US1953467A - Method and apparatus for dispensing gas material - Google Patents

Method and apparatus for dispensing gas material Download PDF

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Publication number
US1953467A
US1953467A US606270A US60627032A US1953467A US 1953467 A US1953467 A US 1953467A US 606270 A US606270 A US 606270A US 60627032 A US60627032 A US 60627032A US 1953467 A US1953467 A US 1953467A
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container
gas
main
main container
liquefied gas
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US606270A
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Leo I Dana
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Linde Air Products Co
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Linde Air Products Co
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Priority to BE395656A priority patent/BE395656A/en
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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
    • F17C7/00—Methods or apparatus for discharging liquefied, solidified, or compressed gases from pressure vessels, not covered by another subclass
    • F17C7/02—Discharging liquefied gases
    • F17C7/04—Discharging liquefied gases with change of state, e.g. vaporisation
    • 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
    • F17C2201/00—Vessel construction, in particular geometry, arrangement or size
    • F17C2201/01—Shape
    • F17C2201/0147—Shape complex
    • F17C2201/0166—Shape complex divided in several chambers
    • 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
    • F17C2201/00—Vessel construction, in particular geometry, arrangement or size
    • F17C2201/03—Orientation
    • F17C2201/035—Orientation with substantially horizontal main axis
    • 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
    • F17C2203/00—Vessel construction, in particular walls or details thereof
    • F17C2203/03—Thermal insulations
    • F17C2203/0304—Thermal insulations by solid means
    • 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
    • F17C2203/00—Vessel construction, in particular walls or details thereof
    • F17C2203/06—Materials for walls or layers thereof; Properties or structures of walls or their materials
    • F17C2203/0602—Wall structures; Special features thereof
    • F17C2203/0612—Wall structures
    • F17C2203/0626—Multiple walls
    • F17C2203/0629—Two walls
    • 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
    • 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
    • F17C2205/0329—Valves manually 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
    • F17C2205/0388—Arrangement of valves, regulators, filters
    • F17C2205/0391—Arrangement of valves, regulators, filters inside the pressure 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
    • 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
    • F17C2223/0161—Liquefied gas, e.g. LPG, GPL cryogenic, e.g. LNG, GNL, PLNG
    • 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
    • F17C2223/04—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by other properties of handled fluid before transfer
    • F17C2223/042—Localisation of the removal point
    • F17C2223/043—Localisation of the removal point in the gas
    • 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
    • F17C2223/04—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by other properties of handled fluid before transfer
    • F17C2223/042—Localisation of the removal point
    • F17C2223/046—Localisation of the removal point in the liquid
    • F17C2223/047—Localisation of the removal point in the liquid with a dip tube
    • 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
    • F17C2225/00—Handled fluid after transfer, i.e. state of fluid after transfer from the vessel
    • F17C2225/01—Handled fluid after transfer, i.e. state of fluid after transfer from the vessel characterised by the phase
    • F17C2225/0107—Single phase
    • F17C2225/0123—Single phase gaseous, e.g. CNG, GNC
    • 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
    • F17C2225/00—Handled fluid after transfer, i.e. state of fluid after transfer from the vessel
    • F17C2225/01—Handled fluid after transfer, i.e. state of fluid after transfer from the vessel characterised by the phase
    • F17C2225/0146—Two-phase
    • F17C2225/0153—Liquefied gas, e.g. LPG, GPL
    • Y—GENERAL 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
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T137/00—Fluid handling
    • Y10T137/4673—Plural tanks or compartments with parallel flow
    • Y10T137/469—Sequentially filled and emptied [e.g., holding type]
    • Y—GENERAL 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
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T137/00—Fluid handling
    • Y10T137/4673—Plural tanks or compartments with parallel flow
    • Y10T137/4841—With cross connecting passage

