US3807422A - Charging sequence system and process - Google Patents

Charging sequence system and process Download PDF

Info

Publication number
US3807422A
US3807422A US32964273A US3807422A US 3807422 A US3807422 A US 3807422A US 32964273 A US32964273 A US 32964273A US 3807422 A US3807422 A US 3807422A
Authority
US
United States
Prior art keywords
pressure
container
gas
valve
containers
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
Inventor
Jones R Mc
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority to US3719196D priority Critical patent/US3719196A/en
Priority to DE19712121328 priority patent/DE2121328A1/en
Priority to GB1336571A priority patent/GB1335254A/en
Priority to FR7116193A priority patent/FR2091237A5/fr
Priority to US29597672 priority patent/US3837377A/en
Application filed by Individual filed Critical Individual
Priority to US32964273 priority patent/US3807422A/en
Application granted granted Critical
Publication of US3807422A publication Critical patent/US3807422A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17DPIPE-LINE SYSTEMS; PIPE-LINES
    • F17D1/00Pipe-line systems
    • F17D1/02Pipe-line systems for gases or vapours
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17BGAS-HOLDERS OF VARIABLE CAPACITY
    • F17B1/00Gas-holders of variable capacity
    • F17B1/02Details
    • F17B1/12Gas admission or discharge arrangements
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C13/00Details of vessels or of the filling or discharging of vessels
    • F17C13/04Arrangement or mounting of valves
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C13/00Details of vessels or of the filling or discharging of vessels
    • F17C13/12Arrangements or mounting of devices for preventing or minimising the effect of explosion ; Other safety measures
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C5/00Methods or apparatus for filling containers with liquefied, solidified, or compressed gases under pressures
    • F17C5/002Automated filling apparatus
    • F17C5/007Automated filling apparatus for individual gas tanks or containers, e.g. in vehicles
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17DPIPE-LINE SYSTEMS; PIPE-LINES
    • F17D1/00Pipe-line systems
    • F17D1/02Pipe-line systems for gases or vapours
    • F17D1/04Pipe-line systems for gases or vapours for distribution of gas
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2227/00Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
    • F17C2227/04Methods for emptying or filling
    • F17C2227/043Methods for emptying or filling by pressure cascade
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T137/00Fluid handling
    • Y10T137/0318Processes
    • Y10T137/0324With control of flow by a condition or characteristic of a fluid
    • Y10T137/0379By fluid pressure
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T137/00Fluid handling
    • Y10T137/2496Self-proportioning or correlating systems
    • Y10T137/2559Self-controlled branched flow systems
    • Y10T137/2562Dividing and recombining
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T137/00Fluid handling
    • Y10T137/2496Self-proportioning or correlating systems
    • Y10T137/2559Self-controlled branched flow systems
    • Y10T137/2564Plural inflows
    • Y10T137/2567Alternate or successive inflows
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T137/00Fluid handling
    • Y10T137/2496Self-proportioning or correlating systems
    • Y10T137/2559Self-controlled branched flow systems
    • Y10T137/265Plural outflows
    • Y10T137/2668Alternately or successively substituted outflow
    • Y10T137/2693Pressure responsive
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T137/00Fluid handling
    • Y10T137/4673Plural tanks or compartments with parallel flow
    • Y10T137/469Sequentially filled and emptied [e.g., holding type]

