Petroleum Equipment Institute PEI RP 200 Recommended Practices for Installation of Aboveground Storage Systems for Motor Vehicle Fueling Flashcards

1
Q

To which types of tanks do the recommended practices in this document apply? (PEI RP200-13, Section 1.3)

A

aboveground, stationary, shop fabricated tanks and associated piping, and equipment intended to dispense gasoline, diesel and related petroleum products into motor vehicles at commercial an retail service stations and marinas

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2
Q

What type of a plan may be required by federal regulations if a facility could reasonably be expected to discharge product to navigable waters? (PEI RP200-13, Section 1.8)

A

Spill Prevention, Control, and Countermeasure Plan

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3
Q

From whom should approval of aboveground storage facilities be sought? What other agencies may be involved in granting approvals for aboveground tank installations? (PEI RP200-13, Section 1.9)

A

Local authorites, in addition to state and national codes

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4
Q

How must aboveground tanks be positioned with regard to property lines and buildings? (PEI RP200-13, Section 2.3)

A

Aboveground tanks must be postioned to meet the setback and distance from buildings requirements of the local juristiction

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5
Q

How much space should be provided between tanks to allow for passage and inspection? (PEI RP200-13, Section 2.4)

A

To allow passage between tanks for inspection, provide a minimum spacing equivalent to 1/6 of the sum of the adjacent tank diameters, but not less than three feet.

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6
Q

When aboveground tanks are installed at retail service stations, they are typically required to be separated by substantial distances from which parts of the facility? (PEI RP200-13, Section 2.6)

A

dispenser islands, buildings, filling points, and property lines

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7
Q

In general, how do requirements for commercial fleet facilities differ from requirements for retail service stations? (PEI RP200-13, Section 2.7)

A

They are not open to the public and are limited to their own fleet usually so no mininmum separtion of tanks and dispensers may be required. Distance to property lines and buildings may be less restrictive as well

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8
Q

What traffic flow characteristics are desirable for the off-loading area for an aboveground tank? (PEI RP200-13, Section 2.10)

A

Dispensing should be easily accessible and located where it will not interfere with other traffic flow

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9
Q

How shall aboveground tanks be protected from vandalism and accidental damage? (PEI RP200-13, Section 2.13)

A

by Installing Bollards, concrete wheel stops, fencing, and other barriers

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10
Q

Where should aboveground tanks be located with regard to underground utilities or overhead power lines? (PEI RP200-13, Section 2.15)

A

They should not be located above underground utilities or directly beneath over head lines

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11
Q

When the ability of the soil beneath an aboveground tank to bear the weight of the fully loaded tank is questionable, what are three solutions that a storage system designer should consider? (PEI RP200-13, Section 3.3)
a)

b)

c)

A

Replacing subsoil
Placing reinforced concrete slab on grade or on pilings
Stablizing fine soil with geotextile or compacted mixture of hydrated lime, dry cement, or pulverized soil

Only a qualified individulal should determine the method used

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12
Q

When constructing an aboveground tank foundation, what are appropriate materials to use for the base course? (PEI RP200-13, Section 3.5)

A

Crushed stone

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13
Q

How can a suitable foundation for vertical tanks be constructed? (PEI RP200-13, Section 3.6)

A

A suitable foundation for vertical tanks can be constructed with a finished course of clean, compacted sand, gravel, or crushed rock that is placed over the base course.

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14
Q

Where is a sand cushion typically used when installing an aboveground tank? (PEI RP200-13, Figure 3.2)

A

Between a concrete slab and tank bottom

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15
Q

How high above the surrounding ground surface should the surface on which a vertical tank bottom rests be located? (PEI RP200-13, Section 3.6)

A

At least 6 inches

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16
Q

What materials may be used for constructing saddle supports for horizontal tanks? (PEI RP200-13, Section 3.7)

A

Saddle supports for hor­ izontal tanks may be constructed of steel or reinforced concrete, and must be installed on a firm and stable foundation.

