US20070151621A1 - Automatic shutoff and metering device - Google Patents
Automatic shutoff and metering device Download PDFInfo
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- US20070151621A1 US20070151621A1 US11/325,761 US32576106A US2007151621A1 US 20070151621 A1 US20070151621 A1 US 20070151621A1 US 32576106 A US32576106 A US 32576106A US 2007151621 A1 US2007151621 A1 US 2007151621A1
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- scale
- liquefied gas
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- shutoff valve
- container
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- 238000000034 method Methods 0.000 claims abstract description 37
- 239000007788 liquid Substances 0.000 claims description 5
- 238000005259 measurement Methods 0.000 claims description 5
- 239000007789 gas Substances 0.000 description 69
- 238000010586 diagram Methods 0.000 description 6
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 238000012544 monitoring process Methods 0.000 description 3
- 239000001307 helium Substances 0.000 description 2
- 229910052734 helium Inorganic materials 0.000 description 2
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 2
- 238000009413 insulation Methods 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 1
- 230000006978 adaptation Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 230000002045 lasting effect Effects 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 238000009877 rendering Methods 0.000 description 1
- 230000029058 respiratory gaseous exchange Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Images
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C6/00—Methods and apparatus for filling vessels not under pressure with liquefied or solidified gases
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2205/00—Vessel construction, in particular mounting arrangements, attachments or identifications means
- F17C2205/01—Mounting arrangements
- F17C2205/0153—Details of mounting arrangements
- F17C2205/0157—Details of mounting arrangements for transport
- F17C2205/0161—Details of mounting arrangements for transport with wheels
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2205/00—Vessel construction, in particular mounting arrangements, attachments or identifications means
- F17C2205/03—Fluid connections, filters, valves, closure means or other attachments
- F17C2205/0302—Fittings, valves, filters, or components in connection with the gas storage device
- F17C2205/0323—Valves
- F17C2205/0326—Valves electrically actuated
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2205/00—Vessel construction, in particular mounting arrangements, attachments or identifications means
- F17C2205/03—Fluid connections, filters, valves, closure means or other attachments
- F17C2205/0302—Fittings, valves, filters, or components in connection with the gas storage device
- F17C2205/0323—Valves
- F17C2205/0332—Safety valves or pressure relief valves
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2221/00—Handled fluid, in particular type of fluid
- F17C2221/01—Pure fluids
- F17C2221/016—Noble gases (Ar, Kr, Xe)
- F17C2221/017—Helium
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
- F17C2223/01—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the phase
- F17C2223/0146—Two-phase
- F17C2223/0153—Liquefied gas, e.g. LPG, GPL
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
- F17C2227/04—Methods for emptying or filling
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2250/00—Accessories; Control means; Indicating, measuring or monitoring of parameters
- F17C2250/03—Control means
- F17C2250/032—Control means using computers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2250/00—Accessories; Control means; Indicating, measuring or monitoring of parameters
- F17C2250/04—Indicating or measuring of parameters as input values
- F17C2250/0404—Parameters indicated or measured
- F17C2250/0408—Level of content in the vessel
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2250/00—Accessories; Control means; Indicating, measuring or monitoring of parameters
- F17C2250/04—Indicating or measuring of parameters as input values
- F17C2250/0404—Parameters indicated or measured
- F17C2250/0421—Mass or weight of the content of the vessel
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2250/00—Accessories; Control means; Indicating, measuring or monitoring of parameters
- F17C2250/06—Controlling or regulating of parameters as output values
- F17C2250/0605—Parameters
- F17C2250/061—Level of content in the vessel
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2250/00—Accessories; Control means; Indicating, measuring or monitoring of parameters
- F17C2250/07—Actions triggered by measured parameters
- F17C2250/072—Action when predefined value is reached
- F17C2250/075—Action when predefined value is reached when full
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2260/00—Purposes of gas storage and gas handling
- F17C2260/02—Improving properties related to fluid or fluid transfer
- F17C2260/024—Improving metering
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2270/00—Applications
- F17C2270/05—Applications for industrial use
- F17C2270/0509—"Dewar" vessels
Definitions
- the field of cryogenics requires liquefied gases when conducting experiments and observations.
- the two types of liquefied gases used in most cryogenic applications are liquid helium and liquid nitrogen (LN2).
- LN2 liquid helium and liquid nitrogen
- Dewar flasks special containers known as Dewar flasks (Dewars) are used.
- the Dewars used are generally about six feet tall and three feet in diameter.
- the Dewar is designed to provide very good thermal insulation.
- a pressure relief valve is provided to prevent pressure from building up.
- the excellent insulation of the Dewar results in the LN2 lasting a long time without the need for expensive refrigeration equipment.
- determining when the Dewar is full is a difficult task that requires constant monitoring.
- the LN2 will continue to pour out of a relief vent and is wasted. This waste of LN2 is expensive and dangerous. Inhaling LN2 causes minor to severe breathing difficulty, which is a safety hazard to cryogenic lab personnel. Additionally, determining the level of remaining LN2 is difficult when traditional level gauges are mounted on top of the Dewar. While in use, the top of the Dewar is often covered with frost, rendering the gauge difficult to read and subject to measurement inaccuracies.
- a method for filling a pressurized container involves automatically adjusting a shutoff valve between a supply of a pressurized medium and the pressurized container based on a weight of the pressurized medium contained in the pressurized container.
