US2339134A - Butane gas tank feed device - Google Patents

Butane gas tank feed device Download PDF

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US2339134A
US2339134A US213946A US21394638A US2339134A US 2339134 A US2339134 A US 2339134A US 213946 A US213946 A US 213946A US 21394638 A US21394638 A US 21394638A US 2339134 A US2339134 A US 2339134A
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tank
gas
liquid
evaporation
tube
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Baker Robin
James C Fleming
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    • 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
    • F17C7/00Methods or apparatus for discharging liquefied, solidified, or compressed gases from pressure vessels, not covered by another subclass
    • F17C7/02Discharging liquefied gases
    • F17C7/04Discharging liquefied gases with change of state, e.g. vaporisation
    • 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
    • F17C2270/00Applications
    • F17C2270/01Applications for fluid transport or storage
    • F17C2270/0142Applications for fluid transport or storage placed underground
    • F17C2270/0144Type of cavity
    • F17C2270/0147Type of cavity by burying vessels
    • 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
    • Y10T137/6416With heating or cooling of the system
    • Y10T137/6552With diversion of part of fluid to heat or cool the device or its contents

Definitions

  • Patented Jan. 11, 1944 UNITED STATES PATENT OFFICE This invention relates to an improvement in butane gas tanks and more particularly to the manner of removing the butane from the tank.
  • butan gas for domestic and commercial purposes has become quitecommon in various sections of the United States.
  • Butane maintains a. liquid state at temperatures below 32 F. and may be held in a liquid state under pressure at higher temperatures.
  • the tanks in which butane is stored usually operate under pressure obtained by temperature or other methods.
  • the object of this invention is to feed the agitated liquid fuel into an evaporation tube, whereby the lower specific gravity liquid fuels are carried oil! in vapor with the higher specific gravity liquid fuels, thereby vaporizing a more even B. t. u. content for feeding into the house line and to the appliances.
  • This object is accomplished'by removing the liquid butane from a point near the bottom of the tank and conducting it through a small opening in the evaporation tubewhere the liquid is generated-into a gas for use, which may thereafter be directed upwardly through a gas chamber and outlet tube, through a conventional control valve and pressure regulator to a desired point of use, such as an ordinary gas stove.
  • Fig. 1 is a side elevation of a butane gas tank and fittings, with parts broken away and in section and embodying this invention
  • Fig. 2 is a vertical section therethrough on the line 2-4 of Fig. 1;
  • Another object of the invention is to set up an agitation and circulation of the liquids in the tank by the creation 0! unequal temperatures, brought about by the evaporation of the liquids in the tube.
  • a feature of this invention is the provision of a gas outlet tube of relatively large diameter with respect to the outlet pipe, so that wet gas will fall back into the evaporation tube from the outlet pipe, permitting only dry gas to be directed to the point of use.
  • a thermo-insulated hood or box encloses the various fittings to keep the temperature of such fittings and gas outlet tube above the evaporation point.
  • the tube i0 substantially at th liquid level designated generally by the numeral II to provide evaporation area in the tube l0.
  • the evaporation tube Ill extends downwardly substantially to the bottom of tank I and is secured thereto as by welding.
  • the lower end of said tube has a small opening I! which permits the agitated liquid fuel to enter the tube ill for evaporation of the gas therei'rom.'
  • the evaporated gas is stored in gas storage chamber 9.
  • This enlarged diameter of the gas outlet tube i3 permits the wet gas particles to settle back into the evaporation tube i0, whereby only dry gas will be fed outward to the point of use.
  • the upper end of the gas outlet tube I3 is connected with an excess flow valve H which in turn communicates with a gas line I5 leading to the point of use, such as an ordinary stove.
  • the gas line I5 is provided with a manually controlled valve I6 therein and with a regulator H, which holds the back pressure on the gas storage chamber 8 and tank 1.
  • a pressure gauge It may be provided also and preferably connected with the pipe line ii to indicate the pressure of the gas passing therethrough and likewise the pressure in the tank 1.
  • the pressure in the evaporation tube has a tendency todrop, which permits additional liquid butane to be forced into the evaporation tube by the pressure in the tank. This will cause the liquid level to rise in the tube thereby agitating the liquid fuel in both the evaporation tube In and tank I.