Definitions

  • the present invention relates in general to the art of charging and withdrawing gas from containers. More specifically, the present invention relates to a charging level of the pollutants of carbon monoxide, oxides of nitrogen and hydrocarbons over the emission levels experienced by gasoline.
  • Natural gas for use as a fuel in internal combustion engines can be stored in vehicles as a gas in suitable containers, often referred to as tanks or bottles. Typically, presently available tanks are rated at 2,265 p.s.i. at standard temperature conditions.
  • a specific form of the present invention contemplates a source of pressurized gas which may include a compressor, a series of containers to be charged, and sequence fill and transfer valve means for each container.
  • the sequencer valve means each has a fill position and a transfer position.
  • Means is provided for maintaining each sequencer valve means in its fill position and in communication with its container below a pre- I determined pressure, typically the rated pressure of the containers.
  • Means is also provided for each sequencer valve means to change the valves position from its fill position to its transfer position in response to the predetermined pressure existing in its associated container and to then establish communication between a downstream valve and the gas source.
  • Means is also provided to prevent gas communication between a container and the source of pressurized gas when another container is being charged.
  • each sequencer valve means control the flow of gas from the source of pressurized gas to succeeding containers in a series of containers by preventing gas communication beyond the valve means admitting to gas flow to its container. This may be done by connecting the source of gas to the containers in series through the sequencer valve means and providing each sequencer valve means with meansfor preventing gas flow downstream from it when it is admitting to gas flow into its container.
  • the means for maintaining each of the valves in its fill position until a predetermined pressure is reached be temperature compensated in order that utilization of available container volume be maximized.
  • the temperature within a container being charged control the predetermined pressureto compensate for variations in container temperature owing to such factors as ambient temperature.
  • the predetermined pressure would be higher than the rated pressure of the container.
  • the predetermined pressure would be lower than the rated pressure of the container.
  • the present invention also contemplates the selective charging of other vessels or containers from the storage containers by charging from the storage container having the lowest beginning pressure initially and ending at the storage container having the highest beginning initial pressure.
  • a preferred form of the sequencer valve means of the present invention contemplates the combining of the sequencer fill and transfer valve and a transfer sequencer valve.
  • a valve spool for the fill and transfer sequencer valve is disposed in a bore of a housing for translation between a fill position and a transfer position.
  • Inlet means to the bore is provided from an outlet means from the bore of the next sequencer valve upstream and from the source of gas for the first valve.
  • the spool in the fill position masks the outlet means but communicates the particular valves container with the inlet port.
  • the spool prevents communication from the inlet port to the container but allows communication through the valve to the next subsequent sequencer valves inlet.
  • the position of the spool is determined by pressure on a reference pressure side thereof and on a side in direct communication with its associated container such that when container pressure reaches the predetermined value it overcomes the effect of the reference pressure and any biasing means to shift the spool to the transfer position.
  • each valve On the withdrawal side of each valve a draw and bypass spool is provided, the position of which between a draw position and a bypass position is determined by its container pressure and a reference pressure.
  • the reference pressure is the pressure of the tanks receiving gas from the container and, preferably, a biasing spring.
  • the valves container In the bypass position of each valve, the valves container is out of communication with the tanks but the tanks are in communication with the next upstream valve, or the source of gas in the case of the last valve.
  • upstream valves In the draw position of each valve, upstream valves are out of communication with the tanks but the container for the particular valve is in communication with the tanks. As a consequence, the lowest pressure containers will exhaust first.
  • FIG. 1 is a flow sheet illustrating the charging and withdrawal system and process of the present invention.
  • FIG. 2 is a view of the preferred sequential fill limiter and discharge valve assembly of the present invention.
  • FIG. 1 a natural gas compressor is illustrated.
  • This compressor may be of any well known forms and obviously compresses gas from a source at relatively low pressure to some predetermined pressure for discharge into a line 12.
  • a bank of containers or bottles consisting of containers 14, 16 and 18 are in communication with line 12 through respective sequential fill and discharge valves 20, 22 and 24.
  • the containers are connected in series through their respective sequential fill and discharge valves both for their charging and discharge.
  • Each container can, of course, be replaced by two or more containers.
  • container 14 when there is not enough time to bring all the containers up to rated pressure between withdrawals, container 14 will always have a residual pressure before charging in excess of the residual pressure in containers 16 and 18. Similarly, container 16 will have a residual pressure before charging in excess of the pressure existing in container 18. Of course, if there is sufficient charging time between withdrawals, all the containers will be at the same pressure. But for purposes of this discussion it will be assumed that there is insufficient time to bring all the containers up to their rated pressure before withdrawal to a vehicles gas storage tanks.
  • Sequential fill and discharge valve for container 14 controls the flow of gas to downstream containers 16 and 18 such that when container 14 is being charged no gas passes past valve 20 to the downstream containers.
  • sequential fill and discharge valve 24 prevents discharge of gas from containers l4 and 16 until the gas in container 18 is effectively exhausted.
  • sequential fill and discharge valve 22 prevents the withdrawal of gas from container 14 until container 16 is effectively exhausted.
  • each of the valves 20, 22 and 24 has a fill side and a withdrawal side, indicated in FIG. 1 for the fill side by reference numerals 20a, 22a and 24a, and for the withdrawal side by reference numerals 20b, 22b and 24b.
  • valves 20 and 22 are in series gas communication through a line 26.
  • line 12 from the compressor leads directly to the withdrawal side of valve 20 so that when valve 20 is in its draw position gas from the compressor will pass through the valve and through a line 27 to the inlet side of the valve.
  • the fill side of valves 22 and 24 are in series gas communication through a line 28.
  • valves 20 and 22 are in series gas communication through a line 30, and the withdrawal sides of valves 22 and 24 are in series gas communication through a line 32.
  • the withdrawal side of valve 24 leads to the vehicle tanks to be charged through a line 34.
  • the system illustrated in FIG. 1 has a transfer valve 36 in line 34 emanating from the withdrawal side of valve 24 for the initiation of gas withdrawal from the containers.
  • each valve has a fill position and a transfer and off position.
  • Each valve has a valving element, such as a spool, which is positionally responsive to a reference pressure and the particular valves container pressure, such that when the reference pressure exceeds the container pressure the valve is in its fill position and gas can enter the container.
  • the particular valve will go to its transfer and off position.
  • In the transfer position a valve admits to gas flow downstream from it and stops gas flow to its associated cont-' ainer.
  • valve 24 is in its transfer position, gas is recycled through a line 37 back to the compressor inlet, or to a pressure switch which stops the compressor, at the option of the user.