- an apparatus for metering a supply of liquefied gas to a liquefied gas container includes means for determining a current weight of the liquefied gas container and means, associated with the means for determining, for allowing liquefied gas to enter the liquefied gas container.
- the apparatus further includes means, associated with the means for determining and the means for allowing, for indicating a current level of liquefied gas contained in the liquefied gas container.
- a liquefied gas containment system in yet another embodiment, includes a Dewar tank mounted on a scale and seated within a mobile base, an intake and relief valve assembly mounted on top of the Dewar tank and coupled to a main fill line, a shutoff valve coupled between the main fill line and a removable feed line, and a scale linkage connecting the scale and the shutoff valve.
- the system further includes wherein the scale linkage adjusts one or more positions of the shutoff valve based on an amount of the liquefied gas detected in the Dewar tank by the scale.
- a method for maintaining a level of pressurized medium in a pressurized container involves establishing a starting level reading by indicating with a level readout that the pressurized container does not contain a substantial amount of the pressurized medium.
- the method involves adjusting a shutoff valve as an increase in weight of the pressurized container is detected.
- the method further involves adjusting a current level reading on the level readout.
- the method still further involves automatically closing the shutoff valve. The method concludes as the pressurized medium is removed from the pressurized container, and the level readout is updated to indicate an adjusted level based on a current weight of the pressurized container.
- FIG. 1 is a block diagram of an embodiment of a liquefied gas containment system in accordance with the present invention
- FIG. 2 is a block diagram of another embodiment of a liquefied gas containment system in accordance with the present invention.
- FIG. 3 is a flow diagram illustrating an embodiment of a method for filling a liquefied gas container in accordance with the present invention.
- Embodiments of the present invention address problems with filling a liquefied gas container.
- a method for filling a pressurized container is provided. The method involves automatically adjusting a shutoff valve between a supply of a pressurized medium and the pressurized container based on a weight of the pressurized medium contained in the pressurized container.
- embodiments of the present invention are not limited to liquefied gas containment and metering. Embodiments of the present invention are applicable to any gas containment and metering activity that requires continuous knowledge of an amount of a gaseous element filling a container, and automatically discontinuing a filling of the gaseous element into the container once a desired level is reached.
- Alternate embodiments of the present invention utilize an automatic Dewar LN2 supply shutoff and metering system incorporating at least a scale and a shutoff valve linked together. The system is adapted for use with Dewars of different capacities.
- a gauge mechanism accurately records a remaining level of LN2 in the Dewar at all times.
- the entire system is suited for placement on a mobile base.
- FIG. 1 is a block diagram of an embodiment of a liquefied gas containment system, indicated generally at 100 , according to the teachings of the present invention.
- System 100 comprises Dewar tank 102 , mobile base 104 , and scale 106 .
- Dewar tank 102 further comprises intake and relief valve assembly 132 , mounted on top of Dewar tank 102 and mechanically coupled to an outlet end of overhead fill line 130 .
- An inlet end of overhead fill line 130 is mechanically coupled to an outlet end of main fill line 126 by main fill line outlet coupler 128 .
- main fill line outlet coupler 128 is provided so that one or more lengths of overhead fill line 130 are adaptable for use in system 100 .
- main fill line 126 is mechanically coupled to an outlet end of shutoff valve 120 by shutoff valve outlet coupler 124 .
- the inlet end of main fill line 126 is constructed of a flexible component. The flexible component allows one or more Dewar tanks of varying heights to be incorporated within system 100 .
- Feed line 112 is mechanically coupled to an inlet end of shutoff valve 120 by shutoff valve inlet coupler 122 .
- feed line 112 supplies a liquefied gas to system 100 from a main liquefied gas supply (not shown).
- the liquefied gas supplied to system 100 consists of one of liquefied nitrogen, liquefied helium, or the like.
- Dewar tank 102 is secured on scale 106 by at least one tank latch 116 . Moreover, the at least one tank latch 116 is mechanically mounted on top of scale 106 .
- Scale 106 is seated within mobile base 104 with scale seat mounts 107 1 to 107 4 .
- mobile base 104 is constructed with raised sides to prevent a combination of Dewar tank 102 and scale 106 from sliding off. It is noted that for simplicity in description, scale seat mounts 107 1 and 107 4 are shown in FIG. 1 . However, it is understood that scale 106 is seated on each of scale seat mounts 107 1 to 107 4 within mobile base 104 .
- Mobile base 104 further includes mobile base wheels 108 1 to 108 4 .
- mobile/base wheels 108 1 and 108 4 are shown in FIG. 1 . However, it is understood that each of mobile base wheels 108 1 to 108 4 are affixed to a bottom side of mobile base 104 . In one embodiment, the use of each of mobile base wheels 108 1 to 108 4 allows mobile base 104 to transport system 100 to any necessary and convenient location along surface 110 .
- Scale 106 further includes adjustment knob 114 and scale linkage 134 .
- Adjustment knob 114 is used to tare, or determine a weight of, an empty Dewar tank 102 .
- the tare value of the empty Dewar tank 102 is used in the operation of system 100 , as further described below.
- Including adjustment knob 114 allows the use of one or more Dewar tanks with varying dimensions, e.g. of one or more tare values.
- scale linkage 134 provides a mechanical link between scale 106 and shutoff valve 120 .
- scale linkage 134 places shutoff valve 120 in an open position once scale 106 is tared for the weight of the empty Dewar tank 102 .