Definitions

  • This invention relates to a' method and apparatus for dispensing gas material, particularly gas material which is stored in the liquid phase at temperatures below 273 Kelvin,- and has for its principal object to avoid'the present practice of providing two main containers at the place of discharge and yet maintain a'continuous supply of gasmaterial to the 'consumingapparatus.
  • auxiliary container for use at the place of discharge arranged to cooperate with the main container of liquefied gas.
  • a further object is to provide a method and means for continuing the supply of gas material during the process of charging the main container.
  • the invention accordingly comprises the several steps and the relation of one or more of such steps with respect to each of the others, and the apparatus embodying featurf-r. of construction, combinations of elements and arrangement of parts which are adapted to effect-such steps, all' as exemplified in the following detailed disclosure, and the scope of the application of which will be indicated in the claims.
  • the figure is a view mainly in vertical section showing a preferred construction of a container for liquefied gases for use in accordance with the invention.
  • 10 denotes liquefled gas, which is shown as held by an inner receptacle or' basket 11 disposed within a relatively thick-walled pressure vessel or container 12 in such a manner that a comparatively narrow space exists between the walls of these vessels.
  • the inner vesselor basket 11 is provided with means affording communication for. gas pressure from its interior to the space between the walls of the two vessels, for example, an opening at the top of the basket.
  • a container or pressure vessel of the character indicated has associated with it an auxiliary container or vessel, preferably of smaller capacity than the main container.
  • auxiliary container may have any desired relation to the main container but is preferably so disposed that gravity will cause a flow of liquid from the main container into the auxiliary container.
  • an auxiliary container is shown at13 disposed below the main container 12; both comtainers in this instance being enclosed in a comindependent of the vessel 12, it is advantageous in manufacture to have a portion of their walls in common, for example arranged in the manner illustrated where a portion of the lower spherical wall of the vessel 12 forms the top wall of vessel 13.
  • the main pressure vessel 12 is provided with suitable openings and connections/for filling and for withdrawal of gas material that are here shown as comprising a filling conduit 16 and withdrawal conduits 18 and 22.
  • the conduit 16 7 passes through the wall of vessel 12, insulation 15 and envelope 14, and preferably has its inner end depending below the rim of basket 11; the external end being fitted with a suitable closure as a plug 1'7.
  • One end of conduit 18 is disposed in the top of main vessel 12 to withdraw gas therefrom, while the other end joins with gas supply conduit 19 which conducts the gas material to a. consuming apparatus.
  • the conduit 18 After passing to the outside of the envelope 14, the conduit 18 is provided with a stop valve 20 and is in communication with a safety pressure relief valve 21.
  • Theliquid withdrawal conduit 22 leads from a point near the lowest portion of the inner vessel 11, out through the wall of the main vessel 12 and to the outside of the envelope 14, where it is provided with valve 23 and joints conduit 24.
  • Conduit 24 conducts liquefied gas to the consuming apparatus.
  • connection 25 conducts liquefied gas through the common wall into the auxiliary pressure vessel 13'.
  • the flow of' liquefied gas into the auxiliary pressure vessel is controlled by a stop valve 26 at the end of connection 25.
  • the stop valve 26 is proyided with an extended stem and bonnet 2'7,
  • a liquid withdrawal conduit- 31 is connected at v its one end' to the bottom of the auxiliary pressure vessel 13, and at the other end to conduit 24. It is also provided with a stop valve 32 at a point just outside of casing 14.
  • the method of using the cold converter with liquid reserve in accordance with the invention above described is as follows: By operating hand wheel 28, the stop valve 26 is closed. Valves 20, 23, 30 and 32 are also closed and pressure released, for example, by loosening the closure 17. When the pressure has been released, the desired quantity of liquefied gas is introduced through the filling conduit 16. The basket 11, being of relatively small mass, will cause the evaporation of only an inappreciable amount of liquefied gas during the filling operation. After the closure 1'7 is replaced, the valves 20, 23-and 30 are opened, and finally valve 26 is opened by manipulation of hand wheel 28 to permit the fiow of liquefied gas from the main container 11 into the auxiliary container 13.