  • the liquid in the tank 1 has three distinct movements, that is, a thermo-circulation as indicated by the arrows which is due to the chilling of the large tube I0; another circulation is produced by the travel of the liquid toward the opening in the bottom of the tube In.
  • a third movement, which is intermittent, is created by the opening of a gas burner or a Withdrawing of gas from the chamber '9, which will cause an inrush of liquid into the tube I0, causing the level momentarily to rise, and as soon as the pressure becomes equalized, the fluid will s'ettle back, agitating the liquid fuel in the tank.
  • This constant agitation of the fuel in the tank permits the withdrawal of an agitated liquid of substantially an even specific gravity at all times. This is very desirable, as gas burners, when adjusted for a certain B. t. u. gas content, do not function economically on gases of different B. t. u. content.
  • butane gas contains approximately 70% butane which has a boiling point of 32 F. and weighs approximately five pounds per gallon. It contains approximately 3260 B. t. u. per cubic foot, and at 60 F. the gas enclosed within a tank will exert a pressure of approximately twenty pounds per square inch.
  • Commercial butane also contains isobutane and propane in about equal proportions. Isobutane is lighter in specific gravity, weighing approximately four pounds fourteen ounces per gallon, and at 60 temperature will exert a pressure of approximately thirty-five pounds per square inch in a tank.
  • the boiling point of isobutane is approximately 12 F. and it contains approximately 3000 B. t. u. per cubic foot. Propane weighs approximately four pounds twelve ounces per gallon and at 60 F.
  • the agitated liquids are removed from the bottom of the storage tank and are conveyed into the evaporation tube l0. Furthermore, the evaporation of liquids within the tube In causes a lowering of the temperature of this chamber and the liquid butane in the tank is chilled near this chamber thereby setting up a circulation of the liquid butane in the tank, substantially as illustrated by the arrows therein, which will bring about the agitation of the liquid and serve to prevent stratification of liquids of different specific gravities.
  • the butane tank is usually buried in the ground, and to provide access thereto and to the fittings thereof, a hood or housing 19 eXtends upwardly from the tank to the surface of the ground, enclosing the fittings.
  • the hood or housing 19 has a removable cover 20 hinged provided with insulating material 2
  • the outlet tube I3 is enclosed within the hood or housing l9, and also enclosed within this hood or housing and connected with the top of the tank 1 are a filling pipe 22 and a vent pipe 23, both provided with conventional valves 24 at the upper ends thereof.
  • a gauge tube 25 extends through the top of the tank to a point near the bottom thereof and has its upper end enclosed in a housing 26.
  • a combined gas and evaporation chamber 9' is disposed exteriorly of the tank I and a tube In extends into the chamber 9 from a point adjacent the bottom of the tank, having its upper end spaced above the bottom of the chamber 9' in order to maintain a liquid level therein, whereby to provide for evaporation of the butane gas from the liquid in the combined gas and evaporation chamber.
  • the invention operates in thesame way as described above in connection with Figs. 1 to 3.
  • a vertically disposed outlet tube 28 is mounted di- .rectly in the tank Ia and extends through the thereto and both the cover and the side walls are 1 top of the tank being connected with the outlet pipe as described above.
  • Outlet tube 28 extends downwardly in the tank to a point near the bottom thereof where it is provided with an orifice 29 to admit the liquid butane from the tank into the lower end of the tube, the liquid rising in the tube to a liquid level substantially as indicated by the numeral 30.
  • the upper portion of the tube 28 forms an evaporation chamber that permits the butane gas to evaporate and pass off through the outlet pipe to the point of use.
  • This form of the invention will function substantially in the same manner as described above in connection with the other forms thereof, having induced thermo-circulation due to the evaporation of the liquid and the discharge of thegas from the evaporation chamber 3
  • a fuel storage receptacle comprising a tank for liquid fuel, a separate evaporation chamber adjacent the top of the tank and of wide shallow construction, means for withdrawing liquid from a point adjacent the bottom of the tank and directing the same into the evaporation chamber, and means for directing gaseous fuel from said evaporation chamber.
