Note : Les descriptions sont présentées dans la langue officielle dans laquelle elles ont été soumises.
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METHOD AND APPARATUS FOR LIMITING ACIDIC CORROSION
AND CONTAMINATION IN FUEL DELIVERY SYSTEMS
CROSS REFERENCE TO RELATED APPLICATIONS
100011 This application claims priority to U.S. Provisional Patent
Application
Serial No. 62/814,428 filed March 6, 2019. This application is related to U.S.
Patent
Application Serial No 15/914,535 filed March 7, 2018, which claims priority to
US.
Provisional Patent Application Serial No. 62/468,033 filed March 7, 2017, U.S.
Provisional Patent Application Serial No. 62/509,506 filed May 22, 2017, U.S.
Provisional Patent Application Serial No 62/520,891 filed June 16, 2017, and
U.S.
Provisional Patent Application Serial No. 62/563,596 filed September 26, 2017.
The
disclosures of all of the foregoing applications are hereby expressly
incorporated by
reference herein in their entireties.
FIELD OF THE DISCLOSURE
100021 The present disclosure relates to controlling fuel delivery
systems and, in
particular, to a method and apparatus for controlling fuel delivery systems to
limit acidic
corrosion, and/or to limit the accumulation of water and particulate matter in
stored fuel.
BACKGROUND OF THE DISCLOSURE
100031 A fuel delivery system typically includes one or more
underground storage
tanks that store various fuel products and one or more fuel dispensers that
dispense the
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fuel products to consumers. The underground storage tanks may be coupled to
the fuel
dispensers via corresponding underground fuel delivery lines.
[0004] In the context of an automobile fuel delivery system, for
example, the fuel
products may be delivered to consumers' automobiles In such systems, the fuel
products
may contain a blend of gasoline and alcohol, specifically ethanol. Blends
having about
2.5 vol. % ethanol ("E-2.5"), 5 vol. % ethanol ("E-5"), 10 vol. % ethanol ("E-
10"), or
more, in some cases up to 85 vol. % ethanol (ME-85"), are now available as
fuel for cars
and trucks in the United States and abroad. Other fuel products include diesel
and
biodiesel, for example.
[0005] Sumps (i.e., pits) may be provided around the equipment of
the fuel
delivery system. Such sumps may trap liquids and vapors to prevent
environmental
releases. Also, such sumps may facilitate access and repairs to the equipment.
Sumps
may be provided in various locations throughout the fuel delivery system. For
example,
dispenser sumps may be located beneath the fuel dispensers to provide access
to piping,
connectors, valves, and other equipment located beneath the fuel dispensers.
As another
example, turbine sumps may be located above the underground storage tanks to
provide
access to turbine pump heads, piping, leak detectors, electrical wiring, and
other
equipment located above the underground storage tanks.
[0006] Underground storage tanks and sumps may experience premature
corrosion. Efforts have been made to control such corrosion with fuel
additives, such as
biocides and corrosion inhibitors. However, the fuel additives may be
ineffective against
certain microbial species, become depleted over time, and cause fouling, for
example.
Efforts have also been made to control such corrosion with rigorous and time-
consuming
water maintenance practices, which are typically disfavored by retail fueling
station
operators.
[0007] Water and/or particulate matter sometimes also contaminates
the fuel
stored in underground storage tanks. Because these contaminants are generally
heavier
than the fuel product itself, any water or particulate matter found in the
storage tank is
generally confined to a "layer" of fuel mixed with contaminants at bottom of
the tank.
Because dispensation of these contaminants may have adverse effects on
vehicles or
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other end-use applications, efforts have been made to timely detect and
remediate such
contaminants.
SUMMARY
[0008] The present disclosure relates to a method and apparatus for
controlling a
fuel delivery system to limit acidic corrosion. An exemplary control system
includes a
controller, at least one monitor, an output, and a remediation system. The
monitor of the
control system may collect and analyze data indicative of a corrosive
environment in the
fuel delivery system. The output of the control system may automatically warn
an
operator of the fueling station of the corrosive environment so that the
operator can take
preventative or corrective action. The remediation system of the control
system may take
at least one corrective action to remediate the corrosive environment in the
fuel delivery
system.
[0009] The present disclosure further relates to a method and
apparatus for
filtration of fuel contained in a storage tank, in which activation of a fuel
dispensation
pump concurrently activates a filtration system. In particular, a portion of
pressurized
fuel delivered by the dispensation pump is diverted to an eductor designed to
create a
vacuum by the venturi effect. This vacuum draws fluid from the bottom of the
storage
tank, at a point lower than the intake for the dispensation pump so that any
water or
particulate matter at the bottom of the storage tank is delivered to the
eductor before it
can reach the dispensation pump intake. The eductor delivers a mix of the
diverted fuel
and the tank-bottom fluid to a filter, where any entrained particulate matter
or water is
filtered out and removed from the product stream. Clean, filtered fuel is then
delivered
back to the storage tank.
[0010] According to an embodiment of the present disclosure, a fuel
delivery
system is provided including a storage tank containing a fuel product, a fuel
delivery line
in communication with the storage tank, at least one monitor that collects
data indicative
of a corrosive environment in the fuel delivery system, a controller in
communication
with the at least one monitor to receive collected data from the at least one
monitor, and a
remediation system configured to take at least one corrective action to
remediate the
corrosive environment when activated by the controller in response to the
collected data.
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100111 According to another embodiment of the present disclosure, a
fuel
delivery system is provided including a storage tank containing a fuel
product, a fuel
delivery line in communication with the storage tank, a monitor including a
light source,
a corrosive target material exposed to a corrosive environment in the fuel
delivery
system, and a detector configured to detect light from the light source
through the target
material, and a controller in communication with the monitor.
100121 According to yet another embodiment of the present
disclosure, a fuel
delivery system is provided including a storage tank containing a fuel
product, a sump, a
pump having a first portion positioned in the sump and a second portion
positioned in the
storage tank, and a water filtration system. The water filtration system
includes a water
filter positioned in the sump and configured to separate the fuel product into
a filtered
fuel product and a separated water product, a fuel inlet passageway in fluid
communication with the storage tank and the water filter via the pump to
direct the fuel
product to the water filter, a fuel return passageway in fluid communication
with the
water filter and the storage tank to return the filtered fuel product to the
storage tank, and
a water removal passageway in fluid communication with the water filter to
drain the
separated water product from the water filter
100131 According to still another embodiment of the present
disclosure, a fuel
delivery system is provided including a water filtration system. The water
filtration
system includes a filter configured to separate a fuel product into a filtered
fuel product
and a separated water product, an eductor configured to receive a flow of fuel
from a fuel
delivery pump and send the flow of fuel to the filter, and a vacuum port on
the eductor
configured to be operably connected to a source of contaminated fuel, such
that the
vacuum port draws the contaminated fuel into the flow of fuel through the
eductor and
delivers a mixture of fuel and contaminated fuel to the filter.
100141 According to still another embodiment of the present
disclosure, a fuel
delivery system is disclosed including a storage tank containing a fuel
product, a
dispenser, a water filter, a fuel uptake line in fluid communication with the
storage tank
and the dispenser to deliver the fuel product to the dispenser, a filtration
uptake line in
fluid communication with the storage tank and the water filter to deliver the
fuel product
to the water filter, the water filter being configured to separate the fuel
product into a
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filtered fuel product and a separated water product, a fuel return passageway
in fluid
communication with the water filter and the storage tank to return the
filtered fuel
product to the storage tank, and a water removal passageway in fluid
communication with
the water filter to drain the separated water product from the water filter.
[0015] Additional aspect of the present disclosure are further
described below.
1. A fuel delivery system comprising:
a storage tank containing a fuel product;
a fuel delivery line in communication with the storage tank;
at least one monitor that collects data indicative of a corrosive environment
in the
fuel delivery system;
a controller in communication with the at least one monitor to receive
collected
data from the at least one monitor; and
a remediation system configured to take at least one corrective action to
remediate
the corrosive environment when activated by the controller in response to the
collected
data.
2. The fuel delivery system of claim 1, further comprising:
a pump configured to deliver the fuel product from the storage tank to the
fuel
delivery line: and
a sump positioned around at least a portion of the pump,
3. The fuel delivery system of claim 2, wherein the remediation system
includes a
first air passageway configured to ventilate the sump into the storage tank.
4. The fuel delivery system of claim 3, further comprising a second air
passageway
configured to pull air from the surrounding atmosphere into the sump.
5. The fuel delivery system of claim 1, wherein the remediation system
includes at
least one radiation source.
6. The fuel delivery system of claim 5, wherein the at least one radiation
source is a
ultraviolet-C light source.
7. The fuel delivery system of claim 1, wherein the at least one monitor
includes a
light source, a corrosive target material exposed to the corrosive environment
in the fuel
delivery system, and a detector configured to detect light from the light
source through
the target material.
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8. The fuel delivery system of claim 7, wherein the corrosive target
material is
constructed of copper or low carbon steel.
9. The fuel delivery system of claim 7, wherein the corrosive target
material
includes a plurality of pores.
10. The fuel delivery system of claim 7, wherein the corrosive target
material is one
of a woven mesh and a perforated sheet.
11. A fuel delivery system comprising:
a storage tank containing a hid product;
a fuel delivery line in communication with the storage tank;
a monitor including a light source, a corrosive target material exposed to a
corrosive environment in the fuel delivery system, and a detector configured
to detect
light from the light source through the target material; and
a controller in communication with the monitor.
12. The fuel delivery system of claim 11, wherein the corrosive target
material is
constructed of copper or low carbon steel.
13. The fuel delivery system of claim 11, wherein the corrosive target
material
includes a plurality of pores.
14. The fuel delivery system of claim 11, wherein the corrosive target
material is one
of a woven mesh and a perforated sheet.
15. The fuel delivery system of claim 11, wherein the monitor further
comprises:
a first housing that contains the light source and the detector; and
a second housing that contains the corrosive target material, the second
housing
being removably coupled to the first housing.
16. The fuel delivery system of claim 15, wherein the first housing is
hermetically
sealed from corrosive environment in the fuel delivery system and is at least
partially
transparent.
17. The fuel delivery system of claim 15, wherein the second housing
includes a
reflective surface positioned downstream of the light source and upstream of
the detector.
18. The fuel delivery system of claim 15, wherein the first and second
housings are
positioned in at least one of:
a vapor space of the storage tank; and
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a vapor space of a sump.
19. The fuel delivery system of claim 15, wherein the second housing has
relatively
small side openings adjacent to the corrosive target material and relatively
large side
openings opposite from the corrosive target material.
20. The fuel delivery system of claim 15, wherein the second housing has
bottom
openings concentrated beneath the corrosive target material.
21. The fuel delivery system of claim 11, wherein the corrosive target
material of the
monitor has:
a first configuration in which the corrosive target material is exposed to the
corrosive environment in the fuel delivery system; and
a second configuration in which the corrosive target material is removed from
the
corrosive environment in the fuel delivery system and is positioned between
the light
source and the detector.
22. The fuel delivery system of claim 11, wherein the detector is one of a
photosensor
and a camera.
23. A fuel delivery system comprising:
a storage tank containing a fuel product;
a sump;
a pump having a first portion positioned in the sump and a second portion
positioned in the storage tank; and
a water filtration system comprising-
a water filter positioned in the sump and configured to separate the fuel
product into a filtered fuel product and a separated water product;
a fuel inlet passageway in fluid communication with the storage tank and
the water filter via the pump to direct the fuel product to the water filter,
a fuel return passageway in fluid communication with the water filter and
the storage tank to return the filtered fuel product to the storage tank; and
a water removal passageway in fluid communication with the water filter
to drain the separated water product from the water filter.
24. The fuel delivery system of claim 23, wherein the fuel inlet passageway
is
coupled to the pump at a location upstream of a leak detector.
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25. The fuel delivery system of claim 23, further comprising:
an inlet valve positioned along the fuel inlet passageway; and
a controller that opens the inlet valve at a predetermined start time outside
of
high-demand fuel dispensing hours
26. The fuel delivery system of claim 23, further comprising:
a drain valve positioned along the water removal passageway;
a high-level water sensor positioned in the water filter; and
a controller that opens the drain valve when the high-level water sensor
detects
water in the water filter.
27. The fuel delivery system of claim 26, further comprising a low-level
water sensor
positioned in the water filter, wherein the controller closes the drain valve
when the low-
level water sensor does not detect water in the water filter.
28. The fuel delivery system of claim 26, wherein the high-level water
sensor is
positioned beneath an entry into the fuel return passageway.
29. The fuel delivery system of claim 23, wherein the water removal
passageway
extends out of the sump to drain the separated water product continuously out
of the
sump.
30. The fuel delivery system of claim 23, wherein the water removal
passageway
extends to a second storage tank positioned in the sump to drain the separated
water
product into the storage tank.
31. The fuel delivery system of claim 30, further comprising:
a high-level water sensor positioned in the second storage tank; and
a controller that sends a communication requiring the second storage tank to
be
emptied when the high-level water sensor detects water in the second storage
tank.
32. The fuel delivery system of claim 23, further comprising a selective
absorbent in
fluid communication with the water removal passageway to remove oil from the
separated water product.