- scale linkage 134 is mechanically coupled to level gauge link 136 .
- level gauge link 136 provides an analog measurement to level gauge 118 . The operation of level gauge 118 is further described below.
- adjustment knob 114 is adjusted until a starting reading of scale 106 is substantially equal to the weight of Dewar tank 102 when Dewar tank 102 does not contain a substantial amount of liquefied gas.
- scale linkage 134 is adjusted to an initial starting position so that a final reading of scale 106 , e.g., a reading of scale 106 when Dewar tank 102 is filled with liquefied gas, will position shutoff valve 120 in a closed position.
- current valve positions of shutoff valve 120 will be maintained by current positions of scale linkage 134 .
- Scale linkage 134 is adjusted to position shutoff valve 120 in a fully-open position prior to operation.
- feed line 112 is attached to shutoff valve 120 with shutoff valve inlet coupler 122 .
- a liquefied gas is supplied to system 100 by feed line 112 .
- the liquefied gas As the liquefied gas enters system 100 , the liquefied gas is transported through main fill line 126 and overhead fill line 128 .
- the liquefied gas enters Dewar tank 102 through intake and relief valve assembly 132 .
- scale 106 begins to detect an increase in weight of Dewar tank 102 .
- the increased weight of Dewar tank 102 causes scale 106 to automatically adjust a current position of scale linkage 134 .
- An adjusted position of scale linkage 134 begins closing shutoff valve 120 .
- the adjusted position of scale linkage 134 adjusts a current position of level gauge link 136 .
- an adjusted position of level gauge link 136 changes a current reading of level gauge 118 .
- the current reading of level gauge 118 indicates an increase in the amount of liquefied gas, i.e. a current level, present in Dewar tank 102 .
- scale linkage 134 is continually repositioned, adjusting shutoff valve 120 closer to the closed position.
- scale linkage 134 is in a final position and places shutoff valve 120 in the closed position. Once shutoff valve 120 is in the closed position, shutoff valve 120 is prevented from automatically re-opening.
- the final position of scale linkage 134 adjusts level gauge link 136 to change the current reading of level gauge 118 to indicate that Dewar tank 102 is filled with the liquefied gas.
- level gauge link 136 and scale linkage 134 remain in operation once system 100 is disconnected from feed line 112 .
- level gauge 118 continues to provide an indication of the current level of liquefied gas remaining in Dewar tank 102 .
- feed line 112 is removed from system 100 .
- System 100 is capable of being transported via mobile base 104 .
- scale 106 will record a decrease in weight of Dewar tank 102 .
- level gauge link 136 adjusts the current reading of level gauge 118 .
- Level gauge 118 will indicate a decrease in the amount of liquefied gas present in Dewar tank 102 .
- FIG. 2 is a block diagram of another embodiment of a liquefied gas containment system, indicated generally at 200 , according to the teachings of the present invention.
- System 200 comprises the same Dewar tank 102 , mobile base 104 , and scale 106 as indicated above in FIG. 1 .
- system 200 is identical in every respect to system 100 except that scale linkage 134 , level gauge link 136 , and level gauge 118 are replaced by control unit 202 and level meter 208 .
- control unit 202 comprises valve control interface 204 and level meter interface 206 .
- Valve control interface 204 is electrically coupled to shutoff valve 120 .
- valve control interface 204 is an electrical interface that controls the operation of shutoff valve 120 based on instructions received from control unit 202 .
- Level meter interface 206 is communicatively coupled to level meter 208 .
- level meter 208 comprises an electronic readout to indicate a current level of liquefied gas in Dewar tank 102 . The electronic readout is updated with digital measurements received from level meter interface 206 regarding the current level of liquefied gas in Dewar tank 102 .
- adjustment knob 114 is adjusted so that a starting reading of scale 106 is substantially equal to the weight of Dewar tank 102 when Dewar tank 102 does not contain a substantial amount of liquefied gas.
- control unit 202 is adjusted so that an end reading of scale 106 , e.g., a reading of scale 106 when Dewar tank 102 is filled with liquefied gas, will position shutoff valve 120 in a closed position.
- current valve positions of shutoff valve 120 will be maintained by valve control interface 204 .
- control unit 202 Prior to operation, control unit 202 is configured to position shutoff valve 120 in a fully open position.
- shutoff valve 120 is adjusted and feed line 112 is attached to system 200 , a liquefied gas is supplied to system 200 by feed line 112 .
- the liquefied gas As the liquefied gas enters system 200 , the liquefied gas is transported as described above with respect to FIG. 1 .
- the increased weight of Dewar tank 102 causes scale 106 to notify control unit 202 of an increase in the weight of Dewar tank 102 .
- the notification provided to control unit 202 is further transferred to valve control interface 204 , which automatically begins closing shutoff valve 120 .
- the increase in the weight of Dewar tank 102 is communicated as a meter reading update to meter interface 206 .
- Level meter 208 receives the meter reading update from meter interface 206 , and the electronic readout of level meter 208 is updated to indicate a current amount of liquefied gas in Dewar tank 102 .
- the current reading of level meter 208 indicates an increase in the amount of liquefied gas present in Dewar tank 102 .