  • the metal walls of the auxiliary container being warm, cause evaporation of liquefied 4 gas to occur by the exchange of sensible heat of the mass of metal to latent heat of evaporation of the liquefied gas until the metal has been cooled to the temperature of the liquefied gas. Heat is transferred by conduction to the connected walls of the auxiliary container from the walls of the main pressure container 12.
  • the gas that is evaporated in the auxiliary container passes by means of conduits 29 and 18 to the gas spaces of the main pressure vessel and to the consuming apparatus through connected conduit 19.
  • the consuming apparatus is so controlled that withdrawal through conduit 19 occurs only when the pressure of gas therein exceeds a certain desired maximum.
  • Withdrawal through conduit 24 is likewise controlled by the consuming apparatus so that the desired quantity of gas material is withdrawn through conduit 24 whenthe pressure is equal to or lower than the desired pressure.
  • the valve 23 being open, liquefied gas is withdrawn from the inner vessel 11 of the main container until the supply therein is exhausted.
  • valve 32 is opened and valves 23,
  • valve 26 may be opened to refill the auxiliary container.
  • the exemplary apparatus illustrated and used in accordance with the method of the invention provides a means for maintaining a continuous supply of gas materialto consuming apparatus and avoids having available at the place of 'delivery to the consuming apparatus two separate main continers of liquefied gas or cold converters.
  • the methods of dispensing liquefied gas material are simplified and the cost of apparatus required therefor is reduced.
  • the construction of the apparatus of the present invention provides means under the control of the operator for accelerating the evaporation of a portion of the liquefied gas to develop an increase of pressure when such increase of pressure is most likely to be desired, as after the first charge of liquefied gas has been placed in the main container and after the apparatus has been shut down for a period of time after the dischargeof all of the .as new and desire to secure by Letters Patent, is:
  • a method of dispensing gas material which comprises charging liquefied gas into a thermally insulated container having an associated auxiliary container arranged to have its insulation in common with the main container, charging the auxiliary container directly from the main container, and thereafter discharging gas material in liquid and gas phases as desired from said containers.
  • a method of dispensing gas material which comprises charging liquefied gas into a thermally insulated container having an associated auxiliary container arranged to have its insulation in common with the main container, charging the auxiliary container from the main container, and thereafter discharging gas material independently from said containersin either liquid or gas phases.
  • a method for dispensing gas material which comprises charging liquefied gas into a thermally insulated main container for liquefied gases, to
  • An apparatus for dispensing gas material comprising a main container for liquefied gas, an auxiliary container connected with said main container, heat insulating material surrounding both containers, an envelope surrounding both containers and said insulating material, means for transferring aportion 01' the charge of the main container to the auxiliary container, and means material independently from both containers.
  • auxiliary container connected with said main container, heat insulating material surrounding both containers, an envelope surrounding both containers and said insulating material, means for filling said main container from without said envelope, means within said envelope for filling said auxiliary container by gravity from said main container, and means for discharging gas material from both containers.
  • An apparatus for dispensing gas material comprising a main container ior liquefied gas, .an auxiliary container attached to said .main
  • An apparatus for dispensing gas material comprising a main container of liquefied gas, a depending auxiliary container attached to said main container and having a portion or its bounding wall in common with said main container, heat insulating material surrounding both said containers an envelope surrounding both containers and said insulating material, communicating means in said common wall portion atfording the transfer of a liquid charge from said main container into said auxiliary container and