  • a fuel storage receptacle comprising a tank, an evaporation chamber separate from said tank and of Wide shallow construction, means for withdrawing liquid fuel from a point adjacent the bottom of the tank and directing the same into the evaporation chamber, means for maintaining a liquid level in said evaporation chamber to provide for evaporation of gas from the liquid therein, and means for withdrawing the liberated gas from said chamber.
  • a fuel receptacle comprising a tank adapted to contain liquid fuel, means forming an evaporation chamber adjacent the top of said tank and of wide shallow construction, a tube extending from a point adjacent the bottom of the tank Otherwise, this form of into the evaporation chamber and having the discharge point thereof spaced above the bottom of said chamber for maintaining a liquid level in the evaporation chamber to provide for evaporation of gas from the liquid, and means for withdrawing the liberated gas from said chamber.
  • a fuel storage receptacle comprising a tank, and an enclosed gas storage chamber at an upper portion of the tank and having a substantially closed bottom with a tube separate from said chamber and extending downwardly from the bottom thereof in said tank, said tube having communication with the tank for withdrawing liquid therefrom into the storage chamber.
  • a fuel storage receptacle comprising a tank
  • a fuel storage receptacle comprising a tank for liquid fuel, means forming an enclosed wide evaporation chamber adjacent the tank, and means for withdrawing liquid from the tank for liberation of gas in said evaporation chamber.
  • a fuel storage receptacle comprising a tank for liquid fuel, means forming an enclosed wide shallow evaporation chamber adjacent the tank separate therefrom, and means for withdrawing liquid from the tank for separation of gas in said evaporation chamber.
  • a fuel storage receptacle comprising a tank for liquid fuel, means forming a wide shallow closed-top evaporation chamber at the top of the tank, and means extending downwardly from said evaporation chamber in the tank to a point adjacent the bottom thereof for withdrawing liquid from the tank for liberation of gas in said evaporation chamber.
  • a fuel storage receptacle comprising a tank for liquid fuel, means forming a wide shallow evaporation chamber at the top of the tank, and means extending downwardly from said evaporation chamber, in the tank to a point adjacent the bottom thereof for withdrawing liquid from the tank for liberation of gas in said evaporation chamber, and a bell receiver arranged over the chamber in open communication therewith for withdrawing the liberated gas therefrom.
  • a fuel storage receptacle comprising a tank for liquid fuel, means forming an enclosed wide shallow evaporation chamber extending horizontally at the top of the tank and of appreciable horizontal area, and a conduit extending downwardly from said evaporation chamber in the tank for withdrawing liquid therefrom into the evaporation chamber for liberation of gas therefrom.

Description

Jan. 11, 1944. R. BAKER ETAL BUTANE GAS-TANK FEED DEVICE Filed June 15,
1958 2 Sheets-Sheet 1 1 1 1 1/ 1 1/ 1/ 1.1 l/ I I 1 ,p-INVENTRS, ROBIN BAKER 7 BY JAMES FLEMING 11 11 1 1 11 1 1/ 1 1/ l1 1 1/ I 1/ l/ ,1 H 1 685 4 I ll 3 f I I /1 8 I I: l
H1 11 11 1/ 11 11 11 m 11 /1 11 1 11 11 1 kN ATTORNEY.
Jan. 11, 1944. R. BAKER ETAL BUTANE GAS TANK FEED DEVICE Filed June 15, 1958 2 Sheets-Sheet 2 Fig.4
. INVENTORS ROB! N BA KER I J. m F
,BY AME? C.FLEM/N6 :Q-LA'ITORNEY.
Patented Jan. 11, 1944 UNITED STATES PATENT OFFICE This invention relates to an improvement in butane gas tanks and more particularly to the manner of removing the butane from the tank.
The use of butan gas for domestic and commercial purposes has become quitecommon in various sections of the United States. Butane maintains a. liquid state at temperatures below 32 F. and may be held in a liquid state under pressure at higher temperatures. The tanks in which butane is stored usually operate under pressure obtained by temperature or other methods.