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17
Q

After setting a horizontal tank, how should any residual tilt be corrected? (PEI RP200-13, Section 3.7)

A

with full width shims

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18
Q

Under what circumstances should the saddle supports for horizontal tanks have two-hour fire protection? (PEI RP200-13, Section 3.7)

A

When the tank saddles are higher than 12 inches

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19
Q

When tank saddles are not seal-welded to the tank shell, what materials should be used to isolate the tank shell from the saddle support? What materials are NOT acceptable? (PEI RP200-13, Section 3.7.1)

A

To protect the tank coating, which provides protection against corrosion, carefully isolate the saddles from the tank shell through the use of a dielectric mate­rial.
Information on appropriate isolation materials is available from the tank manufacturer. Roofing felt or concrete expansion joint material is not acceptable

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20
Q

Aboveground tanks located in what type of area must be protected against flotation? (PEI RP200-13, Section 3.9)

A

Areas subject to flooding

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21
Q

What is the purpose of constructing dikes around aboveground tanks and associated piping? (PEI RP200-13, Section 4.1)

A
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22
Q

What should be the minimum volumetric capacity of a diked area? Can local jurisdictions require additional capacity? (PEI RP200-13, Section 4.2)

A

A dike must be able to hold the greatest volume of product that may be released by the largest tank within the dike. Additional dike capacity may be required to allow for rainwater accumulation in the dike or to provide an additional margin of safety.

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23
Q

Within the diked area, what should be the slope from the tank to the dike base? (PEI RP200-13, Section 4.7)

A

Minimum 1inch per 8 linear feet

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24
Q

What are appropriate materials for construction of dike walls? (PEI RP200-13, Section 4.3)

A

Dike walls may be constructed of earth, steel, concrete, or solid masonry

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25
Q

What types of materials may be used to form an impervious barrier on the walls and bottom of a diked area? (PEI RP200-13, Section 4.4)

A

The walls and bottom of a diked area may consist of specially formulated and well­ compacted clay, solid pavement, coatings, or impervious-membrane liners. Concrete, made impervious, may be used.

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26
Q

How should piping and conduit be routed with respect to the dike walls and floor? What should be done if penetration through the dike wall is absolutely unavoidable?
(PEI RP200-13, Section 4.5)

A

Piping and conduit should pass over the top of the dike. Where penetration of the dike wall or floor is absolutely unavoidable, the penetration should be sleeved and sealed so that it is liquid tight

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27
Q

What is the usual minimum distance between the outside base of the dike and any property line? (PEI RP200-13, Section 4.6)

A

NO closer than 10 feet

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28
Q

Where should drainage control points for diked areas be located? (PEI RP200-13, Section 4.7)

A

outside the diked area

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29
Q

What is the definition of “special enclosure” when referring to a flammable liquid storage tank? (PEI RP200-13, Section 5.10)

A

Special enclosures are liquid and vapor tight, not backfilled, and constructed of at least 6 inches of reinforced concrete. They may have openings for inspection only in the top. Tank connections should be designed to prevent liquids and vapors from entering the space between the tank(s) and the special enclosure

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30
Q

What types of forces should tank vaults be designed to resist? (PEI RP200-13, Section 5.2)

A

Vaults should be resistant to earthquakes, hurricane-force winds, and hydrostatic forces

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31
Q

For vaults located aboveground, roofs should be constructed of materials weaker than materials used for construction of the walls and floor. Why is this? (PEI RP200-13, Section 5.2)

A

Vaults located above ground should have roofs constructed of materials that are weaker than materials used for construction of the walls and floor to ensure that in the event of an explosion, the thrust of the explosion will be directed upward.

32
Q

What type of safety procedures must be followed when entering a tank vault? (PEI RP200-13, Section 5.3)

A

Confined space entry safety procedures

33
Q

What are three requirements for normal tank vents for tanks installed inside of vaults? (PEI RP200-13, Section 5.4)
a)

b)

c)

A

extend outside the vault, terminate not less than 12ft above general grade, and be located at least 5ft from building openings

34
Q

How should tank vaults be protected from vehicular collision? (PEI RP200-13, Section 5.8)

A

bollards, posts, curbs, or berms.

