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2231-2238 – Tiered Permitting Program
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PR0507092
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COMPLIANCE INFO
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Last modified
9/30/2022 10:44:25 AM
Creation date
9/30/2022 10:27:12 AM
Metadata
Fields
Template:
EHD - Public
ProgramCode
2231-2238 – Tiered Permitting Program
File Section
COMPLIANCE INFO
RECORD_ID
PR0507092
PE
2231
FACILITY_ID
FA0007093
FACILITY_NAME
QUALEX
STREET_NUMBER
555
STREET_NAME
INDUSTRIAL PARK
STREET_TYPE
DR
City
MANTECA
Zip
95336
APN
22119036
CURRENT_STATUS
02
SITE_LOCATION
555 INDUSTRIAL PARK DR
P_LOCATION
04
P_DISTRICT
005
QC Status
Approved
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EHD - Public
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S/7 <br /> IC. Implementation of Contingency Plan <br /> The contingency plan or spill plan should be implemented in the event of a fire, explosion, <br /> j or any unplanned sudden or non-sudden release of any hazardous waste, chemicals, gas, <br /> fuel, oil or other hazardous material to the air, soil or surface water at the facility. <br /> Refer to the Safety Standard Contingency/spill Plan for details of what to do to implement <br /> the plan. <br /> A small spill, generally less than one gallon, that can be immediately absorbed for proper <br /> disposal, or a spill.that is contained by secondary containment structure does not <br /> constitute a release to the environment and should not trigger the contingency plan. Spills <br /> to a municipal sewer also are not released to the environment and should not require <br /> contingency plan procedures. In each of these cases, proper clean-up should be followed. <br /> Refer to the MSDS for further information. Notification to the Publicly Owned Treatment <br /> Works(POTW) or sewer authority is recommended and may be required. <br /> A Monitoring of Electrolytic Silver Recovery Process <br /> It is important to monitor the operation of electrolytic silver recovery units in order to <br /> determine if the recovery process is effective. <br /> An initial understanding of the control system should be obtained from the manufacturer. <br /> A unit's treatment capacity is dependent on factors such a pH, flow, silver content of <br /> solution, length of residence of solution in the plating cell, and the relationship of current <br /> and time on. Because of the potential variability of some of these factors it is critical to <br /> have an analysis plan to determine the actual effectiveness of recovery. <br /> The analysis plan should include an initial evaluation and a follow-up monitoring plan. <br /> 1. The initial evaluation should collect data to determine the amount of silver in the <br /> incoming solutions before treatment at typical and peak times of operation of the film <br /> or.paper process. Samples are best taken from fix or bleach-fix tanks immediately <br /> after the representative processing has occurred. Fixer or bleach-fix overflow samples <br /> (after electrolytic silver recovery) should also be taken. For both of these sets of <br /> _ samples, the use of silver test strips (paper or copper type) should be adequate to <br /> estimate the percent recovery of silver from the electrolytic unit. This value should be <br /> compared to manufacturers specifications to determine if the unit is set-up properly <br /> and operating as claimed. <br />
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