It is common to collect liquids in storage vessels (tanks). Such liquids can include oil and other hydrocarbon based fluids, water (fresh or brine), hazardous chemicals, and the like. Liquid storage vessels can be buried underground such as underground fuel storage tanks used in automotive service stations, or located above ground such as storage tanks used in association with drilling and refining operations in the oil and gas industry, or the storage of drinking water in municipal water supply systems. Some vessels can be relatively large and can accommodate thousands, or even millions, of gallons of liquid.
Vessels can be closed or open systems. A closed vessel may be used to store various types of pressurized fluids such as liquefied natural gas or other volatile substances. Closed vessels may be specifically sealed off from the surrounding atmosphere to maintain the contents under pressure and hence, in a liquefied form.
Open vessels on the other hand may be provided with screened vents or other mechanisms to allow equalization of the vapor space pressure within the vessel with that of the surrounding atmosphere. For example, it may be desirable to admit atmospheric air to enter the vapor space of the vessel as liquid is pumped (or gravity fed) out of the vessel, and it may be desirable to release pressure from the vapor space of the vessel as additional liquid is pumped or otherwise added to the contents of the vessel.
Atmospheric effects may also alter the interior pressure of a storage vessel with respect to the pressure of the surrounding atmosphere. For example, during the course of a hot summer day solar heating of the exterior of the storage vessel may result in a substantial increase in the internal pressure of the vessel as compared to the ambient atmospheric pressure.
Failure to maintain the interior vapor space of a storage vessel within some range of the pressure of the surrounding atmosphere may lead to a number of problems, such as reduced fluidic flow as efforts are made to transfer liquid to or from the vessel. In some extreme cases, a significant pressure differential may even result in structural damage to a vessel.
At the same time, there are a number of reasons why it may not be desirable to maintain a continuous venting of the vapor space of a liquid storage vessel with the surrounding atmosphere. For example, a continuously open vent, even if the vent is screened, can still admit debris or other substances from the external environment, thereby introducing undesirable contaminants to the stored liquid.
Similarly, evaporated vapors or fumes from the stored liquid, such as water vapor or volatile hydrocarbons, may pass through a continuously open vent to the surrounding atmosphere at an unacceptable rate. This can lead to an undesired loss of product or, in some cases, unacceptable levels of environmental contamination.
Various embodiments of the present invention are generally directed to a vapor pressure equalization assembly for use in abating overpressure and underpressure conditions in a vapor space of a liquid storage tank.
In accordance with some embodiments, a vapor pressure equalization assembly is provided with an underpressure relief assembly and an overpressure relief assembly. These respective assemblies are placed in fluidic communication with the vapor space of a storage tank containing a liquid, and each includes a movable piston sealingly engageable with sealing member.
Respective biasing members, such as coiled springs, exert biasing forces to keep the respective pistons in a normally sealed engagement with the associated sealing members. When a predetermined underpressure differential or overpressure differential between the pressure of the vapor space and that of the surrounding atmosphere arises, the associated piston will move to an open position to allow fluidic communication between the vapor space and the surrounding atmosphere, thereby equalizing the vapor space pressure.
Other features and advantages of the various embodiments of the present invention will become apparent when the following detailed description is read in conjunction with the drawings and appended claims.
For purposes of providing a concrete example, the liquid 104 is contemplated as comprising a non-pressurized hydrocarbon liquid, such as crude oil or similar. Other forms of liquid can readily be used, however.
As will be appreciated, a number of factors may result in changes in the pressure of the vapor space 106 over time. Environmental cycling, such as thermal heating and cooling effects, may result in significant changes in the internal pressure of the vapor space 106 within the tank 102. The pressure of the vapor space 106 may also change due to changes in the amount of liquid 104 within the tank; the pressure of the vapor space 106 will generally tend to rise as additional liquid is introduced into the tank, and the pressure will generally fall as liquid is removed from the tank. Such fluidic transfers can take place via a transfer conduit 108.
