The present invention generally relates to the recovery of fuel vapors in connection with a liquid fuel dispensing facility. More particularly, the present invention relates to controlling the volume of fuel vapor recovered to ensure that the volume is in appropriate proportion to the volume of liquid fuel being dispensed.
Liquid fuel dispensing facilities (i.e. gasoline stations) often suffer from a loss of fuel to the atmosphere due to inadequate vapor collection during fuel dispensing activities, excess liquid fuel evaporation in the containment tank system, and inadequate reclamation of the vapors during tanker truck deliveries. Lost vapor is an air pollution problem which is monitored and regulated by both the federal and state governments. Attempts to minimize losses to the atmosphere have been effected by various vapor recovery methods. Such methods include: “Stage-I vapor recovery” where vapors are returned from the underground fuel storage tank to the delivery truck; “Stage-II vapor recovery” where vapors are returned from a refueled vehicle tank to the underground storage tank; vapor processing where the fuel/air vapor mix from the underground storage tank is received and the vapor is liquefied and returned as liquid fuel to the underground storage tank; burning excess vapor off and venting the less polluting combustion products to the atmosphere; and other fuel/air mix separation methods.
When working properly, Stage-II vapor recovery results in equal exchanges of air or vapor (A) and liquid (L) between the main fuel storage tank and the consumer's gas tank. Ideally, Stage-II vapor recovery produces an A/L ratio very close to 1.0. In other words, returned vapor replaces an equal amount of liquid in the main fuel storage tank during refueling transactions. When the A/L ratio is close to 1.0, refueling vapors are collected, the ingress of fresh air into the storage tank is minimized, and the accumulation of an excess positive or negative pressure in the main fuel storage tank is prevented. This minimizes losses at the fuel dispensing nozzle and evaporation and leakage of excess vapors from the storage tank. Measurement of the A/L ratio thus provides an indication of proper Stage-II vapor collection operation. A low A/L ratio means that the proper amount of fuel vapor is not being recovered for the amount of fuel that has been dispensed.
The present invention recognizes and addresses considerations of prior art constructions and methods.
One embodiment of the present invention provides an air to liquid regulator valve for use with a vapor recovery system that recovers vapors expelled from a vehicle receiving fuel through a fuel supply passage and returns the vapors to an underground storage tank through a vapor return passage in a service station environment. The regulator valve includes a housing defining a fuel flow path in fluid communication with the fuel supply passage and a vapor return path in fluid communication with the vapor return passage, a vapor return orifice defined by the housing and disposed between a first portion and a second portion of the vapor return path, and a vapor flow bypass in fluid communication with the first portion and the second portion of the vapor return path such that the flow of vapors through both the vapor flow bypass and the vapor return orifice is possible.
Another embodiment of the present invention provides a vapor recovery system that recovers vapors expelled from a vehicle during refueling at a fuel dispensing point and returns the vapors to an underground storage tank in a service station environment, the system including an air to liquid regulator valve associated with the fuel dispensing point. The regulator valve includes a housing defining vapor return path, a vapor return orifice defined by the housing and disposed between a first portion and a second portion of the vapor return path, and a vapor flow bypass in fluid communication with the first portion and the second portion of the vapor return path such that the flow of vapors through both the vapor flow bypass and the vapor return orifice is possible. The system also includes a vapor pump that is in fluid communication with the underground storage tank, and a vapor flow passage that is in fluid communication with the vapor flow path of the air to liquid regulator valve and the vapor pump.
Yet another embodiment of the present invention provides an air to liquid regulator valve for use with a vapor recovery system that recovers vapors expelled from a vehicle receiving fuel through a fuel supply passage and returns the vapors to an underground storage tank through a vapor return passage in a service station environment. The regulator valve includes a housing defining a fuel flow path in fluid communication with the fuel supply passage and a vapor return path in fluid communication with the vapor return passage, a vapor return orifice defined by the housing and disposed between a first portion and a second portion of the vapor return path, and a vapor piston including a metering element, wherein the metering element is insertable into the vapor return orifice to regulate the flow of vapors therethrough, and the metering element is configured to prevent the flow of vapors through the vapor return orifice when the metering element is fully seated in the vapor return orifice. A vapor flow bypass is in fluid communication with the first portion and the second portion of the vapor return path such that the flow of vapors through the vapor flow bypass is possible when the metering nose prevents the flow of vapors through the vapor return orifice. A first flow adjustment mechanism selectively adjusts the vapor flow bypass such that an amount of vapor that is allowed to bypass the vapor return orifice during a fueling operation is adjustable.