33. The fuel delivery system of claim 23, wherein the fuel return
passageway returns
the filtered fuel product to the storage tank in a manner that promotes
circulation in the
storage tank.
34. A fuel delivery system comprising:
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a water filtration system comprising:
a filter configured to separate a fuel product into a filtered fuel product
and a separated water product
an eductor configured to receive a flow of fuel from a fuel delivery pump
and send the flow of fuel to the filter,
a vacuum port on the eductor configured to be operably connected to a
source of contaminated fuel, such that the vacuum port draws the contaminated
fuel into
the flow of fuel through the eductor and delivers a mixture of fuel and
contaminated fuel
to the filter.
35. The fuel delivery system of claim 34, further comprising:
a storage tank containing a fuel product;
a fuel dispenser; and
a pump having a fuel uptake line connected to the eductor and the dispenser,
such
that the pump is configured to discharge the fuel product to the eductor and a
dispensing
nozzle simultaneously.
36. The fuel delivery system of claim 35, further comprising a sump, the
pump
having a first portion positioned in the sump and a second portion positioned
in the
storage tank.
37. The fuel delivery system of claim 36, further comprising a filtration
uptake line
extending from the tank to the vacuum port of the eductor, wherein:
a first gap is formed between a bottom of the storage tank and an inlet to the
fuel
uptake line; and
a second gap is formed between the bottom of the storage tank and an inlet to
the
filtration uptake line,
the first gap larger than the second gap, whereby contaminants settled at the
bottom of the storage tank flow into the filtration uptake line before the
fuel uptake line.
38. The fuel delivery system of claim 34, wherein the filter comprises:
a filter element;
a fuel inlet above the filter element;
a fuel outlet below the top of the filter element; and
a water removal passageway below the fuel outlet.
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39. A fuel delivery system comprising:
a storage tank containing a fuel product;
a dispenser;
a water filter;
a fuel uptake line in fluid communication with the storage tank and the
dispenser
to deliver the fuel product to the dispenser;
a filtration uptake line in fluid communication with the storage tank and the
water
filter to deliver the fuel product to the water filter, the water filter being
configured to
separate the fuel product into a filtered fuel product and a separated water
product;
a fuel return passageway in fluid communication with the water filter and the
storage tank to return the filtered fuel product to the storage tank; and
a water removal passageway in fluid communication with the water filter to
drain
the separated water product from the water filter.
40. The fuel delivery system of claim 39, further comprising:
a pump positioned along the fuel uptake line; and
an eductor positioned along the filtration uptake line.
41 The fuel delivery system of claim 39, wherein an inlet to the
filtration uptake line
is positioned closer to a bottom surface of the storage tank than an inlet to
the fuel uptake
line.
BRIEF DESCRIPTION OF THE DRAWINGS
[0016] The above-mentioned and other features and advantages of
this disclosure,
and the manner of attaining them, will become more apparent and the invention
itself will
be better understood by reference to the following description of embodiments
of the
invention taken in conjunction with the accompanying drawings, wherein:
[0017] FIG. 1 depicts an exemplary fuel delivery system of the
present disclosure
showing above ground components, such as a fuel dispenser, and below ground
components, such as a storage tank containing a fuel product, a fuel delivery
line, a
turbine sump, and a dispenser sump;
[0018] FIG. 2 is a cross-sectional view of the storage tank and the
turbine sump
of FIG. 1;
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[0019] FIG. 3 is a schematic view of an exemplary control system of
the present
disclosure, the control system including a controller, at least one monitor,
an output, and
a remediation system;
[0020] FIG. 4 is a schematic view of a first exemplary electrical
monitor for use
in the control system of FIG. 3;
[0021] FIG. 5 is a schematic view of a second exemplary electrical
monitor for
use in the control system of FIG. 3,
[0022] FIG. 6 is a schematic view of a third exemplary optical
monitor for use in
the control system of FIG 3;
[0023] FIG. 7 includes photographs of the corrosive samples tested
in Example 1;
[0024] FIG. 8 is a graphical representation of the relative
transmitted light
intensity through each sample of Example 1 over time;
[0025] FIG. 9 is a graphical representation of the normalized
transmitted light
intensity through each sample of Example 1 over time;
[0026] FIG. 10 is a graphical representation of the transmitted
light intensity
through the corrosive sample tested in Example 2 over time;
[0027] FIG. 11 is a perspective view of the turbine sump having a
water filtration
system;
[0028] FIG. 12 is a perspective view of the turbine sump having a
water filtration
system similar to FIG. 11 and also including a water storage tank;
[0029] FIG. 13 shows an exemplary method for operating the water
filtration
system;
[0030] FIG. 14 is a schematic view of another exemplary water
filtration system
utilizing continuous filtration by eduction;
[0031] FIG. 15 is an enlarged portion of the schematic view of FIG.
14,
illustrating the components of the water filtration system;
[0032] FIG. 16 is a perspective view of another exemplary optical
monitor
including an upper housing with a light source and an optical detector and a
lower
housing with a corrosive target material and a reflective surface;
[0033] FIG. 17 is an exploded perspective view of the lower housing
and the
corrosive target material of FIG. 16;
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[0034] FIG. 18 is a top plan view of the lower housing and the
corrosive target
material of FIG. 16;
[0035] FIG. 19 is a partial cross-sectional view of the optical
monitor of FIG. 16;
[0036] FIG. 20 is a graphical representation of the relative
humidity and
temperature over time in a turbine sump with a desiccant; and
[0037] FIG. 21 is a schematic view of another exemplary water
filtration system
utilizing continuous filtration by eduction,
[0038] FIG. 22 is an enlarged portion of the schematic view of FIG.
21,
illustrating the components of the water filtration system;
[0039] FIG. 23 is a perspective view of yet another exemplary water
filtration
system utilizing continuous filtration by eduction;
[0040] FIG. 24A is side elevation, section and partial cutaway view
of the water
filtration system of FIG 23;
[0041] FIG. 24B is side elevation, enlarged view of a portion of
the water
filtration system of FIG. 24A;
[0042] FIG. 25 is a side elevation, section view of a portion of
the water filtration
system of FIG. 23, illustrating the water filter at partial water capacity;
100431 FIG. 26 is another side elevation, section view of a portion
of the water
filtration system of FIG. 23, illustrating the water filter at full water
capacity; and
[0044] FIG. 27 is a perspective view of an automatic shutoff valve
used in the
water filter shown in FIGS. 23-26,
[0045] Corresponding reference characters indicate corresponding
parts
throughout the several views. The exemplifications set out herein illustrate
exemplary
embodiments of the invention and such exemplifications are not to be construed
as
limiting the scope of the invention in any manner.
DETAILED DESCRIPTION
[0046] An exemplary fuel delivery system 10 is shown in FIG, 1,
Fuel delivery
system 10 includes a fuel dispenser 12 for dispensing a liquid fuel product 14
from a
liquid storage tank 16 to consumers. Each storage tank 16 is fluidly coupled
to one or
more dispensers 12 via a corresponding fuel delivery line 18. Storage tank 16
and
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delivery line 18 are illustratively positioned underground, but it is also
within the scope
of the present disclosure that storage tank 16 and/or delivery line 18 may be
positioned
above ground.
[0047] Fuel delivery system 10 of FIG. 1 also includes a pump 20 to
draw fuel
product 14 from storage tank 16 and to convey fuel product 14 through delivery
line 18 to
dispenser 12. Pump 20 is illustratively a submersible turbine pump ("STP")
having a
turbine pump head 22 located above storage tank 16 and a submersible motor 24
located
inside storage tank 16. However, it is within the scope of the present
disclosure that other
types of pumps may be used to transport fuel product 14 through fuel delivery
system 10.
[0048] Fuel delivery system 10 of FIG. 1 further includes various
underground
sumps (i.e., pits). A first, dispenser sump 30 is provided beneath dispenser
12 to protect
and provide access to piping (e.g., delivery line 18), connectors, valves, and
other
equipment located therein, and to contain any materials that may be released
beneath
dispenser 12. A second, turbine sump 32, which is also shown in FIG. 2, is
provided
above storage tank 1610 protect and provide access to pump 20, piping (e.g.,
delivery
line 18), leak detector 34, electrical wiring 36, and other equipment located
therein.
Turbine sump 32 is illustratively capped with an underground lid 38 and a
ground-level
manhole cover 39, which protect the equipment inside turbine sump 32 when
installed
and allow access to the equipment inside turbine sump 32 when removed.
[0049] According to an exemplary embodiment of the present
disclosure, fuel
delivery system 10 is an automobile fuel delivery system. In this embodiment,
fuel
product 14 may be a gasoline/ethanol blend that is delivered to consumers'
automobiles,
for example. The concentration of ethanol in the gasoline/ethanol blended fuel
product
14 may vary from 0 vol. % to 15 vol. % or more. For example, fuel product 14
may
contain about 2.5 vol. % ethanol ("E-2.5"), about 5 vol. % ethanol ("E-5"),
about 7.5 vol.
% ethanol ("E-7.5"), about 10 vol % ethanol ("E-10"), about 15 vol. % ethanol
("E-15"),
or more, in some cases up to about 85 vol % ethanol (ME-85"). As discussed in
U.S.
Publication No. 2012/0261437, the disclosure of which is expressly
incorporated herein
by reference in its entirety, the ethanol may attract water into the
gasoline/ethanol
blended fuel product 14. The water in fuel product 14 may be present in a
dissolved
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state, an emulsified state, or a free water state. Eventually, the water may
also cause
phase separation of fuel product 14.
[0050] In addition to being present in storage tank 16 as part of
the
gasoline/ethanol blended fuel product 14, ethanol may find its way into other
locations of
fuel delivery system 10 in a vapor or liquid state, including dispenser sump
30 and
turbine sump 32. In the event of a fluid leak from dispenser 12, for example,
some of the
gasoline/ethanol blended fuel product 14 may drip from dispenser 12 into
dispenser sump
30 in a liquid state. Also, in the event of a vapor leak from storage tank 16,
vapor in the
ullage of storage tank 16 may escape from storage tank 16 and travel into
turbine sump
32. In certain situations, turbine sump 32 and/or components contained
therein (e.g.,
metal fittings, metal valves, metal plates) may be sufficiently cool in
temperature to
condense the ethanol vapor back into a liquid state in turbine sump 32. Along
with
ethanol, water from the surrounding soil, fuel product 14, or another source
may also find
its way into sumps 30, 32 in a vapor or liquid state, such as by dripping into
sumps 30, 32
in a liquid state or by evaporating and then condensing in sumps 30, 32.
Ethanol and/or
water leaks into sumps 30, 32 may occur through various connection points in
sumps 30,
32, for example. Ethanol and/or water may escape from ventilated sumps 30, 32
but may
become trapped in unventilated sumps 30, 32.
[0051] In the presence of certain bacteria and water, ethanol that
is present in fuel
delivery system 10 may be oxidized to produce acetate, according to Reaction I
below.
CH3CH20H + H20 4 CH3C00" + it 2 112.
(I)
[0052] The acetate may then be protonated to produce acetic acid,
according to
Reaction II below.
CH3C00- + Er- -> cH3coce
01)
[0053] The conversion of ethanol to acetic acid may also occur in
the presence of
oxygen according to Reaction III below.
2 CI-130-120H +02 2 CI-13COOH +2 H20
(III)
[0054] Acetic acid producing bacteria or AA13 may produce acetate
and acetic
acid by a metabolic fermentation process, which is used commercially to
produce
vinegar, for example. Acetic acid producing bacteria generally belong to the
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Acetobacteraceae family, which includes the genera Acetobacter, Gluconobacter,
and
Gluconacetobacter. . Acetic acid producing bacteria are very prevalent in
nature and may
be present in the soil around fuel delivery system 10, for example. Such
bacteria may
find their way into sumps 30, 32 to drive Reactions I-III above, such as when
soil or
debris falls into sumps 30, 32 or when rainwater seeps into sumps 30, 32.
[0055] The products of Reactions I-III above may reach equilibrium
in sumps 30,
32, with some of the acetate and acetic acid dissolving into liquid water that
is present in
sumps 30, 32, and some of the acetate and acetic acid volatilizing into a
vapor state. In
general, the amount acetate or acetic acid that is present in the vapor state
is proportional
to the amount of acetate or acetic acid that is present in the liquid state
(i.e, the more
acetate or acetic acid that is present in the vapor state, the more acetate or
acetic acid that
is present in the liquid state).
[0056] Even though acetic acid is classified as a weak acid, it may
be corrosive to
fuel delivery system 10, especially at high concentrations. For example, the
acetic acid
may react to deposit metal oxides (e.g., rust) or metal acetates on metallic
fittings of fuel
delivery system 10. Because Reactions are microbiologically-
influenced reactions,
these deposits in fuel delivery system 10 may be tubular or globular in shape.
[0057] To limit corrosion in fuel delivery system 10, a control
system 100 and a
corresponding monitoring method are provided herein. As shown in FIG. 3, the
illustrative control system 100 includes controller 102, one or more monitors
104 in
communication with controller 102, output 106 in communication with controller
102,
and remediation system 108 in communication with controller 102, each of which
is
described further below.