Description

April 3, 1934. L. DANA 1,953,46
METHOD AND APPARATUS FOR DISPENSING .GAS MATERIAL I Fiied April 19,1932
INVENTOR Patented Apr. 3, 1934 DIETHOD AND APPARATUS FOR DISPENS- ING GAS MATERIAL Leo I. Dana, Buffalo, N.'Y., assignor to The Linde Air Products Company, New York, Y.
Application April 19,1932, Serial No. 606,270 9 Claims. (o1. 62-1) This invention relates to a' method and apparatus for dispensing gas material, particularly gas material which is stored in the liquid phase at temperatures below 273 Kelvin,- and has for its principal object to avoid'the present practice of providing two main containers at the place of discharge and yet maintain a'continuous supply of gasmaterial to the 'consumingapparatus.
More specifically, it is anobject to provide an auxiliary container for use at the place of discharge arranged to cooperate with the main container of liquefied gas.
A further object is to provide a method and means for continuing the supply of gas material during the process of charging the main container.
Other objects of the invention will in part be obvious and will in part appear hereinafter.
The invention accordingly comprises the several steps and the relation of one or more of such steps with respect to each of the others, and the apparatus embodying featurf-r. of construction, combinations of elements and arrangement of parts which are adapted to effect-such steps, all' as exemplified in the following detailed disclosure, and the scope of the application of which will be indicated in the claims.
For a fuller understanding of the nature and objects of the invention reference should be had to the following detailed description taken in connection with the accompanying drawing, in which: a
The figure is a view mainly in vertical section showing a preferred construction of a container for liquefied gases for use in accordance with the invention.
Referring nowto the drawing, 10 denotes liquefled gas, which is shown as held by an inner receptacle or' basket 11 disposed within a relatively thick-walled pressure vessel or container 12 in such a manner that a comparatively narrow space exists between the walls of these vessels. The inner vesselor basket 11 is provided with means affording communication for. gas pressure from its interior to the space between the walls of the two vessels, for example, an opening at the top of the basket.
In accordance with the present invention, a container or pressure vessel of the character indicated has associated with it an auxiliary container or vessel, preferably of smaller capacity than the main container. Such auxiliary container may have any desired relation to the main container but is preferably so disposed that gravity will cause a flow of liquid from the main container into the auxiliary container. To this end an auxiliary container is shown at13 disposed below the main container 12; both comtainers in this instance being enclosed in a comindependent of the vessel 12, it is advantageous in manufacture to have a portion of their walls in common, for example arranged in the manner illustrated where a portion of the lower spherical wall of the vessel 12 forms the top wall of vessel 13. 7
The main pressure vessel 12 is provided with suitable openings and connections/for filling and for withdrawal of gas material that are here shown as comprising a filling conduit 16 and withdrawal conduits 18 and 22. The conduit 16 7 passes through the wall of vessel 12, insulation 15 and envelope 14, and preferably has its inner end depending below the rim of basket 11; the external end being fitted with a suitable closure as a plug 1'7. One end of conduit 18 is disposed in the top of main vessel 12 to withdraw gas therefrom, while the other end joins with gas supply conduit 19 which conducts the gas material to a. consuming apparatus. After passing to the outside of the envelope 14, the conduit 18 is provided with a stop valve 20 and is in communication with a safety pressure relief valve 21. Theliquid withdrawal conduit 22 leads from a point near the lowest portion of the inner vessel 11, out through the wall of the main vessel 12 and to the outside of the envelope 14, where it is provided with valve 23 and joints conduit 24.
Conduit 24 conducts liquefied gas to the consuming apparatus. k
From the bottom of inner vessel 11, a connection 25 conducts liquefied gas through the common wall into the auxiliary pressure vessel 13'. The flow of' liquefied gas into the auxiliary pressure vessel is controlled by a stop valve 26 at the end of connection 25. The stop valve 26 is proyided with an extended stem and bonnet 2'7,
' external to the envelope 14 with a stop valve 30.
A liquid withdrawal conduit- 31 is connected at v its one end' to the bottom of the auxiliary pressure vessel 13, and at the other end to conduit 24. It is also provided with a stop valve 32 at a point just outside of casing 14.
In order to insure an uninterrupted supply of gas material to consuming apparatus, it has been the usual practice to install at the place of delivery to consuming apparatus two main cold converters or containing devices having pressure vessels for holding liquefied gas insulated against the infiux of heat. 'When the contents of one cold converter becomes exhausted, withdrawal is continued from the other cold converter and the exhausted cold converter refilled.
Heretofore it was customary, when refilling cold converters, to close the withdrawal valves and release the pressure to the atmosphere, whereby the liquefied gas being placed in the exhausted converter may fiow in readily. To add liquefied gas to a partially filled cold converter would generally result in a relatively great loss of gas material, as liquefied gas under pressure is usually at a higher temperature than its boiling point at atmospheric pressure. The release of such pressure gas, in consequence, would cause evaporation and boiling of the liquefied gas until its temperature was lowered to the boiling point at the lower pressure. These losses are avoided by the practice of the present invention.