  • the reference pressure is supplied by reference pressure vessels 38, 40 and 42 through lines 44, 46 and 48 for valves 20, 22 and 24, respectively.
  • Gas communication from and to valves 20, 22 and 24 to and from containers 14, 16 and 18 is through lines 50, 52 and 54, respectively.
  • each valve has a container bypass position and container draw position. In the container draw position for a given valve, gas can be drawn from that valves container. In the bypass position for a given valve, gas cannot be withdrawn from its container but only from a container upstream from it, or in the case of valve 20, from compressor 10.
  • each valve has a second valving element, such as a spool, which is positionally responsive from its draw position to its bypass position when container pressure drops below a given valve relative to the pressure in the tanks being charged. Conversely, each valve shifts from its bypass position to its draw position when its container pressure exceeds a given value relative to the pressure in the tanks being charged.
  • the withdrawal side of each of the valves 20, 22 and 24 is in pressure communication with the tanks being charged through parallel branch lines 56, 58 and 60, respectively, all of which are connected to the tanks being charged downstream of transfer valve 36 through a common line 62.
  • valve 22 is identical in construction to valves and 24 and is connected into the system illustrated in FIG. 1 identically, save for minor details to be described subsequently.
  • valve 22 has a housing 64 having aligned bores 66 and 68 which receive fill limiter and transfer spool 70 and a draw and bypass spool 72. Spool 70 is in fill side 22a and spool 72 is in transfer side 22b. The fill side of the valve will be initially described.
  • Line 26 from valve 20 opens into bore 66 for incoming gas and, as such, constitutes an inlet line for the valve.
  • Line 28 also opens into the bore for outgoing gas to valve 24 and, as such, constitutes an outlet line from the valve.
  • a chamber 74 midway between the fill and transfer side of the valve is in communication with container 16 through line 52.
  • a reference pressure chamber 76 is in pressure communication with reference pressure vessel 40 through line 46.
  • Spool 70 is generally cylindrical and has an annular, relatively elongated flow channel 78 bounded by lands 80 and 82'for communicating inlet line 26 with outlet line 28 when the pressure in chamber 74 is sufficient to overcome the pressure in reference chamber 76.
  • An axial passage 84 in spool 70 opens into chamber 74 and is in communication with an annular channel 86 through one or more radial passages 88.
  • Channel 86 is in communication with inlet line 26 in the fill position of the valve, which is the position illustrated in FIG. 2.
  • Means are provided to prevent axial gas flow between the lands of the spool and the wall of the bore such as a pair of O-rings 90.on either axial side of channel 78 and a pair of O-rings 92 on either axial side of channel 86.
  • the reference pressure chamber is in direct communication with reference pressure vessel 40.
  • the latter vessel is in thermal communication with container 16.
  • the pressure in the reference pressure chamber is determined by the temperature of gas within container 116. Because the gas in the reference pressure chamber line 46 and vessel 40 constitutes a closed system, the reference pressure in the chamber is a direct function of temperature. As a consequence, when the temperature in container 16 is relatively high, so will be the pressure in reference pressure chamber 76. The converse is also true.
  • the pressure in vessel 40, acting in chamber 76, is such that during charging spool 70 will shift to its transfer position when the pressure exerted on it from container 16, acting in chamber 74, reaches a predetermined value of, say, 2,265 p.s.i. at 70 F.
  • spool 72 On the withdrawal side of the valve, spool 72 is capable of translation in bore 68 between a draw position and a bypass position.
  • the position illustrated in FIG. 2 is the draw position.
  • Line 32 opens into a transfer chamber 94 and is in direct communication through this chamber with chamber 74 and container 16 when spool 72 is in its draw position.
  • Line' opens into bore 68 and emanates from the transfer chamber of valve 20.
  • spool 72 sees the pressure in the tanks being charged through line 58 which opens into a reference pressure chamber 96.
  • a biasing spring 98 is disposed to act between an end of housing 64 and spool 72 and exerts predetermined biasing pressure on the spool of, say, 50 p.s.i., which tends to move the spool to its bypass position.
  • Spool 72 has an annular bypass channel 100 disposed to bridge the distance between line 30 and a line 101 in the draw position and between lines 30 and 32 to communicate the two in the spools bypass position.
  • Line 101 is blocked in each valve except in valve 20 where it is shown by reference numeral 27.
  • Line 27 leads to the part of valve 20 corresponding to line 26 in FIG. 2.
  • O-rings are provided to prevent leakage of gas from or to the channel along the interface bet ween the spool and the wall of bore 68. These O-rings are indicated by reference numerals 102, 104 and 106 and are disposed in lands 108, 1.10 and 112, respectively.
  • Spool 72 shifts to its bypass position when the pressure in the tanks being charged and biasing spring 98 is sufficient to overcome the pressure within container 16 acting in chamber 74.
  • line 34 leads from the valve at the same location that line 32 leaves valve 22 but goes directly to the tanks being charged.
  • Line 37 leads either to a compressor shutdown device or the compressor inlet when all tanks are filled.
  • the compressor will be in direct communication with line 26 through line 30, channel 100 and line 101. With this communication, the compressor directly charges the vehicles tanks.
  • the spool of valve 20 corresponding to spool 72 will move to the bypass position, dropping container 14 out of fluid circuit.
  • compressor 10 will still be in communication with the vehicles tanks through channel 100 and line 26 (the latter corresponding to line 32 in FIG. 2).
  • valve 20 the compressor is connected through line 12 to the part corresponding to line 30 in FIG. 2 so that when all available gas has been transferred from container14 to the vehicle being charged, the movement of the spool of valve 20 corresponding to spool 72 will connect the compressor directly to the vehicle. During this final filling mode no gas will be placed in the storage tanks.
  • container 18 So long as container 18 has more pressure than the vehicle to be charged, withdrawal will begin with container 18.
  • the draw and bypass spool of valve 24 for this container will be in its draw position. In the draw position, container 18 will communicate with the tanks in the vehicle through the transfer chamber of that particular valve and line 34.
  • the biasing spring of valve 24 and tank pressure will force the draw and bypass spool to its bypass position and gas transfer to the tanks of the vehicle will switch to container 16. The same sequence of events occurs in changing from container 16 to container 14.
  • valve 20 admits to direct communication between the tanks of the vehicle being charged and the compressor.
  • the present invention provides a charging system and process which, by charging storage containers having the highest beginning residual pressure first, maximizes the filling of vehicle tanks because the charging sequence maximizes available container pressure.
  • the system and process of the present invention also maximizes vehicle tank filling by drawing from the container having the lowest beginning pressure, then progressively shifting to containers having gas under higher pressure. This again assures the effective maximum utilization of the filling force afforded by container pressure.
  • the fill time for vehicles using compressed gas is maximized.
  • a process for charging a plurality of containers with a gas in an order to produce the maximum available driving pressure in them in a given amount of charging time comprising:
  • a process for charging a plurality of containers with a gas in an order to produce the maximum available driving pressure in them in a given amount of charging time and then for withdrawing gas from the charged containers in an order to produce the maximum fill in tanks being charged by the container comprising:

