UST Technician and Operator Exam with precise ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
detailed solutions ||\\//||
Automatic line leak detector includes, but is not limited to, any device or mechanism that ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
alerts the owner or operator of an underground storage tank to the presence of a leak by:
||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
a. restricting the flow
||\\//|| ||\\//|| ||\\//||
b. activating an audile or visual alarm
||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
c. shutting off the flow
||\\//|| ||\\//|| ||\\//|| ||\\//||
d. all of the above
||\\//|| ||\\//|| ||\\//|| ||\\//||
d. all of the above
||\\//|| ||\\//|| ||\\//|| ||\\//||
By December 22, 1998, all automatic line leak detectors installed on single-walled
||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
pressurized piping must be capable of: ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
a. triggering an audible and visual alarm
||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
b. shutting down the pumping-system
||\\//|| ||\\//|| ||\\//|| ||\\//||
c. shutting off flow at the dispenser
||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
d. restricting the flow
||\\//|| ||\\//|| ||\\//||
b. shutting down the pumping-system
||\\//|| ||\\//|| ||\\//|| ||\\//||
When automatic line leak detectors are required for monitoring pressurized piping with
||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
secondary containment, they must be capable of detecting a ___ gph release. ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
a. 3
||\\//||
b. .1
||\\//||
,c. .2
||\\//||
d. 1 ||\\//||
a. 3
||\\//||
An automatic tank gauge is capable of:
||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
a. measuring diesel product temperature
||\\//|| ||\\//|| ||\\//|| ||\\//||
b. activating low level alarms for premium grade gasoline
||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
c. measuring all product level alarms for premium grade gasoline
||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
d. all of the above
||\\//|| ||\\//|| ||\\//|| ||\\//||
d. all of the above
||\\//|| ||\\//|| ||\\//|| ||\\//||
When an automatic tank gauge is utilized for single-walled tank leak detection, it shall test
||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
the tank at least monthly after the product delivery or when the tank is filled to within ___
||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
percent of the highest operating level during the previous months:
||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
a. 5
||\\//||
b. 10
||\\//||
c. 15
||\\//||
d. 20||\\//||
b. 10
||\\//||
When an automatic tank gauge is utilized for single-walled tank leak detection, it shall
||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
generate a post-test hard copy data report of the following information, except:
||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
a. liquid volume
||\\//|| ||\\//||
b. fuel depth
||\\//|| ||\\//||
,c. outside air temperature
||\\//|| ||\\//|| ||\\//||
d. time and date of test
||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
c. outside air temperature
||\\//|| ||\\//|| ||\\//||
Approved cathodic protection methodologies include: ||\\//|| ||\\//|| ||\\//|| ||\\//||
a. corrosion inhibiting paint
||\\//|| ||\\//|| ||\\//||
b. sacrificial anodes
||\\//|| ||\\//||
c. impressed current systems
||\\//|| ||\\//|| ||\\//||
d. both b and c
||\\//|| ||\\//|| ||\\//|| ||\\//||
d. both b and c
||\\//|| ||\\//|| ||\\//|| ||\\//||
The following product piping requires cathodic protection:
||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
a. single walled steel
||\\//|| ||\\//|| ||\\//||
b. single walled fiberglass
||\\//|| ||\\//|| ||\\//||
c. flexible plastic
||\\//|| ||\\//||
d. double walled fiberglass
||\\//|| ||\\//|| ||\\//||
a. single walled steel
||\\//|| ||\\//|| ||\\//||
Cathodic protection systems must be inspected by a certified cathodic protection tester
||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
within ___ months of installation:
||\\//|| ||\\//|| ||\\//|| ||\\//||
a. 3
||\\//||
b. 6
||\\//||
c. 12
||\\//||
, d. 18
||\\//||
b. 6
||\\//||
Interior linings must be inspected by a coating expert within ___ years of installation
||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
a. 3
||\\//||
b. 5
||\\//||
c. 10
||\\//||
d. 2||\\//||
b. 5
||\\//||
Temporary closure requirements are designed for tanks that will be utilized for the storage
||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
of hazardous substances within the next___:
||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
a. 36 months
||\\//|| ||\\//||
b. 12 months
||\\//|| ||\\//||
c. 6 months
||\\//|| ||\\//||
d. 18 months
||\\//|| ||\\//||
b. 12 months
||\\//|| ||\\//||
During a period of temporary closure, the owner or operator shall inspect the thank at least
||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
once every ___ months, to ensure that the temporary closure measures are in place
||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