Various forms of butane tanks have been provided heretofore which utilize the upper portion of the tank itself as an evaporation chamber, whereby the lighter gases evaporate first and the evaporation continues until th liquid residue left in the bottom of the tank becomes so heavy that no gas will evaporate. As the use of the tank continues, this low gravit liquid accumulates until the eillciency of the gas system is impaired.
The object of this invention is to feed the agitated liquid fuel into an evaporation tube, whereby the lower specific gravity liquid fuels are carried oil! in vapor with the higher specific gravity liquid fuels, thereby vaporizing a more even B. t. u. content for feeding into the house line and to the appliances.
This object is accomplished'by removing the liquid butane from a point near the bottom of the tank and conducting it through a small opening in the evaporation tubewhere the liquid is generated-into a gas for use, which may thereafter be directed upwardly through a gas chamber and outlet tube, through a conventional control valve and pressure regulator to a desired point of use, such as an ordinary gas stove.
be understood that the design may be varied and changes made in the minor details of construction within the scope of the invention as claimed, without departing from the spirit thereof.
In the accompanying drawings: I I
Fig. 1 is a side elevation of a butane gas tank and fittings, with parts broken away and in section and embodying this invention;
Fig. 2 is a vertical section therethrough on the line 2-4 of Fig. 1;
' l0 has one end extending into the chamber 8 Another object of the invention is to set up an agitation and circulation of the liquids in the tank by the creation 0! unequal temperatures, brought about by the evaporation of the liquids in the tube.
A feature of this invention is the provision of a gas outlet tube of relatively large diameter with respect to the outlet pipe, so that wet gas will fall back into the evaporation tube from the outlet pipe, permitting only dry gas to be directed to the point of use. A thermo-insulated hood or box encloses the various fittings to keep the temperature of such fittings and gas outlet tube above the evaporation point.
We have illustrated in the accompanying drawing a preferred embodiment of this invention together with modifications thereof, but it is to to a point level with or spaced above the bottom of the chamber to supply gas thereto and to maintain a predetermined quantity of liquid in.
the tube i0 substantially at th liquid level designated generally by the numeral II to provide evaporation area in the tube l0.
The evaporation tube Ill extends downwardly substantially to the bottom of tank I and is secured thereto as by welding. The lower end of said tube has a small opening I! which permits the agitated liquid fuel to enter the tube ill for evaporation of the gas therei'rom.' The evaporated gas is stored in gas storage chamber 9.
Communicating with the upper portion or the gas storage chamber 8 and carried by the top of the tank I is a bell-shaped outlet tube ii of enlarged diameter into which the gas passes as it rises from the liquid in the evaporation tube in. This enlarged diameter of the gas outlet tube i3 permits the wet gas particles to settle back into the evaporation tube i0, whereby only dry gas will be fed outward to the point of use. The upper end of the gas outlet tube I3 is connected with an excess flow valve H which in turn communicates with a gas line I5 leading to the point of use, such as an ordinary stove. The gas line I5 is provided with a manually controlled valve I6 therein and with a regulator H, which holds the back pressure on the gas storage chamber 8 and tank 1. A pressure gauge It may be provided also and preferably connected with the pipe line ii to indicate the pressure of the gas passing therethrough and likewise the pressure in the tank 1.
As the liquid evaporates and the gas is used, the pressure in the evaporation tube has a tendency todrop, which permits additional liquid butane to be forced into the evaporation tube by the pressure in the tank. This will cause the liquid level to rise in the tube thereby agitating the liquid fuel in both the evaporation tube In and tank I.
The liquid in the tank 1 has three distinct movements, that is, a thermo-circulation as indicated by the arrows which is due to the chilling of the large tube I0; another circulation is produced by the travel of the liquid toward the opening in the bottom of the tube In. A third movement, which is intermittent, is created by the opening of a gas burner or a Withdrawing of gas from the chamber '9, which will cause an inrush of liquid into the tube I0, causing the level momentarily to rise, and as soon as the pressure becomes equalized, the fluid will s'ettle back, agitating the liquid fuel in the tank. This constant agitation of the fuel in the tank permits the withdrawal of an agitated liquid of substantially an even specific gravity at all times. This is very desirable, as gas burners, when adjusted for a certain B. t. u. gas content, do not function economically on gases of different B. t. u. content.