Other objects, features and aspects for the present invention are discussed in greater detail below. The accompanying drawings are incorporated in and constitute a part of this specification, and illustrate one or more embodiments of the invention. These drawings, together with the description, serve to explain the principles of the invention.
A full and enabling disclosure of the present invention, including the best mode thereof, to one of ordinary skill in the art, is set forth more particularly in the remainder of this specification, including reference to the accompanying drawings, in which;
Repeat use of reference characters in the present specification and drawings is intended to represent same or analogous features or elements of the invention.
Reference will now be made in detail to presently preferred embodiments of the invention, one or more examples of which are illustrated in the accompanying drawings. Each example is provided by way of explanation, not limitation, of the invention. In fact, it will be apparent to those skilled in the art that modifications and variations can be made in the present invention without departing from the scope and spirit thereof. For instance, features illustrated or described as part of one embodiment may be used on another embodiment to yield a still further embodiment. Thus, it is intended that the present invention covers such modifications and variations as come within the scope of the appended claims and their equivalents.
A first embodiment of the present invention is described in connection with
As illustrated in
The data acquisition system 140 preferably includes standard computer storage and central processing capabilities, keyboard input device(s), and audio and visual output interfaces among other conventional features. Entities such as the California Air Resources Board (CARB) have produced requirements for Enhanced Vapor Recovery (EVR) equipment. These include stringent vapor recovery system monitoring requirements to determine continuously whether or not the systems are working properly. In locations subject to these enhanced requirements, the data acquisition system 140 may also function as an in-station diagnostic monitor. For example, where required, the data acquisition system 140 may be the Veeder-Root Company TLS-350™ tank monitor. Both the dispenser controller 120 and the data acquisition system 140 may be further communicatively coupled to an off-site or remote system (not shown) for communicating information and receiving instructions remotely, in which case both systems may communicate with the remote system over telephone lines or other network lines, including the Internet.
Referring additionally to
Each fuel dispensing point of the fuel dispenser units 200a and 200b includes a blend manifold 260, a coaxial vapor/liquid splitter 261, a vapor return passage 220, a fuel supply passage 230 and the mechanical A/L regulator valve 500. As shown, the mechanical A/L regulator valve 500 is preferably disposed adjacent the coaxial vapor/liquid splitter 261. The vapor return passages 220 may be joined together before connecting with a common vapor return pipe 410 (
The fuel dispenser units 200a and 200b also include liquid fuel dispensing meters 240. The liquid fuel dispensing meters 240 provide dispensed liquid fuel quantity information to the dispenser controller 120 via a liquid fuel dispensing meter interface 270, or control system, and interface wiring 130. The control system 270 may be a microcontroller, a microprocessor, or other electronics with associated memory and software programs running thereon. The control system 270 typically controls aspects of the fuel dispenser units 200a and 200b, such as a gallons (or liters) display 215, a price display 216, receipt of payment transactions, and the like, based on fuel flow information received from the liquid fuel dispensing meters 240.
The main fuel storage system 300 includes one or more main fuel storage tanks 310a and 310b. The fuel storage tanks 310a and 310b are typically provided underground, however, underground placement of the tank is not required for application of the invention. As best seen in
The means for connecting the fuel dispenser units 200a and 200b and the main fuel storage system 300 include a vapor return pipeline 410 and one or more fuel supply pipelines 420. The vapor return pipeline 410 and the fuel supply pipelines 420 are connected to the vapor return passages 220 and fuel supply passages 230, respectively, associated with multiple fuel dispensing points 210. Fuel supply pipelines 420 may be double-walled pipes having secondary containment, as is well known. An exemplary underground fuel delivery system is illustrated in U.S. Pat. No. 6,435,204, which is hereby incorporated by reference in its entirety.