35
Q

Under what circumstance can a tank designed for use underground be used for aboveground storage? (PEI RP200-13, Section 6.1)

36
Q

Underwriters Laboratories standard 142 prescribes requirements for what type of tanks? (PEI RP200-13, Section 6.2.1)

A

the UL 142 standard prescribes details for welds, flanges, bracing, and flat bulkheads of compartmented tanks

37
Q

What items should be checked for damage or imperfections prior to installation? (PEI RP200-13, Section 6.4)

A

Inspect tanks and all other materials when they are delivered and before they are installed to verify that they are not visibly damaged and that their coatings are intact

38
Q

How should tanks be handled at the job site? (PEI RP200-13, Section 6.5 and WARNING)

A

Tanks should not be dropped, dragged, or handled with sharp objects. Any movement of the tank on the job site should be accomplished with lifting cable or chains attached to lifting lugs provided

39
Q

What are two methods that should NOT be used to dispense product from aboveground tanks? (PEI RP200-13, Section 7.2)
a)

b)

A

Product dispensing from aboveground tanks should not be accomplished by pressurizing the tank or by gravity flow.

40
Q

In remote pumping systems, does the supply piping operate under pressure, suction or gravity? (PEI RP200-13, Section 7.2)

A

Remote-pumping systems employ a pump that is located in, on, or near the aboveground tank to move product under pressure to a remote-dispensing location.

41
Q

At which tank openings should fire valves be installed? (PEI RP200-13, Section 7.3)

A

Install a fire valve at any tank opening where stored product could flow by gravity.

42
Q

How many block valves should a piping system contain? (PEI RP200-13, Section 7.4)

A

A piping system should contain a sufficient number of lockable block valves to allow the tank and piping to be isolated and secured. Each connection to an aboveground tank, through which product normally flows, should be provided with a block valve that is located as close as practical to the shell of the tank.

43
Q

Under what condition will a pressure regulating valve installed underneath a suction pump allow product to flow? (PEI RP200-13, Section 7.2.1, Figure 7.2)

A

The pressure-regulating valve is open only when the suction pump is operating and a vacuum is present on the pump side of the valve. To function properly, install the pressure-regulating valve directly under the suction pump and limit the hose length to 14 feet. Longer hose lengths or pressure-regulating valves located away from the suction-pump inlet may delay the closing of the valve, resulting in a release of fuel from the air eliminator.

44
Q

If a pressure regulating valve is installed in a suction pumping system, what is the maximum dispensing hose length allowed? Why is this? (PEI RP200-13, Section 7.2.1)

45
Q

External fire valves should be constructed of what material? (PEI RP200-13, Section 7.3)

A

steel or nodular iron to prevent failure under fire conditions.

46
Q

What does an anti-siphon valve prevent? Where should it be located? (PEI RP200-13, Section 7.5)

A

Where the liquid level in a tank is at a higher elevation than the supply piping or dispensing unit, a leak in the piping or dispenser can create a siphon and result in a continuous release. For both suction- and remote-pumping systems, install a valve to prevent gravity-discharge flow into the supply piping when the dispenser is not in use.

Locate the valve adjacent to and downstream of the block valve at the tank outlet.

47
Q

Which portions of aboveground piping should be equipped with a pressure relief device? (PEI RP200-13, Section 7.7)

A

Pro­ vide pressure relief for any segment of piping that could
be subjected to thermal expansion.

48
Q

How close to the tank bottom should an internal fill tube be installed? (PEI RP200-13, Section 8.2.1)

A

To minimize the generation of static electricity, fire codes typically require that product inlets entering the tank top extend to within 6 inches of the tank bottom and that they be installed to minimize vibration. A 1/8 inch hole may be drilled in the submerged-fill tube near the top of the tank to prevent fuel from siphon­ing through the fill piping. To protect the tank bottom, the lowest point of the fill tube should be no less than 4 inches above the tank bottom

49
Q

Should gasoline and diesel tanks share the same fill piping? (PEI RP200-13, Section 8.2.1)

A

NO they can not share the same fill piping

50
Q

What should be installed on the fill pipe if deliveries are to be made directly into the top of the tank? (PEI RP200-13, Section 8.2.2)

A

Provide a spill container around the fill pipe to prevent the spillage of fuel when the delivery hose is discon­ nected. An oveifill prevention valve that automatically clos­ es when the liquid level in the tank reaches a set point can be used to partially fulfill overfill protection requirements.