Accordingly, a vapor pressure equalization assembly is provided at 110. As described below, the vapor pressure equalization assembly 110 (hereinafter “assembly”) normally operates in a closed mode to seal the vapor space 106 from the surrounding environment. This normally prevents harmful environmental pollutants from passing out of the tank from the vapor space 106 and into the surrounding environment.
When the pressure of the vapor space 106 falls outside a predetermined threshold range, however, the assembly 110 transitions to an open mode to facilitate fluidic transfer between the vapor space and the surrounding atmosphere.
The threshold range is bounded by an upper threshold differential value and a lower threshold differential value. When the vapor space pressure exceeds the upper threshold value, the assembly 110 opens to facilitate a transfer of vapors from the vapor space 106 to the surrounding environment. Once the vapor space pressure is reduced to within the upper threshold value, the assembly 110 transitions back to the normally closed mode.
Similarly, when the vapor space pressure falls below the lower threshold value, the assembly 110 opens to facilitate a transfer of atmospheric air from the surrounding environment into the vapor space 106, after which the assembly 110 transitions back to the normally closed mode.
While the vapor pressure equalization assembly 110 is shown mounted on a top surface 116 of the storage vessel 102 (see
The vapor pressure equalization assembly 110 includes an underpressure (vacuum) relief assembly 120 and an overpressure relief assembly 122. These assemblies 120, 122 are respectively mounted via threaded bores in a housing 124 of the manifold 112 and extend into an interior manifold chamber 126.
The underpressure relief assembly 120 includes a substantially cylindrical relief assembly body 128 which sealingly engages the housing 124 via annular sealing member 129. A vent cap flange (weather guard) 130 is affixed to an upper end of the assembly body 128. A number of spaced apart vent apertures 132 are spatially arranged about the relief assembly body 128, as shown. An annular screen 134 of a durable fine wire mesh or the like is supported to surround the relief assembly body 128 and cover the apertures 132. The covering flange 130 and a lower extent of the screen 134 are shown in
A piston 136 normally seals the vapor space 106 from the surrounding atmosphere by engaging an annular sealing member 138. The sealing member 138 is characterized as an elastomeric o-ring, although other sealing configurations can be used as desired. The sealing member 138 is supported by a threaded insert member 140 which engages the body 128 as shown. A number of guide legs 142, in this case four (4), extend upwardly from the piston 136 to maintain the piston 136 in a centered relation with an annular interior wall surface of the insert member 140.
A piston shaft, or rod 144 extends upwardly from the piston 136 and terminates at an annular flange support 146. The flange support 146 is characterized as a thick washer but can take other forms as desired. A biasing member 148, characterized as a coiled tapered spring, is compressed between the insert member 140 and the flange support 146 to provide an upwardly directed force upon the piston 136. It is contemplated that the force supplied by the spring 148 will be relatively small. Generally, in some embodiments the spring 148 is sized to overcome the weight of the piston 136, shaft 144 and support flange 146, since gravity will tend to urge these members downwardly away from the sealing member 138.
The interior fluidic pressure of the vapor space 106 will also apply an upwardly directed force upon the piston 136. The amount of this upwardly directed force will be determined in relation to the pressure of the vapor space 106 and the areal extent of the downwardly facing surface of the piston 136. This upwardly directed force will be countered by a downwardly directed force by the atmospheric pressure of the surrounding atmosphere upon the areal extent of the upwardly facing surface of the piston 136.
So long as the interior pressure of the vapor space 106 is substantially that of the surrounding atmosphere, the piston 136 will be retained via the biasing of the spring 148 in sealing engagement with the sealing member 138. However, once the pressure of the vapor space 106 is sufficiently reduced with respect to the pressure of the surrounding atmosphere, the piston 136 will become unseated from the sealing member 138 and will begin to move downwardly.