Commercial butane gas contains approximately 70% butane which has a boiling point of 32 F. and weighs approximately five pounds per gallon. It contains approximately 3260 B. t. u. per cubic foot, and at 60 F. the gas enclosed within a tank will exert a pressure of approximately twenty pounds per square inch. Commercial butane also contains isobutane and propane in about equal proportions. Isobutane is lighter in specific gravity, weighing approximately four pounds fourteen ounces per gallon, and at 60 temperature will exert a pressure of approximately thirty-five pounds per square inch in a tank. The boiling point of isobutane is approximately 12 F. and it contains approximately 3000 B. t. u. per cubic foot. Propane weighs approximately four pounds twelve ounces per gallon and at 60 F. it exerts a pressure of approximately seventyfive pounds per square inch in a tank. The boiling point is approximately -48 F. and it has approximately 2550 B. t. 11. per cubic foot. There are traces of heavier fuels in the liquified gas; consequently when the fuel remains in an unagitated static condition, these liquids of varying specific gravities tend to stratify, which happens when the evaporation methods used heretofore are employed.
By this invention, the agitated liquids are removed from the bottom of the storage tank and are conveyed into the evaporation tube l0. Furthermore, the evaporation of liquids within the tube In causes a lowering of the temperature of this chamber and the liquid butane in the tank is chilled near this chamber thereby setting up a circulation of the liquid butane in the tank, substantially as illustrated by the arrows therein, which will bring about the agitation of the liquid and serve to prevent stratification of liquids of different specific gravities.
The butane tank is usually buried in the ground, and to provide access thereto and to the fittings thereof, a hood or housing 19 eXtends upwardly from the tank to the surface of the ground, enclosing the fittings. The hood or housing 19 has a removable cover 20 hinged provided with insulating material 2| which serves to keep the temperature within the hood above the point of evaporation.
The outlet tube I3 is enclosed within the hood or housing l9, and also enclosed within this hood or housing and connected with the top of the tank 1 are a filling pipe 22 and a vent pipe 23, both provided with conventional valves 24 at the upper ends thereof. A gauge tube 25 extends through the top of the tank to a point near the bottom thereof and has its upper end enclosed in a housing 26.
The modification of the invention which is shown in Fig. 4, is similar in structure and operation to that described above, except that a combined gas and evaporation chamber 9' is disposed exteriorly of the tank I and a tube In extends into the chamber 9 from a point adjacent the bottom of the tank, having its upper end spaced above the bottom of the chamber 9' in order to maintain a liquid level therein, whereby to provide for evaporation of the butane gas from the liquid in the combined gas and evaporation chamber. the invention operates in thesame way as described above in connection with Figs. 1 to 3.
In the further modification shown in Fig. 5, a vertically disposed outlet tube 28 is mounted di- .rectly in the tank Ia and extends through the thereto and both the cover and the side walls are 1 top of the tank being connected with the outlet pipe as described above. Outlet tube 28 extends downwardly in the tank to a point near the bottom thereof where it is provided with an orifice 29 to admit the liquid butane from the tank into the lower end of the tube, the liquid rising in the tube to a liquid level substantially as indicated by the numeral 30. The upper portion of the tube 28 forms an evaporation chamber that permits the butane gas to evaporate and pass off through the outlet pipe to the point of use. This form of the invention will function substantially in the same manner as described above in connection with the other forms thereof, having induced thermo-circulation due to the evaporation of the liquid and the discharge of thegas from the evaporation chamber 3|.
While the system has been described in connection with butane gas, it is to be understood that any liquid suitable for the purpose may be used.
We claim:
1. A fuel storage receptacle comprisinga tank for liquid fuel, a separate evaporation chamber adjacent the top of the tank and of wide shallow construction, means for withdrawing liquid from a point adjacent the bottom of the tank and directing the same into the evaporation chamber, and means for directing gaseous fuel from said evaporation chamber.
2. A fuel storage receptacle comprising a tank, an evaporation chamber separate from said tank and of Wide shallow construction, means for withdrawing liquid fuel from a point adjacent the bottom of the tank and directing the same into the evaporation chamber, means for maintaining a liquid level in said evaporation chamber to provide for evaporation of gas from the liquid therein, and means for withdrawing the liberated gas from said chamber.