- valve control interface 204 continually adjusts shutoff valve 120 closer to the closed position. At the time when scale 106 detects that Dewar tank 102 is filled with the liquefied gas, valve control interface 204 has placed shutoff valve 120 in the closed position. Once shutoff valve 120 is placed in the fully closed position, valve control interface 204 will no longer change the valve position of shutoff valve 120 . In one embodiment, the closed position of shutoff valve 120 translates to the current reading of level meter 208 to indicate that Dewar tank 102 is filled with the liquefied gas. Moreover, control unit 202 remains in operation once system 100 is disconnected from feed line 112 .
- level meter 208 continues to provide an electronic indication, e.g., digital readout, of the amount of liquefied gas remaining in Dewar tank 102 .
- system 200 is capable of being transported via mobile base 104 .
- scale 106 will record a decrease in weight of Dewar tank 102 .
- control unit 202 adjusts the current reading of level meter 208 .
- Level meter 208 will indicate a decrease in the amount of liquefied gas present in Dewar tank 102 .
- FIG. 3 is a flow diagram illustrating an embodiment of a method, according to the teachings of the present invention, for filling a pressurized container with a pressurized medium.
- the pressurized medium is a one of a gas or a liquid.
- the pressurized medium is a liquefied gas.
- the method of FIG. 3 begins at block 302 . Once the pressurized container is placed into position, the method of FIG. 3 begins.
- the method of FIG. 3 is designed to fill a Dewar tank connected to a liquefied gas supply shutoff and metering system which includes a scale and a shutoff valve linked together.
- the system is capable of accommodating Dewars of different capacities.
- a gauge mechanism accurately records a remaining level of LN2 in the Dewar at all times.
- the entire system is suited for placement on a mobile base.
- the method begins by establishing a starting reading on a scale with a scale linkage before proceeding to block 304 .
- establishing the starting reading on the scale further includes adjusting the scale until the starting reading is substantially equal to a weight of the container when the container does not contain a substantial amount of gas.
- adjusting the scale linkage continues by adjusting the scale linkage to an initial starting position to place a shutoff valve, attached to the liquefied gas container, in a fully open position before proceeding to block 306 .
- adjusting the scale linkage further includes adjusting for a final reading that will place the shutoff valve in a closed position.
- the final reading corresponds to a reading of the scale when the container is filled with the liquefied gas.
- the method attaches a gas feed line to the shutoff valve before proceeding to block 308 .
- the method detects an increase in weight of the container. As the weight of the container increases, adjusting a current position of the scale linkage is adjusted at block 310 . In one embodiment, the current position of the shutoff valve is maintained by a current position of the scale linkage.
- the method concludes by positioning the shutoff valve in a fully closed position and the scale linkage in a final position once the scale detects that the container is substantially filled with the liquefied gas. In one embodiment, the scale linkage is prevented from automatically re-opening the shutoff valve once the shutoff valve is in the fully closed position.
Abstract
A method for filling a pressurized container is provided. The method involves automatically adjusting a shutoff valve between a supply of a pressurized medium and the pressurized container based on a weight of the pressurized medium contained in the pressurized container.
Description
- The field of cryogenics requires liquefied gases when conducting experiments and observations. The two types of liquefied gases used in most cryogenic applications are liquid helium and liquid nitrogen (LN2). In order to store LN2, for example, special containers known as Dewar flasks (Dewars) are used. For practical purposes, the Dewars used are generally about six feet tall and three feet in diameter. The Dewar is designed to provide very good thermal insulation. In the case of storing LN2, the leakage of heat into the extremely cold interior of the flask results in a slow “boiling-off” of the LN2. A pressure relief valve is provided to prevent pressure from building up. The excellent insulation of the Dewar results in the LN2 lasting a long time without the need for expensive refrigeration equipment.
- When filling the Dewar with LN2, determining when the Dewar is full is a difficult task that requires constant monitoring. When the Dewar is overfilled, the LN2 will continue to pour out of a relief vent and is wasted. This waste of LN2 is expensive and dangerous. Inhaling LN2 causes minor to severe breathing difficulty, which is a safety hazard to cryogenic lab personnel. Additionally, determining the level of remaining LN2 is difficult when traditional level gauges are mounted on top of the Dewar. While in use, the top of the Dewar is often covered with frost, rendering the gauge difficult to read and subject to measurement inaccuracies.
- Economics also play a role in the storage of liquefied gases. The ability to provide a readily-available source of liquefied gas improves the chance of successful studies in a cryogenic lab. As stated above, the loss of LN2 when filling Dewars using traditional means results in an accelerated consumption of purchased liquefied gas. Working environments, such as lab size, often result in multiple Dewars operating in more than one area at any given time. Further, each Dewar requires individual servicing and monitoring.
- For the reasons stated above and for other reasons stated below which will become apparent to those skilled in the art upon reading and understanding the present application, there is a need in the art for an improved method for filling a liquefied gas container.
- Embodiments of the present invention address problems with gas metering and containment and will be understood by reading and studying the following specification. In one embodiment, a method for filling a pressurized container is provided. The method involves automatically adjusting a shutoff valve between a supply of a pressurized medium and the pressurized container based on a weight of the pressurized medium contained in the pressurized container.
- In another embodiment, an apparatus for metering a supply of liquefied gas to a liquefied gas container is provided. The apparatus includes means for determining a current weight of the liquefied gas container and means, associated with the means for determining, for allowing liquefied gas to enter the liquefied gas container The apparatus further includes means, associated with the means for determining and the means for allowing, for indicating a current level of liquefied gas contained in the liquefied gas container.