[0058] Controller 102 of control system 100 illustratively includes
a
microprocessor 110 (e.g., a central processing unit (CPU)) and an associated
memory
112 Controller 102 may be any type of computing device capable of accessing a
computer-readable medium having one or more sets of instructions (es.,
software code)
stored therein and executing the instructions to perform one or more of the
sequences,
methodologies, procedures, or functions described herein. In general,
controller 102 may
access and execute the instructions to collect, sort, and/or analyze data from
monitor 104,
determine an appropriate response, and communicate the response to output 106
and/or
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remediation system 108. Controller 102 is not limited to being a single
computing
device, but rather may be a collection of computing devices (e.g., a
collection of
computing devices accessible over a network) which together execute the
instructions.
The instructions and a suitable operating system for executing the
instructions may reside
within memory 112 of controller 102, for example. Memory 112 may also be
configured
to store real-time and historical data and measurements from monitors 104, as
well as
reference data. Memory 112 may store information in database arrangements,
such as
arrays and look-up tables.
[0059] Controller 102 of control system 100 may be part of a larger
controller
that controls the rest of fuel delivery system 10. In this embodiment,
controller 102 may
be capable of operating and communicating with other components of fuel
delivery
system 10, such as dispenser 12 (FIG. 1), pump 20 (FIG. 2), and leak detector
34 (FIG,
2), for example. An exemplary controller 102 is the TS-550 evo Fuel
Management
System available from Franklin Fueling Systems Inc. of Madison, Wisconsin,
[0060] Monitor 104 of control system 100 is configured to
automatically and
routinely collect data indicative of a corrosive environment in fuel delivery
system 10. In
operation, monitor 104 may draw in a liquid or vapor sample from fuel delivery
system
and directly test the sample or test a target material that has been exposed
to the
sample, for example. In certain embodiments, monitor 104 operates
continuously,
collecting samples and measuring data approximately once every second or
minute, for
example. Monitor 104 is also configured to communicate the collected data to
controller
102. In certain embodiments, monitor 104 manipulates the data before sending
the data
to controller 102. In other embodiments, monitor 104 sends the data to
controller 102 in
raw form for manipulation by controller 102. The illustrative monitor 104 is
wired to
controller 102, but it is also within the scope of the present disclosure that
monitor 104
may communicate wirelessly (e g., via an internet network) with controller
102.
[0061] Depending on the type of data being collected by each
monitor 104, the
location of each monitor 104 in fuel delivery system 10 may vary. Returning to
the
illustrated embodiment of FIG. 2, for example, monitor 104' is positioned in
the liquid
space (e.g, middle or bottom) of storage tank 16 to collect data regarding the
liquid fuel
product 14 in storage tank 16, monitor 104" is positioned in the ullage or
vapor space
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(i.e., top) of storage tank 16 to collect data regarding any vapors present in
storage tank
16, monitor 104th is positioned in the liquid space (i.e., bottom) of turbine
sump 32 to
collect data regarding any liquids present in turbine sump 32, and monitor
104" is
positioned in the vapor space (i.e., top) of turbine sump 32 to collect data
regarding any
vapors present in turbine sump 32. Monitor 104 may be positioned in other
suitable
locations of fuel delivery system 10, including delivery line 18 and dispenser
sump 30
(FIG. 1), for example. Various monitors 104 for use in control system 100 of
FIG. 3 are
discussed further below.
[0062] Output 106 of control system 100 may be capable of
communicating an
alarm or warning from controller 102 to an operator. Output 106 may include a
visual
indication device (e g., a gauge, a display screen, lights, a printer), an
audio indication
device (e.g., a speaker, an audible alarm), a tactile indication device, or
another suitable
device for communicating information to the operator, as well as combinations
thereof
Controller 102 may transmit information to output 106 in real-time, or
controller 102 may
store information in memory 112 for subsequent transmission or download to
output 106.
[0063] Remediation system 108 of control system 100 may be capable
of taking
at least one corrective action to remediate the corrosive environment in fuel
delivery
system 10. Various embodiments of remediation system 108 are described below,
[0064] The illustrative output 106 and remediation system 108 are
wired to
controller 102, but it is also within the scope of the present disclosure that
output 106
and/or remediation system 108 may communicate wirelessly (e.g., via an
Internet
network) with controller 102. For example, to facilitate communication between
output
106 and the operator, output 106 may be located in the operator's control room
or office.
[0065] In operation, and as discussed above, controller 102
collects, sorts, and/or
analyzes data from monitor 104, determines an appropriate response, and
communicates
the response to output 106 and/or remediation system 108. According to an
exemplary
embodiment of the present disclosure, output 106 warns the operator of a
corrosive
environment in fuel delivery system 10 and/or remediation system 108 takes
corrective
action before the occurrence of any corrosion or any significant corrosion in
fuel delivery
system 10. In this embodiment, corrosion may be prevented or minimized. It is
also
within the scope of the present disclosure that output 106 may alert the
operator to the
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occurrence of corrosion in fuel delivery system 10 and/or remediation system
108 may
take corrective action to at least avoid further corrosion.
[0066] Various factors may influence whether controller 102 issues
an alarm or
warning from output 106 that a corrosive environment is present in fuel
delivery system
or becoming more likely to develop. Similar factors may also influence whether
controller 102 instructs remediation system 108 to take corrective action in
response to
the corrosive environment. As discussed further below, these factors may be
evaluated
based on data obtained from one or more monitors 104.
[0067] One factor indicative of a corrosive environment includes
the
concentration of acidic molecules in fuel delivery system 10, with controller
102 issuing
an alarm or warning from output 106 and/or activating remediation system 108
when the
measured concentration of acidic molecules in fuel delivery system 10 exceeds
an
acceptable concentration of acidic molecules in fuel delivery system 10. The
concentration may be expressed in various units. For example, controller 102
may
activate output 106 and/or remediation system 108 when the measured
concentration of
acidic molecules in fuel delivery system 10 exceeds 25 ppm, 50 ppm, 100 ppm,
150 ppm,
200 ppm, or more, or when the measured concentration of acidic molecules in
fuel
delivery system 10 exceeds 25 mg/L, 50 mg/L, 100 mg/L, 150 mg/L, 200 mg/L, or
more.
At or beneath the acceptable concentration, corrosion in fuel delivery system
10 may be
limited. Controller 102 may also issue an alarm or warning from output 106
and/or
activate remediation system 108 when the concentration of acidic molecules
increases at
an undesirably high rate.
100681 Another factor indicative of a corrosive environment
includes the
concentration of hydrogen ions in fuel delivery system 10, with controller 102
issuing an
alarm or warning from output 106 and/or activating remediation system 108 when
the
measured concentration of hydrogen ions in fuel delivery system 10 exceeds an
acceptable concentration of hydrogen ions in fuel delivery system 10. For
example,
controller 102 may activate output 106 and/or remediation system 108 when the
hydrogen ion concentration causes The pH in fuel delivery system 10 to drop
below 5, 4,
3, or 2, for example. Within the acceptable pH range, corrosion in fuel
delivery system
10 may be limited. Controller 102 may also issue an alarm or warning from
output 106
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and/or activate remediation system 108 when the concentration of hydrogen ions
increases at an undesirably high rate.
[0069] Yet another factor indicative of a corrosive environment
includes the
concentration of bacteria in fuel delivery system 10, with controller 102
issuing an alarm
or warning from output 106 and/or activating remediation system 108 when the
measured
concentration of bacteria in fuel delivery system 10 exceeds an acceptable
concentration
of bacteria in fuel delivery system 10. At or beneath the acceptable
concentration, the
production of corrosive materials in fuel delivery system 10 may be limited.
Controller
102 may also issue an alarm or warning from output 106 and/or activate
remediation
system 108 when the concentration of bacteria increases at an undesirably high
rate.
[0070] Yet another factor indicative of a corrosive environment
includes the
concentration of water in fuel delivery system 10, with controller 102 issuing
an alarm or
warning from output 106 and/or activating remediation system 108 when the
measured
concentration of water in fuel delivery system 10 exceeds an acceptable
concentration of
water in fuel delivery system 10. At or beneath the acceptable concentration,
the
production of corrosive materials in fuel delivery system 10 may be limited.
Controller
102 may also issue an alarm or warning from output 106 and/or activate
remediation
system 108 when the concentration of water increases at an undesirably high
rate. The
water may be present in liquid and/or vapor form.
100711 Controller 102 may be programmed to progressively vary the
alarm or
warning communication from output 106 as the risk of corrosion in fuel
delivery system
increases. For example, controller 102 may automatically trigger: a minor
alarm (e.g.,
a blinking light) when monitor 104 detects a relatively low acid concentration
level (e.g.,
5 ppm) in fuel delivery system 10 or a relatively steady acid concentration
level over
time; a moderate alarm (e.g., an audible alarm) when monitor 104 detects a
moderate acid
concentration level (e g., 10 ppm) in fuel delivery system 10 or a moderate
increase in the
acid concentration level over time; and a severe alarm (e.g., a telephone call
or an e-mail
to the gas station operator) when monitor 104 detects a relatively high acid
concentration
level (e.g., 25 ppm) in fuel delivery system 10 or a relatively high increase
in the acid
concentration level over time.
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[0072] The alarm or warning communication from output 106 allows
the operator
to manually take precautionary or corrective measures to limit corrosion of
fuel delivery
system 10. For example, if an alarm or warning communication is signaled from
turbine
sump 32 (FIG. 2), the operator may remove manhole cover 39 and lid 38 to clean
turbine
sump 32, which may involve removing bacteria and potentially corrosive liquids
and
vapors from turbine sump 32. As another example, the operator may inspect fuel
delivery system 10 for a liquid leak or a vapor leak that allowed ethanol
and/or its acidic
reaction products to enter turbine sump 32 in the first place.
[0073] Even if no immediate action is required, the alarm or
warning
communication from output 106 may allow the operator to better plan for and
predict
when such action may become necessary. For example, the minor alarm from
output 106
may indicate that service should be performed within about 2 months, the
moderate alarm
from output 106 may indicate that service should be performed within about 1
month,
and the severe alarm from output 106 may indicate that service should be
performed
within about 1 week.
[0074] As discussed above, control system 100 includes one or more
monitors
104 that collect data indicative of a corrosive environment in fuel delivery
system 10.
Each monitor 104 may vary in the type of data that is collected, the type of
sample that is
evaluated for testing, and the location of the sample that is evaluated for
testing, as
exemplified below.
[0075] In one embodiment, monitor 104 collects electrical data
indicative of a
corrosive environment in fuel delivery system 10. An exemplary elecrical
monitor 104a
is shown in FIG. 4 and includes an energy source 120, a corrosive target
material 122 that
is exposed to a liquid or vapor sample S from fiiel delivery system 10, and a
sensor 124.
To enhance the longevity of monitor 104a, energy source 120 and/or sensor 124
may be
protected from any corrosive environment in fuel delivery system 10, unlike
target
material 122. Target material 122 may be designed to corrode before the
equipment of
fuel delivery system 10 corrodes. Target material 122 may be constructed of or
coated
with a material that is susceptible to acidic corrosion, such as copper or low
carbon steel.
Also, target material 122 may be relatively thin or small in size compared to
the
equipment of fuel delivery system 10 such that even a small amount of
corrosion will
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impact the structural integrity of target material 122. For example, target
material 122
may be in the form of a thin film or wire.
100761 In use, energy source 120 directs an electrical current
through target
material 122. When target material 122 is intact, sensor 124 senses the
electrical current
traveling through target material 122. However, when exposure to sample S
causes target
material 122 to corrode and potentially break, sensor 124 will sense a
decreased electrical
current, or no current, traveling through target material 122. It is also
within the scope of
the present disclosure that the corrosion and/or breakage of target material
122 may be
detected visually, such as by using a camera as sensor 124. First monitor 104a
may share
the data collected by sensor 124 with controller 102 (FIG. 3) to signal a
corrosive
environment in fuel delivery system 10 when the electrical current reaches an
undesirable
level or changes at an undesirable rate, for example. After use, the corroded
target
material 122 may be discarded and replaced.
100771 Another exemplary electrical monitor 104b is shown in FIG. 5
and
includes opposing, charged metal plates 130. The electrical monitor 104b
operates by
measuring electrical properties (e.g., capacitance, impedence) of a liquid or
vapor sample
S that has been withdrawn from fuel delivery system 10. In the case of a
capacitance
monitor 104b, for example, the sample S is directed between plates 130.
Knowing the
size of plates 130 and the distance between plates 130, the dielectric
constant of the
sample S may be calculated. As the quantity of acetate, acetic acid, and/or
water in the
sample S varies, the dielectric constant of the sample S may also vary. The
electrical
monitor 104b may share the collected data with controller 102 (FIG. 3) to
signal a
corrosive environment in fuel delivery system 10 when the dielectric constant
reaches an
undesirable level or changes at an undesirable rate, for example. One example
of
electrical monitor 104b is a water content monitor that may be used to monitor
the water
content of fuel product 14 or another sample S from fuel delivery system 10.
