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2900 - Site Mitigation Program
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PR0505722
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Entry Properties
Last modified
1/30/2020 11:03:05 AM
Creation date
1/30/2020 9:59:46 AM
Metadata
Fields
Template:
EHD - Public
ProgramCode
2900 - Site Mitigation Program
File Section
WORK PLANS
RECORD_ID
PR0505722
PE
2951
FACILITY_ID
FA0006961
FACILITY_NAME
KJAX
STREET_NUMBER
5451
Direction
E
STREET_NAME
HARDING
STREET_TYPE
WAY
City
STOCKTON
Zip
95202
APN
10122041
CURRENT_STATUS
02
SITE_LOCATION
5451 E HARDING WAY
P_LOCATION
99
P_DISTRICT
002
QC Status
Approved
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EHD - Public
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V <br /> I.r <br /> REMOVAL AND DISPOSAL OF USED UNDERGROUND PETROLEUM STORAGE TANKS 5 <br /> s7 SECTION 4—REMOVAL OF UNDERGROUND TANKS <br /> V <br /> 4.1 Preparation opposite the vent. When inert gases are used, they <br /> should be introduced under low pressure to avoid the <br /> 4.1.1 Observe the special safety precautions in 1.3 generation of static electricity. When using CO2 or N2, <br /> through 1.3.2.2. pressures in the tank should not exceed 5 pounds per <br /> 4.1.2 Drain product piping into the tank, being square inch gauge. <br /> careful to avoid any spillage. Cap or remove product CAUTION.• The process of introducing compressed <br /> piping• gases into the tank may create a potential ignition <br /> 4.1.3 Remove residues and liquids from the tank as hazard as the result of the development of static elec- <br /> described in 3.2.4.Also observe the restrictions in 3.1.2. trical charges. The discharging device must therefore be <br /> grounded. Explosions have resulted from the discharg- <br /> 4.1.4 Excavate to the top of tank. ing of CO2 fire extinguishers into tanks containing a <br /> 4.1.5 Remove the fill pipe,gauge pipe,vapor recovery flammable vapor-air mixture. CO2 extinguishers should <br /> r. truck connection, submersible pumps, and other tank not be used for inerting flammable atmospheres. <br /> fixtures. Remove the drop tube, except when it is 4.2.4 If the method described in 4.2.3 is not practical, <br /> planned to vapor-free the tank by using an eductor as in the vapors in the tank may be displaced by adding solid <br /> 4.2.5. Cap or remove all non-product lines, such as carbon dioxide (dry ice) to the tank in the amount of at <br /> vapor recovery lines, except the vent line. The vent line least 1.5 pounds per 100 gallons of tank capacity. The <br /> should remain connected until the tank is purged.Tem- dry ice should be crushed and distributed evenly over <br /> porarily plug-all other tank openings so that all vapors the greatest possible area in the tank to promote rapid <br /> will exit through the vent line during the vapor-freeing evaporation. As the dry ice vaporizes, flammable <br /> process. vapors will flow out of the tank and may surround the <br /> area.Therefore, where practical, plug all tank openings <br /> 4.2 Purging except the vent after introducing the solid CO2 and con- <br /> 4.2.1 Remove flammable vapors by one of the tinue to observe all normal safety precautions regarding <br /> methods described in 4.2.2 through 4.2.7,or as required flammable or combustible vapors. Make sure that all of <br /> by local codes.These methods provide a means for tem- the dry ice has evaporated before proceeding. <br /> porary vapor-freeing of the tank atmosphere.However, CAUTION.• Skin contact with dry ice may produce <br /> it is important to recognize that the tank may continue burns. <br /> to be a source of flammable vapors even after following 4.2.5 Flammable vapors may be exhausted from the <br /> the vapor-freeing procedures described in 4.2.2 through <br /> 4.2.7.For this reason,caution must always be exercised tank by one of two methods of tank ventilation listed <br /> when handling or working around tanks that have below: <br /> stored flammable or combustible liquids. Before in- a. Ventilation using an eductor-type air mover usually <br /> itiating work in the tank area or on the tank, a com- driven by compressed air is illustrated in Figure 1. The <br /> �— bustible gas indicator should be used to assess vapor eductor-type air mover must be properly bonded to pre- <br /> concentrations in the tank and work area. vent the generation and discharge of static electricity. <br /> When using this method, the fill (drop) tube should <br /> ` 4.2.2 Vent all vapors from the tank at a:-minimum remain in place to ensure ventilation at the bottom of <br /> t height of 12 feet above grade and 3 feet-above any adja- the tank.Tanks equipped with fill(drop) tubes that are <br /> cent roof lines until the tank is purged of flammable not removable should be purged by this method. An <br /> y vapors. The work area should be fr6e from sources of eductor extension shall be used to discharge vapors a <br /> ignition (see 1.3.2). minimum of 12 feet above grade. <br /> 4.2.3 Flammable and combustible vapors may be b. Ventilation with a diffused air blower is illustrated in <br /> purged with an inert gas such as carbon dioxide (CO2) Figure 2. When using this purging method, it is im- <br /> `� or nitrogen (N2). This method should not be utilized if perative that the air-diffusing pipe is properly bonded to <br /> the tank is to be entered for any reason, as the tank prevent the discharge of a spark. Fill(drop)tubes must <br /> atmosphere will be oxygen deficient. The inert gas be removed to allow proper diffusion of the air in the <br /> �- should be introduced through a single tank opening at a tank. Air supply should be from a compressor that has <br /> point near the bottom of the tank at the end of the tank been checked to ensure a clean air supply and is free <br />
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