- In yet another embodiment, a liquefied gas containment system is provided. The system includes a Dewar tank mounted on a scale and seated within a mobile base, an intake and relief valve assembly mounted on top of the Dewar tank and coupled to a main fill line, a shutoff valve coupled between the main fill line and a removable feed line, and a scale linkage connecting the scale and the shutoff valve. The system further includes wherein the scale linkage adjusts one or more positions of the shutoff valve based on an amount of the liquefied gas detected in the Dewar tank by the scale.
- In still another embodiment, a method for maintaining a level of pressurized medium in a pressurized container is provided. The method involves establishing a starting level reading by indicating with a level readout that the pressurized container does not contain a substantial amount of the pressurized medium. As the pressurized medium enters the pressurized container, the method involves adjusting a shutoff valve as an increase in weight of the pressurized container is detected. As the weight of the pressurized container increases, the method further involves adjusting a current level reading on the level readout. Once the pressurized container is substantially filled with the pressurized medium, the method still further involves automatically closing the shutoff valve. The method concludes as the pressurized medium is removed from the pressurized container, and the level readout is updated to indicate an adjusted level based on a current weight of the pressurized container.
-
FIG. 1 is a block diagram of an embodiment of a liquefied gas containment system in accordance with the present invention; -
FIG. 2 is a block diagram of another embodiment of a liquefied gas containment system in accordance with the present invention; and -
FIG. 3 is a flow diagram illustrating an embodiment of a method for filling a liquefied gas container in accordance with the present invention. - In the following detailed description, reference is made to the accompanying drawings that form a part hereof, and in which is shown by way of illustration specific illustrative embodiments in which the invention may be practiced. These embodiments are described in sufficient detail to enable those skilled in the art to practice the invention, and it is to be understood that other embodiments may be utilized and that logical, mechanical and electrical changes may be made without departing from the spirit and scope of the present invention. The following detailed description is, therefore, not to be taken in a limiting sense.
- Embodiments of the present invention address problems with filling a liquefied gas container. Particularly, in one embodiment, a method for filling a pressurized container is provided. The method involves automatically adjusting a shutoff valve between a supply of a pressurized medium and the pressurized container based on a weight of the pressurized medium contained in the pressurized container.
- Although the examples of embodiments in this specification are described in terms of liquefied gas containment and metering, embodiments of the present invention are not limited to liquefied gas containment and metering. Embodiments of the present invention are applicable to any gas containment and metering activity that requires continuous knowledge of an amount of a gaseous element filling a container, and automatically discontinuing a filling of the gaseous element into the container once a desired level is reached. Alternate embodiments of the present invention utilize an automatic Dewar LN2 supply shutoff and metering system incorporating at least a scale and a shutoff valve linked together. The system is adapted for use with Dewars of different capacities. In addition, a gauge mechanism accurately records a remaining level of LN2 in the Dewar at all times. Moreover, the entire system is suited for placement on a mobile base.
-
FIG. 1 is a block diagram of an embodiment of a liquefied gas containment system, indicated generally at 100, according to the teachings of the present invention.System 100 comprises Dewartank 102,mobile base 104, andscale 106. Dewartank 102 further comprises intake andrelief valve assembly 132, mounted on top of Dewartank 102 and mechanically coupled to an outlet end ofoverhead fill line 130. An inlet end ofoverhead fill line 130 is mechanically coupled to an outlet end ofmain fill line 126 by main fillline outlet coupler 128. In one embodiment, main fillline outlet coupler 128 is provided so that one or more lengths ofoverhead fill line 130 are adaptable for use insystem 100. Accommodating one or more lengths ofoverhead fill line 130 allows one or more Dewar tanks of varying diameters to be incorporated withinsystem 100. An inlet end ofmain fill line 126 is mechanically coupled to an outlet end ofshutoff valve 120 by shutoffvalve outlet coupler 124. In one embodiment, the inlet end ofmain fill line 126 is constructed of a flexible component. The flexible component allows one or more Dewar tanks of varying heights to be incorporated withinsystem 100.Feed line 112 is mechanically coupled to an inlet end ofshutoff valve 120 by shutoffvalve inlet coupler 122. In one embodiment,feed line 112 supplies a liquefied gas tosystem 100 from a main liquefied gas supply (not shown). Moreover, the liquefied gas supplied tosystem 100 consists of one of liquefied nitrogen, liquefied helium, or the like. - In one embodiment,