51
Q

What is the leading cause of product release from aboveground tanks? (PEI RP200-13, Section 8.2.3)

A

Overfilling

52
Q

At what liquid level in an aboveground tank should an overfill alarm sound? At what liquid level should flow into the tank be stopped? (PEI RP200-13, Section 8.2.3)

A

Overfill-protection systems should sound an audible or visual alarm when the liquid level of the tank approaches the maximum allowable fill level and should automatically shut off the flow of fuel to the tank when the maximum allowable fill level is reached.

53
Q

When gauging systems are installed in aboveground tanks, what type of cover should be provided for the tank opening? (PEI RP200-13, Section 8.4)

A

tank-top opening that is equipped with a lockable, vapor­ tight, non-sparking cover that can be used to manually gauge the tank contents.

54
Q

What is the maximum normal operating pressure for an aboveground tank? What is the maximum pressure allowed under emergency venting conditions? (PEI RP200-13, Section 8.5)

A

Aboveground tanks are limited to ser­ vice at 1.0 psig maximum internal operating pressure and to 2.5 psig under emergency-venting conditions

55
Q

Why is normal venting necessary? What features may normal tank vents also include? (PEI RP200-13, Section 8.5.1, Figure 8-3)

A

Normal venting is nec­essary to prevent tank distortion due to excess internal pressure or vacuum resulting from filling, emptying, or ambient-temperature changes.
In addition to allowing tanks to “breathe,” normal tank vents may include features to exclude precipitation, prevent flame propagation, or remain closed until certain pressure or vacuum conditions are met.

56
Q

What do emergency vents provide for? Where are emergency vents required? (PEI RP200-13, Section 8.5.2)

A

Emergency vents provide for vapor release in the event of excessive pressure build-up resulting from exposure of the tank to fire.

Emergency venting is required for both the tank and the interstice of secondarily contained tanks. Interstices of double-walled tanks are required to vent with sufficient capacity to vent the combined volume of the primary tank and the interstice by use of a properly sized emergency vent or by form of construction.

57
Q

What are acceptable materials for aboveground piping? (PEI RP200-13, Section 9.2)

A

. Aboveground pip­ing may be threaded, flanged, or welded Schedule 40 galvanized or painted/coated black steel pipe. Use com­patible 150# nodular iron or steel fittings, flanges, and couplings and 250/300# ground joint unions. Do not use low-melting-point materials such as fiberglass, brass, or aluminum for aboveground piping. Nonmetallic piping and flexible connectors should be listed specifically for aboveground use.

58
Q

What piping material should not be used for diesel fuel? (PEI RP200-13, Section 9.2)

A

Do not use galvanized pipe for diesel fuel, kerosene, or jet fuel storage systems

59
Q

How should underground piping associated with an aboveground tank be sloped? (PEI RP200-13, Section 10.4)

A

slope of 1/8 inch per foot to a low-point.

60
Q

In traffic areas, piping trenches for underground piping should be deep enough to allow for what thickness of bedding material? What thickness of compacted backfill material and paving? (PEI RP200-13, Section 10.4)

A

In traffic areas, ensure that the trench is sufficiently deep to permit 6 inches of bedding and at least 18 inches of compacted backfill material and pave­ment over the piping.

61
Q

When galvanic cathodic protection is applied to underground steel piping, what must be done to submerged pumps, dispensers, tanks and other metallic components that are NOT intended to be protected by the galvanic cathodic protection system? (PEI RP200-13, Section 11.5)
NOTE: When impressed current cathodic protection is used, all metallic components should be electrically continuous.

A

Galvanic cathodic protection, using magnesium or zinc anodes, may be used to provide corrosion protection to steel structures that are in contact with the soil. Verify that protected structures are electrically continuous. Bond isolated piping that is to be protected with #12TW or THHN stranded or solid wire. Electrically isolate structures that are protected with galvanic anodes from all other unprotected storage­ system components through the use of isolation bushings or flanges. Take special care to isolate galvanically pro­tected components from metallic conduit and the facility electrical ground.

62
Q

What three items should tank coatings be inspected for prior to installing the tank? (PEI RP200-13, Section 11.3)

A

inspected for thickness, pinholes (holidays), and hardness prior to installing the tank.