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)

Abstract

Each container in a bank of containers is individually charged with a gas in the order of the highest residual pressure remaining in the containers at the time charging is initiated. Gas withdrawal from the containers begins with the container at the lowest beginning pressure.

Description

United States Patent. [1 1 McJones [451 Apr. 30, 1974 CHARGING SEQUENCE SYSTEM AND PROCESS [76] Inventor: Robert W. McJones, 529 Via Del Monte, Palos Verdes Estates, Calif. 90224 i 22 Filed: Feb. 5, 1973 21 Appl. No.: 329,642
Related US. Application Data [60] Division of Seri No. 92,814, Nov. 25, 1970, Pat. No. 3,719,196, which is a continuation-in-part of Ser. No. 34,966, May 6, 1970.
[52] US. Cl 137/12, 137/110, 137/112,
137/119, 137/256 [51] Int. Cl. Fl7d l/02 [58] Field of Search 137/ 12 [56] References Cited UNITED STATES PATENTS 2,779,348 1/1957 Robertson 1. 137/121 3,151,625 10/1964 Keeney 137/121 3,241,580 3/1966 Lichtenberger 141/35 X Primary ExaminerHarold W. Weakley Attorney, Agenl, or Firm-Christie, Parker & Hale 7] ABSTRACT Each container in a bank of containers is individually charged with a gas in the order of the highest residual pressure remaining in the containers at the time charging is initiated. Gas withdrawal from the containers begins with the container at the lowest beginning pressure.
2 Claims, 2 Drawing Figures PATENTEDAPR 30 m4 SHEET 1 BF 2 CROSS-REFERENCE TO RELATED APPLICATION The present application is a division of US. Pat. application Ser. No. 92,814, filed Nov. 25, 1970, now U.S. Pat. No. 3,719,196, which in turn was a continuation-in-part application of US. Pat. application Ser. No. 34,966, filed May 6, 1970.
BACKGROUND OF THE INVENTION The present invention relates in general to the art of charging and withdrawing gas from containers. More specifically, the present invention relates to a charging level of the pollutants of carbon monoxide, oxides of nitrogen and hydrocarbons over the emission levels experienced by gasoline.
Natural gas for use as a fuel in internal combustion engines can be stored in vehicles as a gas in suitable containers, often referred to as tanks or bottles. Typically, presently available tanks are rated at 2,265 p.s.i. at standard temperature conditions.
Obviously, the natural gas tanks in a vehicle must be recharged from time to time. The time to recharge tanks when a natural gas, compressor is used alone is often too great for orderly refueling. As a consequence,
it is necessary to augment compressor charging in some cases by the use of a storage bank of containers maintained, whenever possible, at some limiting high pressure. However, during large refueling demands on a refueling system it is not always possibleto maintain the storage bank of containers at their maximum rated pressure.
Obviously, at any time it is highly desirable to charge a vehicles natural gas tanks to the highest pressure possible within a given period of time.
SUMMARY OF THE INVENTION process and system which employs at least two storage containers or vessels which are sequentially charged in the order of the highest residual pressure existing in a container before charging commences.
A specific form of the present invention contemplates a source of pressurized gas which may include a compressor, a series of containers to be charged, and sequence fill and transfer valve means for each container. The sequencer valve means each has a fill position and a transfer position. Means is provided for maintaining each sequencer valve means in its fill position and in communication with its container below a pre- I determined pressure, typically the rated pressure of the containers. Means is also provided for each sequencer valve means to change the valves position from its fill position to its transfer position in response to the predetermined pressure existing in its associated container and to then establish communication between a downstream valve and the gas source. Means is also provided to prevent gas communication between a container and the source of pressurized gas when another container is being charged.
In a more specific form, the system of the present invention contemplates that each sequencer valve means control the flow of gas from the source of pressurized gas to succeeding containers in a series of containers by preventing gas communication beyond the valve means admitting to gas flow to its container. This may be done by connecting the source of gas to the containers in series through the sequencer valve means and providing each sequencer valve means with meansfor preventing gas flow downstream from it when it is admitting to gas flow into its container.
It is preferred that the means for maintaining each of the valves in its fill position until a predetermined pressure is reached be temperature compensated in order that utilization of available container volume be maximized. In greater detail, it is preferred that the temperature within a container being charged control the predetermined pressureto compensate for variations in container temperature owing to such factors as ambient temperature. Thus on a warm day where the density of a given amount of gas is low but its pressure relatively high, the predetermined pressure would be higher than the rated pressure of the container. Conversely, on a cold day for a given amount of gas, the predetermined pressure would be lower than the rated pressure of the container. This is detailed in copending application Ser. No. 34,966 of which this application constitutes a continuation-in-part.
The present invention also contemplates the selective charging of other vessels or containers from the storage containers by charging from the storage container having the lowest beginning pressure initially and ending at the storage container having the highest beginning initial pressure.
A preferred form of the sequencer valve means of the present invention contemplates the combining of the sequencer fill and transfer valve and a transfer sequencer valve. A valve spool for the fill and transfer sequencer valve is disposed in a bore of a housing for translation between a fill position and a transfer position. Inlet means to the bore is provided from an outlet means from the bore of the next sequencer valve upstream and from the source of gas for the first valve. The spool in the fill position masks the outlet means but communicates the particular valves container with the inlet port. In the transfer position, the spool prevents communication from the inlet port to the container but allows communication through the valve to the next subsequent sequencer valves inlet. The position of the spool is determined by pressure on a reference pressure side thereof and on a side in direct communication with its associated container such that when container pressure reaches the predetermined value it overcomes the effect of the reference pressure and any biasing means to shift the spool to the transfer position.
On the withdrawal side of each valve a draw and bypass spool is provided, the position of which between a draw position and a bypass position is determined by its container pressure and a reference pressure. The reference pressure is the pressure of the tanks receiving gas from the container and, preferably, a biasing spring. In the bypass position of each valve, the valves container is out of communication with the tanks but the tanks are in communication with the next upstream valve, or the source of gas in the case of the last valve. In the draw position of each valve, upstream valves are out of communication with the tanks but the container for the particular valve is in communication with the tanks. As a consequence, the lowest pressure containers will exhaust first.
These and other features, aspects and advantages of the present invention will become more apparent from the following description, appended claims and drawmgs.
BRIEF DESCRIPTION OF THE FIGURES FIG. 1 is a flow sheet illustrating the charging and withdrawal system and process of the present invention; and
FIG. 2 is a view of the preferred sequential fill limiter and discharge valve assembly of the present invention.
DESCRIPTION OF THE PREFERRED EMBODIMENTS The system of the present invention will be described initially with reference to FIG. 1. In this Figure, a natural gas compressor is illustrated. This compressor may be of any well known forms and obviously compresses gas from a source at relatively low pressure to some predetermined pressure for discharge into a line 12. A bank of containers or bottles consisting of containers 14, 16 and 18 are in communication with line 12 through respective sequential fill and discharge valves 20, 22 and 24. The containers are connected in series through their respective sequential fill and discharge valves both for their charging and discharge. Each container can, of course, be replaced by two or more containers.
In the embodiment illustrated and for reasons to become apparent subsequently, when there is not enough time to bring all the containers up to rated pressure between withdrawals, container 14 will always have a residual pressure before charging in excess of the residual pressure in containers 16 and 18. Similarly, container 16 will have a residual pressure before charging in excess of the pressure existing in container 18. Of course, if there is sufficient charging time between withdrawals, all the containers will be at the same pressure. But for purposes of this discussion it will be assumed that there is insufficient time to bring all the containers up to their rated pressure before withdrawal to a vehicles gas storage tanks.
Sequential fill and discharge valve for container 14 controls the flow of gas to downstream containers 16 and 18 such that when container 14 is being charged no gas passes past valve 20 to the downstream containers.
Conversely, during withdraw] of gas from the containers, sequential fill and discharge valve 24 prevents discharge of gas from containers l4 and 16 until the gas in container 18 is effectively exhausted. The same is true of sequential fill and discharge valve 22 which prevents the withdrawal of gas from container 14 until container 16 is effectively exhausted.
To accomplish these ends, each of the valves 20, 22 and 24 has a fill side and a withdrawal side, indicated in FIG. 1 for the fill side by reference numerals 20a, 22a and 24a, and for the withdrawal side by reference numerals 20b, 22b and 24b.
The fill side of valves 20 and 22 are in series gas communication through a line 26. As will become apparent subsequently, line 12 from the compressor leads directly to the withdrawal side of valve 20 so that when valve 20 is in its draw position gas from the compressor will pass through the valve and through a line 27 to the inlet side of the valve. The fill side of valves 22 and 24 are in series gas communication through a line 28.
The withdrawal sides of valves 20 and 22 are in series gas communication through a line 30, and the withdrawal sides of valves 22 and 24 are in series gas communication through a line 32. The withdrawal side of valve 24 leads to the vehicle tanks to be charged through a line 34.
The system illustrated in FIG. 1 has a transfer valve 36 in line 34 emanating from the withdrawal side of valve 24 for the initiation of gas withdrawal from the containers.
The fill side of each valve has a fill position and a transfer and off position. Each valve has a valving element, such as a spool, which is positionally responsive to a reference pressure and the particular valves container pressure, such that when the reference pressure exceeds the container pressure the valve is in its fill position and gas can enter the container. When the container pressure exceeds the reference pressure, the particular valve will go to its transfer and off position. In the transfer position a valve admits to gas flow downstream from it and stops gas flow to its associated cont-' ainer. When valve 24 is in its transfer position, gas is recycled through a line 37 back to the compressor inlet, or to a pressure switch which stops the compressor, at the option of the user. In FIG. 1, the reference pressure is supplied by reference pressure vessels 38, 40 and 42 through lines 44, 46 and 48 for valves 20, 22 and 24, respectively. Gas communication from and to valves 20, 22 and 24 to and from containers 14, 16 and 18 is through lines 50, 52 and 54, respectively.