Dewar tank 102 is secured onscale 106 by at least onetank latch 116. Moreover, the at least onetank latch 116 is mechanically mounted on top ofscale 106.Scale 106 is seated withinmobile base 104 with scale seat mounts 107 1 to 107 4. In one embodiment,mobile base 104 is constructed with raised sides to prevent a combination ofDewar tank 102 and scale 106 from sliding off. It is noted that for simplicity in description, scale seat mounts 107 1 and 107 4 are shown inFIG. 1 . However, it is understood thatscale 106 is seated on each of scale seat mounts 107 1 to 107 4 withinmobile base 104.Mobile base 104 further includes mobile base wheels 108 1 to 108 4. It is noted that for simplicity in description, mobile/base wheels 108 1 and 108 4 are shown inFIG. 1 . However, it is understood that each of mobile base wheels 108 1 to 108 4 are affixed to a bottom side ofmobile base 104. In one embodiment, the use of each of mobile base wheels 108 1 to 108 4 allowsmobile base 104 to transportsystem 100 to any necessary and convenient location alongsurface 110. -
Scale 106 further includesadjustment knob 114 andscale linkage 134.Adjustment knob 114 is used to tare, or determine a weight of, anempty Dewar tank 102. The tare value of theempty Dewar tank 102 is used in the operation ofsystem 100, as further described below. Includingadjustment knob 114 allows the use of one or more Dewar tanks with varying dimensions, e.g. of one or more tare values. In one embodiment,scale linkage 134 provides a mechanical link betweenscale 106 andshutoff valve 120. Moreover,scale linkage 134places shutoff valve 120 in an open position oncescale 106 is tared for the weight of theempty Dewar tank 102. In another embodiment,scale linkage 134 is mechanically coupled tolevel gauge link 136. Moreover,level gauge link 136 provides an analog measurement tolevel gauge 118. The operation oflevel gauge 118 is further described below. - Prior to operation,
adjustment knob 114 is adjusted until a starting reading ofscale 106 is substantially equal to the weight ofDewar tank 102 whenDewar tank 102 does not contain a substantial amount of liquefied gas. In one embodiment, once the starting reading ofscale 106 is established,scale linkage 134 is adjusted to an initial starting position so that a final reading ofscale 106, e.g., a reading ofscale 106 whenDewar tank 102 is filled with liquefied gas, will positionshutoff valve 120 in a closed position. Moreover, current valve positions ofshutoff valve 120 will be maintained by current positions ofscale linkage 134.Scale linkage 134 is adjusted to positionshutoff valve 120 in a fully-open position prior to operation. In one embodiment, oncescale linkage 134 is adjusted,feed line 112 is attached toshutoff valve 120 with shutoffvalve inlet coupler 122. Next, a liquefied gas is supplied tosystem 100 byfeed line 112. As the liquefied gas enterssystem 100, the liquefied gas is transported throughmain fill line 126 andoverhead fill line 128. Eventually, the liquefied gas entersDewar tank 102 through intake andrelief valve assembly 132. As the liquefied gas begins to fillDewar tank 102,scale 106 begins to detect an increase in weight ofDewar tank 102. In one embodiment, the increased weight ofDewar tank 102 causes scale 106 to automatically adjust a current position ofscale linkage 134. An adjusted position ofscale linkage 134 begins closingshutoff valve 120. In one embodiment, the adjusted position ofscale linkage 134 adjusts a current position oflevel gauge link 136. Moreover, an adjusted position of level gauge link 136 changes a current reading oflevel gauge 118. In the case of an increase in weight ofDewar tank 102, the current reading oflevel gauge 118 indicates an increase in the amount of liquefied gas, i.e. a current level, present inDewar tank 102. - As additional liquefied gas enters
system 100,scale linkage 134 is continually repositioned, adjustingshutoff valve 120 closer to the closed position. At a time whenscale 106 detects thatDewar tank 102 is substantially filled with the liquefied gas,scale linkage 134 is in a final position and placesshutoff valve 120 in the closed position. Onceshutoff valve 120 is in the closed position,shutoff valve 120 is prevented from automatically re-opening. In one embodiment, the final position ofscale linkage 134 adjustslevel gauge link 136 to change the current reading oflevel gauge 118 to indicate thatDewar tank 102 is filled with the liquefied gas. Moreover,level gauge link 136 andscale linkage 134 remain in operation oncesystem 100 is disconnected fromfeed line 112. Further,level gauge 118 continues to provide an indication of the current level of liquefied gas remaining inDewar tank 102. In one embodiment, onceDewar tank 102 is filled,feed line 112 is removed fromsystem 100.System 100 is capable of being transported viamobile base 104. As the liquefied gas is used,scale 106 will record a decrease in weight ofDewar tank 102. In response,level gauge link 136 adjusts the current reading oflevel gauge 118.Level gauge 118 will indicate a decrease in the amount of liquefied gas present inDewar tank 102. - Filling a Dewar tank with liquefied gas using the automated shutoff and metering mechanism described above eliminates a need for constant manual monitoring of a fill operation. The fill operation is started and proceeds without additional intervention required. The amount of liquefied gas used to fill the Dewar tank is never over-exceeded. Further, the addition of a level gauge near the bottom of the Dewar tank provides constant indication of the amount of liquefied gas remaining in the Dewar tank. The placement of the level gauge near the bottom of the tank eliminates difficulties in reading the gauge under conditions of frost accumulation on the top of the Dewar tank.
