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DOE-HDBK-3010-94
Appendix B; Plutonium Recovery Facility
normally open only enough to maintain a small flow through the heat exchanger. A
temperature detector on the bath controls the position of the inlet valve to allow for
quick compensation of temperature fluctuations. The bath heating element is
controlled by a thermostat, but the bath temperature signal provides an alarm and
deenergizes the element if temperature exceeds 76 F. The pressure sensor on the
gaseous HF outlet line will also shut off the heater if pressure begins to rise
continuously.
A level sensor on the evaporator controls the position of the liquid HF inlet valve.
Nitrogen purge lines are provided on the system as well. They exhaust to the HF
storage tank scrubbing system. The final major feature of the evaporation system is
the installed rupture disc and relief valve. The rupture disc is designed to fail at 14
psig. The resultant pressurization of the piping between the rupture disc and the relief
valve will cause the installed pressure sensor to trigger an alarm locally, in the dry
line operating room and in the main control room. The sensor's signal will also cause
the liquid HF supply valve to the evaporator to shut.
The evaporator relief valve will lift at approximately 20 psig. The relief line will pass
through a single HEPA filter installed to preserve the integrity of the radiological
envelope within airlock areas. The line then passes through the ceiling of the room to
a roof vent elevated 15 feet above the actual roof of the building. This release will be
accompanied by an audible alarm on the roof triggered by the evaporator pressure
sensor. The limited flowrate needed to relieve pressure from the evaporator will not
create a significant personnel hazard due to the elevation of the roof vent.
The evaporator room itself is equipped with fluorine detectors, which are also in the
ventilation exhaust header. These units alarm in the same locations as the pressure
relief alarms.
2.3 H A Z A R D I DE N T I FI CA T I ON
This document presents in tabular form the hazards identified by the team evaluating the H-1
Plutonium Recovery Facility. It follows the process flow of the facility as it would occur,
and then identifies potential hazards in supporting activities in accordance with the building
layout. The two general types of hazards identified are as follows:
A-
Material of concern for release or a potential hazard in direct contact with a
material of concern.
Page B-62


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