As the piston 136 is drawn downwardly, the spring 148 will be compressed, and atmospheric air will pass through the respective screen 134 and vent apertures 132, past the piston 136 (between adjacent legs 142) and into the interior chamber 126 of the manifold. This will continue until the pressure within the interior chamber 126 (and hence, the vapor space 106) is raised to a sufficient level that the combined upwardly directed bias force from the vapor space pressure and the spring 148 will once again close the piston 136.
The vacuum relief assembly 120 thus automatically operates in response to the pressure differential between the vapor space pressure and the surrounding atmospheric pressure. The setpoint at which the vacuum relief assembly 120 opens (i.e., the threshold pressure differential) can be adjusted in a number of ways such as by adjusting the compression force of the spring 148 via nuts 150, 152.
The pressure relief assembly 122 operates in a similar fashion to automatically rectify overpressure conditions, and utilizes many of the same components incorporated into the vacuum relief assembly 120. As denoted in
A normally closed piston 162 abuts a sealing member (o-ring) 164 supported by an insert member 166. A biasing member 168, in this case a second coiled spring, applies a downwardly directed biasing force upon the piston 162 to maintain the piston in the normally closed position.
The internal pressure of the vapor space 106 applies an upwardly directed force upon the piston 162 in relation to the areal extent of the exposed lower surface of the piston, and the exterior atmospheric pressure applies a downwardly directed force upon the piston 162 in relation to the areal extent of the exposed upper surface of the piston.
When the interior pressure within the chamber 126 exceeds the external atmospheric pressure sufficiently to overcome the biasing force of the spring 168, the piston 162 will move upwardly off of the sealing member 164, facilitating a flow of gasses from the vapor space 106 to flow past the piston 162, through the apertures 158 and through the screen 160 to the exterior atmosphere. A number of legs 170 extend from the piston 162 to maintain the piston in a desired centered relation during such movement, and the escaped vapors will pass between these legs as before.
When a sufficient volume of gasses from the vapor space have been vented to reduce the vapor space/exterior pressure differential to a resulting force that is less than the biasing force of the spring 168, the piston 162 will be automatically reseated on the sealing member 164, thereby closing the pressure relief assembly 122.
The spring 168 is compressed between the piston 162 and an annular support 172. The support 172 is coupled to a distal end of a threaded shaft 174, which extends through the body 154. A threaded nut 175 operates as a jam nut to set the depth of the threaded shaft 174 within the body 154, and hence, the compression force of the spring 168.
To adjust the force of the spring 168, a user removes a protective cover 176 and rotates the nut 175 to threadingly advance or retract the threaded shaft 174 to the desired depth. Although not shown, a flat surface can be provided at the proximal end of the shaft 174 to secure the shaft during such operations. The cover 176 is then replaced onto the proximal end of the shaft 174, and a wire tie-off tag 178 can be used to secure an ear 176A of the cover 176 to discourage further adjustment and to provide indication of tampering.
An alternative embodiment for the vapor pressure equalization assembly is denoted at 110A in
An intermediary access port 180, in fluidic communication with the manifold chamber 126 and axially aligned with the coupling 114, is disposed on the manifold 112A between the respective assemblies 120A, 122A. A removable threaded cover 182 normally closes the access port 180. The access port provides access for a test device 184 (see
In some embodiments, the underpressure and pressure relief assemblies 120A, 122A in
Alternatively, the underpressure relief assembly 120A of
As before, the depth of the shaft 188, and hence the setpoint for the piston 136, can be adjusted by advancing the threaded shaft 188 relative to jam nut 189, and a protective cover 190 can be installed as before.
Unlike many prior art equalization systems which fail to hold a setpoint pressure differential, the various embodiments disclosed herein maintain the storage tank in a continuously sealed (closed) condition until and only at such time that the pressure within the vapor space exceeds the upper threshold level or falls below the lower threshold level, after which the system returns to maintain a sealed condition. The pressure in the vapor space will thus not necessarily equal that of the surrounding atmosphere, but will be within the predetermined range of acceptable pressure differentials.