An
exemplary water content monitor is the ICM-W monitor available from MP Filtri,
which
uses a capacitive sensor to measure the relative humidity (RH) of the tested
fluid. As the
RH increases toward a saturation point, the water in the fluid may transition
from a
dissolved state, to an emulsified state, to a free water state. Other
exemplary water
content monitors are described in the above-incorporated U.S. Publication No.
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2012/0261437. Another example of electrical monitor 104b is a humidity sensor
that
may be used to monitor the humidity in the vapor space of storage tank 16
and/or turbine
sump 32.
[0078] In another embodiment, monitor 104 collects elecrochemical
data
indicative of a corrosive environment in fuel delivery system 10. An exemplary
electrochemical monitor (not shown) performs potentiometric titration of a
sample that
has been withdrawn from fuel delivery system 10. A suitable potentiometric
titration
device includes an electrochemical cell with an indicator electrode and a
reference
electrode that maintains a consistent electrical potential. As a titrant is
added to the
sample and the electrodes interact with the sample, the electric potential
across the
sample is measured. Potentiometric or chronopotentiometric sensors, which may
be
based on solid-state reversible oxide films, such as that of iridium, may be
used to
measure potential in the cell. As the concentration of acetate or acetic acid
in the sample
varies, the potential may also vary. The potentiometric titration device may
share the
collected data with controller 102 (FIG. 3) to signal a corrosive environment
in fuel
delivery system 10 when the potential reaches an undesirable level or changes
at an
undesirable rate, for example. An electrochemical monitor may also operate by
exposing
the sample to an electrode, performing a reduction-oxidation with the sample
at the
electrode, and measuring the resulting current, for example.
100791 In yet another embodiment, monitor 104 collects optical data
indicative of
a corrosive environment in fuel delivery system 10. An exemplary optical
monitor 104c
is shown in FIG. 6 and includes a light source 140 (e.g., LED, laser), an
optical target
material 142 that is exposed to a liquid or vapor sample S from fuel delivery
system 10,
and an optical detector 144 (e.g., photosensor, camera). To enhance the safety
of monitor
104c, light source 140 may be a low-energy and high-output device, such as a
green
LED. Target material 142 may be constructed of or coated with a material (e
g., an acid-
sensitive polymer) that changes optical properties (e.g., color, transmitted
light intensity)
in the presence of the sample S.
[0080] Optical monitor 104c may enable real-time, continuous
monitoring of fuel
delivery system 10 by installing light source 140, target material 142, and
detector 144
together in fuel delivery system 10. To enhance the longevity of this real-
time monitor
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104c, light source 140 and/or detector 144 may be protected from any corrosive
environment in fuel delivery system 10, unlike target material 142. For
example, light
source 140 and/or detector 144 may be contained in a sealed housing, whereas
target
material 142 may be exposed to the surrounding environment in fuel delivery
system 10.
[0081] Alternatively, optical monitor 104c may enable manual,
periodic
monitoring of fuel delivery system 10. During exposure, target material 142
may be
installed alone in fuel delivery system 10. During testing, target material
142 may be
periodically removed from fuel delivery system 10 and positioned between light
source
140 and detector 144. In a first embodiment of the manual monitor 104c, light
source
140 and detector 144 may be sold as a stand-alone, hand-held unit that is
configured to
receive the removed target material 142. In a second embodiment of the manual
monitor
104c, light source 140 may be sold along with a software application to
convert the
operator's own smartphone or mobile device into a suitable detecor 144.
Detector 144 of
monitor 104c may transmit information to controller 102 (FIG, 3) in real-time
or store
information in memory for subsequent transmission or download.
[0082] One suitable target material 142 includes a pH indicator
that changes color
when target material 142 is exposed to an acidic pH with 1-1+ protons, such as
a pH less
than about 5, 4, 3, or 2, for example. The optical properties of target
material 142 may be
configured to change before the equipment of fuel delivery system 10 corrodes.
Detector
144 may use optical fibers as the sensing element (i.e., intrinsic sensors) or
as a means of
relaying signals to a remote sensing element (i.e., extrinsic sensors).
[0083] In use, light source 140 directs a beam of light toward
target material 142.
Before target material 142 changes color, for example, detector 144 may detect
a certain
reflection, transmission (i.e., spectrophotometry), absorbtion (i.e.,
densitometry), and/or
refraction of the the light beam from target material 142. However, after
target material
142 changes color, detector 144 will detect a different reflection,
transmission,
absorttion, and/or refraction of the the light beam. It is also within the
scope of the
present disclosure that the changes in target material 142 may be detected
visually, such
as by using a camera (e.g., a smartphone camera) as detector 144. Third
monitor 104c
may share the data collected by detector 144 with controller 102 (FIG. 3) to
signal a
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corrosive environment in fuel delivery system 10 when the color reaches an
undesirable
level or changes at an undesirable rate, for example.
[0084] Another suitable target material 142 includes a sacrificial,
corrosive
material that corrodes (e.g., rusts) when exposed to a corrosive environment
in fuel
delivery system 10. For example, the corrosive target material 142 may include
copper
or low carbon steel. The corrosive target material 142 may have a high surface
area to
volume ratio to provide detector 144 with a large and reliable sample size.
For example,
as shown in FIG. 6, the corrosive target material 142 may be in the form of a
woven mesh
or perforated sheet having a large plurality of pores 143.
[0085] In use, light source 140 directs a beam of light along an
axis A toward the
corrosive target material 141 Before target material 142 corrodes, detector
144 may
detect a certain amount of light that passes from the light source 140 and
through the
open pores 143 of the illuminated target material 142 along the same axis A.
However,
as target material 142 corrodes, the material may visibly swell as rust
accumulates in and
around some or all of the pores 143. This accumulating rust may obstruct or
prevent light
from traveling through pores 143, so detector 144 (e.g., a photodiode) will
detect a
decreasing amount of light through the corroding target material 142_ It is
also within the
scope of the present disclosure that the changes in target material 142 may be
detected
visually, such as by using a camera or another suitable imaging device as
detector 144.
Detector 144 may capture an image of the illuminated target material 142 and
then
evaluate the image (e.g., pixels of the image) for transmitted light
intensity, specific light
patterns, etc. As discussed above, third monitor 104c may share the data
collected by
detector 144 with controller 102 (FIG. 3) to signal a corrosive environment in
fuel
delivery system 10 when the transmitted light intensity reaches an undesirable
level or
changes at an undesirable rate, for example. After use, the corroded target
material 142
may be discarded and replaced.
[0086] Another exemplary optical monitor 104e' is shown in FIGS. 16-
19.
Optical monitor 104c' of FIGS. 16-19 is similar to optical monitor 104c of
FIG. 6 and
includes several components and features in common with optical monitor 104c
as
indicated by the use of common reference numbers between optical monitors
104c,
104c', including a light source 140', a corrosive target material 142', and an
optical
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detector 144'. Optical monitor 104c' may be mounted in the vapor space of
storage tank
16 and/or turbine sump 32 of fuel delivery system 10 (FIG 2).
100871 The illustrative optical monitor 104c' is generally
cylindrical in shape and
has a longitudinal axis L. In the illustrated embodiment of FIG. 19, light
source 140' and
target material 142' are located on a first side of axis L (illustratively the
right side of
axis L), and optical detector 144' is located on a second side of axis L
(illustratively the
left side of axis L). Light source 140' and optical detector 144' are
substantially coplanar
and are located above target material 142'. The illustrative target material
142' is a L-
shaped mesh sheet, with a vertical portion 145a' of target material 142'
extending parallel
to axis L and a horizontal portion 145b' of target material 142' extending
perpendicular
to axis L.
100881 The illustrative optical monitor 104c' includes a reflective
surface 500'
positioned downstream of light source 140' and upstream of optical detector
144',
wherein the reflective surface 500' is configured to reflect incident light
from light source
140' toward optical detector 144'. In the illustrated embodiment of FIG. 19,
the incident
light from light source 140' travels downward and inward toward axis L along a
first axis
At toward reflective surface 500', and then the reflected light from
reflective surface 500'
travels upward and outward from axis L along a second axis A2 toward optical
detector
144'. Reflective surface 500' may produce a specular reflection with the
reflected light
traveling along a single axis Az, as shown in FIG. 19, or a diffuse reflection
with the
reflected light traveling in many different directions. Reflective surface
500' may be a
shiny, mirrored, or otherwise reflective surface. Reflective surface 500' may
be shaped
and oriented to direct the reflected light toward optical detector 144'. For
example, in
FIG. 19, the reflective surface 500' is flat and is angled about 10 degrees
relative to a
horizontal plane to direct the reflected light toward optical detector 144'.
The angled
reflective surface 500' of FIG. 19 may also encourage drainage of any
condensation (fuel
or aqueous) that forms upon reflective surface 500'.
100891 The illustrative optical monitor 104e also includes at least
one printed
circuit board (PCB) 502' that mechanically and electrically supports light
source 140'
and optical detector 144'. PCB 502' may also allow light source 140' and/or
optical
detector 144' to communicate with controller 102 (FIG. 3). Light source 140'
and optical
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detector 144' are illustratively coupled to the same PCB 502', but it is also
within the
scope of the present disclosure to use distinct PCBs.
[0090] The illustrative optical monitor 104c' further includes a
cover 510', an
upper housing 512', and a lower housing 514'. Lower housing 514' may be
removably
coupled to upper housing 512', such as using a snap connection 515', a
threaded
connection, or another removable connection.
[0091] Upper housing 512' contains light source 140', optical
detector 144', and
circuit board 502'. Upper housing 512' may be hermetically sealed to separate
and
protect its contents from the potentially corrosive environment in fuel
delivery system 10
(FIG. 2). However, upper housing 512' may be at least partially or entirely
transparent to
permit the passage of light, as discussed further below.
[0092] Lower housing 514' contains target material 142' and
reflective surface
500'. Reflective surface 500' may be formed directly upon lower housing 514'
(e.g., a
reflective coating) or may be formed on a separate component (e.g., a
reflective panel)
that is coupled to lower housing 514'. In the illustrated embodiment of FIG.
19,
reflective surface 500' is located on bottom wall 516' of lower housing 514'.
Unlike the
contents of upper housing 512', which are separated from the vapors in fuel
delivery
system 10, the contents of lower housing 514', particularly target material
142', are
exposed to the vapors in fuel delivery system 10. The illustrative lower
housing 514' has
bottom wall 516' with a plurality of bottom openings 517' and a side wall 518'
with a
plurality of side openings 519' to encourage the vapors in fuel delivery
system 10 to enter
lower housing 514' and interact with target material 142'. Openings 517', 519'
may vary
in shape, size, and location. In general, lower housing 514' should be
designed to be
sufficiently solid to support and protect its contents while being
sufficiently open to
expose its contents to the vapors in fuel delivery system 10. For example, the
bottom
openings 517' may be concentrated beneath target material 142'. Also, the side
openings
519' adjacent to target material 142' may be relatively small, whereas the
side openings
519' opposite from target material 142' may be relatively large.
[0093] In use, and as shown in FIG. 19, light source 140' directs a
beam of light
along the first axis Ai, through the transparent upper housing 512', and
toward target
material 142'. The L-shaped configuration of target material 142' may block
any direct
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light pathways between light source 140' and reflective surface 500' to ensure
that all of
the light from light source 140' encounters target material 142' before
reaching reflective
surface 500'. The light that is able to pass through the pores 143' of target
material 142'
continues to reflective surface 500', which then reflects the light along the
second axis
A2, back through the transparent upper housing 512', and to optical detector
144'.
Optical detector 144' may signal a corrosive environment in fuel delivery
system 10
when the transmitted light intensity through the corroding target material
142' reaches an
undesirable level or changes at an undesirable rate, for example. After use,
lower
housing 514' may be detached (e.g_, unsnapped) from upper housing 512' to
facilitate
removal and replacement of the corroded target material 142' and/or reflective
surface
500' without disturbing the contents of upper housing 512'.
100941 Optical monitor 104e may be configured to detect one or more
errors. If
the light intensity detected by detector 144' is too high (e.g., at or near
100%), optical
monitor 104c' may issue a "Target Material Error" to inform the operator that
target
material 142' may be missing or damaged. To avoid false alarms caused by
exposure to
ambient light, such as when opening turbine sump 32 (FIG. 2), optical monitor
104c'
may only issue the "Target Material Error" when the high light intensity is
detected for a
predetermined period of time (e.g, 1 hour or more). On the other hand, if the
light
intensity detected by detector 144' is too low (e.g., at or near 0%), optical
monitor 104c'
may issue a "Light or Reflector Error" to inform the operator that light
source 140'
and/or reflective surface 500' may be missing or damaged. In this scenario,
the entire
lower housing 514', including reflective surface 500', may be missing or
damaged.
100951 Optical monitor 104c' may be combined with one or more other
monitors
of the present disclosure. For example, in the illustrated embodiment of FIG.
16, PCB
502' of optical monitor 104c' also supports a humidity sensor 520', which
passes through
upper housing 512' for exposure to the vapors in fuel delivery system 10 (FIG.
2) PCB
502' may also support a temperature sensor (not shown), which may be used to
compensate for any temperature-related fluctuations in the performance of
light source
140' and/or optical detector 144'.