The withdrawal side of each valve has a container bypass position and container draw position. In the container draw position for a given valve, gas can be drawn from that valves container. In the bypass position for a given valve, gas cannot be withdrawn from its container but only from a container upstream from it, or in the case of valve 20, from compressor 10. To effect this type of operation each valve has a second valving element, such as a spool, which is positionally responsive from its draw position to its bypass position when container pressure drops below a given valve relative to the pressure in the tanks being charged. Conversely, each valve shifts from its bypass position to its draw position when its container pressure exceeds a given value relative to the pressure in the tanks being charged. The withdrawal side of each of the valves 20, 22 and 24 is in pressure communication with the tanks being charged through parallel branch lines 56, 58 and 60, respectively, all of which are connected to the tanks being charged downstream of transfer valve 36 through a common line 62.
With reference to FIG. 2, a more detailed depiction of sequential fill and discharge valve 22 is presented. This valve is identical in construction to valves and 24 and is connected into the system illustrated in FIG. 1 identically, save for minor details to be described subsequently.
In general, valve 22 has a housing 64 having aligned bores 66 and 68 which receive fill limiter and transfer spool 70 and a draw and bypass spool 72. Spool 70 is in fill side 22a and spool 72 is in transfer side 22b. The fill side of the valve will be initially described.
Line 26 from valve 20 opens into bore 66 for incoming gas and, as such, constitutes an inlet line for the valve. Line 28 also opens into the bore for outgoing gas to valve 24 and, as such, constitutes an outlet line from the valve. A chamber 74 midway between the fill and transfer side of the valve is in communication with container 16 through line 52. A reference pressure chamber 76 is in pressure communication with reference pressure vessel 40 through line 46.
Spool 70 is generally cylindrical and has an annular, relatively elongated flow channel 78 bounded by lands 80 and 82'for communicating inlet line 26 with outlet line 28 when the pressure in chamber 74 is sufficient to overcome the pressure in reference chamber 76. An axial passage 84 in spool 70 opens into chamber 74 and is in communication with an annular channel 86 through one or more radial passages 88. Channel 86 is in communication with inlet line 26 in the fill position of the valve, which is the position illustrated in FIG. 2.
Means are provided to prevent axial gas flow between the lands of the spool and the wall of the bore such as a pair of O-rings 90.on either axial side of channel 78 and a pair of O-rings 92 on either axial side of channel 86.
The reference pressure chamber, as previously mentioned, is in direct communication with reference pressure vessel 40. The latter vessel is in thermal communication with container 16. As such, the pressure in the reference pressure chamber is determined by the temperature of gas within container 116. Because the gas in the reference pressure chamber line 46 and vessel 40 constitutes a closed system, the reference pressure in the chamber is a direct function of temperature. As a consequence, when the temperature in container 16 is relatively high, so will be the pressure in reference pressure chamber 76. The converse is also true.
The pressure in vessel 40, acting in chamber 76, is such that during charging spool 70 will shift to its transfer position when the pressure exerted on it from container 16, acting in chamber 74, reaches a predetermined value of, say, 2,265 p.s.i. at 70 F.
On the withdrawal side of the valve, spool 72 is capable of translation in bore 68 between a draw position and a bypass position. The position illustrated in FIG. 2 is the draw position. Line 32 opens into a transfer chamber 94 and is in direct communication through this chamber with chamber 74 and container 16 when spool 72 is in its draw position. Line' opens into bore 68 and emanates from the transfer chamber of valve 20.
One end of spool 72 sees the pressure in the tanks being charged through line 58 which opens into a reference pressure chamber 96. In addition, a biasing spring 98 is disposed to act between an end of housing 64 and spool 72 and exerts predetermined biasing pressure on the spool of, say, 50 p.s.i., which tends to move the spool to its bypass position.
Spool 72 has an annular bypass channel 100 disposed to bridge the distance between line 30 and a line 101 in the draw position and between lines 30 and 32 to communicate the two in the spools bypass position. Line 101 is blocked in each valve except in valve 20 where it is shown by reference numeral 27. Line 27 leads to the part of valve 20 corresponding to line 26 in FIG. 2. Again, O-rings are provided to prevent leakage of gas from or to the channel along the interface bet ween the spool and the wall of bore 68. These O-rings are indicated by reference numerals 102, 104 and 106 and are disposed in lands 108, 1.10 and 112, respectively.
Spool 72 shifts to its bypass position when the pressure in the tanks being charged and biasing spring 98 is sufficient to overcome the pressure within container 16 acting in chamber 74.
The differences in the system connections for the valves 20 and 24 over those for valve 22 will now be described.
For valve 24, line 34 leads from the valve at the same location that line 32 leaves valve 22 but goes directly to the tanks being charged. Line 37 leads either to a compressor shutdown device or the compressor inlet when all tanks are filled. In other words, envisioning valve 22 as valve 20 during withdrawal, the compressor will be in direct communication with line 26 through line 30, channel 100 and line 101. With this communication, the compressor directly charges the vehicles tanks. When the pressure in container 14 approaches vehicle tank pressure, the spool of valve 20 corresponding to spool 72 will move to the bypass position, dropping container 14 out of fluid circuit. However, compressor 10 will still be in communication with the vehicles tanks through channel 100 and line 26 (the latter corresponding to line 32 in FIG. 2).
For valve 20, the compressor is connected through line 12 to the part corresponding to line 30 in FIG. 2 so that when all available gas has been transferred from container14 to the vehicle being charged, the movement of the spool of valve 20 corresponding to spool 72 will connect the compressor directly to the vehicle. During this final filling mode no gas will be placed in the storage tanks.
The filling sequence of containers 14, 16 and 18 will now be described. Typically, the pressure in the containers will progressively decrease from container 14 to container 18 before the beginning of filling'and each container will be below its filled pressure. In this condition, the fill limiter and transfer spool of valve 20 corresponding to spool of valve 22 will be in its fill position. Since no vehicle is connected at the outlet of valve 24, all withdrawal valves will be in the draw position. The compressor is then connected through lines 12 and 27 to container 14. Communication with containers downstream of valve 20 is not possible because the fill limiter and transfer spool of valve 20 prevents communication with downstream valves by blocking line 26. When the pressure in container 14 is sufficient to overcome the pressure in the reference chamber of the valve, the spool will be. forced to its transfer position, and lines 12 and 26 will be in communication with one another. At this time, container 16 will begin to be filled and container 14 will be out of communication with the compressor 10. The same sequence of events will progressively occur for containers l6 and 18.
So long as container 18 has more pressure than the vehicle to be charged, withdrawal will begin with container 18. The draw and bypass spool of valve 24 for this container will be in its draw position. In the draw position, container 18 will communicate with the tanks in the vehicle through the transfer chamber of that particular valve and line 34. When the pressure in the tanks of the vehicle and the pressure in container 18 approach one another, the biasing spring of valve 24 and tank pressure will force the draw and bypass spool to its bypass position and gas transfer to the tanks of the vehicle will switch to container 16. The same sequence of events occurs in changing from container 16 to container 14.
In the event that container 18 should have less pressure than the vehicle to be charged at the beginning of withdrawal, container 16 will transfer its gas first, followed by container 14. As previously mentioned, valve 20 admits to direct communication between the tanks of the vehicle being charged and the compressor.
The present invention provides a charging system and process which, by charging storage containers having the highest beginning residual pressure first, maximizes the filling of vehicle tanks because the charging sequence maximizes available container pressure. The system and process of the present invention also maximizes vehicle tank filling by drawing from the container having the lowest beginning pressure, then progressively shifting to containers having gas under higher pressure. This again assures the effective maximum utilization of the filling force afforded by container pressure. Thus, for a given capacity charging system the fill time for vehicles using compressed gas is maximized.
The present invention has been specifically described with reference to its presently preferred embodiment. The spirit and scope of the appended claims should not, however, necessarily be limited to the foregoing description. For example, while the invention has been described with reference to the charging of the fuel tanks of vehicles using natural gas, the invention has utility in other environments.
What is claimed is:
l. A process for charging a plurality of containers with a gas in an order to produce the maximum available driving pressure in them in a given amount of charging time comprising:
charging the container having the highest initial pressure with the gas to a predetermined pressure and then charging as many of the remaining containers in the order of their highest initial pressure with the gas to the predetermined pressure as is possible in the charging time.
2. A process for charging a plurality of containers with a gas in an order to produce the maximum available driving pressure in them in a given amount of charging time and then for withdrawing gas from the charged containers in an order to produce the maximum fill in tanks being charged by the container comprising:
charging the container having the highest initial pressure with the gas to a predetermined pressure and then charging as many of the remaining containers successively and individually in the order of thier highest initial pressure with the gas to the predetermined pressure as is possible in the charging time, and then charging the tanks with gas from the containers by withdrawing gas from the container having the lowest initial pressure first and then withdrawing gas successively and individually from the remaining containers in the order of their lowest initial pressure until the tanks have been charged.
' UTED STATES PATENT UFFICE CERTWMATE @F @QEUHN Patent No. 3,,807,422 Dated A ril 30, 1974 Inve Robert W. Mcjenes It is certified that error appears in the above ide'ntified patent and that said Letters Patent are hereby corrected as shown below:
In the specification: Colum 4, line 60 "valve" should be -value u In the claims:' Claim 2, column 8 line 28, "thier" should be --their--.,
Signed and sea led this 12th day of November .1974.
(SEAL) Attest:
MCCOY M'. GIBSON JR. 7 C. MARSHALL DANN Atteeting Officer Commissioner of Patents