-
FIG. 2 is a block diagram of another embodiment of a liquefied gas containment system, indicated generally at 200, according to the teachings of the present invention.System 200 comprises thesame Dewar tank 102,mobile base 104, and scale 106 as indicated above inFIG. 1 . In one embodiment,system 200 is identical in every respect tosystem 100 except thatscale linkage 134,level gauge link 136, andlevel gauge 118 are replaced bycontrol unit 202 andlevel meter 208. Moreover,control unit 202 comprisesvalve control interface 204 andlevel meter interface 206.Valve control interface 204 is electrically coupled toshutoff valve 120. In one embodiment,valve control interface 204 is an electrical interface that controls the operation ofshutoff valve 120 based on instructions received fromcontrol unit 202.Level meter interface 206 is communicatively coupled tolevel meter 208. In one embodiment,level meter 208 comprises an electronic readout to indicate a current level of liquefied gas inDewar tank 102. The electronic readout is updated with digital measurements received fromlevel meter interface 206 regarding the current level of liquefied gas inDewar tank 102. - In operation similar to that described with respect to
FIG. 1 above,adjustment knob 114 is adjusted so that a starting reading ofscale 106 is substantially equal to the weight ofDewar tank 102 whenDewar tank 102 does not contain a substantial amount of liquefied gas. In one embodiment, once the starting reading ofscale 106 is established,control unit 202 is adjusted so that an end reading ofscale 106, e.g., a reading ofscale 106 whenDewar tank 102 is filled with liquefied gas, will positionshutoff valve 120 in a closed position. Moreover, current valve positions ofshutoff valve 120 will be maintained byvalve control interface 204. Prior to operation,control unit 202 is configured to positionshutoff valve 120 in a fully open position. Onceshutoff valve 120 is adjusted andfeed line 112 is attached tosystem 200, a liquefied gas is supplied tosystem 200 byfeed line 112. As the liquefied gas enterssystem 200, the liquefied gas is transported as described above with respect toFIG. 1 . In one embodiment, the increased weight ofDewar tank 102 causes scale 106 to notifycontrol unit 202 of an increase in the weight ofDewar tank 102. The notification provided to controlunit 202 is further transferred tovalve control interface 204, which automatically begins closingshutoff valve 120. In one embodiment, the increase in the weight ofDewar tank 102 is communicated as a meter reading update tometer interface 206.Level meter 208 receives the meter reading update frommeter interface 206, and the electronic readout oflevel meter 208 is updated to indicate a current amount of liquefied gas inDewar tank 102. In the case of an increase in weight ofDewar tank 102, the current reading oflevel meter 208 indicates an increase in the amount of liquefied gas present inDewar tank 102. - As additional liquefied gas enters
system 200,valve control interface 204 continually adjustsshutoff valve 120 closer to the closed position. At the time whenscale 106 detects thatDewar tank 102 is filled with the liquefied gas,valve control interface 204 has placedshutoff valve 120 in the closed position. Onceshutoff valve 120 is placed in the fully closed position,valve control interface 204 will no longer change the valve position ofshutoff valve 120. In one embodiment, the closed position ofshutoff valve 120 translates to the current reading oflevel meter 208 to indicate thatDewar tank 102 is filled with the liquefied gas. Moreover,control unit 202 remains in operation oncesystem 100 is disconnected fromfeed line 112. Further,level meter 208 continues to provide an electronic indication, e.g., digital readout, of the amount of liquefied gas remaining inDewar tank 102. Similar to the embodiment described above with respect toFIG. 1 ,system 200 is capable of being transported viamobile base 104. As the liquefied gas is used,scale 106 will record a decrease in weight ofDewar tank 102. In response,control unit 202 adjusts the current reading oflevel meter 208.Level meter 208 will indicate a decrease in the amount of liquefied gas present inDewar tank 102. -
FIG. 3 is a flow diagram illustrating an embodiment of a method, according to the teachings of the present invention, for filling a pressurized container with a pressurized medium. In one embodiment, the pressurized medium is a one of a gas or a liquid. In a similar embodiment, the pressurized medium is a liquefied gas. The method ofFIG. 3 begins atblock 302. Once the pressurized container is placed into position, the method ofFIG. 3 begins. In one embodiment, the method ofFIG. 3 is designed to fill a Dewar tank connected to a liquefied gas supply shutoff and metering system which includes a scale and a shutoff valve linked together. The system is capable of accommodating Dewars of different capacities. In addition, a gauge mechanism accurately records a remaining level of LN2 in the Dewar at all times. Moreover, the entire system is suited for placement on a mobile base. - At
block 302, the method begins by establishing a starting reading on a scale with a scale linkage before proceeding to block 304. In one embodiment, establishing the starting reading on the scale further includes adjusting the scale until the starting reading is substantially equal to a weight of the container when the container does not contain a substantial amount of gas. - At
block 304, the method continues by adjusting the scale linkage to an initial starting position to place a shutoff valve, attached to the liquefied gas container, in a fully open position before proceeding to block 306. In one embodiment, adjusting the scale linkage further includes adjusting for a final reading that will place the shutoff valve in a closed position. Moreover, the final reading corresponds to a reading of the scale when the container is filled with the liquefied gas. - At
block 306, the method attaches a gas feed line to the shutoff valve before proceeding to block 308. Atblock 308, as liquefied gas enters the container, the method detects an increase in weight of the container. As the weight of the container increases, adjusting a current position of the scale linkage is adjusted atblock 310. In one embodiment, the current position of the shutoff valve is maintained by a current position of the scale linkage. Atblock 312, the method concludes by positioning the shutoff valve in a fully closed position and the scale linkage in a final position once the scale detects that the container is substantially filled with the liquefied gas. In one embodiment, the scale linkage is prevented from automatically re-opening the shutoff valve once the shutoff valve is in the fully closed position. - Although specific embodiments have been illustrated and described herein, it will be appreciated by those of ordinary skill in the art that any arrangement, which is calculated to achieve the same purpose, may be substituted for the specific embodiment shown. This application is intended to cover any adaptations or variations of the present invention. Therefore, it is manifestly intended that this invention be limited only by the following claims and the equivalents thereof.
Claims (26)
1. A method for filling a pressurized container, the method comprising:
automatically adjusting a shutoff valve between a supply of a pressurized medium and the pressurized container based on a weight of the pressurized medium contained in the pressurized container.