100961 In still yet another embodiment, monitor 104 collects
spectroscopic data
indicative of a corrosive environment in fuel delivery system 10 An exemplary
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spectrometer (not shown) operates by subjecting a liquid or vapor sample from
fuel
delivery system 10 to an energy source and measuring the radiative energy as a
function
of its wavelength and/or frequency. Suitable spectrometers include, for
example, infrared
(TR) electromagnetic spectrometers, ultraviolet (UV) electromagnetic
spectrometers, gas
chromatography¨mass spectrometers (GC-MS), and nuclear magnetic resonance
(NMR)
spectrometers Suitable spectrometers may detect absorption from a ground state
to an
excited state, and/or fluorescence from the excited state to the ground state.
The
spectroscopic data may be represented by a spectrum showing the radiative
energy as a
function of wavelength and/or frequency. It is within the scope of the present
disclosure
that the spectrum may be edited to hone in on certain impurites in the sample,
such as
acetate and acetic acid, which may cause corrosion in fuel delivery system 10,
as well as
sulfuric acid, which may cause odors in fuel delivery system 10. As the
impurities
develop in fuel delivery system 10, peaks corresponding to the impurities
would form
and/or grow on the spectrum. The spectrometer may share the collected data
with
controller 102 (FIG. 3) to signal a corrosive environment in fuel delivery
system 10 when
the impurity level reaches an undesirable level or changes at an undesirable
rate, for
example.
00971 In still yet another embodiment, monitor 104 collects
microbial data
indicative of a corrosive environment in fuel delivery system 10. An exemplary
microbial detector (not shown) operates by exposing a liquid or vapor sample
from fuel
delivery system 10 to a fluorogenic enzyme substrate, incubating the sample
and
allowing any bacteria in the sample to cleave the enzyme substrate, and
measuring
fluorescence produced by the cleaved enzyme substrate. The concentration of
the
fluorescent product may be directly related to the concentration of acetic
acid producing
bacteria (e.g., Acetobacter, Gluconobacter, Gluconacetobacter)in the sample.
Suitable
microbial detectors are commercially available from Mycometer, Inc. of Tampa,
Florida.
The microbial detector may share the collected data with controller 102 (FIG.
3) to signal
a corrosive environment in fuel delivery system 10 when the fluorescent
product
concentration reaches an undesirable level or changes at an undesirable rate,
for example.
100981 To minimize the impact of other variables in monitor 104, a
control
sample may be provided in combination with the test sample. For example,
monitor 104c
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of FIG. 6 may include a non-corrosive control material for comparison with the
corrosive
target material 142. This comparison would minimize the impact of other
variables in
monitor 104c, such as decreasing output from light source 140 over time.
[0099] As discussed above, control system 100 of FIG. 3 includes a
remediation
system 108 capable of taking at least one corrective action to remedi ate the
corrosive
environment in fuel delivery system 10. Controller 102 may activate
remediation system
108 periodically (e.g., hourly, daily) in a preventative manner. Alternatively
or
additionally, controller 102 may activate remediation system 108 when the
corrosive
environment is detected by monitor 104 Various embodiments of remediation
system
108 are described below with reference to FIG. 2.
[00100] In a first embodiment, remediation system 108 is configured
to ventilate
turbine sump 32 of fuel delivery system 10. In the illustrated embodiment of
FIG. 2,
remediation system 108 includes a first ventilation passageway 160 and a
second
ventilation or siphon passageway 170
[00101] The first ventilation passageway 160 illustratively includes
an inlet 162 in
communication with the surrounding atmosphere and an outlet 164 in
communication
with the upper vapor space (i.e., top) of turbine sump 32. hi FIG. 2, the
first ventilation
passageway 160 is positioned in lid 38 of turbine sump 32, but this position
may vary. A
control valve 166 (e.g., bulkhead-style vacuum breaker, check valve) may be
provided
along the first ventilation passageway 160. Control valve 166 may be biased
closed and
opened when a sufficient vacuum develops in turbine sump 32, which allows air
from the
surrounding atmosphere to enter turbine sump 32 through the first ventilation
passageway
160.
[00102] The second ventilation or siphon passageway 170 is
illustratively coupled
to a siphon port 26 of pump 20 and includes an inlet 172 positioned in the
lower vapor
space (i e., middle) of turbine sump 32 and an outlet 174 positioned in
storage tank 16. A
control valve 176 (e.g., automated valve, flow orifice, check valve, or
combination
thereof) may be provided in communication with controller 102 (FIG. 3) to
selectively
open and close the second ventilation passageway 170. Other features of the
second
ventilation passageway 170 not shown in FIG. 2 may include a restrictor, a
filter, and/or
one or more pressure sensors.
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[00103] When pump 20 is active (i.e.., turned on) to dispense fuel
product 14,
pump 20 generates a vacuum at siphon port 26. The vacuum from pump 20 draws
vapor
(e.g., fuel/air mixture) from turbine sump 32, directs the vapor to the
manifold of pump
20 where it mixes with the circulating liquid fuel flow, and then discharges
the vapor into
storage tank 16 through the second ventilation passageway 170. As the vacuum
in
turbine sump 32 increases, control valve 166 may also open to draw fresh air
from the
surrounding atmosphere and into turbine sump 32 through the first ventilation
passageway 160. When pump 20 is inactive (i.e., turned off), controller 102
(FIG. 3)
may close control valve 176 to prevent back-flow through the second
ventilation
passageway 170. Additional information regarding the second ventilation
passageway
170 is disclosed in U.S. Patent No. 7,051,579, the disclosure of which is
expressly
incorporated herein by reference in its entirety.
[00104] The vapor pressure in turbine sump 32 and/or storage tank 16
may be
monitored using the one or more pressure sensors (not shown) and controlled.
To
prevent over-pressurization of storage tank 16, for example, the vapor flow
into storage
tank 16 through the second ventilation passageway 170 may be controlled. More
specifically, the amount and flow rate of vapor pulled into storage tank 16
through the
second ventilation passageway 170 may be limited to be less than the amount
and flow
rate of fuel product 14 dispensed from storage tank 16. In one embodiment,
control valve
176 may be used to control the vapor flow through the second ventilation
passageway
170 by opening the second ventilation passageway 170 for limited durations and
closing
the second ventilation passageway 170 when the pressure sensor detects an
elevated
pressure in storage tank 16. In another embodiment, the restrictor (not shown)
may be
used to limit the vapor flow rate through the second ventilation passageway
170 to a level
that will avoid an elevated pressure in storage tank 16.
[00105] Other embodiments of the first ventilation passageway 160
are also
contemplated. In a first example, the first ventilation passageway 160 may be
located in
the interstitial space between a primary pipe and a secondary pipe (e.g., XP
Flexible
Piping available from Franklin Fueling Systems Inc. of Madison, Wisconsin)
using a
suitable valve (e.g., APTfl' brand test boot valve stems available from
Franklin Fueling
Systems Inc. of Madison, Wisconsin). In a second example, the first
ventilation
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passageway 160 may be a dedicated fresh air line into turbine sump 32. In a
third
example, the first ventilation passageway 160 may be incorporated into a
pressure/vacuum (PV) valve system. Traditional PV valve systems communicate
with
storage tank 16 and the surrounding atmosphere to help maintain proper
pressure
differentials therebetween. One such PV valve system is disclosed in U.S.
Patent No.
8,141,577, the disclosure of which is expressly incorporated herein by
reference in its
entirety. In one embodiment, the PV valve system may be modified to pull fresh
air
through turbine sump 32 on its way into storage tank 16 when the atmospheric
pressure
exceeds the ullage pressure by a predetermined pressure differential (i.e.,
when a
sufficient vacuum exists in storage tank 16). In another embodiment, the PV
valve
system may be modified to include a pair of tubes (e.g., coaxial tubes) in
communication
with the surrounding atmosphere, wherein one of the tubes communicates with
storage
tank 116 to serve as a traditional PV vent when the ullage pressure exceeds
the
atmospheric pressure by a predetermined pressure differential, and another of
the tubes
communicates with turbine sump 32 to introduce fresh air into turbine sump 32.
1001061 Other embodiments of the second ventilation passageway 170
are also
contemplated. In a first example, instead of venting the fuel/air mixture from
turbine
sump 32 into storage tank 16 as shown in FIG. 2, the mixture may be directed
through a
filter and then released into the atmosphere. In a second example, instead of
using siphon
port 26 as the vacuum source for the second ventilation passageway 170 as
shown in FIG.
2, the vacuum source may be an existing vacuum pump in fuel delivery system 10
(e.g.,
9000 Mini-Jet available from Franklin Fueling Systems Inc. of Madison,
Wisconsin), a
supplemental and stand-alone vacuum pump, or a vacuum created by displaced
fuel in
storage tank 16 and/or fuel delivery line 18. In one embodiment, and as
discussed above,
the second ventilation passageway 170 may be incorporated into the PV valve
system to
pull fresh air through turbine sump 32 and then into storage tank 16 when fuel
is
displaced from storage tank 16. In another embodiment, the second ventilation
passageway 170 may communicate with an in-line siphon port on fuel delivery
line 18 to
pull air from turbine sump 32 when fuel is displaced along fuel delivery line
18.
1001071 In a second embodiment, remediation system 108 is configured
to irradiate
bacteria in turbine sump 32 of fuel delivery system 10. In the illustrated
embodiment of
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FIG. 2, a first radiation source 180 is positioned on an outer wall of turbine
sump 32, and
a second radiation source 180' is positioned in the ullage of storage tank 16.
Exemplary
radiation sources 180, 180' include ultraviolet-C (UV-C) light sources. When
activated
by controller 102 (FIG 3), radiation sources 180, 180' may irradiate and
destroy any
bacteria in turbine sump 32 and/or storage tank 16, especially acetic acid
producing
bacteria (e.g., Acetobacter, Ginconobacter, Gluconacetobacter).
[00108] In a third embodiment, remediation system 108 is configured
to filter
water from fuel product 14. An exemplary water filtration system 200 is shown
in FIG.
11 and is located together with pump 20 in turbine sump 32 above storage tank
16 (FIG
1). The illustrative water filtration system 200 includes a fuel inlet
passageway 202
coupled to port 27 of pump 20, a water filter 204, a fuel return passageway
206 from the
upper end of water filter 204, and a water removal passageway 208 from the
lower end of
water filter 204. The port 27 of pump 20 may be located upstream of leak
detector 34
and its associated check valve (not shown) such that the water filtration
system 200
avoids interfering with leak detector 34.
1001091 Water filter 204 is configured to separate water, including
emulsified
water and free water, from fuel product 14. Water filter 204 may also be
configured to
separate other impurities from fuel product 14. Water filter 204 may operate
by
coalescing the water into relatively heavy droplets that separate from the
relatively light
fuel product 14 and settle at the lower end of water filter 204. Incoming fuel
pressure
drives fuel radially outwardly through the sidewall of filter element 207
(FIG. 15), which
is made from a porous filter substrate adapted to allow fuel to pass
therethrough while
preventing water passage therethrough. Any water that is separated from the
fuel is
driven downwardly through the bottom of filter element 207, which is made from
a
porous filter substrate that allows the passage of water therethrough. The
separated water
then falls by gravity to the bottom of the filter housing. Exemplary water
filters 204
including filter element 207 are available from DieselPure Inc. Such water
filters 204
may reduce the water content of fuel product 14 to 200 ppm or less, according
to the SAE
J1488 ver.2010 test method
[00110] The illustrative water filtration system 200 also includes
one or more inlet
valves 203 to selectively open and close the fuel inlet passageway 202 and one
or more
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drain valves 209 to selectively open and close the water removal passageway
208. In
certain embodiments, valves 203, 209 are solenoid valves that are controlled
through
controller 102. In other embodiments, valves 203, 209 are manual valves that
are
manually controlled by a user In the embodiment of FIGS. 14-15, inlet solenoid
valve
203 is provided downstream of strainer 205, which includes a mesh screen to
protect
valve 203 from exposure to solid sediment. A further manual ball valve 203' is
provided
downstream of solenoid valve 203 for manual on/off control of the illustrated
filtration
system 200', the details of which are further discussed below.
1001111 In operation, water filtration system 200 circulates fuel
product 14 through
water filter 204. Water filtration system 200 may operate at a rate of
approximately 15 to
20 gallons per minute (GPM), for example When pump 20 operates with inlet
valve 203
open, pump 20 directs some or all of fuel product 14 from storage tank 16,
through port
27 of pump 20, through the open fuel inlet passageway 202, and through water
filter 204
If a customer is operating dispenser 12 (FIG. 1) during operation of water
filtration
system 200, pump 20 may direct a portion of the fuel product 14 to dispenser
12 via the
delivery line 18 (FIG. 1) and another portion of the fuel product 14 to water
filter 204 via
the fuel inlet passageway 202. It is also within the scope of the present
disclosure that the
operation of water filtration system 200 may be interrupted during operation
of dispenser
12 by temporarily closing inlet valve(s) 203 and/or 203' to water filter 204.