Claims (2)

1. A process for charging a plurality of containers with a gas in an order to produce the maximum available driving pressure in them in a given amount of charging time comprising: charging the container having the highest initial pressure with the gas to a predetermined pressure and then charging as many of the remaining containers in the order of their highest initial pressure with the gas to the predetermined pressure as is possible in the charging time.
2. A process for charging a plurality of containers with a gas in an order to produce the maximum available driving pressure in them in a given amount of charging time and then for withdrawing gas from the charged containers in an order to produce the maximum fill in tanks being charged by the container comprising: charging the container having the highest initial pressure with the gas to a predetermined pressure and then charging as many of the remaining containers successively and individually in the order of thier highest initial pressure with the gas to the predetermined pressure as is possible in the charging time, and then charging the tanks with gas from the containers by withdrawing gas from the container having the lowest initial pressure first and then withdrawing gas successively and individually from the remaining containers in the order of their lowest initial pressure until the tanks have been charged.
US32964273 1970-05-06 1973-02-05 Charging sequence system and process Expired - Lifetime US3807422A (en)

Priority Applications (6)

Application Number Priority Date Filing Date Title
US3719196D US3719196A (en) 1970-05-06 1970-11-25 Charging sequence system and process
DE19712121328 DE2121328A1 (en) 1970-05-06 1971-04-30 Charging method and charging device for natural gas or the like with temperature compensation
GB1336571A GB1335254A (en) 1970-05-06 1971-05-05 Temperature compensated gas storage systems
FR7116193A FR2091237A5 (en) 1970-05-06 1971-05-05
US29597672 US3837377A (en) 1970-05-06 1972-10-10 Temperature compensated charging system and process for natural gas and the like
US32964273 US3807422A (en) 1970-05-06 1973-02-05 Charging sequence system and process

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
US3496670A 1970-05-06 1970-05-06
US9281470A 1970-11-25 1970-11-25
US29597672 US3837377A (en) 1970-05-06 1972-10-10 Temperature compensated charging system and process for natural gas and the like
US32964273 US3807422A (en) 1970-05-06 1973-02-05 Charging sequence system and process

Publications (1)

Publication Number Publication Date
US3807422A true US3807422A (en) 1974-04-30

Family

ID=27488261

Family Applications (3)

Application Number Title Priority Date Filing Date
US3719196D Expired - Lifetime US3719196A (en) 1970-05-06 1970-11-25 Charging sequence system and process
US29597672 Expired - Lifetime US3837377A (en) 1970-05-06 1972-10-10 Temperature compensated charging system and process for natural gas and the like
US32964273 Expired - Lifetime US3807422A (en) 1970-05-06 1973-02-05 Charging sequence system and process

Family Applications Before (2)

Application Number Title Priority Date Filing Date
US3719196D Expired - Lifetime US3719196A (en) 1970-05-06 1970-11-25 Charging sequence system and process
US29597672 Expired - Lifetime US3837377A (en) 1970-05-06 1972-10-10 Temperature compensated charging system and process for natural gas and the like

Country Status (4)

Country Link
US (3) US3719196A (en)
DE (1) DE2121328A1 (en)
FR (1) FR2091237A5 (en)
GB (1) GB1335254A (en)

Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4480654A (en) * 1982-08-26 1984-11-06 Firey Joseph C Multipressure compressor
US4522159A (en) * 1983-04-13 1985-06-11 Michigan Consolidated Gas Co. Gaseous hydrocarbon fuel storage system and power plant for vehicles and associated refueling apparatus
US4523548A (en) * 1983-04-13 1985-06-18 Michigan Consolidated Gas Company Gaseous hydrocarbon fuel storage system and power plant for vehicles
US4531558A (en) * 1983-04-13 1985-07-30 Michigan Consolidated Gas Co. Gaseous fuel refueling apparatus
US4776366A (en) * 1985-11-13 1988-10-11 Michigan Consolidated Gas Company Gaseous fueled torch apparatus and fueling module therefor
US4849648A (en) * 1987-08-24 1989-07-18 Columbia Energy Storage, Inc. Compressed gas system and method
US4923152A (en) * 1985-08-05 1990-05-08 Gerard Barkats Two-liquid propulsive system for an artificial satellite and utilization of said system for ejecting the satellite
US4930550A (en) * 1985-11-13 1990-06-05 Fuel Concepts, Inc. Gaseous fueled torch apparatus and fueling module therefor
US5632146A (en) * 1996-01-02 1997-05-27 Apt Incorporated Load shaping compressed air system
US6070610A (en) * 1996-12-10 2000-06-06 Expo Safety Systems Limited Fluid operated timer for a plurality of reservoirs
JP2001254867A (en) * 2000-01-28 2001-09-21 Greenfield Ag Switching device for filling station and gas filling station
US20070071609A1 (en) * 2005-09-26 2007-03-29 Sturman Industries, Inc. Digital pump with multiple outlets
US20110232772A1 (en) * 2008-12-03 2011-09-29 Taiyo Nippon Sanso Corporation Method for supplying gas
RU2647301C1 (en) * 2017-05-25 2018-03-15 Игорь Анатольевич Мнушкин Gas-chemical cluster
US10400954B2 (en) 2015-02-20 2019-09-03 Kobe Steel, Ltd. Gas filling system