In the embodiment illustrated in
As shown in
Referring additionally to
As shown in
The liquid fuel dispensing meter 240 communicates through the vapor barrier 205 via a pulser signal line from pulser 241 to the control system 270. The control system 270 regulates the proportional valve 244, via a valve communication line, to open and close during fueling operations. The proportional valve 244 may be a proportional solenoid controlled valve, such as described in U.S. Pat. No. 5,954,080, which is incorporated herein by reference in its entirety. As the control system 270 directs the proportional valve 244 to open to allow increased fuel flow, the fuel enters the proportional valve 244 and exists into the liquid fuel dispenser meter 240. The flow rate of the displaced volume of the fuel is measured by the liquid fuel dispenser meter 240 which communicates the flow rate of the displaced volume of fuel to the control system 270 via the pulser signal line. A pulse signal is generated on the pulser signal line in the example illustrated, such as by a Hall-effect sensor as described in U.S. Pat. No. 7,028,561, which is incorporated herein by reference in its entirety. In this manner, the control system 270 uses the pulser signal from the pulser signal line to determine the flow rate of fuel flowing through the fuel dispenser unit 200a and being delivered to the vehicle 12. The control system 270 updates the total gallons dispensed on the gallons display 215 via a gallons display communication line, as well as the cost of fuel dispensed on the price display 216 via a price display communication line.
As fuel leaves the liquid fuel dispensing meter 240, the fuel enters a flow switch 242. The flow switch 242 generates a flow switch communication signal via a flow switch signal line to the control system 270 to communicate when fuel is flowing through liquid fuel dispensing meter 240. The flow switch communication signal indicates to the control system 270 that fuel is actually flowing in the fuel delivery path and that subsequent pulser signals from liquid fuel dispensing meter 240 are due to actual fuel flow.
After the fuel enters the flow switch 242, it exits through the fuel supply passage 230 to be delivered to the blend manifold 260. The blend manifold 260 receives fuels of varying octane values from the various underground fuel storage tanks 310a and 310b and ensures that fuel of the octane level selected by the consumer is delivered to the consumer's vehicle 12. After flowing through the blend manifold 260, the fuel passes through the fuel hose 212 and fuel nozzle 210 for delivery into the fuel tank 24 of the vehicle 12. Flexible fuel hose 212 includes a product delivery line 231 and the vapor return passage 220. Both lines 231 and 220 are fluidly connected to the underground fuel storage tanks 310a and 310b through the fuel dispenser unit 200a, as previously discussed. The vapor return passage 220 is separated from the product delivery line 231 by the coaxial vapor/liquid splitter 261.
During delivery of fuel into the vehicle's fuel tank 24, the incoming fuel displaces air in the fuel tank 24 containing fuel vapors. Vapor is recovered from the fuel tank 24 of the vehicle 12 through the vapor return passage 220 with the assistance of the vapor pump 250. As previously noted, the vapor pump 250 of the present embodiment is a variable speed pump. As fuel is dispensed from the fuel nozzle 210 into the fuel tank 24 of the vehicle 12, the flowing fuel causes the mechanical A/L regulator valve 500 to open, thereby opening the vapor return passage 220 to the fuel tank 24.
More specifically, referring additionally to
The vapor tube 530 includes a first end 532, a second end 534 and a cylindrical portion 536 extending therebetween. The first end 532 of the vapor tube 530 is received concentrically within the housing 550 about the vapor flow path 552 and the vapor return orifice 554. In this embodiment, the vapor tube 530 is retained within the housing 550 by an annular lip 537 formed about the second end 534 of the vapor tube 530 that interacts with an annular groove 538 formed about the inner surface of the housing 550. The cylindrical portion 536 of the vapor tube 530 thus forms a portion of the vapor return path 552.
The vapor piston 520 includes a metering element, or nose 522, and a magnet 524 that are disposed on a shuttle body 526. The vapor piston 520 is slidably received within the cylindrical portion 536 of vapor tube 530 such that back and forth motion of the vapor piston 520 within the vapor tube 530 causes the metering nose 522 to regulate the flow of fuel vapor through the vapor return orifice 554.
The liquid piston 510 includes a magnet 512 and is slidably mounted along the outer surface of the vapor tube 530. The spring 540 is also mounted about the outer surface of the vapor tube 520 and is arranged such that the liquid piston 510 is urged into the closed position (
The high flow adjustment mechanism 560 includes a high flow adjustment screw 562 that is rotationally received in a first bore 558 defined by the housing 550. The high flow adjustment screw 562 includes a head 564 that is received in a smooth portion of the first bore 558 and a threaded shank 566 that is received in a correspondingly threaded portion of the first bore 558. As such, rotation of the high flow adjustment screw 562 causes the high flow adjustment screw 562 to move along the longitudinal axis of the first bore 558, thereby causing a distal end 568 of the treaded shank 566 to either project farther into, or be withdrawn from, the vapor return path 552. In this manner, the high flow adjustment screw 562 can be used to adjust the amount of vapor recovered for a given amount of fuel that is dispensed at a given rate, as discussed in greater detail below.