The method of using the cold converter with liquid reserve in accordance with the invention above described is as follows: By operating hand wheel 28, the stop valve 26 is closed. Valves 20, 23, 30 and 32 are also closed and pressure released, for example, by loosening the closure 17. When the pressure has been released, the desired quantity of liquefied gas is introduced through the filling conduit 16. The basket 11, being of relatively small mass, will cause the evaporation of only an inappreciable amount of liquefied gas during the filling operation. After the closure 1'7 is replaced, the valves 20, 23-and 30 are opened, and finally valve 26 is opened by manipulation of hand wheel 28 to permit the fiow of liquefied gas from the main container 11 into the auxiliary container 13. The metal walls of the auxiliary container being warm, cause evaporation of liquefied 4 gas to occur by the exchange of sensible heat of the mass of metal to latent heat of evaporation of the liquefied gas until the metal has been cooled to the temperature of the liquefied gas. Heat is transferred by conduction to the connected walls of the auxiliary container from the walls of the main pressure container 12. The gas that is evaporated in the auxiliary container passes by means of conduits 29 and 18 to the gas spaces of the main pressure vessel and to the consuming apparatus through connected conduit 19.
The consuming apparatus is so controlled that withdrawal through conduit 19 occurs only when the pressure of gas therein exceeds a certain desired maximum. Withdrawal through conduit 24 is likewise controlled by the consuming apparatus so that the desired quantity of gas material is withdrawn through conduit 24 whenthe pressure is equal to or lower than the desired pressure. The valve 23 being open, liquefied gas is withdrawn from the inner vessel 11 of the main container until the supply therein is exhausted.
At this time valve 32 is opened and valves 23,
26 and 20 are closed so that. the main container is completely sealed and withdrawal of gas material continues from the auxiliary container 13 through conduits 29 and 31. The pressure in tainer by opening valve 23 and closing valve 32,-
after which the valve 26 may be opened to refill the auxiliary container.
It will thus be seen that the exemplary apparatus illustrated and used in accordance with the method of the invention, as described, provides a means for maintaining a continuous supply of gas materialto consuming apparatus and avoids having available at the place of 'delivery to the consuming apparatus two separate main continers of liquefied gas or cold converters. By this invention, the methods of dispensing liquefied gas material are simplified and the cost of apparatus required therefor is reduced.
It will also be seen that the construction of the apparatus of the present invention provides means under the control of the operator for accelerating the evaporation of a portion of the liquefied gas to develop an increase of pressure when such increase of pressure is most likely to be desired, as after the first charge of liquefied gas has been placed in the main container and after the apparatus has been shut down for a period of time after the dischargeof all of the .as new and desire to secure by Letters Patent, is:
1. A method of dispensing gas material which comprises charging liquefied gas into a thermally insulated container having an associated auxiliary container arranged to have its insulation in common with the main container, charging the auxiliary container directly from the main container, and thereafter discharging gas material in liquid and gas phases as desired from said containers.
2. A method of dispensing gas material which comprises charging liquefied gas into a thermally insulated container having an associated auxiliary container arranged to have its insulation in common with the main container, charging the auxiliary container from the main container, and thereafter discharging gas material independently from said containersin either liquid or gas phases.
3. A method for dispensing gas material which comprises charging liquefied gas into a thermally insulated main container for liquefied gases, to
said main container, common heat insulation for Y for discharging gas said containers, means for transferring a portion of the charge from the main container to the auxiliary container, and means associated with both containers for independently discharging gas material therefrom.
5. An apparatus for dispensing gas material comprising a main container for liquefied gas, an auxiliary container connected with said main container, heat insulating material surrounding both containers, an envelope surrounding both containers and said insulating material, means for transferring aportion 01' the charge of the main container to the auxiliary container, and means material independently from both containers.
6. An apparatus for dispensing gas material comprising a main container for liquefied gas, an
auxiliary container connected with said main container, heat insulating material surrounding both containers, an envelope surrounding both containers and said insulating material, means for filling said main container from without said envelope, means within said envelope for filling said auxiliary container by gravity from said main container, and means for discharging gas material from both containers.
'7. An apparatus for dispensing gas material,
comprising a main container for liquefied gas, an
auxiliary container connected with said main container, heat insulating material surrounding both containers, an envelope surrounding both containersand said insulating material, means for filling said main container from without said envelope, means within said envelope for filling said auidliary container from said main container, a gas phase withdrawal conduit having branches connected to the upper portions of each 01' said containeraand a liquid phase withdrawal conduit having branches connected to the lower portion oi! each of said containers.
8. An apparatus for dispensing gas material comprising a main container ior liquefied gas, .an auxiliary container attached to said .main
container arranged to have a portion of its wall in common with said main container, heat insulating material surrounding said containers an envelope surrounding both containers and said insulating material, gravity means for transferring a charge of liquid from said main container to said auxiliary container, and means affording the discharge of gas material from both of said containers.
9. An apparatus for dispensing gas material comprising a main container of liquefied gas, a depending auxiliary container attached to said main container and having a portion or its bounding wall in common with said main container, heat insulating material surrounding both said containers an envelope surrounding both containers and said insulating material, communicating means in said common wall portion atfording the transfer of a liquid charge from said main container into said auxiliary container and
US606270A 1932-04-19 1932-04-19 Method and apparatus for dispensing gas material Expired - Lifetime US1953467A (en)