Families Citing this family (51)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3844306A (en) * 1973-03-07 1974-10-29 R Hill Gas supply system
US3847173A (en) * 1973-09-13 1974-11-12 R Hill Gas supply system
US4527600A (en) * 1982-05-05 1985-07-09 Rockwell International Corporation Compressed natural gas dispensing system
US4483376A (en) * 1982-09-07 1984-11-20 Bresie Don A Natural gas loading station
GB2127533B (en) * 1982-09-30 1986-04-23 Cornelius Co Filling compressed gas bottles
CH655862A5 (en) * 1983-03-31 1986-05-30 Bucher Guyer Ag Masch METHOD FOR ACCELERATING THE AIR EXCHANGE WHEN FILLING OR EMPTYING A PRESSURE ROOM AND DEVICE FOR IMPLEMENTING THE SAME.
EP0300222B1 (en) * 1987-07-23 1992-08-12 GebràœDer Sulzer Aktiengesellschaft Filling device for a gaseous-fuel reservoir
US4817684A (en) * 1987-09-16 1989-04-04 Michigan Consolidated Gas Company Method and apparatus for sorptively storing a multiconstituent gas
US5259424A (en) * 1991-06-27 1993-11-09 Dvco, Inc. Method and apparatus for dispensing natural gas
US5238030A (en) * 1991-06-27 1993-08-24 Dvco Method and apparatus for dispensing natural gas
EP0607750B1 (en) * 1993-01-22 1997-11-19 Maschinenfabrik Sulzer-Burckhardt AG Filling device for a mobile pressure vessel with a gaseous fuel and process for operating such a device
US5385176A (en) * 1993-07-19 1995-01-31 Price Compressor Company, Inc. Natural gas dispensing
US5542459A (en) * 1993-07-19 1996-08-06 Price Compressor Company Inc. Process and apparatus for complete fast filling with dehydrated compressed natural gas
DE59404467D1 (en) 1993-11-08 1997-12-04 Burckhardt Ag Maschf Method and device for the rapid refueling of a pressure container with a gaseous medium
US5406988A (en) * 1993-12-01 1995-04-18 Pacific Cryogenics, Inc. Method and apparatus for dispensing compressed gas into a vehicle
US5488978A (en) * 1994-05-02 1996-02-06 Gas Research Institute Apparatus and method for controlling the charging of NGV cylinders from natural gas refueling stations
US5564306A (en) * 1994-05-25 1996-10-15 Marcum Fuel Systems, Inc. Density compensated gas flow meter
US5628349A (en) * 1995-01-25 1997-05-13 Pinnacle Cng Systems, Llc System and method for dispensing pressurized gas
US5586587A (en) * 1995-06-14 1996-12-24 Morton International, Inc. High rate pressure vessel filling process
US5699839A (en) * 1995-07-14 1997-12-23 Acurex Environmental Corporation Zero-vent liquid natural gas fueling station
JP2762253B2 (en) * 1996-01-31 1998-06-04 本田技研工業株式会社 Compressed natural gas filling equipment
US6394764B1 (en) 2000-03-30 2002-05-28 Dresser-Rand Company Gas compression system and method utilizing gas seal control
DE10201273A1 (en) * 2002-01-15 2003-07-24 Linde Ag Gas tank filling system for road vehicle running on hydrogen has two-stage compressor system with intercooler and includes low- intermediate and high-pressure reservoirs
US6619336B2 (en) 2002-02-14 2003-09-16 Air Products And Chemicals, Inc. System and method for dispensing pressurized gas
US6779568B2 (en) * 2002-07-16 2004-08-24 General Hydrogen Corporation Gas distribution system
US7311116B2 (en) * 2003-12-10 2007-12-25 Proton Energy Systems, Inc. Gas regulation system and process for operating the gas regulation system
EP1559949A1 (en) * 2004-01-28 2005-08-03 Gaveco AB A method and a system for refuelling of gas driven vehicles and a vehicle gas container
US7168464B2 (en) * 2004-09-09 2007-01-30 Pinnacle Cng Systems, Llc Dual-service system and method for compressing and dispensing natural gas and hydrogen
US7152637B2 (en) * 2005-02-17 2006-12-26 Air Products And Chemicals, Inc. Method and apparatus for dispensing compressed gas
US20060180237A1 (en) * 2005-02-17 2006-08-17 Hoke Bryan C Jr System and method for dispensing compressed gas
US8122918B2 (en) * 2005-08-31 2012-02-28 Honda Motor Co. Ltd. Pressure differential system for controlling high pressure refill gas flow into on board vehicle fuel tanks
DE102006016554A1 (en) * 2006-04-07 2007-10-11 L'Air Liquide, S.A. a Directoire et Conseil de Surveillance pour l'Etude et l'Exploitation des Procédés Georges Claude Method for filling at least one compressed gas container with at least one gas, intermediate piece for connecting to an opening of a compressed gas container and compressed gas cylinder fitting
US8757193B2 (en) * 2006-08-07 2014-06-24 Baker Hughes Incorporated Control line reducing hydraulic control system and control valve therefor
DE102006047313B4 (en) * 2006-10-06 2009-08-20 Deutsches Zentrum für Luft- und Raumfahrt e.V. Device for the rapid filling of compressed gas containers
US8020589B2 (en) * 2007-01-04 2011-09-20 Air Products And Chemicals, Inc. Hydrogen dispensing station and method of operating the same
US8286670B2 (en) 2007-06-22 2012-10-16 L'air Liquide Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Method for controlled filling of pressurized gas tanks
CN100580305C (en) * 2007-07-12 2010-01-13 徐焕恩 Safe and low consumption intelligent gas-supplying system for gas bottle group
FR2919375B1 (en) 2007-07-23 2009-10-09 Air Liquide METHOD FOR FILLING A PRESSURIZED GAS IN A RESERVOIR
US8375999B2 (en) * 2009-08-31 2013-02-19 GM Global Technology Operations LLC Offboard heat management during compressed gas filling of vehicular hydrogen storage tanks
US20120012225A1 (en) * 2010-07-19 2012-01-19 Marc Moszkowski Method of filling CNG tanks
CN102352961A (en) * 2011-07-27 2012-02-15 北京万源瀚德汽车密封系统有限公司 Gas pressure stabilizing system
US10018304B2 (en) 2012-01-31 2018-07-10 J-W Power Company CNG fueling system
US10851944B2 (en) 2012-01-31 2020-12-01 J-W Power Company CNG fueling system
US9765930B2 (en) 2012-01-31 2017-09-19 J-W Power Company CNG fueling system
JP5591854B2 (en) * 2012-03-19 2014-09-17 本田技研工業株式会社 Mobile body and fuel filling system thereof
ES2734553T3 (en) 2013-05-31 2019-12-10 Nuvera Fuel Cells Llc Method and system of resupply of distributed hydrogen
JP6484243B2 (en) * 2013-08-28 2019-03-13 ヌヴェラ・フュエル・セルズ,エルエルシー Integrated electrochemical compressor and cascade storage method and system
JP5886820B2 (en) * 2013-12-13 2016-03-16 株式会社神戸製鋼所 Gas filling device and gas filling method
US10240721B2 (en) 2015-10-08 2019-03-26 Oneh2, Inc. Method, apparatus, and system for refueling hydrogen vehicles
CN110382944B (en) * 2017-03-30 2021-10-01 全耐塑料高级创新研究公司 Hydrogen storage system
DE102019103119A1 (en) * 2019-02-08 2020-08-13 Mesa Parts GmbH Overflow valve for closing and opening a fluid line system

