like other pressurized systems, the barrier pressure should be above the maximum pressure that the inboard seal will be subject to. This differential can range from a minimum of 25-psi to large differentials to account for possible upset conditions.
Seal Flush Plan 54Advantages
Disadvantages
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