As shown
schematically in FIG. 14, water filter 204 may produce a clean or filtered
fuel product 14
near the upper end of water filter 204 and a separated water product, which
may be a
water/oil mixture, near the lower end of water filter 204. Alternatively,
water filter 204A
shown in FIGS. 21 and 22 may utilize water/oil separation to product a clean
or filtered
fuel product 14, as described further below. For purposes of the present
disclosure,
"water filter 204" can interchangeably refer to water filter 204 shown in
FIGS. 14 and 15
and described in detail herein, or to water filter 204A shown in FIGS. 21 and
22 and
described in detail herein. As used herein, "oil" may refer to oil and oil-
based products
including motor fuel, such as gasoline and diesel.
[00112] The clean or filtered fuel product 14 that is discharged by
water filter 204,
such as rising to the upper end of water filter 204, may be returned
continuously to
storage tank 16 via the fuel return passageway 206 The filtered fuel product
14 may be
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returned to storage tank 16 in a dispersed and/or forceful manner that
promotes
circulation in storage tank 16, which prevents debris from settling in storage
tank 16 and
promotes filtration of such debris. By returning the filtered fuel product 14
to storage
tank 16, water filtration system 200 may reduce the presence of water and
avoid
formation of a corrosive environment in fuel delivery system 10 (FIG. 1),
including
storage tank 16 and/or sump 32 of fuel delivery system 10. Water filtration
system 200
may be distinguished from an in-line system that delivers a filtered fuel
product to
dispenser 12 (FIG. 1) solely to protect a consumer's vehicle.
100113] The separated water product that is discharged by water
filter 204, such as
by settling at the lower end of water filter 204, may be drained via the water
removal
passageway 208 when drain valve 209 is open. The separated water product may
be
directed out of turbine sump 32 and above grade for continuous removal, as
shown in
FIG. 11. Alternatively, the separated water product may be directed via
passageway 208
to a storage tank 210 inside turbine sump 32 for batch removal when necessary,
as shown
in FIGS. 12, 14 and 22. If the separated water product is a water/oil mixture,
the
separated water product may be subjected to further processing to remove any
oil from
the remaining water. For example, a selective absorbent, such as the Smart
Sponge
available from AbTech Industries Inc., may be used to absorb and remove any
oil from
the remaining water.
[00114] Referring to FIG. 14, storage tank 210 further includes a
vent line 236
operable to vent the headspace above the separated water product as the level
within tank
210 increases. In an exemplary embodiment, vent line 236 may be routed to the
headspace above fuel product 14 within underground storage tank 16, such that
any
treatment or capture of the vapor within tank 210 may be routed through
existing
infrastructure used for treatment/capture of fuel vapor within tank 16.
Alternatively, tank
210 may be vented to a dedicated space as required or desired for a particular
application.
[00115] The illustrative water filtration systems 200, 200' of FIGS.
11, 12, 14 and
15 include a high-level water sensor 220 and a low-level water sensor 222
operably
connected to water filter 204. The water sensors 220 and 222 may be
capacitance sensors
capable of distinguishing fuel product 14 from water. The high-level water
sensor 220
may be located beneath the entry into fuel return passageway 206 to prevent
water from
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entering fuel return passageway 206. The illustrative water filtration system
200 of FIG.
12 further includes a high-level water sensor 224 in storage tank 210. The
high-level
water sensor 224 may be an optical sensor capable of distinguishing the
separated water
product from air. Sensors 220, 222, and 224 may be low-power devices suitable
for
operation in turbine sump 32. In one exemplary embodiment, filter 204 may have
a
water capacity of about 2.75 liters (0.726 gallons) between the levels of
sensors 220, 222.
[00116] Turning to FIG. 14, water filtration system 200' is shown.
Water filtration
system 200' is similar to filtration system 200 described above and includes
several
components and features in common with system 200 as indicated by the use of
common
reference numbers between systems 200, 200'. However, water filtration system
200'
further includes eductor 230 in fuel inlet passageway 202 which operates to
effect
continuous fuel filtration during operation of pump 20, while also allowing
for normal
operation of fuel dispenser 12 served by pump 20 as further described below_
[00117] As fuel is withdrawn from tank 16 by operation of pump 20, a
portion of
the fuel which would otherwise be delivered to dispenser 12 via delivery line
18 is
instead diverted to fuel inlet passageway 202. In an exemplary embodiment,
this diverted
flow may be less than 15 gallons/minute, such as between 10 and 12
gallons/minute.
This diverted flow of pressurized fuel passes through eductor 230, as shown in
FIGS. 14
and 15, which is a venturi device having a constriction in the cross-sectional
area of the
eductor flow path. As the flow of fuel passes through this construction, a
negative
pressure (i.e., a vacuum) is formed at vacuum port 232 (FIG. 15), which may be
separate
flow tube terminating in an aperture formed in the sidewall of eductor 230
downstream of
the constriction.
[00118] Filtration uptake line 234 is connected to vacuum port 232
and extends
downwardly into tank 16, such that filtration uptake line 234 draws fuel from
the bottom
of tank 16. In an exemplary embodiment, gap G2 between the inlet of line 234
and the
bottom surface of tank 16 is zero or near-zero, such that all or substantially
all water or
sediment which may be settled at the bottom of tank 16 is accessible to
filtration uptake
line 234. For example, line 234 may be a rigid or semi-rigid tube with an
inlet haying an
angled surface formed, e.g., by a cut surface forming a 45-degree angle with
the
longitudinal axis of the tube. This angled surface forms a point at the inlet
of line 234
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which can be lowered into abutting contact with the lower surface of tank 16,
while the
open passageway exposed by the angled surface allows the free flow of fuel
into line 234.
Other inlet configuration may also be used for line 234, including traditional
inlet
openings close to, but not abutting, the lower surface of the tank.
[00119] By contrast to the zero or near-zero gap G2 for filtration
uptake line 234, a
larger gap Gi is formed between the intake of fuel uptake line 19 and the
bottom surface
of tank 16. For example, the intake opening to submersible pump 24 (FIG. 1)
may be
about 4-6 inches above the lower surface of tank 16. Where the pump is located
above
fuel product 14, the intake opening into fuel uptake line may instead be about
4-6 inches
above the lower surface of tank 16. This elevation differential reflected by
gaps Gi and
G2 ensures that any water or contaminated fuel settled at the bottom of tank
16 will be
taken up by filtration uptake line 234 rather than fuel uptake line 19. At the
same time,
the relatively high elevation of the intake opening serving delivery line 18
ensures that
any accumulation of contaminated fuel will be safely within gap Gi, such that
only clean
fuel will be delivered to dispenser 12. In this way, filtration system 200'
simultaneously
remediates contamination and protects against uptake of any contaminated fuel
that may
exist in tank 16, thereby providing "double protection" against delivery of
contaminated
fuel to dispenser 12
[00120] The illustrative filtration system 200' also achieves this
dual
mitigation/prevention functionality with low-maintenance operation, by using
eductor
230 to convert the operation of pump 20 into the motive force for the
operation of system
200'. In particular, a single only pump 20 used in conjunction with system
200' both
provides clean fuel to dispenser(s) 12 via delivery line 18, while also
ensuring that any
accumulation of contaminated fiiel at the bottom of tank 16 is remediated by
uptake into
filtration line 234 and subsequent delivery to filter 204 The lack of a
requirement of
extra pumping capacity lowers both initial cost and running costs. Moreover,
the
additional components of system 200', such as eductor 230, filter 204, valves
203, 209
and water tank 210, all require little to no regular maintenance.
[00121] Filtration system 200' also achieves its dual
mitigation/prevention
function in an economically efficient manner by using an existing pump to
power the
filtration process, while avoiding the need for large-capacity filters. As
described in
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detail above, filtration system 200' is configured to operate in conjunction
with the
normal use of fuel delivery system 10 (FIG. 0, such that the filtration occurs
whenever
dispensers 12 are used to fuel vehicles. This ensures that filtration system
200' will
operate with a frequency commensurate with the frequency of use of fuel
delivery system
10. This high frequency of operation allows filter 204 to be specified with a
relatively
small filtration capacity for a given system size, while ensuring that
filtration system 200'
retains sufficient overall capacity to mitigate even substantial
contamination. For
example, a throughput of 10-12 gallons/minute through filter 204 may be
sufficient to
treat all the fuel contained in a tank 16 sized to serve 6-8 fitel dispensers
12 (FIG 1) with
each dispenser 12 capable of delivering 15-20 gallons of clean fuel per
minute. In this
system sizing example, eductor 230 may be sized to deliver 0.1-03 gallons per
minute of
fluid via filtration uptake line 234 with a maximum vertical lift of 15 feet,
using a flow
through fuel inlet passageway 202 of 10-12 gallons per minute at an inlet
pressure of
about 30 PSIG (resulting in a pressure of at least 5 PSIG at the outlet of
eductor 230).
1001221 An alternative water filtration system 200A is shown in
FIGS. 21 and 22.
Water filtration system 200A is similar to filtration system 200' described
above and
includes several components and features in common with systems 200 and 200',
as
indicated by the use of common reference numbers between systems 200, 200' and
200A.
Moreover, common reference numbers are used for common components of systems
200'
and 200A, and structures of filtration system 200A have reference numbers
which
correspond to similar or identical structures of filtration system 200',
except with "A"
appended thereto as further described below. Filtration systems 200' and 200A
may be
used interchangeably in connection with fuel delivery system 10 and its
associated
systems.
1001231 However, filtration system 200A includes filter 204A
utilizing an oil/water
separation tank 205A to accomplish the primary removal of water from fuel
product 14,
rather than a filter element 207 as described above with respect to filtration
system 200'.
In addition, the routing of fuel flows and the use of eductor 230A in
generating the
motive force for fuel filtration contrasts with system 200', as described in
further detail
below.
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1001241 Similar to system 200', filtration system 200A uses a
diverted flow of fuel
from submersible turbine pump 20 as the primary driver of fluid flows through
eductor
230, such that pump 20 provides the primary motive force for filtration. In
the illustrated
embodiment of FIG. 22, eductor 230A receives the motive fuel flow from the
outlet of
pump 20, e.g., along a discharge fluid passageway. However, it is contemplated
that
eductor 230 can receive a diverted flow on the suction side of pump 20,
including from
fuel uptake line 19, for example. The diverted fuel flow passes through port
27 of pump
20, as shown in FIG. 21, and through inlet passageway 202, strainer 205 and
inlet valve
203 in a similar fashion to system 200'. However, unlike system 200',
filtration system
200A positions eductor 230 downstream of both valve 203, and the outlet fuel
flow from
eductor 230A is delivered directly to fuel return passageway 206 and then to
storage tank
16. This is in contrast to the flow of fluid discharged from eductor 230
described above,
which directs both the motive fuel flow from inlet passageway 202, and the
filtration
flow from uptake line 234, to filter 204 (FIG. 15),
1001251 As best seen in FIG. 22, filter 204A is functionally
interposed between
eductor 230A and fuel filtration uptake line 234A. As the motive fuel flow
passes
through eductor 230A from inlet passageway 202 to return passageway 206A, the
vacuum created by eductor 230A is transmitted to the interior of filter 204A
via filter
return passageway 216A which extends from the vacuum port of eductor 230A to
an
aperture in the upper portion (e.g., the top wall) of filter 204A. This
connection creates a
vacuum pressure within filter 204A, which draws a flow of fluid (e.g., fuel or
a fuel/water
mixture) from the bottom of tank 16 via filtration uptake line 234A. This
filtration flow
enters filter 204A at its top portion, but is delivered to the bottom portion
of filter 204A
via dip tube 214A (FIG. 22).
1001261 In operation, filter 204A will operate in a steady state in
which tank 205A
is always filled with fluid drawn from tank 16. New fluid received from uptake
line
234A is deposited at the bottom of filter 204A via dip tube 214A, and an equal
flow of
fluid is discharged from the top of filter 204A via return passageway 216. In
an
exemplary embodiment, the flow rate through filter 204A is slow enough,
relative to the
internal volume of filter 204A, to allow for natural separation and
stratification of water
and fuel within the volume of filter 204A, such that any water contained in
the incoming
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fuel remains at the bottom of filter 204A and only clean fuel is present at
the top of filter
204A.
[00127] In an exemplary embodiment, the flow rate through filter
204A is
controlled with a combination of vacuum pressure from eductor 230A and the
cross-
sectional size of the channel defined by dip tube 214A. These two variables
may be
controlled to produce a nominal flow rate (i.e., throughput) through filter
204A, as well
as a fluid velocity through dip tube 214A. In particular, the vacuum level
produced by
eductor 230A is positively correlated with both flow rate and fluid velocity,
while the
cross-section of dip tube 214A is positively correlated with flow rate but
negatively
correlated with fluid velocity. To preserve the ability for natural fluid
stratification and
avoid turbulence at the bottom of filter 204A, flow rate should be kept low
enough to
allow incoming fuel to remain coagulated as a volume of fuel separate from any
surrounding water, rather than separating out into smaller droplets that would
need to re-
coagulate before "floating" out of the water layer. For example, an exemplary
fluid
velocity which produces such favorable fluid mechanics for filter 204A may be
as high as
1,0, 2.0, 3,0 or 4.0 ft/second, such as about 3.3 ft/second,
1001281 In one exemplary arrangement, oil/water separation tank 205A
has a
nominal volume of 1.1 gallons, dip tube 214A defines a fluid flow cannula with
an
internal diameter of 0.25 inches, and vacuum level generated by eductor 230A
is
maintained between 12-15 inHg. This configuration produces a flow rate of
about 0.50
gallons per minute (gpm) and an incoming fluid velocity (at the exit of dip
tube 214A
into the lower portion of filter 204A) of about 3.27 ft/sec. In this
arrangement,
throughput of filter 204A is maximized while preventing unfavorable fluid flow
characteristics as described above. Moreover, if vacuum is increased to 18
inHg, aeration
of the incoming fuel can create unfavorable effects, such as foaming of diesel
fuel.