a. 6
||\\//||
b. 12
||\\//||
c. 18
||\\//||
detailed solutions ||\\//||
Automatic line leak detector includes, but is not limited to, any device or mechanism that ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
alerts the owner or operator of an underground storage tank to the presence of a leak by:
||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
a. restricting the flow
||\\//|| ||\\//|| ||\\//||
b. activating an audile or visual alarm
||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
c. shutting off the flow
||\\//|| ||\\//|| ||\\//|| ||\\//||
d. all of the above
||\\//|| ||\\//|| ||\\//|| ||\\//||
d. all of the above
||\\//|| ||\\//|| ||\\//|| ||\\//||
By December 22, 1998, all automatic line leak detectors installed on single-walled
||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
pressurized piping must be capable of: ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
a. triggering an audible and visual alarm
||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
b. shutting down the pumping-system
||\\//|| ||\\//|| ||\\//|| ||\\//||
c. shutting off flow at the dispenser
||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
d. restricting the flow
||\\//|| ||\\//|| ||\\//||
b. shutting down the pumping-system
||\\//|| ||\\//|| ||\\//|| ||\\//||
When automatic line leak detectors are required for monitoring pressurized piping with
||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
secondary containment, they must be capable of detecting a ___ gph release. ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
a. 3
||\\//||
b. .1
||\\//||
,c. .2
||\\//||
d. 1 ||\\//||
a. 3
||\\//||
An automatic tank gauge is capable of:
||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
a. measuring diesel product temperature
||\\//|| ||\\//|| ||\\//|| ||\\//||
b. activating low level alarms for premium grade gasoline
||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
c. measuring all product level alarms for premium grade gasoline
||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
d. all of the above
||\\//|| ||\\//|| ||\\//|| ||\\//||
d. all of the above
||\\//|| ||\\//|| ||\\//|| ||\\//||
When an automatic tank gauge is utilized for single-walled tank leak detection, it shall test
||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
the tank at least monthly after the product delivery or when the tank is filled to within ___
||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
percent of the highest operating level during the previous months:
||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
a. 5
||\\//||
b. 10
||\\//||
c. 15
||\\//||
d. 20||\\//||
b. 10
||\\//||
When an automatic tank gauge is utilized for single-walled tank leak detection, it shall
||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
generate a post-test hard copy data report of the following information, except:
||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
a. liquid volume
||\\//|| ||\\//||
b. fuel depth
||\\//|| ||\\//||
,c. outside air temperature
||\\//|| ||\\//|| ||\\//||
d. time and date of test
||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
c. outside air temperature
||\\//|| ||\\//|| ||\\//||
Approved cathodic protection methodologies include: ||\\//|| ||\\//|| ||\\//|| ||\\//||
a. corrosion inhibiting paint
||\\//|| ||\\//|| ||\\//||
b. sacrificial anodes
||\\//|| ||\\//||
c. impressed current systems
||\\//|| ||\\//|| ||\\//||
d. both b and c
||\\//|| ||\\//|| ||\\//|| ||\\//||
d. both b and c
||\\//|| ||\\//|| ||\\//|| ||\\//||
The following product piping requires cathodic protection:
||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
a. single walled steel
||\\//|| ||\\//|| ||\\//||
b. single walled fiberglass
||\\//|| ||\\//|| ||\\//||
c. flexible plastic
||\\//|| ||\\//||
d. double walled fiberglass
||\\//|| ||\\//|| ||\\//||
a. single walled steel
||\\//|| ||\\//|| ||\\//||
Cathodic protection systems must be inspected by a certified cathodic protection tester
||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
within ___ months of installation:
||\\//|| ||\\//|| ||\\//|| ||\\//||
a. 3
||\\//||
b. 6
||\\//||
c. 12
||\\//||
, d. 18
||\\//||
b. 6
||\\//||
Interior linings must be inspected by a coating expert within ___ years of installation
||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
a. 3
||\\//||
b. 5
||\\//||
c. 10
||\\//||
d. 2||\\//||
b. 5
||\\//||
Temporary closure requirements are designed for tanks that will be utilized for the storage
||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
of hazardous substances within the next___:
||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
a. 36 months
||\\//|| ||\\//||
b. 12 months
||\\//|| ||\\//||
c. 6 months
||\\//|| ||\\//||
d. 18 months
||\\//|| ||\\//||
b. 12 months
||\\//|| ||\\//||
During a period of temporary closure, the owner or operator shall inspect the thank at least
||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
once every ___ months, to ensure that the temporary closure measures are in place
||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//|| ||\\//||
a. 6
||\\//||
b. 12
||\\//||
c. 18
||\\//||