3. A fuel receptacle comprising a tank adapted to contain liquid fuel, means forming an evaporation chamber adjacent the top of said tank and of wide shallow construction, a tube extending from a point adjacent the bottom of the tank Otherwise, this form of into the evaporation chamber and having the discharge point thereof spaced above the bottom of said chamber for maintaining a liquid level in the evaporation chamber to provide for evaporation of gas from the liquid, and means for withdrawing the liberated gas from said chamber.
4. A fuel storage receptacle comprising a tank, and an enclosed gas storage chamber at an upper portion of the tank and having a substantially closed bottom with a tube separate from said chamber and extending downwardly from the bottom thereof in said tank, said tube having communication with the tank for withdrawing liquid therefrom into the storage chamber.
5. A fuel storage receptacle comprising a tank,
1 a separated enlarged gas storage chamber at an upper portion of the tank having a substantially closed bottom, and an evaporation tube connected with the bottom of said storage chamber and extending downwardly therefrom in said tank, said tube having communication with the tank for withdrawing liquid therefrom and for maintaining a liquid level in the tube, said tube being of sufficiently large diameter for evaporation of gas from the liquid therein.
6. A fuel storage receptacle comprising a tank for liquid fuel, means forming an enclosed wide evaporation chamber adjacent the tank, and means for withdrawing liquid from the tank for liberation of gas in said evaporation chamber.
7. A fuel storage receptacle comprising a tank for liquid fuel, means forming an enclosed wide shallow evaporation chamber adjacent the tank separate therefrom, and means for withdrawing liquid from the tank for separation of gas in said evaporation chamber.
8. A fuel storage receptacle comprising a tank for liquid fuel, means forming a wide shallow closed-top evaporation chamber at the top of the tank, and means extending downwardly from said evaporation chamber in the tank to a point adjacent the bottom thereof for withdrawing liquid from the tank for liberation of gas in said evaporation chamber.
9. A fuel storage receptacle comprising a tank for liquid fuel, means forming a wide shallow evaporation chamber at the top of the tank, and means extending downwardly from said evaporation chamber, in the tank to a point adjacent the bottom thereof for withdrawing liquid from the tank for liberation of gas in said evaporation chamber, and a bell receiver arranged over the chamber in open communication therewith for withdrawing the liberated gas therefrom.
10. A fuel storage receptacle comprising a tank for liquid fuel, means forming an enclosed wide shallow evaporation chamber extending horizontally at the top of the tank and of appreciable horizontal area, and a conduit extending downwardly from said evaporation chamber in the tank for withdrawing liquid therefrom into the evaporation chamber for liberation of gas therefrom.
ROBDI BAKER. JAMES C. FLEMING.
US213946A 1938-06-15 1938-06-15 Butane gas tank feed device Expired - Lifetime US2339134A (en)

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2463493A (en) * 1944-08-24 1949-03-01 Bastian Blessing Co Gas dispensing device
US2500936A (en) * 1936-06-27 1950-03-21 Bastian Blessing Co Gas generating apparatus
US2516761A (en) * 1945-03-22 1950-07-25 T H Duff Dispensing system for liquefied gases
US2525874A (en) * 1944-08-31 1950-10-17 Bastian Blessing Co Vaporizer for liquefied petroleum gas dispensing systems
US2564226A (en) * 1941-05-27 1951-08-14 Bastian Blessing Co Gas dispensing device

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2500936A (en) * 1936-06-27 1950-03-21 Bastian Blessing Co Gas generating apparatus
US2564226A (en) * 1941-05-27 1951-08-14 Bastian Blessing Co Gas dispensing device
US2463493A (en) * 1944-08-24 1949-03-01 Bastian Blessing Co Gas dispensing device
US2525874A (en) * 1944-08-31 1950-10-17 Bastian Blessing Co Vaporizer for liquefied petroleum gas dispensing systems
US2516761A (en) * 1945-03-22 1950-07-25 T H Duff Dispensing system for liquefied gases

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