[00129] Additional elements may be provided create operator control
(or control
via controller 102, shown in FIG. 3) over one or more constituent elements of
the fluid
velocity. For example, an adjustable or restricting flow orifice, such a ball
valve or flow
orifice plate, may be provided in the motive flow to eductor 230A. In an
exemplary
embodiment, this restriction may be placed downstream of eductor 230A in fuel
return
passageway 206A for example. This adjustable flow orifice may constrict the
flow
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through passageway 206A, which establishes a back pressure on eductor 230A and
thereby limits or defines the nominal vacuum pressure generated by eductor
230A.
Another control element may be a similar adjustable or restricting flow
orifice placed in
filtration uptake line 234A, which limits the uptake flow rate to ensure the
nominal flow
volume and speed is achieved. In the above-described example of 0.50 gpm, a
flow
orifice diameter of 0.0938 inches in uptake line 234A has been found to
produce the
target flow rate of 0_50 gpm and the target flow speed of about 3.3 ft/sec
when the
vacuum pressure on eductor 230A is set to a target range of 12-15 inHg.
[00130] The size of filter 204A may be scaled up or down to
accommodate any
desired filtration capacity, and the particular configuration of filtration
system 200A can
be modified in keeping with the principles articulated above. For example,
increasing the
cross-section of dip tube 214A decreases fluid velocity, such that the nominal
flow rate
through filtration uptake line 234A may be increased without producing an
unfavorable
fluid velocity. Similarly, the nominal volume of tank 205A may be decreased if
no
turbulence is experienced in the stratification of the contained fluids, or
may be increased
in order to accommodate a modest level of turbulence.
1001311 If water is present in the fluid drawn from the bottom of
storage tank 16
through uptake line 234A (FIG. 21), the water will naturally separate from the
fuel and
settle to the bottom of filter 204A, where the water is collected and retained
for later
withdrawal (described below). The clean fuel 14, which floats to the top of
the stratified
fluids within filter 204A, will be drawn back through eductor 230 via filter
return
passageway 216A and allowed to mix with the motive flow of fuel to be
discharged to
tank 16 via fuel return passageway 206A. In this way, filter return passageway
216A
combines with fuel return passageway 206A to form the fuel return passageway
which
returns filtered fuel product from filter 204A to the storage tank.
[00132] If sufficient water accumulates within filter 204A, the
water reaches high-
level water sensor 220A (FIG 22) exposed to the interior of tank 205A and
positioned
above the lower portion of filter 204A. In the illustrated embodiment, high-
level water
sensor 22A is located on the upper portion of the filter 204A, at a height
that results in a
majority of the fluid in the filter 204A being below sensor 220A. In some
embodiments,
60%, 70%, 80% or 90% of the internal volume of filter 204A may be below sensor
220A.
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This arrangement allows a significant amount of water to accumulate to avoid
frequent
draining procedures, while also using the remaining filter volume as a secure
buffer of
clean fuel above the water level to prevent accidental discharge of water or
contaminated
fuel from filter 204A to storage tank 16.
[00133] When contacted with water, sensor 220A activates and sends a
signal to
controller 102 (FIG. 3), which may then activate an alarm or initial a
remediation
protocol, or take other corrective action as described herein. For example,
activation of
water sensor 220A may issue a notification to prompt an operator to drain the
water
accumulated in tank 205A, or may initiate a similarly automated water removal
process.
[00134] FIG. 22 illustrates water removal passageway 208A, which is
functionally
interposed between filtration uptake line 234A and dip tube 214A. To initiate
a water
removal procedure either by a human operator or by operation of controller 102
(FIG. 3),
uptake valve 212A may first be closed to prevent any further uptake of fuel 14
from tank
16. Water outlet valve 209A may then be opened, and a pump (not shown)
attached to
water removal passageway 208A may be activated to draw water from the bottom
of
filter 204A via dip tube 214A. Where the water withdrawal is done by a human
operator,
a hand pump or manually operable electric pump may be used. Alternatively, an
automated electric pump may be used by the operator, or controlled by
controller 102
(FIG. 3) to automatically drain the water as part of a corrective action
protocol.
[00135] In an exemplary embodiment, check valve 218A may be provided
in
uptake line 234 between tank 16 and uptake valve 212A, in order to provide
additional
insurance against a backflow of water into tank 16 during water withdrawal
Check valve
218A also guards against any potential siphoning of water from filter 204A,
which may
be located physically above tank 16, into tank 16 via dip tube 214A and
filtration uptake
line 234A.
[00136] The water withdrawal process may be calibrated, either by a
human
operator or controller 102 (FIG. 3), to withdraw a predetermined quantity of
fluid upon
initiation of a water removal protocol. The predetermined amount may be the
volume of
fluid calculated to exist below water sensor 220A and within water filter
204A, for
example. Optionally, inlet valve 203 may be closed during the water removal
process, in
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order to prevent a competing suction pressure from eductor 230. Alternatively,
turbine
pump 20 (FIG. 21) may be shut down and inlet valve 203 may be left open.
1001371 Turning now to FIG. 23, filtration system 2008 includes
another
separator-type filter 204B and is otherwise similarly constructed to
filtration system
200A described above. Common reference numbers are used for common components
of
systems 200', 200A and 200B, and structures of filtration system 20013 have
reference
numbers which correspond to similar or identical structures of filtration
systems 200' and
200A, except with "B" appended thereto as further described below. Filtration
system
20013 has all the same functions and features as filtration system 200A
described above,
except as noted below. Filtration systems 200', 200A and 20013 may be used
interchangeably in connection with fuel delivery system 10 and its associated
systems.
1001381 However, filter 204B of filtration system 2008 includes
sensor valve
assembly 244, shown in FIGS. 24B-27, which can be used in lieu of (or in
addition to)
high-level water sensor 220A (FIG. 22) to sense the presence of water near the
top of
tank 20513 and, in conjunction with sensor 242 (FIG. 24B), issue a signal or
alert
indicative of this high-water condition.
1001391 As best seen in Fig_ 23, the components of filtration system
200B are
sized and configured to fit within sump 32, together with a typical set of
existing
components including turbine pump 22, delivery lines 18 and associated shutoff
valves
and ancillary structures. In the illustrative embodiment of FIGS. 24A and 24B,
mounting
bracket 240 is provided to provide structural support for tank 205B and
associated
structures from the flow lines between inlet passageway 202B and return
passageway
2068.
1001401 Like filtration systems 200, 200' and 200A described above,
filtration
system 200B may also be applied to other sumps or parts of fuel delivery
system 10, such
as dispenser sump 30 (FIG. 1). Also similar to systems 200' and 200A, system
200B
uses a diverted flow of fuel from submersible turbine pump 20 as the primary
driver of
fluid flows through eductor 230, via inlet passageway 202B and strainer 205
(FIG 24A),
such that pump 20 provides the primary motive force for filtration.
1001411 Fuel flows downstream to fuel return passageway 2068 to
return to the
underground storage tank 16 (FIG. 24A), passing eductor 230 to create vacuum
pressure
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in filter return passageway 216B, which in turn transmits the vacuum pressure
to the
interior of tank 205B via valve assembly 244 (as further described below).
This vacuum
pressure also within tank 205B is sufficient to draw fuel from UST 16 via
filtration
uptake line 2348, which extends to the bottom of UST 16 as seen in FIG. 24A
and also
described in detail herein with respect to other filtration system
configurations. The fuel
drawn through uptake line 234B provides a slow and steady flow into the bottom
of tank
2058 via dip tube 214B, also described in greater detail with respect to
filtration system
200A. During steady-state operation, the vacuum in return passageway 2168
draws fuel
back to the primary return flow through fuel return passageway 20613. In the
illustrated
embodiment of FIGS. 24A and 2411, strainer 205 is provided between valve
assembly
244 and eductor 230.
1001421 Turning now to FIG, 25, filter 2048 is shown partially
filled with water W
and, during steady-state operation, the remainder of tank 2058 is filled with
fuel floating
above water W. In this configuration, float 248 resides at the bottom of the
interior
cavity 252 of sensor valve body 246 of sensor assembly 244, retained by snap
ring 250.
Fuel deposited into tank 20513 via dip tube 214B rises to float on the heavier
water W,
while any water contained in the deposited fuel stratifies to remain in water
W. Because
water W is well below float 248, pure fuel is continuously cycled through
sensor valve
assembly via ports 249 in valve body 246, This pure fuel is then drawn into
vacuum port
254 to be returned to UST 16 via return passageway 216B (FIG. 24B).
1001431 During the steady-state, low-water operation depicted by
FIG. 25, a
vacuum is maintained throughout the components of water filtration system
20013 as
described herein. This vacuum maintains a steady flow of fuel through filter
return
passageway 21613 via eductor 230, as shown in FIG. 24B. This flow is measured
by flow
sensor 242, which is in fluid communication with the suction port of eductor
230 and/or
the interior flow path defined by passageway 216B. Sensor 242 detects the
presence
(and, optionally, the rate) of fluid flow through the suction port of eductor
230, and issues
a signal (or a lack of a signal) indicative of such fluid flow. This signal
may be received
by controller 102, for example, or may simply be received by an operator via
an indicator
(light, siren, etc.).
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[00144] In FIG. 26, the level of water W has risen such that a
portion of sensor
valve assembly 244 is submerged below the level of water W. Float 248 has a
density
below that of water W, but above that of the hydrocarbon fuel stratified above
water W as
described above. Details of an exemplary float 248 can be found in U.S. Patent
No.
8,878,682, entitled METHOD AND APPARATUS FOR DETECTION OF PHASE
SEPARATION IN STORAGE TANKS USING A FLOAT SENSOR and filed October
16, 2009, the entire disclosure of which is hereby expressly incorporated
herein by
reference. As the level of water W rises to engage float 248, float 248 rises
within
interior cavity 252, eventually approaching the top wall of cavity 252 and
port 254
When float 248 get near enough to port 254, the concentration of vacuum
pressure at port
254 draws float 248 into contact with the top wall of cavity 252 as
illustrated in FIG. 26,
shutting off (or substantially reducing) the flow of fluid. Because port 254
becomes
blocked as a result of a high water level, shutting off the flow of fluid from
filter 204B
prevents any of water W from reentering UST 16,
[00145] The ceasing of fluid flow through passageway 216B also stops
fluid flow
at the vacuum port of eductor 230. In addition, the flow of fluid may reduce
before
ceasing completely. Sensor 242 detects the reduction and/or cessation of fluid
flow, and
issues a signal (or a lack of a signal) indicative of cessation of flow or of
a reduction of
flow below a predetermined threshold nominal value. Controller 102 may issue
an alert
and/or initiate remediation when sensor 242 indicates the high level of water
W shown in
FIG. 26. As described in detail above with respect to filtration system 200A,
remediation
may include draining of water W. To facilitate such draining, water filtration
system
200B may be equipped with the same water removal passageway 208 and associated
structures found in filtration system 200A, as shown in FIG. 22 and described
in detail
above. When water W is removed from tank 205B, float 248 falls away from port
254
toward its bottom-seated position shown in FIG. 25, once again allowing fluid
to flow
through the vacuum port of eductor 230.
[00146] As noted above, water filter 204B may be located within a
sump (e.g.,
sump 32 shown in FIG. 23) and therefore near or above grade. Because water W
may be
allowed to accumulate within tank 205B, below-freezing weather has the
potential to
create ice within tank 205B. To address this potential in cold-weather
installations, a
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temperature probe may be installed within or on the outside wall of tank 205B
and
configured to issue a signal to controller 102 or a system operator When the
temperature
probe indicates temperatures near, at, or below freezing, the operator or
controller 102
may initiate a flow of fuel from UST 16 through filter 204B, as described
herein.