The low flow adjustment mechanism 580 includes a low flow adjustment screw 582 that is rotationally received in a second bore 559 defined by the housing 550, and a vapor flow bypass 590 that is in fluid communication with both the portion of the vapor flow path 552 both upstream and downstream of vapor return orifice 554. The low flow adjustment screw 582 includes a head 584 that is received in a smooth portion of the second bore 559 and a threaded shank 586 that is received in a correspondingly threaded portion of the second bore 559. As such, rotation of the low flow adjustment screw 582 within the second bore 559 causes the low flow adjustment screw 582 to move along the longitudinal axis of the second bore 559, thereby causing a distal end 588 of the threaded shank 586 to either project farther into, or be withdrawn from, the vapor flow bypass 590. In this manner, the low flow adjustment screw 582 can be used to adjust the amount of vapor that is allowed to bypass the vapor return orifice 554 during fueling operations. Note, the distal end 588 of the low flow adjustment screw 582 can be fully seated within a portion of the vapor flow bypass 590 such that the flow of vapor through the vapor flow bypass 590 is prevented.
In use, a user activates the fuel nozzle 210 causing pressurized fuel to enter the fuel flow path 556 of the A/L regulator valve 500, as discussed above. As best seen in
The vacuum maintained by the vapor pump 250 causes the vapor laden air that is displaced by the ingress of fuel into the fuel tank 24 to be drawn through the A/L regulator valve 500 into the vapor return passage 220. As noted above, as the rate at which fuel is dispensed increases, the vapor piston of the A/L regulator valve 500 opens further and more air is drawn into the vapor return passage 220 and associated vapor return pipeline 410.
Testing reveals that the disclosed system functions as desired when a vacuum level as low as 80 mBar is maintained on the downstream side of the A/L regulator valves 500. However, it is possible for small amounts of fuel to be drawn into the vapor return passages 220 through the associated nozzles 210 during vapor recovery. This fuel tends to collect in the lowest portion of the associated vapor return passage 220, thereby effectively blocking the vapor return passage 220 and preventing further vapor recovery if the fuel is not cleared. Although proper vapor recovery is achieved through clear vapor return passages 220 when an 80 mBar vacuum is maintained, an 80 mBar vacuum is typically not great enough to ensure that any ingested fuel is further drawn through the vapor pump 250 so that the vapor return passages 220 remain clear and the recovery of vapor is continuous. As such, preferably, a vacuum of about 200 mBar may be maintained on the downstream side of the A/L regulator valves 500 in the present embodiment. Note, higher vacuum levels can also be used as long as they are adequate for maintaining the vapor return passages 220 in an unobstructed condition.
In the present example, graph line 600 reveals that for the desired initial setting, the A/L ratio of 1:1 is maintained across a substantial portion of the operating range of the associated fuel dispensing point 210 (
Similarly, the amount of vapor that is recovered for a given amount of fuel that is dispensed can be increased by withdrawing the high flow adjustment screw 562 farther from the vapor flow path 552 than in its initial setting, thereby reducing the restriction to the flow of vapor through the vapor flow path 552. The increased slope of graph line 620, when compared to the slope of graph line 600, reflects the fact that more vapor is recovered for a given amount of fuel dispensed when compared to the initial setting of the high flow adjustment screw 562.
However, the reduced slope and increased slope of graph lines 610 and 620, respectively, as compared to the slope of the graph line 600 of the initial setting, reflect the fact that as the rate at which fuel is being dispensed decreases, the high flow adjustment mechanism 560 becomes less efficient with regard to adjusting the amount of vapor recovered relative to the amount of fuel being dispensed. More specifically, for the preferred embodiment discussed, a vapor flow adjustment of 10 liters per minute at a fuel dispensing rate of 40 liters per minute results in a corresponding change of approximately 1 liter per minute vapor flow at the reduced fuel flow rate of 20 liters per minute. The low flow adjustment mechanism 580 facilitates the adjustment of recovered vapor amounts across the full spectrum of fuel dispensing rates.