2. The method of claim 1 , wherein the pressurized medium is one of a gas or a liquid.
3. The method of claim 1 , wherein automatically adjusting the shutoff valve further comprises:
establishing a starting reading on a scale with a scale linkage positioned to place the shutoff valve in a fully open position;
adjusting a current position of the scale linkage as the weight of the pressurized container increases; and
once the scale detects that the thermal container is substantially filled with the pressurized medium, positioning the shutoff valve in a fully closed position and the scale linkage in a final position.
4. The method of claim 3 , wherein establishing the starting reading on the scale further comprises taring the scale until the starting reading is substantially equal to a weight of the thermal container when the pressurized container does not contain a substantial amount of the pressurized medium.
5. The method of claim 3 , wherein adjusting a current position of the scale linkage further comprises adjusting a current position of the shutoff valve.
6. The method of claim 3 , wherein the shutoff valve is prevented from automatically re-opening once the shutoff valve is in the fully closed position.
7. An apparatus for metering a supply of liquefied gas to a liquefied gas container, the apparatus comprising:
means for determining a current weight of the liquefied gas container;
means, associated with the means for determining, for allowing liquefied gas to enter the liquefied gas container; and
means, associated with the means for determining and the means for allowing, for indicating a current level of liquefied gas contained in the liquefied gas container.
8. The apparatus of claim 7 , wherein the means for determining a current weight further comprises a scale with adjustments for liquefied gas containers of varying dimensions.
9. The apparatus of claim 7 , wherein the means for allowing liquefied gas to enter the liquefied gas container further comprises a shutoff valve mechanically linked to the means for determining the current weight.
10. The apparatus of claim 7 , wherein the means for allowing liquefied gas to enter the liquefied gas container further comprises a shutoff valve electrically linked to the means for determining the current weight.
11. The apparatus of claim 7 , wherein the means for indicating a current level of liquefied gas further comprises one of a mechanical level gauge and an electronic level meter.
12. A liquefied gas containment system, comprising:
a Dewar tank mounted on a scale and seated within a mobile base;
an intake and relief valve assembly mounted on top of the Dewar tank and coupled to a main fill line;
a shutoff valve coupled between the main fill line and a removable feed line;
a scale linkage connecting the scale and the shutoff valve; and
wherein the scale linkage adjusts one or more positions of the shutoff valve based on an amount of the liquefied gas detected in the Dewar tank by the scale.
13. The system of claim 12 , wherein an inlet end of the main fill line is adjustable.
14. The system of claim 12 , wherein the scale linkage maintains a current position of the shutoff valve once the removable feed line is disconnected from the Dewar tank.
15. The system of claim 12 , wherein the scale linkage is a mechanical linkage between the scale and the shutoff valve.
16. The system of claim 15 , wherein the mechanical linkage further comprises a level gauge link coupled to a level gauge readout.
17. The system of claim 16 , wherein the level gauge readout records a current level of liquefied gas in the Dewar tank.
18. The system of claim 12 , wherein the scale linkage is an electrical linkage between the scale and the shutoff valve.
19. The system of claim 18 , wherein the electrical linkage further comprises a level meter interface coupled to an electronic level readout.
20. The system of claim 19 , wherein the electronic level readout records a current level of liquefied gas in the Dewar tank.
21. A method for maintaining a level of pressurized medium in a pressurized container, the method comprising:
establishing a starting level reading by indicating with a level readout that the pressurized container does not contain a substantial amount of the pressurized medium;
as the pressurized medium enters the pressurized container, adjusting a shutoff valve as an increase in weight of the pressurized container is detected;
as the weight of the pressurized container increases, adjusting a current level reading on the level readout;
once the pressurized container is substantially filled with the pressurized medium, automatically closing the shutoff valve; and
as the pressurized medium is removed from the pressurized container, updating the level readout to indicate an adjusted level based on a current weight of the pressurized container.
22. The method of claim 21 , wherein the pressurized medium is one of a gas or a liquid.
23. The method of claim 21 , wherein establishing the starting level reading further comprises mounting the pressurized container on a scale.
24. The method of claim 23 , wherein mounting the pressurized container on the scale further comprises adjusting the scale until the starting reading is substantially equal to a weight of the container when the pressurized container does not contain a substantial amount of the pressurized medium.
25. The method of claim 21 , wherein the level readout is a digital measurement of the current level reading, indicated by an electronic readout.
26. The method of claim 21 , wherein the level readout is an analog measurement of the current level reading, indicated by a level gauge readout.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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US11/325,761 US20070151621A1 (en) | 2006-01-05 | 2006-01-05 | Automatic shutoff and metering device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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US11/325,761 US20070151621A1 (en) | 2006-01-05 | 2006-01-05 | Automatic shutoff and metering device |
Publications (1)
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US20070151621A1 true US20070151621A1 (en) | 2007-07-05 |
Family
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US11/325,761 Abandoned US20070151621A1 (en) | 2006-01-05 | 2006-01-05 | Automatic shutoff and metering device |
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US6609381B1 (en) * | 2002-05-16 | 2003-08-26 | Louis A. Morgan | Controlled fill station for delivery of a measured amount of cryogenic gas to a cylinder |
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US3636994A (en) * | 1969-03-14 | 1972-01-25 | Aga Ab | Pneumatic control device |
US3727651A (en) * | 1971-03-17 | 1973-04-17 | R Biever | Portable high volume gas supply system |
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