Because the UST 16 is located underground and well below grade, the incoming
fuel is
reliably above freezing and can be used to maintain the internal temperature
of tank 205B
above freezing. This incoming flow may be maintained until the temperature
probe
reaches a threshold above-freezing temperature, regardless of whether
controller 102 is
calling for fuel flow for filtration purposes. Although this temperature-
control system
and method are described with respect to filtration system 20011, the same
system may
also be applied in the same way to other filtration systems made in accordance
with the
present disclosure, including systems 200, 200' and 200A,
[00147] Controller 102 (FIG. 3), or a human operator, may also use
inlet valve 203
to selectively activate or deactivate the fuel filtration process enabled by
filtration
systems 200A or 200B (or, alternatively, systems 200 or 200', it being
understood that
systems 200, 200', 200A and 200B may be used interchangeably as noted herein),
For
example, controller 102 may be programmed with a pre-determined schedule for
fuel
filtration, and may open valve 203 to initiate a filtration cycle After a
predetermined
amount of time during which the filtration cycle is active and filtration is
occurring as
described above, controller 102 may close valve 203 to stop the filtration
cycle. After a
predetermined amount of time during which the filtration cycle is not active,
a new cycle
may begin. Alternatively, in some embodiments, valve 203 may be omitted or
left open,
such that fuel filtration occurs any time pump 20 is active
[00148] The use of the separator-type filters 204A, 204B allow
filtration systems
200A, 200B to be virtually maintenance free, with the only regular maintenance
task
being the periodic removal of accumulated water from filter 204A, 20413. Even
this
maintenance task may be automated as noted above In contrast to filtration
system 200',
which uses a substrate-type filter 207 as described in detail above,
filtration systems
200A, 200B have no substrate filters which would require replacement or
service.
1001491 The separator-type filters 204A, 204B may also be sized to
fit existing or
newly-installed sumps, such as turbine sump 32 of fuel delivery system 10
(FIG. 1). As
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noted above, a system designer has flexibility in sizing the volume of filters
204A, 204B
by controlling the flow rate of fluid to be filtered. Therefore, where there
is a
requirement for a filtration system to accommodate a small space within a
sump, filters
204A, 204B can be sized accordingly and the nominal filtration flow rate per
can be set
at an appropriate percentage of the filter volume as described in detail
above.
[00150] However, it is contemplated that a filter substrate, such as
filter 207, or
any other coalescing filter element, particulate filter element, or a
combination thereof
may be used inside filters 204A, 204B, as required or desired for a particular
application.
[00151] As discussed herein, filtration systems 200, 200', 200A and
20013 utilize
submersible pump 20, already existing as a component of fuel delivery system
10, as a
motive fuel flow source to power a vacuum generating device, illustrated with
respect to
the various embodiments as eductor 230. Although the illustrative filtration
systems
200', 200A, 200B use eductor 230 to draw the contaminated fuel from the bottom
of tank
16, other equipment may be used to perform this operation, such as another
type of
venturi device or a supplemental pump (in addition to pump 20). For example, a
flow
from the pump 20, including a primary and/or diverted flow, may be used to
drive an
impeller which drives a separate pump for filtration, similar to the operation
of a
turbocharger system of an internal combustion engine, which uses exhaust gases
to power
an impeller. The dedicated filtration pump powered by the flow of the primary
pump
may then be used in place of eductor 230 to drive filtration flows as
described herein.
[00152] Yet another alternative is to use a dedicated, electrically
powered pump
for filtration flows. This dedicated pump may be used in place of eductor 230
or 230A as
shown in Figs. 15 and 22, for example. In this configuration of filtration
system 200,
200', 200A or 200B, fuel return passageway 206, 206A or 206B is used only for
return of
filtered fuel flows, with no need for a separate motive flow of fuel as
described herein
with respect to venturi-based systems. The dedicated filtration pump may have
a low-
flow configuration sufficient for only the filtration flow desired for the
throughput of
filter 204, 204A or 204B.
[00153] In still another alternative arrangement, pump 20 may be
configured as a
diaphragm-type pump, in which a primary stroke of the pump is used for
delivery of fuel
to dispenser 12 via delivery line 18 (FIG. 1), while the reverse stroke can be
used to drive
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filtration flows as described herein. In this configuration, of filtration
system 200, 200',
200A or 200B eductor 230 is omitted. If the flows resulting from the reverse
stroke of
the diaphragm pump 20 are commensurate with the desired filtration flows
through filter
204, 204A or 20413, then fuel return passageway 206, 206A or 20613 is again
used only
for filtration flows with no separate excess or motive flow. If the flows from
the reverse
stroke of diaphragm pump 20 are higher than the desired flows through filter
204, 204A
or 204B, then fuel return passageway 206, 206A or 206B may be also be sized to
discharge excess flows back to tank 16.
[00154] Referring next to FIG. 13, an exemplary method 300 is
disclosed for
operating water filtration systems 200, 200', 200A, 200B. Method 300 may be
performed using controller 102 (FIG 3). Method 300 is described below with
reference
to the illustrative water filtration system 200 of FIG. 12, though the
disclosed method is
also applicable to systems 200', 200A and 200B.
1001551 In step 302 of method 300, controller 102 determines whether
a
predetermined start time has been reached. The start time may occur at a
desired time,
preferably outside of high-demand fuel dispensing hours (e.g., 4:30 to 7:30
AM), and
with a desired frequency For example, the start time may occur daily at about
8:00 PM.
When the start time of step 302 is reached, method 300 continues to step 304.
It is also
within the scope of the present disclosure that method 300 may be initiated
based on an
input from one or more monitors 104 (FIG_ 3). It is further within the scope
of the
present disclosure that method 300 may be initiated only when a certain
minimum level
of fuel product 14 is present in storage tank 16, such as about 20 to 30
inches of fuel
product 14, more specifically about 24 inches of fuel product 14.
1001561 In step 304 of method 300, controller 102 operates water
filter 204 to filter
fuel product 14. As discussed above, this filtering step 304 may involve
opening inlet
valve 203 of fuel inlet passageway 202 and activating pump 20. After passing
through
water filter 204, the filtered fuel product 14 may be returned continuously to
storage tank
16 via fuel return passageway 206.
[00157] In step 306 of method 300, controller 102 determines whether
a
predetermined cycle time has expired. The cycle time may vary. For example,
the cycle
time may be about 1-10 hours, more specifically about 7-9 hours, and more
specifically
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about 8 hours. If the cycle time has expired, method 300 continues to step
307, in which
controller 102 closes inlet valve 203 of fuel inlet passageway 202 to water
filter 204 and
resets the cycle time before returning to step 302 to await a new start time.
If the cycle
time has not yet expired, method 300 continues to step 308.
1001581 In step 308 of method 300, controller 102 determines whether
a water
level in water filter 204 is too high. Step 308 may involve communicating with
the high-
level water sensor 220 in water filter 204. If the high-level water sensor 220
detects
water (i.e., activates), method 300 continues to steps 310 and 312. If the
high-level water
sensor 220 does not detect water (i e., deactivates), method 300 skips steps
310 and 312
and continues to step 314.
[00159] In step 310 of method 300, controller 102 drains the
separated water
product from water filter 204. As discussed above, this draining step 310 may
involve
opening drain valve 209 of water removal passageway 208. From step 310, method
continues to step 312,
[00160] In step 312 of method 300, controller 102 determines whether
a water
level in water filter 204 is sufficiently low, Step 312 may involve
communicating with
the low-level water sensor 222 in water filter 204. If the low-level water
sensor 222 still
detects water (i.e., activates), method 300 returns to step 310 to continue
draining water
filter 204. Once the low-level water sensor 222 no longer detects water (i.e.,
deactivates),
method 300 continues to step 314 Controller 102 may initiate an alarm if the
draining
step 310 is performed for a predetermined period of time without deactivating
the low-
level water sensor 222. Controller 102 may also initiate an alarm if a
discrepancy exists
between the high-level water sensor 220 and the low-level water sensor 222,
specifically
if the high-level water sensor 220 detects water (i.e., activates) but the low-
level water
sensor 222 does not detect water (i.e., deactivates).
[00161] In step 314 of method 300, controller 102 determines whether
a water
level in storage tank 210 is too high. Step 314 may involve communicating with
the
high-level water sensor 224 in storage tank 210. Step 314 may also involve
calculating
the volume of water contained in storage tank 210 based on prior draining
steps 310 from
water filter 204. This volume calculation may involve logging the number of
draining
steps 310 from water filter 204 triggered by the high water-level sensor 220
and
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determining the known volume of water drained between sensors 220 and 222
during
each draining step 310. If the high-level water sensor 224 does not detect
water (i.e.,
deactivates) or the calculated water volume inside storage tank 210 is lower
than a
predetermined limit, method 300 returns to step 304 to continue operating
water filter
204. If the high-level water sensor 224 detects water (i.e., activates) or the
calculated
water volume inside storage tank 210 reaches the predetermined limit, method
300
continues to step 316.
[00162] In step 316 of method 300, controller 102 initiates an alarm
or sends
another communication requiring storage tank 210 to be emptied and replaced.
Controller 102 also closes inlet valve 203 of fuel inlet passageway 202 and
resets the
cycle time. After storage tank 210 is emptied and replaced, controller 102
returns to step
302 to await a new start time.
[00163] In a fourth embodiment, remediation system 108 is configured
to control
the humidity in turbine sump 32 of fuel delivery system 10. In the illustrated
embodiment of FIG. 2, remediation system 108 includes a desiccant 400 (e.g.,
calcium
chloride, silica gel) that is configured to adsorb water from the atmosphere
in turbine
sump 32. Desiccant 400 may be removably coupled to turbine sump 32, such as
being
detachably suspended from lid 38 of turbine sump 32. In this embodiment,
monitor 104""
may be a humidity sensor that is configured to measure the humidity in the
vapor space
of turbine sump 32. Monitor 104"" may also be configured to measure the
temperature in
the vapor space of turbine sump 32. The humidity and/or temperature data may
be
communicated to controller 102 (FIG. 3). When the humidity level increases
above a
predetermined level (e.g., 40%), output 106 may instruct the operator to
inspect turbine
sump 32 and/or to replace desiccant 400.
[00164] The above-described embodiments of remediation system 108
may be
provided individually or in combination, as shown in FIG 2. Thus, remediation
system
108 may be configured to ventilate turbine sump 32 of fuel delivery system 10,
irradiate
bacteria in turbine sump 32 of fuel delivery system 10, operate water
filtration system
200, and/or control the humidity in turbine sump 32 of fuel delivery system 10
[00165] While this invention has been described as having exemplary
designs, the
present invention can be further modified within the spirit and scope of this
disclosure.
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This application is therefore intended to cover any variations, uses, or
adaptations of the
invention using its general principles. Further, this application is intended
to cover such
departures from the present disclosure as come within known or customary
practice in the
art to which this invention pertains and which fall within the limits of the
appended
claims.
EXAMPLES
1. Example 1: Degradation of Transmitted Light Intensity in
Corrosive
Environment
[00166] Various plain steel samples were prepared as summarized in
Table 1
below. Each sample was cut into a 1-inch square.
Table 1
No. Description
Dimensions
1 Fine wire mesh 60x60 mesh, 0.0075" wire
diameter
2 Thick wire mesh 14x14 mesh, 0.035" wire
diameter
3 Perforated sheet 0.033" hole diameter
4 Fine wire mesh 30x30 mesh, 0_012" wire
diameter
Perforated sheet 0.024" hole diameter
[00167] The samples were placed in a sealed glass container together
with a 5%
acetic acid solution. The samples were suspended on a non-corrosive, stainless
steel
platform over the acetic acid solution for exposure to the acetic acid vapor
in the
container. Select samples were removed from the container after about 23, 80,
and 130
hours. Other samples were reserved as control samples.
[00168] Each sample was placed inside a holder and illuminated with
a LED light
source inside a tube to control light pollution. An ambient light sensor from
ams AG was
used to measure the intensity of the light passing through each sample. The
results are
presented in FIGS. 7-9. FIG. 7 includes photographs of the illuminated samples
themselves. FIG. 8 is a graphical representation of the relative light
intensity transmitted
through each sample over time. FIG. 9 is a graphical representation of the
normalized
light intensity transmitted through each sample over time, with an intensity
of 1.00
assigned to each control sample. As shown in FIGS. 7-9, all of the samples
exhibited
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increased corrosion and decreased light transmission over time. The fine wire
mesh
samples (Sample Nos 1 and 4) exhibited the most significant corrosion over
time_
2. Example 2: Real-Time Degradation of Transmitted Light
Intensity in
Corrosive Environment
[00169] Sample No. 4 of Example 1 was placed inside a sealed plastic
bag together
with a paper towel that had been saturated with a 5% acetic acid solution. The
sample
was subjected to illumination testing in the same manner as Example 1, except
that the
sample remained inside the sealed bag during testing. The results are
presented in FIG.
10, which is a graphical representation of the actual light intensity
transmitted through the
sample over time. Like Example 1, the sample exhibited increased corrosion and
decreased light transmission over time.
Example 3: Humidity Control with Desiccant
[00170] A turbine sump having a volume of 11.5 cubic feet and a
stable
temperature between about 65 F and 70 F was humidified to about 95% using
damp
rags. The rags were then removed from the humidified turbine sump. A desiccant
bag
was placed inside the humidified turbine sump, which was then sealed closed.
The
desiccant bag contained 125g of calcium chloride with a gelling agent to
prevent
formation of aqueous calcium chloride.
[00171] The relative humidity and temperature in the turbine sump
were measured
over time, as shown in FIG. 20. After 1 day, the desiccant had adsorbed enough
moisture
to decrease the relative humidity to about 40%. After 3 days, the desiccant
had adsorbed
enough moisture to decrease the relative humidity beneath about 20%. The
relative
humidity eventually decreased beneath 10%.
51