It follows that, depending on the structural integrity of a storage tank, the tank may be able to remain fully sealed against the external environment over a wide range of environmental cycling conditions. For example, a given tank may heat up during a hot day and cool off during the following night, and if the pressure excursions can be safely handled by the tank, no venting to the external atmosphere will take place. This advantageously prevents environmental contamination by eliminating the unnecessary venting of volatile fumes to the surrounding atmosphere, and may prevent the tank owner from incurring fines or other sanctions from a regulatory authority carrying out on-site “sniffer” type inspections in an attempt to detect emitted vapors.
In some embodiments, the respective upper and lower thresholds are set in relation to the structural capabilities of the tank so that, should changes in internal pressure be sufficient to approach those that may result in damage, the system will safely vent (or admit) fluid to prevent such damage, but otherwise prevent such venting or admitting of fluid in all other cases. Exemplary structural capabilities of some types of storage tanks may be on the order of about +6.0 ounces per square inch (6.0 oz/in2) of positive pressure and about −0.4 oz/in2 of negative pressure. The setpoint pressure differential thresholds can be set at some derated percentage, such as 80% of these values.
On-site field calibration operations can also be made as desired.
During an on-site calibration of the system, the user can close the valve 196 and vent the contents of the manifold to the surrounding atmosphere. A pressure/vacuum supply apparatus 198, such as a portable tank, compressor, vacuum pump, etc. can be coupled to the manifold 112 via a first port 192 (see
The user can utilize the apparatus 198 to set the manifold pressure to a first desired level, such as a first vacuum (negative) pressure, and adjust the underpressure relief assembly 120 until the assembly 120 operates to open at this desired level. The holding pressure of the assembly 120 can then be determined via the meter 200. For example, the assembly 120 may be set to operate to nominally open at −0.4 oz/in2 and thereafter close and hold −0.3 oz/in2 of vacuum pressure.
The foregoing steps can then be repeated by supplying a positive pressure to the manifold 112 and adjusting the overpressure relief assembly 122 until the assembly 122 opens at this second desired level. The holding pressure of the assembly 122 can then be determined via the meter 200. For example, the assembly 122 may operate to open at +6.0 oz/in2 and thereafter close and hold +5.9 oz/in2 of positive pressure. In this example, the operational pressure differential range would thus be from −0.4 to +6.0 oz/in2; pressures at or beyond this range would result in the opening of the equalization assembly 110, and the equalization assembly would remain closed for pressure excursions that remained within this range.
It will be appreciated that the various embodiments discussed herein provide a number of advantages over the prior art. The various embodiments provide both overpressure and underpressure relief at specified levels, while normally closing the vapor space of the storage vessel to the surrounding atmosphere at all other times. The assembly is readily constructed and maintained, and is contemplated to provide reliable operation over a variety of changing environmental conditions.
While the various embodiments utilize both underpressure and overpressure vapor pressure equalization, it will be appreciated that a single assembly can be alternatively provided; for example, an equalization assembly can be supplied with just overpressure relief capabilities without the associated underpressure relief capabilities, or vice versa. Similarly, multiple ports with different setpoints can be provided to facilitate greater rates of fluidic exchange between the vapor space and surrounding atmosphere under different environmental and/or operational conditions.
It will be clear that the various embodiments presented herein are well adapted to carry out the objects and attain the ends and advantages mentioned as well as those inherent therein. While presently preferred embodiments have been described for purposes of this disclosure, numerous changes may be made that will readily suggest themselves to those skilled in the art and that are encompassed in the spirit of the invention disclosed and as defined in the appended claims.
This application makes a claim of domestic priority under 35 U.S.C. §119(e) to U.S. Provisional Patent Application No. 61/170,442 filed Apr. 17, 2009.
Number | Date | Country | |
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61170442 | Apr 2009 | US |