63
Q

What type of leak detection should be installed on underground pressurized piping? (PEI RP200-13, Section 12.2.3)

A

Install a line-leak detector that is capa­ble of detecting leaks of 3 gallons per hour (at 10 psi pressure) whenever a remote-pumping system (see Section 7.2) is used with below-grade piping. For maximum environmental protection, second­ ary containment of the below-grade piping with continuous monitoring in addition to a line-leak detector is recommended.

64
Q

Why is it important to control vapor emissions during fuel transfer operations? (PEI RP200-13, Section 12.3)

A

reducing air pollution and is required in some areas

65
Q

Why should sensing devices used in interstitial spaces be easily accessible? (PEI RP200-13, Section 12.2.1)

A

When sensing devices are utilized in interstitial spaces they should be easily accessed for testing and maintenance.

66
Q

Why should sensing devices used in interstitial spaces be easily accessible? (PEI RP200-13, Section 12.2.1)

A

When sensing devices are utilized in interstitial spaces they should be easily accessed for testing and maintenance.

67
Q

What are four ways of performing volumetric methods of release detection? (PEI RP200-13, Section 12.2)

A

visual inspection, Secondary containment, volumetric methods, piping release detection

68
Q

In addition to state and local electrical codes, aboveground tank installations should conform to national electrical codes as well. What abbreviation is commonly used to refer to the national electrical code? What organization publishes the national electrical code?
(PEI RP200-13, Section 13.1)

A

The National Electrical Code NFPA 70 published by the National Fire Protection Association

69
Q

In the national electrical code, what is the distinction between Division 1 and Division 2 locations? (PEI RP200-13, Section 13.2)

A

In Division
1 locations, flammable vapors are usually present in ignitable concentrations. In Division 2 locations, flam­mable vapors can be expected to be present infrequently and only under abnormal conditions.

70
Q

What is an “emergency shut-off?” Where is it located? What does it do? (PEI RP200-13, Section 13.4)

A

switch that will cut off the power to all dispensing devices in the event of an emergency. Locate the switch between 20 and 100 feet from the dispensers.

71
Q

What should be used to protect vertical tank bottoms that rest directly on soil or concrete? (PEI RP200-13, Section 11.3.1)

A

with a coating and or cathodic protection

72
Q

What should be done to electrical conduits entering or leaving classified areas to prevent the migration of fumes or vapors? (PEI RP200-13, Section 13.5)

A

Enclose wiring within Class I, Division 1 areas that is not intrinsically safe in rigid metal conduit. Use explosion-proof boxes, fittings, and joints. Explo­sion-proof flexible fittings up to 3 feet long are permit­ ted. Seal off conduits entering and leaving classified areas, as well as switches and other potential sources of ignition, to prevent the migration of fumes or vapors through the conduit. Route conduit over dikes

73
Q

What is an “intrinsically safe” device? (PEI RP200-13, Section 13.6)

A

Intrinsically safe devices and wiring are incapable of producing a spark or sufficient heat to ignite flammable or combustible materials

74
Q

What should be done to protect aboveground tanks from lightning and static discharge? (PEI RP200-13, Section 13.7)

A

Grounding and Bonding

75
Q

What type of gauge is recommended when conducting an air-and-soap test? What should be the maximum limit of the gauge? What should be used to prevent over-pressurization of the tank? (PEI RP200-13, Section 6.6.2)

A

Pressure gauges must have a scale that will permit detection of small pressure changes that might go undetected on gauges with a broader range. Because gauges are most accurate at mid­ range, and tank-test pressures should not exceed 5 psig, a gauge with a maximum limit of 10 or 15 psig is recommended. Use two gauges to reduce the chance of over-pressurizing the tank due to gauge failure. To prevent over-pressurization dur­ing testing, install a pressure-relief device that has the capability of relieving the entire output of the air source at 0.5 psig greater than the recommended test pressure relief device for proper operation and accuracy before each use

76
Q

When conducting an air-and-soap test, what is it that indicates the presence of a leak? (PEI RP200-13, Section 6.6.3)

77
Q

What is the maximum recommended pressure for testing vertical aboveground tanks? For testing horizontal aboveground tanks? (PEI RP200-13, Section 6.6.3)

A

Pressurize vertical tanks to 1.5-2.5 psig for Vertical
Pressur­ize horizontal tanks to 3-5 psig