Referring additionally to
One method of varying the A/L ratios for the A/L regulator valve 500 is reflected in graph lines 602 and 612 of
Similarly, the amount of vapor that is recovered for a given amount of dispensed fuel can be reduced by extending the low flow adjustment screw 582 farther into the vapor flow bypass 590 than in its initial setting, thereby further restricting the flow of vapor through the vapor flow bypass 590. Note, the “starting point” for the adjustment of the low flow adjustment screw 582 represented by graph line 612 is graph line 610, meaning prior to adjusting the low flow adjustment screw 582, the high flow adjustment screw 562 had been previously adjusted from the initial setting as discussed with regard to
Referring now to graph line 622 of
Although the embodiment of the A/L regulator valve 500 shown in
A second embodiment of the present invention is shown in
A third embodiment of the present invention is shown in
An alternate embodiment of the present invention differs from the first three embodiments in that each fuel dispenser unit 200a and 200b includes a pair of dedicated vapor pumps 250 for the recovery of fuel vapors rather than a vapor pump 250 that is disposed in the common vapor return pipeline 410, as shown in
Each of the previously discussed embodiments disclose a vapor recovery system including one or more variable speed vapor pumps. Note, however, that in each of the previously discussed embodiments, the variable speed vapor pumps can be replaced with fixed speed pumps. Additionally, electronic proportional valves (not shown) can be disposed on the upstream side of the various fixed speed pumps.
As discussed above, the control system 270 receives information from liquid fuel dispensing meter 240 and the pulser 241 regarding the amount of fuel being dispensed. The liquid fuel dispensing meter 240 measures the fuel being dispensed while the pulser 241 generates a pulse per count of liquid fuel dispensing meter 240. In an exemplary embodiment, the pulser 241 generates one thousand and twenty-four (1024) pulses per gallon of fuel dispensed. In yet another alternate embodiment of the present invention, the control system 270 provides fuel flow information to the data acquisition system 140 by way of the interface wiring 130. In this embodiment, the rate at which vapor pump 250 is used to recover vapor is determined by the amount of fuel the data acquisition system 140 determines is being dispensed, based on the information provided by the liquid fuel dispensing meters 240 via interface wiring 130. The vapor pump 250 may be a variable speed pump or a constant speed pump with an electronic proportional valve, a mechanical pressure regulator operating across its inlet and outlet, etc., as previously discussed.
While preferred embodiments of the invention have been shown and described, modifications and variations thereto may be practiced by those of ordinary skill in the art without departing from the spirit and scope of the present invention, which is more particularly set forth in the appended claims. In addition, it should be understood the aspects of the various embodiments may be interchanged without departing from the scope of the present invention. Furthermore, those of ordinary skill in the art will appreciate that the foregoing description is by way of example only, and is not intended to limit the invention as further described in such appended claims.
This application claims priority to U.S. Provisional Patent Application Ser. No. 61/252,822, filed Oct. 19, 2009, the entire disclosure of which is incorporated by reference herein.
Number | Name | Date | Kind |
---|---|---|---|
3081788 | Lewis | Mar 1963 | A |
4649970 | Bower et al. | Mar 1987 | A |
5327944 | Healy | Jul 1994 | A |
5720325 | Grantham | Feb 1998 | A |
5860457 | Andersson | Jan 1999 | A |
6332483 | Healy | Dec 2001 | B1 |
6532999 | Pope et al. | Mar 2003 | B2 |
6533254 | Grifka et al. | Mar 2003 | B1 |
6866299 | Coates | Mar 2005 | B2 |
8167003 | Clever et al. | May 2012 | B1 |
8371341 | Gray | Feb 2013 | B2 |
8539991 | Carmack et al. | Sep 2013 | B1 |
20070267088 | Hughes | Nov 2007 | A1 |
Number | Date | Country |
---|---|---|
4028571 | Feb 1992 | DE |
0703186 | May 1998 | EP |
Entry |
---|
PCT International Search Report dated Dec. 6, 2010, regarding co-pending PCT Application No. PCT/US2010/053065 filed Oct. 18, 2010. |
U.S. Appl. No. 12/906,879, filed Oct. 18, 2010. |
Office Action dated Mar. 20, 2013 for co-pending Chinese patent application 201080056960.X. |
Number | Date | Country | |
---|---|---|---|
20110259470 A1 | Oct 2011 | US |
Number | Date | Country | |
---|---|---|---|
61252822 | Oct 2009 | US |