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Application Number Priority Date Filing Date Title
US606270A US1953467A (en) 1932-04-19 1932-04-19 Method and apparatus for dispensing gas material
DED65634D DE592298C (en) 1932-04-19 1933-03-30 Process for the uninterrupted preparation of compressed gases from their liquid aggregate state
BE395656A BE395656A (en) 1932-04-19 1933-04-13 METHOD AND APPARATUS FOR GAS DISTRIBUTION

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US606270A US1953467A (en) 1932-04-19 1932-04-19 Method and apparatus for dispensing gas material

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2479070A (en) * 1943-06-19 1949-08-16 Linde Air Prod Co Apparatus for and method of dispensing liquefied gases
US3878689A (en) * 1970-07-27 1975-04-22 Carl A Grenci Liquefaction of natural gas by liquid nitrogen in a dual-compartmented dewar
US5373701A (en) * 1993-07-07 1994-12-20 The Boc Group, Inc. Cryogenic station
US11262026B2 (en) * 2018-12-07 2022-03-01 Chart Inc. Cryogenic liquid dispensing system having a raised basin
US11549645B2 (en) 2018-01-19 2023-01-10 Linde Gmbh Cryogenic vessel

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0290432A4 (en) * 1986-11-19 1989-03-07 Pubgas Internat Pty Ltd Storage and transportation of liquid co 2?.
FR3130926A1 (en) * 2021-12-22 2023-06-23 Faurecia Systemes D'echappement Cryogenic fluid storage unit

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2479070A (en) * 1943-06-19 1949-08-16 Linde Air Prod Co Apparatus for and method of dispensing liquefied gases
US3878689A (en) * 1970-07-27 1975-04-22 Carl A Grenci Liquefaction of natural gas by liquid nitrogen in a dual-compartmented dewar
US5373701A (en) * 1993-07-07 1994-12-20 The Boc Group, Inc. Cryogenic station
US11549645B2 (en) 2018-01-19 2023-01-10 Linde Gmbh Cryogenic vessel
US11262026B2 (en) * 2018-12-07 2022-03-01 Chart Inc. Cryogenic liquid dispensing system having a raised basin

Also Published As

Publication number Publication date
BE395656A (en) 1933-05-31
DE592298C (en) 1934-02-06

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