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2779348A (en) * 1952-11-13 1957-01-29 Gulf Oil Corp Fluid production and storage control apparatus
US3151625A (en) * 1962-08-01 1964-10-06 Socony Mobil Oil Co Inc Tank battery fill control
US3241580A (en) * 1962-07-06 1966-03-22 Union Carbide Corp Method and apparatus for dispensing vaporizable liquids

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2283311A (en) * 1940-02-16 1942-05-19 Bendix Aviat Corp Compensating means for pressure responsive devices
US2780231A (en) * 1954-11-26 1957-02-05 Earnest E Westmoreland Automatic tank switching device
US3211175A (en) * 1961-04-03 1965-10-12 Edward H Replogle Valve regulator
DE1224577B (en) * 1963-12-17 1966-09-08 Teves Kg Alfred Automatic, pressure-dependent accumulator shut-off valve for hydraulic systems
US3232485A (en) * 1964-02-11 1966-02-01 Reynolds Metals Co Charging valve construction
US3318345A (en) * 1965-03-15 1967-05-09 Jr Richard W Beall Storage battery filling device
US3524465A (en) * 1968-09-03 1970-08-18 Hypro Inc Unloader valve assembly

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2779348A (en) * 1952-11-13 1957-01-29 Gulf Oil Corp Fluid production and storage control apparatus
US3241580A (en) * 1962-07-06 1966-03-22 Union Carbide Corp Method and apparatus for dispensing vaporizable liquids
US3151625A (en) * 1962-08-01 1964-10-06 Socony Mobil Oil Co Inc Tank battery fill control

Cited By (23)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4480654A (en) * 1982-08-26 1984-11-06 Firey Joseph C Multipressure compressor
US4522159A (en) * 1983-04-13 1985-06-11 Michigan Consolidated Gas Co. Gaseous hydrocarbon fuel storage system and power plant for vehicles and associated refueling apparatus
US4523548A (en) * 1983-04-13 1985-06-18 Michigan Consolidated Gas Company Gaseous hydrocarbon fuel storage system and power plant for vehicles
US4531558A (en) * 1983-04-13 1985-07-30 Michigan Consolidated Gas Co. Gaseous fuel refueling apparatus
FR2580779A1 (en) * 1983-04-13 1986-10-24 Michigan Cons Gas GAS FUEL SUPPLY APPARATUS
FR2580778A1 (en) * 1983-04-13 1986-10-24 Michigan Cons Gas HYDROCARBON GAS FUEL STORAGE DEVICE AND POWER SUPPLY FOR MOTOR VEHICLES AND REFUELING APPARATUS THEREOF
US4923152A (en) * 1985-08-05 1990-05-08 Gerard Barkats Two-liquid propulsive system for an artificial satellite and utilization of said system for ejecting the satellite
US4776366A (en) * 1985-11-13 1988-10-11 Michigan Consolidated Gas Company Gaseous fueled torch apparatus and fueling module therefor
US4930550A (en) * 1985-11-13 1990-06-05 Fuel Concepts, Inc. Gaseous fueled torch apparatus and fueling module therefor
US4849648A (en) * 1987-08-24 1989-07-18 Columbia Energy Storage, Inc. Compressed gas system and method
US5632146A (en) * 1996-01-02 1997-05-27 Apt Incorporated Load shaping compressed air system
WO1997024551A1 (en) * 1996-01-02 1997-07-10 Honeywell Inc. Load shaping compressed air system
CN1086026C (en) * 1996-01-02 2002-06-05 霍尼韦尔公司 Load shaping compressed air system
US6070610A (en) * 1996-12-10 2000-06-06 Expo Safety Systems Limited Fluid operated timer for a plurality of reservoirs
JP2001254867A (en) * 2000-01-28 2001-09-21 Greenfield Ag Switching device for filling station and gas filling station
US6450217B2 (en) * 2000-01-28 2002-09-17 Greenfield Ag Switch-over device for a filling station, and a gas filling station
AU779464B2 (en) * 2000-01-28 2005-01-27 Greenfield Ag Switch-over device for a filling station, and a gas filling station
US20070071609A1 (en) * 2005-09-26 2007-03-29 Sturman Industries, Inc. Digital pump with multiple outlets
US20110232772A1 (en) * 2008-12-03 2011-09-29 Taiyo Nippon Sanso Corporation Method for supplying gas
US8381756B2 (en) * 2008-12-03 2013-02-26 Taiyo Nippon Sanso Corporation Method for supplying gas
US10400954B2 (en) 2015-02-20 2019-09-03 Kobe Steel, Ltd. Gas filling system
RU2647301C1 (en) * 2017-05-25 2018-03-15 Игорь Анатольевич Мнушкин Gas-chemical cluster
RU2647301C9 (en) * 2017-05-25 2018-07-04 Игорь Анатольевич Мнушкин Gas-chemical cluster

Also Published As

Publication number Publication date
DE2121328A1 (en) 1971-11-18
FR2091237A5 (en) 1972-01-14
GB1335254A (en) 1973-10-24
US3837377A (en) 1974-09-24
US3719196A (en) 1973-03-06

Similar Documents

Publication Publication Date Title
US3807422A (en) Charging sequence system and process
US5694985A (en) System and method for compressing natural gas and for refueling motor vehicles
US8156970B2 (en) Temperature-compensated dispensing of compressed gases
US5673735A (en) Process for storing and delivering gas
US2362724A (en) Liquefied petroleum gas dispensing system
CA2111910A1 (en) Installation for refuelling a mobile pressure vessel with a gaseous fuel and a method of operation of an installation of that kind
US20140261864A1 (en) Method for Dispensing Compressed Gases
CA2132946A1 (en) Improved storage system for cryogenic fluids
US2354286A (en) Automatic change-over device
US4328768A (en) Hydrogen fuel storage and delivery system
GB1363737A (en) Low-loss closed-loop supply system for transferring liquid gas from a large container to a small container
US3847173A (en) Gas supply system
US3653394A (en) Priority charging system
US2138988A (en) Automatic change-over device
US3183678A (en) Liquid to gas conversion system
GB1483182A (en) Cryogenic fluid storage and supply system with all-attitude gas vent means
GB812998A (en) Improvements in storing and pumping systems for liquefied gas
US2604230A (en) Liquid supply tank
US5921765A (en) Periodic, on-demand pressurized gas power source and method of providing same
US2996892A (en) Volatile fuel flow control valve
US2788637A (en) Underground storage systems and improved method of operating
US3234745A (en) Multiple tank filling system
EP0885365A1 (en) Method in the utilization of boil-off from liquid gas and apparatus for carrying out the method
CA2103338A1 (en) Fuel supply system with high turn down ratio
US2234325A (en) Superloading automatic change-over device